CN101957092B - Type III absorbing and generating system and type III absorbing heat pump - Google Patents

Type III absorbing and generating system and type III absorbing heat pump Download PDF

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CN101957092B
CN101957092B CN2010105291772A CN201010529177A CN101957092B CN 101957092 B CN101957092 B CN 101957092B CN 2010105291772 A CN2010105291772 A CN 2010105291772A CN 201010529177 A CN201010529177 A CN 201010529177A CN 101957092 B CN101957092 B CN 101957092B
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generator
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CN101957092A (en
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李华玉
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/008—Sorption machines, plants or systems, operating continuously, e.g. absorption type with multi-stage operation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Sorption Type Refrigeration Machines (AREA)

Abstract

The invention provides a type III absorbing and generating system and a type III absorbing heat pump, belonging to the technical field of heat pumps. The type III absorbing and generating system comprises a first absorber, a second absorber, a generator, a solution heat exchanger, a steam separating chamber, a plurality of solution pumps or/and solution throttle valves, and the like, or one path of solution is circulated among the first absorber, the second absorber, the steam separating chamber and a second solution pump and the other path of solution is circulated among the second absorber, a first solution pump, the solution heat exchanger and the generator or the solution enters the second absorber from the first absorber through a third solution pump, enters the generator through the first solution pump and the solution heat exchanger, enters the steam separating chamber through the solution heat exchanger and the second absorber, and enters the first absorber through the second solution pump; the first absorber, a heated medium pipeline and a refrigerant steam channel are respectively communicated with outside; the steam separating chamber and the refrigerant steam channel are communicated with outside; the second absorber and the refrigerant steam channel or/and the heated medium pipeline are communicated with outside; the generator and a drive heat medium pipeline and the refrigerant steam channel are respectively communicated with outside; and a series of type III absorbing heat pumps based on the type III absorbing and generating system are formed by combining a first condenser, a second condenser and an evaporator with other parts.

Description

The 3rd class absorption-generation systems and the 3rd class absorption heat pump
Technical field:
The invention belongs to the low temperature heat technical field of heat pumps.
Background technology:
In the first-class absorption type heat pump technology, by absorber, through solution pump and solution heat exchanger connection generator, generator, through solution heat exchanger, be communicated with again the first kind absorption-generation systems of absorber, take temperature difference between high temperature driven thermal medium and heated medium as driving force.First kind absorption-generation systems, in conjunction with other parts that comprise condenser and evaporimeter, can form multiple concrete first-class absorption type heat pump structure and flow process, and suitable running parameter and corresponding performance index are correspondingly arranged; Its degree that promotes waste heat supply temperature is higher, and its performance index that has is lower.
From the angle of residual heat resources, the temperature of residual heat resources is always high than environment temperature, and the temperature difference between residual heat resources and environment is naturally occurring driving force, utilizes the unit of this driving force to be second-kind absorption-type heat pump.A little less than although the driving force that this driving force adopts compared with first-class absorption type heat pump seems, but work as cryogenic waste heat resource than horn of plenty, when the abundant residual heat resources that mainly exist with the latent heat form are especially arranged, utilize this driving force to supplement as one of temperature difference driving force between high temperature driven thermal medium and heated medium, be about to two kinds of driving forces and merge use, not only can improve the residual heat resources utilization rate, also can reduce high temperature driven heat in the requirement aspect quantity and grade two simultaneously.
take can use simultaneously between high temperature driven thermal medium and heated medium the temperature difference between temperature difference and residual heat resources and environment as driving force as technological means, to realize that heat pump has the superior performance exponential sum and promotes higher waste heat supply temperature as purpose, find the simple and rational novel absorption-generation systems of structure and flow process, and take this novel absorption-generation systems as basis, increase corresponding other parts, obtain the absorption heat pump based on this novel absorption-generation systems, comparatively enrich low temperature exhaust heat utilizing stock number, especially for take latent heat as main, the utilization of the low temperature exhaust heat that stock number is abundant, significant.
This novel absorption heat pump has comprised the driving force of first-class absorption type heat pump and second-kind absorption-type heat pump, can be referred to as the complex class absorption heat pump; But consider the existence of other composite absorption heat pump unit, for avoiding the misunderstanding of calling and can be popular easy to remember, so, by this and first-class absorption type heat pump and second-kind absorption-type heat pump novel absorption heat pump called after the 3rd class absorption heat pump arranged side by side, will comprise two kinds of driving forces at interior absorption-generation systems called after the 3rd class absorption-generation systems.
Summary of the invention:
Main purpose of the present invention is to provide the 3rd class absorption-generation systems and the 3rd class absorption heat pump---at first the 3rd class absorption-generation systems is proposed, then take the 3rd class absorption-generation systems as basis increases different members, obtain the 3rd class absorption heat pump of a series of different structures and flow process.Concrete summary of the invention is as follows:
1. the 3rd class absorption-generation systems, mainly by the first absorber, the second absorber, generator, the first solution pump, the second solution pump, the solution choke valve, solution heat exchanger and minute steam chest form, the first absorber has the weak solution pipeline to be communicated with a minute steam chest through solution choke valve and the second absorber, divide steam chest to also have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump, the second absorber has the weak solution pipeline to be communicated with generator through the first solution pump and solution heat exchanger, generator also has the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger, the first absorber also has respectively heated medium pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, divide steam chest to also have the refrigerant vapour passage be communicated with or have respectively the refrigerant vapour passage to be communicated with outside with outside connected sum cooling medium pipeline with outside, the second absorber also has the refrigerant vapour passage be communicated with or also have respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside with outside, generator also has respectively the thermal medium of driving pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, form two-way circulation the 3rd class absorption-generation systems.
2. the 3rd class absorption-generation systems, in the 1st described the 3rd class absorption-generation systems, when generator is rectifying column, the second absorber has the weak solution pipeline to be communicated with rectifying column through the first solution pump and solution heat exchanger, rectifying column also has the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger, rectifying column also has respectively the thermal medium of driving pipeline to be communicated with, to have heated medium pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside with outside, forms two-way circulation the 3rd class absorption-generation systems.
3. the 3rd class absorption-generation systems, mainly by the first absorber, the second absorber, generator, the first solution pump, the second solution pump, solution heat exchanger and a minute steam chest form, the first absorber has the weak solution pipeline to be communicated with the second absorber, the second absorber also has the weak solution pipeline to be communicated with generator through the first solution pump and solution heat exchanger, generator also has the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber, divide steam chest to also have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump, the first absorber also has respectively heated medium pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, divide steam chest to also have the refrigerant vapour passage to be communicated with outside, the second absorber also has the refrigerant vapour passage be communicated with or also have respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside with outside, generator also has respectively the thermal medium of driving pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, form single channel circulation the 3rd class absorption-generation systems.
4. the 3rd class absorption-generation systems, in the 3rd described the 3rd class absorption-generation systems, when generator is rectifying column, the second absorber has the weak solution pipeline to be communicated with rectifying column through the first solution pump and solution heat exchanger, rectifying column also has the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber, rectifying column also has respectively the thermal medium of driving pipeline to be communicated with outside, there are heated medium pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, divide steam chest to also have the cooling medium pipeline to be communicated with outside, form single channel circulation the 3rd class absorption-generation systems.
5. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption-generation systems of 1-2 item, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, cryogen liquid pump and choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator and to have the refrigerant vapour passage to be communicated with the first condenser in generator, the first condenser also has the cryogen liquid pipeline to be communicated with the second evaporimeter through choke valve, to divide steam chest to have refrigerant vapour passage and outside the connection to be defined as a minute steam chest and to have the refrigerant vapour passage to be communicated with the second condenser, the second condenser also has the cryogen liquid pipeline to be communicated with the first evaporimeter through the cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with the first absorber the first absorber, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter and to have the refrigerant vapour passage to be communicated with the second absorber the second absorber, the first condenser also has the heated medium pipeline to be communicated with outside, the second condenser also has the cooling medium pipeline to be communicated with outside, the first evaporimeter and the second evaporimeter medium pipeline that also has surplus heat respectively is communicated with outside, formation is based on single-stage single-action the 3rd class absorption heat pump of the 3rd class absorption-generation systems, wherein, during without the second evaporimeter, the first condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter through choke valve, and the first evaporimeter also has the refrigerant vapour passage to be communicated with the second absorber.
6. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption-generation systems of 3-4 item, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the cryogen liquid pump, first throttle valve or add the second choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator and to have the refrigerant vapour passage to be communicated with the first condenser in generator, to divide steam chest to have refrigerant vapour passage and outside the connection to be defined as a minute steam chest and to have the refrigerant vapour passage to be communicated with the second condenser, the second condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter through the cryogen liquid pump and the first condenser has the cryogen liquid pipeline with first evaporimeter connected sum the first evaporimeter, to have the cryogen liquid pipeline to be communicated with the second evaporimeter through the first throttle valve, or second condenser have the cryogen liquid pipeline to be communicated with the second evaporimeter through the cryogen liquid pump and the first condenser has respectively the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve through first throttle valve and the second evaporimeter connected sum, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with the first absorber the first absorber, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter and to have the refrigerant vapour passage to be communicated with the second absorber the second absorber, the first condenser also has the heated medium pipeline to be communicated with outside, the second condenser also has the cooling medium pipeline to be communicated with outside, the first evaporimeter and the second evaporimeter medium pipeline that also has surplus heat respectively is communicated with outside, formation is based on single-stage single-action the 3rd class absorption heat pump of the 3rd class absorption-generation systems, wherein: during 1. without the second evaporimeter and the second choke valve, the first condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve, and the first evaporimeter also has the refrigerant vapour passage to be communicated with the second absorber, 2. the second absorber is communicated with and while having the second evaporimeter with outside without the heated medium pipeline, cancel the second choke valve, the second condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter through the cryogen liquid pump and the first condenser has the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter or the second condenser has the cryogen liquid pipeline with second evaporimeter connected sum the first condenser, to have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve through the cryogen liquid pump through first throttle valve and first evaporimeter connected sum the first evaporimeter.
7. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption-generation systems of 3-4 item, increase the solution choke valve, the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the cryogen liquid pump, first throttle valve and the second choke valve, the first absorber is had the weak solution pipeline to be communicated with the second absorber to be adjusted into the first absorber has the weak solution pipeline to be communicated with the second absorber through the solution choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator and to have the refrigerant vapour passage to be communicated with the first condenser in generator, to divide steam chest to have refrigerant vapour passage and outside the connection to be defined as a minute steam chest and to have the refrigerant vapour passage to be communicated with the second condenser, the second condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter through the cryogen liquid pump and the first condenser has the cryogen liquid pipeline with first evaporimeter connected sum the first evaporimeter, to have the cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve through the first throttle valve, or second condenser have the cryogen liquid pipeline to be communicated with the second evaporimeter through the cryogen liquid pump and the first condenser has the cryogen liquid pipeline with first evaporimeter connected sum the first evaporimeter, to have the cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve through the first throttle valve, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with the first absorber the first absorber, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter and to have the refrigerant vapour passage to be communicated with the second absorber the second absorber, the first condenser also has the heated medium pipeline to be communicated with outside, the second condenser also has the cooling medium pipeline to be communicated with outside, the first evaporimeter and the second evaporimeter medium pipeline that also has surplus heat respectively is communicated with outside, formation is based on single-stage single-action the 3rd class absorption heat pump of the 3rd class absorption-generation systems, wherein: the second absorber is communicated with and while having the second evaporimeter with outside without the heated medium pipeline, and the second condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter through the cryogen liquid pump and the first condenser has the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve or the second condenser has the cryogen liquid pipeline with second evaporimeter connected sum the first condenser, to have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve through the cryogen liquid pump through first throttle valve and first evaporimeter connected sum the first evaporimeter.
8. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption-generation systems of 3-4 item, increase by the 3rd solution pump, the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the cryogen liquid pump, first throttle valve and the second choke valve, the first absorber is had the weak solution pipeline to be communicated with the second absorber to be adjusted into the first absorber has the weak solution pipeline to be communicated with the second absorber through the 3rd solution pump, there are refrigerant vapour passage and outside the connection to be defined as generator and to have the refrigerant vapour passage to be communicated with the first condenser in generator, to divide steam chest to have refrigerant vapour passage and outside the connection to be defined as a minute steam chest and to have the refrigerant vapour passage to be communicated with the second condenser, the second condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter through the cryogen liquid pump, the first condenser has the cryogen liquid pipeline with first evaporimeter connected sum the first evaporimeter, to have the cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve through the first throttle valve, or first condenser have respectively the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve through first throttle valve and the first evaporimeter connected sum, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter and to have the refrigerant vapour passage to be communicated with the first absorber the first absorber, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with the second absorber the second absorber, the first condenser also has the heated medium pipeline to be communicated with outside, the second condenser also has the cooling medium pipeline to be communicated with outside, the first evaporimeter and the second evaporimeter medium pipeline that also has surplus heat respectively is communicated with outside, formation is based on single-stage single-action the 3rd class absorption heat pump of the 3rd class absorption-generation systems, wherein: during 1. without the second evaporimeter and the second choke valve, the first condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve, and the first evaporimeter also has the refrigerant vapour passage to be communicated with the first absorber, 2. the second absorber is communicated with and while having the second evaporimeter with outside without the heated medium pipeline, and the first condenser has the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve or the first condenser has the cryogen liquid pipeline to be communicated with the second evaporimeter through the first throttle valve through first throttle valve and first evaporimeter connected sum the first evaporimeter.
9. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second generator, the second solution heat exchanger and increase again choke valve, the first solution pump is set up the weak solution pipeline and is communicated with the second generator through the second solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
10. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase by the second generator, the second solution heat exchanger and increase again choke valve, the first solution pump is set up the weak solution pipeline and is communicated with the second generator through the second solution heat exchanger, the second generator also has the concentrated solution pipeline, and the concentrated solution pipeline after solution heat exchanger converges with generator after the second solution heat exchanger, through the second absorber, with a minute steam chest, be communicated with again, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
11. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, the first absorber is set up the weak solution pipeline and is communicated with the second generator through resolubilization liquid pump and the second solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger, generator is had and drives the thermal medium pipeline and be defined as the second generator and have the refrigerant vapour passage with generator, to be communicated with generator afterwards to have the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve again again with outside the connection, the second generator drives in addition the thermal medium pipeline and is communicated with outside, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
12. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, the first absorber is set up the weak solution pipeline and is communicated with the second generator through resolubilization liquid pump and the second solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger, generator is had and drives the thermal medium pipeline and be defined as the second generator and have the refrigerant vapour passage with generator, to be communicated with generator afterwards to have the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve again again with outside the connection, the second generator drives in addition the thermal medium pipeline and is communicated with outside, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
13. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, the first absorber is set up the weak solution pipeline and is communicated with the second generator through resolubilization liquid pump and the second solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
14. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, the first absorber is set up the weak solution pipeline and is communicated with the second generator through resolubilization liquid pump and the second solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
15. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second generator, increase again choke valve and the second solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and the weak solution pipeline to be arranged through the first solution pump through the first solution pump and solution heat exchanger the second absorber, solution heat exchanger and the second solution heat exchanger are communicated with generator, generator is had the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted into generator has the concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
16. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase by the second generator, increase again choke valve and the second solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and the weak solution pipeline to be arranged through the first solution pump through the first solution pump and solution heat exchanger the second absorber, solution heat exchanger and the second solution heat exchanger are communicated with generator, generator is had the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber to be adjusted into generator has the concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
17. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 15-16 item, have the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline directly with the second generator connected sum, through the second solution heat exchanger, with generator, to be communicated with respectively after the first solution pump, solution heat exchanger again through the first solution pump, solution heat exchanger and the second solution heat exchanger the second absorber, formation is based on single-stage connection in series-parallel economic benefits and social benefits the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
18. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with the second generator through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, the second generator also has the concentrated solution pipeline to be communicated with generator through resolubilization liquid pump and the second solution heat exchanger, generator is had the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted into generator has the concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger and solution heat exchanger, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
19. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with the second generator through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, the second generator also has the concentrated solution pipeline to be communicated with generator through resolubilization liquid pump and the second solution heat exchanger, generator there is is the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber to be adjusted into generator and the concentrated solution pipeline is arranged through the second solution heat exchanger, solution heat exchanger and the second absorber are communicated with a minute steam chest, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
20. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 18-19 item, there is the weak solution pipeline with the second generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline with the generator connected sum, with the second generator, to be communicated with respectively after the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, form single-stage connection in series-parallel economic benefits and social benefits the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
21. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, the first solution pump is set up the weak solution pipeline and through the second solution heat exchanger, with the second generator connected sum, through the 3rd solution heat exchanger, with the 3rd generator, is communicated with respectively, the second generator also has the concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing the first throttle valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator also had the refrigerant vapour passage to be communicated with the 3rd generator, the 3rd generator had the cryogen liquid pipeline to be communicated with the first condenser through increasing the second choke valve more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on the single-stage of the 3rd class absorption-generation systems triple effect the 3rd class absorption heat pump in parallel.
22. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, the first solution pump is set up the weak solution pipeline and through the second solution heat exchanger, with the second generator connected sum, through the 3rd solution heat exchanger, with the 3rd generator, is communicated with respectively, the second generator has the concentrated solution pipeline with the 3rd generator, the concentrated solution pipeline to be arranged after the second solution heat exchanger, and all the concentrated solution pipeline after solution heat exchanger converges with generator after the 3rd solution heat exchanger, through the second absorber, with a minute steam chest, be communicated with again, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing the first throttle valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator also had the refrigerant vapour passage to be communicated with the 3rd generator, the 3rd generator had the cryogen liquid pipeline to be communicated with the first condenser through increasing the second choke valve more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on the single-stage of the 3rd class absorption-generation systems triple effect the 3rd class absorption heat pump in parallel.
23. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 5-8 item, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber is set up the weak solution pipeline and through the second solution heat exchanger, with the second generator connected sum, through the 3rd solution heat exchanger, with the 3rd generator, is communicated with respectively after the resolubilization liquid pump again again, the second generator also has the concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with the first absorber through the 3rd solution heat exchanger, generator is had and drives the thermal medium pipeline and be defined as the second generator and have the refrigerant vapour passage with generator, to be communicated with generator afterwards to have the cryogen liquid pipeline to be communicated with the first condenser through increasing the first throttle valve again again with outside the connection---the refrigerant vapour of the second generator generation is as the driving thermal medium of generator, the 3rd generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing the second choke valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the 3rd generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with the first condenser, the second generator drives in addition the thermal medium pipeline and is communicated with outside, formation is based on the single-stage of the 3rd class absorption-generation systems triple effect the 3rd class absorption heat pump in parallel.
24. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 5-8 item, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber is set up the weak solution pipeline and through the second solution heat exchanger, with the second generator connected sum, through the 3rd solution heat exchanger, with the 3rd generator, is communicated with respectively after the resolubilization liquid pump again again, the second generator also has the concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with the first absorber through the 3rd solution heat exchanger, generator is had and drives the thermal medium pipeline and be defined as the 3rd generator and have the refrigerant vapour passage with generator, to be communicated with generator afterwards to have the cryogen liquid pipeline to be communicated with the first condenser through increasing the second choke valve again again with outside the connection---the refrigerant vapour of the 3rd generator generation is as the driving thermal medium of generator, after the second generator also had the refrigerant vapour passage to be communicated with the 3rd generator, the 3rd generator had the cryogen liquid pipeline to be communicated with the first condenser through increasing the first throttle valve more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the second generator drives in addition the thermal medium pipeline and is communicated with outside, formation is based on the single-stage of the 3rd class absorption-generation systems triple effect the 3rd class absorption heat pump in parallel.
25. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and the weak solution pipeline to be arranged through the first solution pump through the first solution pump and solution heat exchanger the second absorber, solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger are communicated with generator, generator is had the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted into generator has the concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the 3rd generator through the second solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing the first throttle valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator also had the refrigerant vapour passage to be communicated with the 3rd generator, the 3rd generator had the cryogen liquid pipeline to be communicated with the first condenser through increasing the second choke valve more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage serially connected three-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
26. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and the weak solution pipeline to be arranged through the first solution pump through the first solution pump and solution heat exchanger the second absorber, solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger are communicated with generator, generator is had the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber to be adjusted into generator has the concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the 3rd generator through the second solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing the first throttle valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator also had the refrigerant vapour passage to be communicated with the 3rd generator, the 3rd generator had the cryogen liquid pipeline to be communicated with the first condenser through increasing the second choke valve more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage serially connected three-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
27. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, increase again the first solution pump, increase again the second solution pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with the 3rd generator through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, the 3rd generator also has the concentrated solution pipeline to be communicated with the second generator through increasing the first solution pump and the second solution heat exchanger again, the second generator also has the concentrated solution pipeline through increasing the second solution pump and the 3rd solution heat exchanger is communicated with generator again, generator there is is the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted into generator and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger, the second solution heat exchanger and solution heat exchanger are communicated with the second absorber, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing the first throttle valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator also had the refrigerant vapour passage to be communicated with the 3rd generator, the 3rd generator had the cryogen liquid pipeline to be communicated with the first condenser through increasing the second choke valve more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage serially connected three-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
28. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, increase again the first solution pump, increase again the second solution pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with the 3rd generator through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, the 3rd generator also has the concentrated solution pipeline to be communicated with the second generator through increasing the first solution pump and the second solution heat exchanger again, the second generator also has the concentrated solution pipeline through increasing the second solution pump and the 3rd solution heat exchanger is communicated with generator again, generator there is is the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber to be adjusted into generator and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger, the second solution heat exchanger, solution heat exchanger and the second absorber are communicated with a minute steam chest and are communicated with, the second generator has the cryogen liquid pipeline to be communicated with the first condenser through increasing the first throttle valve more again after generator has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with the second generator---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator also had the refrigerant vapour passage to be communicated with the 3rd generator, the 3rd generator had the cryogen liquid pipeline to be communicated with the first condenser through increasing the second choke valve more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with the first condenser, formation is based on single-stage serially connected three-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
29. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase absorption-evaporimeter, the second cryogen liquid pump and the second solution heat exchanger, to divide steam chest to have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump to be adjusted into a minute steam chest has the concentrated solution pipeline to be communicated with the first absorber through the second solution pump and the second solution heat exchanger, the first absorber is had the weak solution pipeline to be communicated with a minute steam chest through solution choke valve and the second absorber to be adjusted into the first absorber has the weak solution pipeline to be communicated with absorption-evaporimeter through the second solution heat exchanger, absorption-evaporimeter also has the weak solution pipeline to be communicated with a minute steam chest through solution choke valve and the second absorber, the first evaporimeter is had the refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, the first evaporimeter is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with the first absorber through the second cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
30. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, cancel the solution choke valve, increase absorption-evaporimeter, the resolubilization liquid pump, the second cryogen liquid pump and the second solution heat exchanger, to divide steam chest to have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump to be adjusted into a minute steam chest has the concentrated solution pipeline to be communicated with absorption-evaporimeter through the second solution pump, absorption-evaporimeter also has the weak solution pipeline to be communicated with the first absorber through resolubilization liquid pump and the second solution heat exchanger, the first absorber is had the weak solution pipeline to be communicated with a minute steam chest through solution choke valve and the second absorber to be adjusted into the first absorber has the weak solution pipeline to be communicated with dividing a steam chest through the second solution heat exchanger and the second absorber, the first evaporimeter is had the refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, the first evaporimeter is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with the first absorber through the second cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
31. the 3rd class absorption heat pump, in the 6th described arbitrary the 3rd class absorption heat pump, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter and the second solution heat exchanger, to divide steam chest to have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump to be adjusted into a minute steam chest has the concentrated solution pipeline to be communicated with the first absorber through the second solution pump and the second solution heat exchanger, the first absorber is had the weak solution pipeline to be communicated with the second absorber to be adjusted into the first absorber has the weak solution pipeline to be communicated with absorption-evaporimeter through the second solution heat exchanger, absorption-evaporimeter also has the weak solution pipeline to be communicated with the second absorber, the first evaporimeter is had the refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline absorption-evaporimeter after increasing choke valve again and absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with the first absorber again, or first evaporimeter set up the cryogen liquid pipeline and with absorption-evaporimeter after absorption-evaporimeter is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber through the second cryogen liquid pump, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
32. the 3rd class absorption heat pump, in the 6th described arbitrary the 3rd class absorption heat pump, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter, resolubilization liquid pump and the second solution heat exchanger, to divide steam chest to have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump to be adjusted into a minute steam chest has the concentrated solution pipeline to be communicated with absorption-evaporimeter through the second solution pump, absorption-evaporimeter also has the weak solution pipeline to be communicated with the first absorber through resolubilization liquid pump and the second solution heat exchanger, the first absorber is had the weak solution pipeline to be communicated with the second absorber to be adjusted into the first absorber has the weak solution pipeline to be communicated with the second absorber through the second solution heat exchanger, the first evaporimeter is had the refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline absorption-evaporimeter after increasing choke valve again and absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with the first absorber again, or first evaporimeter set up the cryogen liquid pipeline and with absorption-evaporimeter after absorption-evaporimeter is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber through the second cryogen liquid pump, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
33. the 3rd class absorption heat pump, in the 7th described arbitrary the 3rd class absorption heat pump, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter and the second solution heat exchanger, to divide steam chest to have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump to be adjusted into a minute steam chest has the concentrated solution pipeline to be communicated with the first absorber through the second solution pump and the second solution heat exchanger, the first absorber is had the weak solution pipeline to be communicated with the second absorber through the solution choke valve to be adjusted into the first absorber has the weak solution pipeline to be communicated with absorption-evaporimeter through the second solution heat exchanger, absorption-evaporimeter also has the weak solution pipeline to be communicated with the second absorber through the solution choke valve, the first evaporimeter is had the refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline absorption-evaporimeter after increasing choke valve again and absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with the first absorber again, or first evaporimeter set up the cryogen liquid pipeline and with absorption-evaporimeter after absorption-evaporimeter is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber through the second cryogen liquid pump, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
34. the 3rd class absorption heat pump, in the 7th described arbitrary the 3rd class absorption heat pump, cancel the solution choke valve, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter, resolubilization liquid pump and the second solution heat exchanger, to divide steam chest to have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump to be adjusted into a minute steam chest has the concentrated solution pipeline to be communicated with absorption-evaporimeter through the second solution pump, absorption-evaporimeter also has the weak solution pipeline to be communicated with the first absorber through resolubilization liquid pump and the second solution heat exchanger, the first absorber is had the weak solution pipeline to be communicated with the second absorber through the solution choke valve to be adjusted into the first absorber has the weak solution pipeline to be communicated with the second absorber through the second solution heat exchanger, the first evaporimeter is had the refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline absorption-evaporimeter after increasing choke valve again and absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with the first absorber again, or first evaporimeter set up the cryogen liquid pipeline and with absorption-evaporimeter after absorption-evaporimeter is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber through the second cryogen liquid pump, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
35. the 3rd class absorption heat pump, in the 8th described arbitrary the 3rd class absorption heat pump, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter and the second solution heat exchanger, to divide steam chest to have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump to be adjusted into a minute steam chest has the concentrated solution pipeline to be communicated with the first absorber through the second solution pump and the second solution heat exchanger, the first absorber is had the weak solution pipeline to be communicated with the second absorber through the 3rd solution pump to be adjusted into the first absorber has the weak solution pipeline to be communicated with absorption-evaporimeter through the second solution heat exchanger, absorption-evaporimeter also has the weak solution pipeline to be communicated with the second absorber through the 3rd solution pump, the first evaporimeter is had the refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline absorption-evaporimeter after increasing choke valve again and absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with the first absorber again, or first evaporimeter set up the cryogen liquid pipeline and with absorption-evaporimeter after absorption-evaporimeter is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber through the second cryogen liquid pump, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
36. the 3rd class absorption heat pump, in the 8th described arbitrary the 3rd class absorption heat pump, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter and the second solution heat exchanger, to divide steam chest to have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump to be adjusted into a minute steam chest has the concentrated solution pipeline to be communicated with absorption-evaporimeter through the second solution pump, the first absorber is had the weak solution pipeline to be communicated with the second absorber through the 3rd solution pump to be adjusted into the first absorber has the weak solution pipeline to be communicated with the second absorber through the second solution heat exchanger, absorption-evaporimeter also has the weak solution pipeline to be communicated with the first absorber through the 3rd solution pump and the second solution heat exchanger, the first evaporimeter is had the refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline absorption-evaporimeter after increasing choke valve again and absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with the first absorber again, or first evaporimeter set up the cryogen liquid pipeline and with absorption-evaporimeter after absorption-evaporimeter is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber through the second cryogen liquid pump, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
37. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase and increase again choke valve or the second cryogen liquid pump, the 3rd absorber and the second solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and the weak solution pipeline to be arranged through the first solution pump through the first solution pump and solution heat exchanger the second absorber, solution heat exchanger and the second solution heat exchanger are communicated with generator, generator is had the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted into generator has the concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger, the 3rd absorber also has the weak solution pipeline to be communicated with the second absorber through solution heat exchanger, there are heated medium pipeline and outside the connection to be adjusted into the first condenser and to have cryogen liquid pipeline first absorber after increasing again choke valve and the first absorber is communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber the first absorber, or be adjusted into the second evaporimeter and have the cryogen liquid pipeline with the first absorber after the first absorber is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump, the 3rd absorber also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber, wherein, when the second evaporimeter, the first condenser has the cryogen liquid pipeline through increasing choke valve and the first absorber after the first absorber is communicated with again and have the refrigerant vapour passage to be communicated with the 3rd absorber again or the first evaporimeter having the cryogen liquid pipeline with the first absorber after the first absorber is communicated with, to have the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump again.
38. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase and increase again choke valve or the second cryogen liquid pump, the 3rd absorber, resolubilization liquid pump and the second solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with the 3rd absorber through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, the 3rd absorber also has the weak solution pipeline to be communicated with generator through resolubilization liquid pump and the second solution heat exchanger, generator is had the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted into generator has the concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger and solution heat exchanger, there are heated medium pipeline and outside the connection to be adjusted into the first condenser and to have cryogen liquid pipeline first absorber after increasing again choke valve and the first absorber is communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber the first absorber, or be adjusted into the second evaporimeter and have the cryogen liquid pipeline with the first absorber after the first absorber is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump, the 3rd absorber also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber, wherein, when the second evaporimeter, the first condenser has the cryogen liquid pipeline through increasing choke valve and the first absorber after the first absorber is communicated with again and have the refrigerant vapour passage to be communicated with the 3rd absorber again or the first evaporimeter having the cryogen liquid pipeline with the first absorber after the first absorber is communicated with, to have the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump again.
39. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase and increase again choke valve or the second cryogen liquid pump, the 3rd absorber and the second solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and the weak solution pipeline to be arranged through the first solution pump through the first solution pump and solution heat exchanger the second absorber, solution heat exchanger and the second solution heat exchanger are communicated with generator, generator is had the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber to be adjusted into generator has the concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger, the 3rd absorber also has the weak solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber, there are heated medium pipeline and outside the connection to be adjusted into the first condenser and to have cryogen liquid pipeline first absorber after increasing again choke valve and the first absorber is communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber the first absorber, or be adjusted into the first evaporimeter and have the cryogen liquid pipeline with the first absorber after the first absorber is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump, the 3rd absorber also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber.
40. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase and increase again choke valve or the second cryogen liquid pump, the 3rd absorber, resolubilization liquid pump and the second solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with the 3rd absorber through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, the 3rd absorber also has the weak solution pipeline to be communicated with generator through resolubilization liquid pump and the second solution heat exchanger, generator there is is the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber to be adjusted into generator and the concentrated solution pipeline is arranged through the second solution heat exchanger, solution heat exchanger and the second absorber are communicated with a minute steam chest, there are heated medium pipeline and outside the connection to be adjusted into the first condenser and to have cryogen liquid pipeline first absorber after increasing again choke valve and the first absorber is communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber the first absorber, or be adjusted into the first evaporimeter and have the cryogen liquid pipeline with the first absorber after the first absorber is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump, the 3rd absorber also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber.
41. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second cryogen liquid pump, the 3rd cryogen liquid pump, the 3rd condenser, the 3rd evaporimeter, the 3rd absorber, the 4th absorber, the second solution heat exchanger, the second solution choke valve, resolubilization liquid pump and second minute steam chest, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with second minute steam chest through the second solution choke valve and the 4th absorber through the first solution pump and solution heat exchanger the second absorber, steam chest also had the concentrated solution pipeline to be communicated with the 3rd absorber through resolubilization liquid pump and solution heat exchanger in second minute, the 3rd absorber also has the weak solution pipeline to be communicated with the second absorber through solution heat exchanger, generator is had the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted into generator has the concentrated solution pipeline to be communicated with the 4th absorber through the second solution heat exchanger, the 4th absorber also has the weak solution pipeline to be communicated with generator through the first solution pump and the second solution heat exchanger, the first condenser is had the cryogen liquid pipeline to be communicated with the second evaporimeter through choke valve to be adjusted into the first condenser has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter through choke valve, the 3rd evaporimeter also has the refrigerant vapour passage to be communicated with the 4th absorber, steam chest also had the refrigerant vapour passage to be communicated with the 3rd condenser in second minute, the 3rd condenser also has the cryogen liquid pipeline to be communicated with the second evaporimeter through the 3rd cryogen liquid pump, there are heated medium pipeline and outside the connection to be adjusted into the second evaporimeter and to have the cryogen liquid pipeline with the first absorber after the first absorber is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump the first absorber, the 3rd absorber also has the heated medium pipeline to be communicated with outside, the 3rd condenser also has the cooling medium pipeline to be communicated with outside, the 3rd evaporimeter medium pipeline that also has surplus heat is communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber, wherein, during without the second evaporimeter and the 3rd evaporimeter, the first condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter through choke valve, the 3rd condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter through the 3rd cryogen liquid pump, the first evaporimeter has the cryogen liquid pipeline with the first absorber after the first absorber is communicated with, to have the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump again, and the first evaporimeter also has the refrigerant vapour passage with the second absorber and the 4th absorber, to be communicated with respectively.
42. the 3rd class absorption heat pump, in the 7th described arbitrary the 3rd class absorption heat pump, increase by the second cryogen liquid pump or increase again choke valve, the 3rd cryogen liquid pump, the 3rd condenser, the 3rd evaporimeter, the 3rd absorber, the 4th absorber, the second solution heat exchanger, the second solution choke valve, resolubilization liquid pump and second minute steam chest, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with the 4th absorber through the second solution choke valve through the first solution pump and solution heat exchanger the second absorber, the 4th absorber also has the weak solution pipeline to be communicated with generator through the first solution pump and the second solution heat exchanger, generator is had the concentrated solution pipeline to be communicated with first minute steam chest through solution heat exchanger and the second absorber to be adjusted into generator has the concentrated solution pipeline to be communicated with second minute steam chest through the second solution heat exchanger and the 4th absorber, steam chest also had the concentrated solution pipeline to be communicated with the 3rd absorber through resolubilization liquid pump and solution heat exchanger in second minute, the 3rd absorber also has the weak solution pipeline to be communicated with first minute steam chest through solution heat exchanger and the second absorber, steam chest also had the refrigerant vapour passage to be communicated with the 3rd condenser in second minute, the 3rd condenser also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, the 3rd evaporimeter also has the refrigerant vapour passage to be communicated with the 4th absorber, there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter and to have the cryogen liquid pipeline with the first absorber after the first absorber is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump the first absorber, or be adjusted into the first condenser and have cryogen liquid pipeline first absorber after increasing again choke valve the first absorber and being communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has the heated medium pipeline to be communicated with outside, the 3rd condenser also has the cooling medium pipeline to be communicated with outside, the 3rd evaporimeter medium pipeline that also has surplus heat is communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber.
43. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 5-8 item, increase by the second generator, the 3rd absorber, resolubilization liquid pump and the second solution heat exchanger, generator is had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator has the refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has the weak solution pipeline to be communicated with the second generator through resolubilization liquid pump and the second solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchange, the second generator also has respectively refrigerant vapour passage and the first condenser connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by generator.
44. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and the weak solution pipeline to be arranged through the first solution pump through the first solution pump and solution heat exchanger the second absorber, solution heat exchanger and the second solution heat exchanger are communicated with the second generator, the second generator also has the concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger, the 3rd absorber also has the weak solution pipeline to be communicated with generator through resolubilization liquid pump and the 3rd solution heat exchanger, generator is had the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted into generator has the concentrated solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger and solution heat exchanger, generator is had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator has the refrigerant vapour passage to be communicated with the 3rd absorber, the second generator also has respectively refrigerant vapour passage and the first condenser connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by generator.
45. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and the weak solution pipeline to be arranged through the first solution pump through the first solution pump and solution heat exchanger the second absorber, solution heat exchanger and the second solution heat exchanger are communicated with the second generator, the second generator also has the concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger, the 3rd absorber also has the weak solution pipeline to be communicated with generator through resolubilization liquid pump and the 3rd solution heat exchanger, generator there is is the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber to be adjusted into generator and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger, solution heat exchanger and the second absorber are communicated with a minute steam chest, generator is had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator has the refrigerant vapour passage to be communicated with the 3rd absorber, the second generator also has respectively refrigerant vapour passage and the first condenser connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by generator.
46. the 3rd class absorption heat pump, in the 43rd described arbitrary the 3rd class absorption heat pump, increase by the 3rd condenser and increase again choke valve, the second generator is had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator has the refrigerant vapour passage to be communicated with the 3rd condenser, generator is set up the refrigerant vapour passage and is communicated with the first condenser, the 3rd condenser also has the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve again, the 3rd condenser also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, by generator, to the first condenser and the 3rd absorber, provide respectively double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
47. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 44-45 item, increase by the 3rd condenser and increase again choke valve, the second generator is had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator has the refrigerant vapour passage to be communicated with the 3rd condenser, generator is set up the refrigerant vapour passage and is communicated with the first condenser, the 3rd condenser also has the cryogen liquid pipeline to be communicated with the first condenser through increasing choke valve again, the 3rd condenser also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, by generator, to the first condenser and the 3rd absorber, provide respectively double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
48. the 3rd class absorption heat pump, in the 5th described arbitrary the 3rd class absorption heat pump, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber is had the weak solution pipeline to be communicated with a minute steam chest through solution choke valve and the second absorber to be adjusted into the first absorber has the weak solution pipeline to be communicated with dividing a steam chest through the 3rd solution heat exchanger and the second absorber, to divide steam chest to have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump to be adjusted into a minute steam chest has the concentrated solution pipeline to be communicated with the first absorber through the second solution pump and the 3rd solution heat exchanger, the first evaporimeter is had the refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has the weak solution pipeline to be communicated with the second generator through resolubilization liquid pump and the second solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger, the second generator also has respectively refrigerant vapour passage and the first absorber connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by the second generator.
49. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 6-8 item, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber is had to the weak solution pipeline directly or be communicated with the second absorber through the solution choke valve or through the resolubilization liquid pump and all be adjusted into the first absorber and have the weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger, to divide steam chest to have the concentrated solution pipeline to be communicated with the first absorber through the second solution pump to be adjusted into a minute steam chest has the concentrated solution pipeline to be communicated with the first absorber through the second solution pump and the 3rd solution heat exchanger, the first evaporimeter is had the refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has the weak solution pipeline to be communicated with the second generator through resolubilization liquid pump and the second solution heat exchanger, the second generator also has the concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger, the second generator also has respectively refrigerant vapour passage and the first absorber connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by the second generator.
50. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 48-49 item, increase by the 3rd condenser and increase again choke valve, the second generator is set up the refrigerant vapour passage and is communicated with the 3rd condenser, the 3rd condenser also has the cryogen liquid pipeline to be communicated with the first evaporimeter through increasing choke valve again, the 3rd condenser also has the heated medium pipeline to be communicated with outside, and formation is based on the 3rd class absorption-generation systems, provide respectively double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour by the second generator to the 3rd condenser and the first absorber.
51. the 3rd class absorption heat pump, in the 48th described arbitrary the 3rd class absorption heat pump, increase by the second cryogen liquid pump, have heated medium pipeline and outside the connection to be adjusted into the first evaporimeter and to set up the cryogen liquid pipeline and with the 3rd absorber after the 3rd absorber is communicated with, have the refrigerant vapour passage to be communicated with the first absorber through the second cryogen liquid pump again the 3rd absorber, formation is based on the 3rd class absorption-generation systems, jointly provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour by the 3rd absorber and the second generator to the first absorber.
52. the 3rd class absorption heat pump, in the 49th described arbitrary the 3rd class absorption heat pump, increase by the second cryogen liquid pump or increase again choke valve, there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter and to set up the cryogen liquid pipeline and with the 3rd absorber after the 3rd absorber is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber through the second cryogen liquid pump the 3rd absorber, or be adjusted into the first condenser and set up cryogen liquid pipeline the 3rd absorber after increasing again choke valve and the 3rd absorber is communicated with and have again the refrigerant vapour passage to be communicated with the first absorber, formation is based on the 3rd class absorption-generation systems, by the 3rd absorber and the second generator, jointly to the first absorber, provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
53. the 3rd class absorption heat pump, described at the 43rd, the second absorber is without in heated medium pipeline and outside arbitrary the 3rd class absorption heat pump that is communicated with, increase by the second cryogen liquid pump or increase again choke valve, there are heated medium pipeline and outside the connection to be adjusted into the second evaporimeter and to set up the cryogen liquid pipeline and with the first absorber after the first absorber is communicated with, have again the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump the first absorber, or be adjusted into the first condenser and set up cryogen liquid pipeline first absorber after increasing again choke valve and the first absorber is communicated with and have again the refrigerant vapour passage to be communicated with the 3rd absorber, formation is based on the 3rd class absorption-generation systems, by the first absorber and generator, jointly to the 3rd absorber, provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour, wherein, when the second evaporimeter, having the heated medium pipeline to be communicated with outside to be adjusted into the first evaporimeter to set up the cryogen liquid pipeline the first absorber has the refrigerant vapour passage to be communicated with the 3rd absorber again or is adjusted into the first condenser through the second cryogen liquid pump and the first absorber after the first absorber is communicated with and set up cryogen liquid pipeline first absorber after increasing choke valve again and the first absorber is communicated with and have the refrigerant vapour passage to be communicated with the 3rd absorber again.
54. the 3rd class absorption heat pump, described at the 44-45 item, the second absorber is without in heated medium pipeline and outside arbitrary the 3rd class absorption heat pump that is communicated with, increase by the second cryogen liquid pump or increase again choke valve, there are heated medium pipeline and outside the connection to be adjusted into the second evaporimeter and to set up the cryogen liquid pipeline and with the first absorber after the first absorber is communicated with, have again the refrigerant vapour passage to be communicated with the 3rd absorber through the second cryogen liquid pump the first absorber, or be adjusted into the first condenser and set up cryogen liquid pipeline first absorber after increasing again choke valve and the first absorber is communicated with and have again the refrigerant vapour passage to be communicated with the 3rd absorber, formation is based on the 3rd class absorption-generation systems, by the first absorber and generator, jointly to the 3rd absorber, provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour, wherein, when the second evaporimeter, having the heated medium pipeline to be communicated with outside to be adjusted into the first evaporimeter to set up the cryogen liquid pipeline the first absorber has the refrigerant vapour passage to be communicated with the 3rd absorber again or is adjusted into the first condenser through the second cryogen liquid pump and the first absorber after the first absorber is communicated with and set up cryogen liquid pipeline first absorber after increasing choke valve again and the first absorber is communicated with and have the refrigerant vapour passage to be communicated with the 3rd absorber again.
55. the 3rd class absorption heat pump, the 5th, 11, 29-30, 48, 51 and based on the 24th of two-way circulation the 3rd class absorption-generation systems, in 50 described arbitrary the 3rd class absorption heat pumps, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with generator, there is the concentrated solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted into generator to have the concentrated solution pipeline to be communicated with the second absorber through newly-increased the second solution heat exchanger and solution heat exchanger in generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
56. the 3rd class absorption heat pump, at 6-8, 12, 31-36, 49, 52 and based on the 24th of single channel circulation the 3rd class absorption-generation systems, in 50 described arbitrary the 3rd class absorption heat pumps, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with generator, generator there is is the concentrated solution pipeline to be communicated with a minute steam chest through solution heat exchanger and the second absorber to be adjusted into generator and the concentrated solution pipeline is arranged through increasing the second solution heat exchanger newly, solution heat exchanger and the second absorber are communicated with a minute steam chest, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
57. the 3rd class absorption heat pump, in the 9th described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and the second solution heat exchanger through the first solution pump and the second solution heat exchanger the second absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the second generator, there is the concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into the second generator to have the concentrated solution pipeline to be communicated with the second absorber through newly-increased the second solution heat exchanger and the second solution heat exchanger in the second generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
58. the 3rd class absorption heat pump, in the 10th described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and the second solution heat exchanger through the first solution pump and the second solution heat exchanger the second absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the second generator, the second generator there is is the concentrated solution pipeline to be communicated with a minute steam chest through the second solution heat exchanger and the second absorber to be adjusted into the second generator and the concentrated solution pipeline is arranged through increasing the second solution heat exchanger newly, the second solution heat exchanger and the second absorber are communicated with a minute steam chest, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
59. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 13-14 item, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator, to be communicated with and to be adjusted into the first absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through resolubilization liquid pump and the second solution heat exchanger through resolubilization liquid pump and the second solution heat exchanger the first absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the second generator, there is the concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger to be adjusted into the second generator to have the concentrated solution pipeline to be communicated with the first absorber through newly-increased the second solution heat exchanger and the second solution heat exchanger in the second generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
60. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 15-17 item, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, the second absorber is had to the weak solution pipeline through the first solution pump, solution heat exchanger and the second solution heat exchanger are communicated with generator and are adjusted into the second absorber and the weak solution pipeline are arranged through the first solution pump, solution heat exchanger and the second solution heat exchanger are communicated with newly-increased absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with generator, there is the concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger to be adjusted into generator the concentrated solution pipeline to be arranged through newly-increased the second solution heat exchanger in generator, the second solution heat exchanger is communicated with the second generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
61. the 3rd class absorption heat pump, in the 18th and the 20th described arbitrary the 3rd class absorption heat pump based on two-way circulation the 3rd class absorption-generation systems, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the second generator, there is the concentrated solution pipeline with the second absorber, to be communicated with and to be adjusted into generator and the concentrated solution pipeline to be arranged through the second solution heat exchanger through the second solution heat exchanger and solution heat exchanger in generator, newly-increased the second solution heat exchanger and solution heat exchanger are communicated with the second absorber, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
62. the 3rd class absorption heat pump, be the 19th and the 20th described arbitrary the 3rd class absorption heat pump based on single channel circulation the 3rd class absorption-generation systems in, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the second generator, generator is had to the concentrated solution pipeline through the second solution heat exchanger, solution heat exchanger and the second absorber are communicated with a minute steam chest and are adjusted into generator and the concentrated solution pipeline are arranged through the second solution heat exchanger, newly-increased the second solution heat exchanger, solution heat exchanger and the second absorber are communicated with a minute steam chest, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
63. the 3rd class absorption heat pump, in the 21st described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the 3rd generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and the 3rd solution heat exchanger through the first solution pump and the 3rd solution heat exchanger the second absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the 3rd generator, there is the concentrated solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger to be adjusted into the 3rd generator to have the concentrated solution pipeline to be communicated with the second absorber through newly-increased the second solution heat exchanger and the 3rd solution heat exchanger in the 3rd generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
64. the 3rd class absorption heat pump, in the 22nd described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the 3rd generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and the 3rd solution heat exchanger through the first solution pump and the 3rd solution heat exchanger the second absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the 3rd generator, the 3rd generator there is is the concentrated solution pipeline to be communicated with a minute steam chest through the 3rd solution heat exchanger and the second absorber to be adjusted into the 3rd generator and the concentrated solution pipeline is arranged through increasing the second solution heat exchanger newly, the 3rd solution heat exchanger and the second absorber are communicated with a minute steam chest, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
65. the 3rd class absorption heat pump, in the 23rd described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the 3rd generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through resolubilization liquid pump and the 3rd solution heat exchanger through resolubilization liquid pump and the 3rd solution heat exchanger the first absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the 3rd generator, there is the concentrated solution pipeline to be communicated with the first absorber through the 3rd solution heat exchanger to be adjusted into the 3rd generator to have the concentrated solution pipeline to be communicated with the first absorber through newly-increased the second solution heat exchanger and the 3rd solution heat exchanger in the 3rd generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
66. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 25-26 item, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, the second absorber is had to the weak solution pipeline through the first solution pump, solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger are communicated with generator and are adjusted into the second absorber and the weak solution pipeline are arranged through the first solution pump, solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger are communicated with newly-increased absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with generator, there is the concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger to be adjusted into generator to have the concentrated solution pipeline to be communicated with the second generator through newly-increased the second solution heat exchanger and the 3rd solution heat exchanger in generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
67. the 3rd class absorption heat pump, in the 27th described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the 3rd generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the 3rd generator, generator is had to the concentrated solution pipeline through the 3rd solution heat exchanger, the second solution heat exchanger and solution heat exchanger are communicated with the second absorber and are adjusted into the 3rd generator and the concentrated solution pipeline are arranged through the 3rd solution heat exchanger, the second solution heat exchanger, newly-increased the second solution heat exchanger and solution heat exchanger are communicated with the second absorber, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
68. the 3rd class absorption heat pump, in the 28th described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the 3rd generator, to be communicated with and to be adjusted into the second absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and solution heat exchanger through the first solution pump and solution heat exchanger the second absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the 3rd generator, generator is had to the concentrated solution pipeline through the 3rd solution heat exchanger, the second solution heat exchanger, solution heat exchanger and the second absorber are communicated with a minute steam chest and are adjusted into the 3rd generator and the concentrated solution pipeline are arranged through the 3rd solution heat exchanger, the second solution heat exchanger, newly-increased the second solution heat exchanger, solution heat exchanger and the second absorber are communicated with a minute steam chest, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
69. the 3rd class absorption heat pump, the 37th, in 39 described arbitrary the 3rd class absorption heat pumps, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, the second absorber is had to the weak solution pipeline through the first solution pump, solution heat exchanger and the second solution heat exchanger are communicated with generator and are adjusted into the second absorber and the weak solution pipeline are arranged through the first solution pump, solution heat exchanger and the second solution heat exchanger are communicated with newly-increased absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with generator, there is the concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger to be adjusted into generator to have the concentrated solution pipeline to be communicated with the 3rd absorber through newly-increased the second solution heat exchanger and the second solution heat exchanger in generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
70. the 3rd class absorption heat pump, in the 38th described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the 3rd absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through resolubilization liquid pump and the second solution heat exchanger through resolubilization liquid pump and the second solution heat exchanger the 3rd absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with generator, there is the concentrated solution pipeline with the second absorber, to be communicated with and to be adjusted into generator and the concentrated solution pipeline to be arranged through newly-increased the second solution heat exchanger through the second solution heat exchanger and solution heat exchanger in generator, the second solution heat exchanger and solution heat exchanger are communicated with the second absorber, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
71. the 3rd class absorption heat pump, in the 40th described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the 3rd absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through resolubilization liquid pump and the second solution heat exchanger through resolubilization liquid pump and the second solution heat exchanger the 3rd absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with generator, generator is had to the concentrated solution pipeline through the second solution heat exchanger, solution heat exchanger and the second absorber are communicated with a minute steam chest and are adjusted into generator and the concentrated solution pipeline are arranged through increasing the second solution heat exchanger newly, the second solution heat exchanger, solution heat exchanger and the second absorber are communicated with a minute steam chest, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
72. the 3rd class absorption heat pump, in the 41st described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the 4th absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and the second solution heat exchanger through the first solution pump and the second solution heat exchanger the 4th absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with generator, there is the concentrated solution pipeline to be communicated with the 4th absorber through the second solution heat exchanger to be adjusted into generator to have the concentrated solution pipeline to be communicated with the 4th absorber through newly-increased the second solution heat exchanger and the second solution heat exchanger in generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
73. the 3rd class absorption heat pump, in the 42nd described arbitrary the 3rd class absorption heat pump, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator, to be communicated with and to be adjusted into the 4th absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and the second solution heat exchanger through the first solution pump and the second solution heat exchanger the 4th absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with generator, generator there is is the concentrated solution pipeline to be communicated with second minute steam chest through the second solution heat exchanger and the 4th absorber to be adjusted into generator and the concentrated solution pipeline is arranged through newly-increased the second solution heat exchanger, the second solution heat exchanger and the 4th absorber are communicated with second minute steam chest, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
74. the 3rd class absorption heat pump, the 43rd, 46, in 53 described arbitrary the 3rd class absorption heat pumps, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator, to be communicated with and to be adjusted into the 3rd absorber and to have the weak solution pipeline to be communicated with newly-increased absorber through resolubilization liquid pump and the second solution heat exchanger through resolubilization liquid pump and the second solution heat exchanger the 3rd absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the second generator, there is the concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger to be adjusted into the second generator to have the concentrated solution pipeline to be communicated with the 3rd absorber through newly-increased the second solution heat exchanger and the second solution heat exchanger in the second generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
75. the 3rd class absorption heat pump, at 44-45, 47, in 54 described arbitrary the 3rd class absorption heat pumps, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, the second absorber is had to the weak solution pipeline through the first solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second generator and are adjusted into the second absorber and the weak solution pipeline are arranged through the first solution pump, solution heat exchanger and the second solution heat exchanger are communicated with newly-increased absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the second generator, there is the concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger to be adjusted into the second generator to have the concentrated solution pipeline to be communicated with the 3rd absorber through newly-increased the second solution heat exchanger and the second solution heat exchanger in the second generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
76. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 9-28 item, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, low pressure generator is set up the concentrated solution pipeline and is communicated with newly-increased absorber through newly-increased the second solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with low pressure generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
77. the 3rd class absorption heat pump, at 5-8, 29-42, in described arbitrary the 3rd class absorption heat pump of 48-52 item, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, generator is set up the concentrated solution pipeline and is communicated with newly-increased absorber through newly-increased the second solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
78. the 3rd class absorption heat pump, at 43-47, in described arbitrary the 3rd class absorption heat pump of 53-54 item, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, the second generator is set up the concentrated solution pipeline and is communicated with newly-increased absorber through newly-increased the second solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased the first solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through newly-increased solution pump, newly-increased the first solution heat exchanger and newly-increased the second solution heat exchanger are communicated with the second generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber as additional high-temperature heat supply end.
79. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 9-28 item, increase high temperature condenser and high temperature choke valve, high pressure generator is set up the refrigerant vapour passage and is communicated with the high temperature condenser, the high temperature condenser also has the cryogen liquid pipeline to be communicated with the first condenser through the high temperature choke valve, the high temperature condenser also has the heated medium pipeline to be communicated with outside, forms take three class absorption heat pump of high temperature condenser as additional high-temperature heat supply end.
80. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 21-28 item, increase high temperature condenser and high temperature choke valve, middle pressure generator is set up the refrigerant vapour passage and is communicated with the high temperature condenser, the high temperature condenser also has the cryogen liquid pipeline to be communicated with the first condenser through the high temperature choke valve, the high temperature condenser also has the heated medium pipeline to be communicated with outside, forms take three class absorption heat pump of high temperature condenser as additional high-temperature heat supply end.
81. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 79-80 item, increase first flow control valve and second adjustable valve, having respectively heated medium pipeline and outside the connection to be adjusted into outside and the heated medium pipeline to be arranged and be divided into two-way after the first condenser is communicated with the first condenser and high temperature condenser---the first via has the heated medium pipeline to be communicated with outside through the first flow choke valve with high temperature condenser after the high temperature condenser is communicated with again, second tunnel the second flow throttle valve is communicated with outside, formation is take adjustable type three class absorption heat pump of high temperature condenser as additional high-temperature heat supply end.
82. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 9-20 item, increase secondary absorber, second-stage generator, secondary solution pump and secondary solution heat exchanger, there is the cryogen liquid pipeline with the first condenser, to be communicated with and to be adjusted into low pressure generator and to have the cryogen liquid pipeline to be communicated with the second evaporimeter through increasing again choke valve through increasing again choke valve low pressure generator, low pressure generator is had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into low pressure generator has the refrigerant vapour passage to be communicated with secondary absorber, secondary absorber also has the weak solution pipeline to be communicated with second-stage generator through secondary solution pump and secondary solution heat exchanger, second-stage generator also has the concentrated solution pipeline to be communicated with secondary absorber through the secondary solution heat exchanger, second-stage generator also has the refrigerant vapour passage to be communicated with the first condenser, secondary absorber also has the heated medium pipeline to be communicated with outside, second-stage generator drives in addition the thermal medium pipeline and is communicated with outside, formation is take the single-stage economic benefits and social benefits as the first order, two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to secondary absorber by low pressure generator, wherein, while only having the first evaporimeter, low pressure generator has the cryogen liquid pipeline to be communicated with the first evaporimeter through increasing choke valve again.
83. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 9-20 item, increase secondary absorber, second-stage generator, the secondary solution pump, the secondary solution heat exchanger, secondary condenser and two-step throttle valve, low pressure generator is set up refrigerant vapour and is communicated with secondary absorber, secondary absorber also has the weak solution pipeline to be communicated with second-stage generator through secondary solution pump and secondary solution heat exchanger, second-stage generator also has the concentrated solution pipeline to be communicated with secondary absorber through the secondary solution heat exchanger, second-stage generator also has the refrigerant vapour passage to be communicated with secondary condenser, secondary condenser also has the cryogen liquid pipeline to be communicated with the first condenser through the two-step throttle valve, secondary absorber and secondary condenser also have respectively the heated medium pipeline to be communicated with outside, second-stage generator drives in addition the thermal medium pipeline and is communicated with outside, formation is take the single-stage economic benefits and social benefits as the first order, by low pressure generator, to the first condenser and secondary absorber, provide respectively two-stage the 3rd class absorption heat pump of refrigerant vapour.
84. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 21-28 item, increase secondary absorber, second-stage generator, secondary solution pump and secondary solution heat exchanger, there is the cryogen liquid pipeline with the first condenser, to be communicated with and to be adjusted into middle pressure generator and to have the cryogen liquid pipeline to be communicated with the second evaporimeter through increasing again the first throttle valve through increasing again the first throttle valve in middle pressure generator, there is the cryogen liquid pipeline with the first condenser, to be communicated with and to be adjusted into low pressure generator and to have the cryogen liquid pipeline to be communicated with the second evaporimeter through increasing again the second choke valve through increasing again the second choke valve low pressure generator, low pressure generator is had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into low pressure generator has the refrigerant vapour passage to be communicated with secondary absorber, secondary absorber also has the weak solution pipeline to be communicated with second-stage generator through secondary solution pump and secondary solution heat exchanger, second-stage generator also has the concentrated solution pipeline to be communicated with secondary absorber through the secondary solution heat exchanger, second-stage generator also has the refrigerant vapour passage to be communicated with the first condenser, secondary absorber also has the heated medium pipeline to be communicated with outside, second-stage generator drives in addition the thermal medium pipeline and is communicated with outside, formation is take the single-stage triple effect as the first order, two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to secondary absorber by low pressure generator, wherein, while only having the first evaporimeter, middle pressure generator has the cryogen liquid pipeline to be communicated with the first evaporimeter through increasing choke valve again, and low pressure generator has the cryogen liquid pipeline to be communicated with the first evaporimeter through increasing the second choke valve again.
85. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of 21-28 item, increase secondary absorber, second-stage generator, the secondary solution pump, the secondary solution heat exchanger, secondary condenser and two-step throttle valve, low pressure generator is set up refrigerant vapour and is communicated with secondary absorber, secondary absorber also has the weak solution pipeline to be communicated with second-stage generator through secondary solution pump and secondary solution heat exchanger, second-stage generator also has the concentrated solution pipeline to be communicated with secondary absorber through the secondary solution heat exchanger, second-stage generator also has the refrigerant vapour passage to be communicated with secondary condenser, secondary condenser also has the cryogen liquid pipeline to be communicated with the first condenser through the two-step throttle valve, secondary absorber and secondary condenser also have respectively the heated medium pipeline to be communicated with outside, second-stage generator drives in addition the thermal medium pipeline and is communicated with outside, formation is take the single-stage triple effect as the first order, by low pressure generator, to the first condenser and secondary absorber, provide respectively two-stage the 3rd class absorption heat pump of refrigerant vapour.
The accompanying drawing explanation:
Fig. 1 is according to two-way circulation the 3rd class absorption-generation systems provided by the present invention the 1st kind of structure and schematic flow sheet.
Fig. 2 is according to two-way circulation the 3rd class absorption-generation systems provided by the present invention the 2nd kind of structure and schematic flow sheet.
Fig. 3 is according to single channel circulation the 3rd class absorption-generation systems provided by the present invention the 1st kind of structure and schematic flow sheet.
Fig. 4 is according to single channel circulation the 3rd class absorption-generation systems provided by the present invention the 2nd kind of structure and schematic flow sheet.
Fig. 5 be according to provided by the present invention, based on the 1st single-stage single-action the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Fig. 6 be according to provided by the present invention, based on the 2nd single-stage single-action the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Fig. 7 be according to provided by the present invention, based on the 1st single-stage single-action the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Fig. 8 be according to provided by the present invention, based on the 2nd single-stage single-action the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Fig. 9 be according to provided by the present invention, based on the 3rd single-stage single-action the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 10 be according to provided by the present invention, based on the 1st single-stage parallel double-effect the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Figure 11 be according to provided by the present invention, based on the 1st single-stage parallel double-effect the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 12 be according to provided by the present invention, based on the 2nd single-stage parallel double-effect the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Figure 13 be according to provided by the present invention, based on the 2nd single-stage parallel double-effect the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 14 be according to provided by the present invention, based on the 1st single-stage of two-way circulation the 3rd class absorptions-generation systems economic benefits and social benefits the 3rd class absorption heat pump system architecture and the schematic flow sheet of connecting.
Figure 15 be according to provided by the present invention, based on the 1st single-stage connection in series-parallel economic benefits and social benefits the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 16 be according to provided by the present invention, based on the 2nd single-stage of two-way circulation the 3rd class absorptions-generation systems economic benefits and social benefits the 3rd class absorption heat pump system architecture and the schematic flow sheet of connecting.
Figure 17 be according to provided by the present invention, based on the 2nd single-stage connection in series-parallel economic benefits and social benefits the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 18 be according to provided by the present invention, based on the 1st single-stage parallel connection triple effect the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorptions-generation systems.
Figure 19 be according to provided by the present invention, based on the 1st single-stage parallel connection triple effect the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorptions-generation systems.
Figure 20 be according to provided by the present invention, based on the 2nd single-stage parallel connection triple effect the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorptions-generation systems.
Figure 21 be according to provided by the present invention, based on the 2nd single-stage parallel connection triple effect the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorptions-generation systems.
Figure 22 be according to provided by the present invention, based on the 1st single-stage serially connected three-effect the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Figure 23 be according to provided by the present invention, based on the 1st single-stage serially connected three-effect the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 24 be according to provided by the present invention, based on the 2nd single-stage serially connected three-effect the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Figure 25 be according to provided by the present invention, based on the 2nd single-stage serially connected three-effect the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 26 be according to provided by the present invention, based on the 1st one generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Figure 27 be according to provided by the present invention, based on the 2nd one generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Figure 28 be according to provided by the present invention, based on the 1st one generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 29 be according to provided by the present invention, based on the 2nd one generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 30 be according to provided by the present invention, based on the 3rd one generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Figure 31 be according to provided by the present invention, based on the 4th one generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Figure 32 be according to provided by the present invention, based on the 3rd one generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 33 be according to provided by the present invention, based on the 4th one generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 34 be according to provided by the present invention, based on the 5th one generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of two-way circulation the 3rd class absorption-generation systems.
Figure 35 be according to provided by the present invention, based on the 5th one generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of single channel circulation the 3rd class absorption-generation systems.
Figure 36 be according to provided by the present invention, based on two-way circulation the 3rd class absorption-generation systems and have the 1st double-generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of three heat supply ends.
Figure 37 be according to provided by the present invention, based on two-way circulation the 3rd class absorption-generation systems and have the 2nd double-generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of three heat supply ends.
Figure 38 be according to provided by the present invention, based on single channel circulation the 3rd class absorption-generation systems and have the 1st double-generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of four heat supply ends.
Figure 39 be according to provided by the present invention, based on two-way circulation the 3rd class absorption-generation systems and have the 1st double-generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of four heat supply ends.
Figure 40 be according to provided by the present invention, based on two-way circulation the 3rd class absorption-generation systems and have the 3rd double-generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of three heat supply ends.
Figure 41 be according to provided by the present invention, based on single channel circulation the 3rd class absorption-generation systems and have the 2nd double-generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of four heat supply ends.
Figure 42 be according to provided by the present invention, based on two-way circulation the 3rd class absorption-generation systems and have the 1st double-generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of two heat supply ends.
Figure 43 be according to provided by the present invention, based on single channel circulation the 3rd class absorption-generation systems and have the 1st double-generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of two heat supply ends.
Figure 44 be according to provided by the present invention, based on two-way circulation the 3rd class absorption-generation systems and have the 2nd double-generator two-stage the 3rd class absorption heat pump system architecture and schematic flow sheet of two heat supply ends.
Here it is pointed out that in double-generator two-stage the 3rd class absorption heat pump shown in Figure 37-44, the second absorber 2 generally is not used in external heat supply; Therefore, no matter whether the second absorber 2 provides thermic load to heated medium, within it is not included in Figure 37-44 said " three heat supply ends " and " two heat supply ends ".
Figure 45 is according to provided by the present invention, economic benefits and social benefits the 3rd class absorption heat pump system architecture and the schematic flow sheet of connecting based on single channel circulation the 3rd class absorption-generation systems and take newly-increased absorber as the single-stage of adding high-temperature heat supply end.
Figure 46 be according to provided by the present invention, based on two-way circulation the 3rd class absorptions-generation systems and take newly-increased absorber as adding single-stage single-action the 3rd class absorption heat pump system architecture and the schematic flow sheet of high-temperature heat supply end.
Figure 47 be according to provided by the present invention, based on two-way circulation the 3rd class absorptions-generation systems and take the high temperature condenser as adding single-stage parallel double-effect the 3rd class absorption heat pump system architecture and the schematic flow sheet of high-temperature heat supply end.
Figure 48 be according to provided by the present invention, based on two-way circulation the 3rd class absorptions-generation systems and take the high temperature condenser as adding adjustable type single-stage parallel double-effect the 3rd class absorption heat pump system architecture and the schematic flow sheet of high-temperature heat supply end.
Figure 49 be according to provided by the present invention, based on two-way circulation the 3rd class absorptions-generation systems and take single-stage two-stage three class absorption heat pump system architecture and the schematic flow sheet of economic benefits and social benefits as the first order of connecting.
Figure 50 be according to provided by the present invention, based on single channel circulation the 3rd class absorption-generation systems the 3rd class absorption heat pump system architecture and the schematic flow sheet of the two-stage take the single-stage parallel double-effect as the first order.
In figure, 1-the first absorber, 2-the second absorber, 3-generator (rectifying column), 4-the first solution pump, 5-the second solution pump, 6-solution choke valve/first solution choke valve, 7-solution heat exchanger, 8-divide steam chest/first minute steam chest, 9-the 3rd solution pump.
in figure, A-the first condenser, B-the second condenser, C-evaporimeter/first evaporimeter, D-the second evaporimeter, E-choke valve/first throttle valve, F-cryogen liquid pump/first cryogen liquid pump, G-the second choke valve, H-the second generator, I-the second solution heat exchanger, J-increases choke valve/increase again first throttle valve again, K-resolubilization liquid pump/increase again the first solution pump, L-the 3rd generator, M-the 3rd solution heat exchanger, N-increases the second choke valve again, O-increases the second solution pump again, P-the second cryogen liquid pump, Q-absorption-evaporimeter, R-the 3rd absorber, S-the 3rd cryogen liquid pump, T-the 4th absorber, second minute steam chest of U-, V-the second solution choke valve, W-the 3rd condenser, X-the 3rd evaporimeter.
In figure, a1-increases absorption-evaporimeter newly, and b1-increases absorber newly, and c1-increases solution pump newly, and d1-increases the first solution heat exchanger newly, and e1-increases the second solution heat exchanger newly, and f1-increases choke valve newly, and g1-increases the cryogen liquid pump newly; A2-high temperature condenser, b2-high temperature choke valve, c2-first flow control valve, d2-second adjustable valve; The a3-secondary absorber, b3-second-stage generator, c3-secondary solution pump, d3-secondary solution heat exchanger, e3-secondary condenser, f3-two-step throttle valve.
It should be noted that:
(1) two-way circulation, refer to that in the 3rd class absorption-generation systems flow process, two-way solution carries out independent loops separately.
(2) single channel circulation, refer to that in the 3rd class absorption-generation systems flow process, single channel solution circulates successively between each parts.
(3) in Fig. 1-2, the weak solution of the first absorber 1 is flowed through the second absorber 2 heat absorptions again and is realized the part vaporization after solution choke valve 6 reducing pressure by regulating flows; In Fig. 3-4, the concentrated solution of generator (rectifying column) 3 is flowed through the second absorber 2 heat absorptions again and is realized the part vaporization after solution heat exchanger 7 step-downs.
(4) solution heat exchanger is not only realized the heat exchange between different solutions, also can play the effect of solution choke valve reducing pressure by regulating flow, and namely from the angle of balance pressure reduction, the effect of solution heat exchanger and solution choke valve is identical; When solution heat exchanger or solution choke valve were not set, between parts, the balance of pressure reduction also can rely on pipe resistance to realize.
(5) when employing is working media such as ammonia spirit, minute vapour of minute steam chest needs distillation process, increases the cooling medium pipeline this moment and is communicated with outside.
(6), in single channel shown in Fig. 3-4 circulation the 3rd class absorption-generation systems, in theory, between the first absorber 1 and the second absorber 2, be connected with following concrete mode:
1. when the pressure of the second absorber 2, the 3rd solution pump 9 can be set or utilize gravity pressure reduction to overcome the flow of solution resistance during higher than the pressure of the first absorber 1.
2. when the pressure of the first absorber 1, adopt solution choke valve 6 or carry out balance pressure reduction by pipeline self resistance during higher than the pressure of the second absorber 2.
While 3. adopting single evaporimeter, the 3rd solution pump 9 and solution choke valve 6 all do not arrange; Can consider to rely on gravity pressure reduction to overcome the flow of solution resistance.
(7) in single-stage economic benefits and social benefits the 3rd class absorption heat pump, generator 3 and the second generator H all can be used as high pressure generator or low pressure generator, and they are high pressure generator or low pressure generator for the corresponding title of the effect according to them in heat pump; In like manner, in single-stage triple effect the 3rd class absorption heat pump, generator 3, the second generator H and the 3rd generator L all can be used as high pressure generator, middle pressure generator or low pressure generator, corresponding high pressure generator, middle pressure generator or the low pressure generator of being referred to as of the effect according to them in heat pump.
(8) " parallel connection " in " single-stage parallel double-effect the 3rd class absorption heat pump " refers to when the 3rd class absorption heat pump high temperature driven heat realizes double-effect process that solution circulation is in parallel; " single-stage triple effect in parallel " is also like this.
(9) " series connection " in " single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump " refers to that when the 3rd class absorption heat pump high temperature driven heat realized double-effect process, solution circulation was series connection; " single-stage serially connected three-effect " is also like this.
(10) such as " single-stage " in terms such as " single-stage economic benefits and social benefits ", be to have quoted the address in the first-class absorption type heat pump, " economic benefits and social benefits " are also to call from the angle that high temperature driven thermal medium first-class absorption type heat pump is had an effect.
(11) in Figure 49-50 such as " secondary " in parts such as " second-stage generators ", be for the first order heat pump structure that promotes waste heat supply temperature and flow process.
(12) about term " refrigerant vapour provides device ".For writing conveniently, take newly-increased absorber for the 3rd class absorption heat pump that adds high-temperature heat supply end in, be defined as follows parts and provide device for refrigerant vapour:
1. in single-stage single-action, single-stage economic benefits and social benefits and single-stage triple effect the 3rd class absorption heat pump, based on the second evaporimeter in the 3rd class absorption heat pump of two-way circulation the 3rd class absorption-generation systems, based on the low pressure evaporator in the 3rd class absorption heat pump of single channel circulation the 3rd class absorption-generation systems, while only having the first evaporimeter, the first evaporimeter provides device for refrigerant vapour.
2. in one generator two-stage the 3rd class absorption heat pump, to the first absorber, the absorption-evaporimeter of refrigerant vapour is provided or the first absorber of refrigerant vapour is provided to the 3rd absorber.
3. in double-generator two-stage the 3rd class absorption heat pump, to the 3rd absorber, provide the generator of refrigerant vapour.
4. in double-generator two-stage the 3rd class absorption heat pump, to the first absorber, provide the second generator of refrigerant vapour.
5. in double-generator two-stage the 3rd class absorption heat pump, jointly to the first absorber, provide the 3rd absorber and second generator (combination) of refrigerant vapour.
6. in double-generator two-stage the 3rd class absorption heat pump, jointly to the 3rd absorber, provide the first absorber and the generator (combination) of refrigerant vapour.
(13) about term " cryogen liquid provides device ".For writing conveniently, take newly-increased absorber for the 3rd class absorption heat pump that adds high-temperature heat supply end in, be defined as follows parts and provide device for cryogen liquid:
1. in the 3rd class absorption heat pump based on two-way circulation the 3rd class absorptions-generation systems, the second evaporimeter during two evaporimeters of existence and the first evaporimeter a when evaporimeter is only arranged.
2. in the 3rd class absorption heat pump based on single channel circulation the 3rd class absorptions-generation systems, the first evaporimeter or the second evaporimeter during two evaporimeters of existence, the first evaporimeter a when evaporimeter is only arranged.
The specific embodiment:
At first be noted that in the statement of structure and flow process, in inessential situation, do not repeat statement.Below in conjunction with accompanying drawing and example, describe the present invention in detail.
Two-way circulation the 3rd class absorption-generation systems shown in Figure 1 is achieved in that
1. on structure, it is mainly by the first absorber, the second absorber, generator, the first solution pump, the second solution pump, the solution choke valve, solution heat exchanger and minute steam chest form, the first absorber 1 has the weak solution pipeline to be communicated with a minute steam chest 8 through solution choke valve 6 and the second absorber 2, divide steam chest 8 to also have the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution pump 5, the second absorber 2 has the weak solution pipeline to be communicated with generator 3 through the first solution pump 4 and solution heat exchanger 7, generator 3 also has the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7, the first absorber 1 also has respectively heated medium pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, divide steam chest 8 to also have the refrigerant vapour passage to be communicated with outside, the second absorber 2 also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, generator 3 also has respectively the thermal medium of driving pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside.
2. on flow process, from warm refrigerant vapour in a road of outside (cryogen liquid absorbs remaining thermogenetic steam or afterheat steam), enter the first absorber 1, by the concentrated solution from minute steam chest 8, absorbed also heat release in heated medium, the second absorber 2, heat absorption the part vaporization of flowing through of flowing through after solution choke valve 6 reducing pressure by regulating flows of the weak solution of the first absorber 1, solution after vaporization enters minute steam chest 8 to carry out that vapour, liquid separate and externally discharges low temperature (low pressure) refrigerant vapour and solution concentration is improved, and the concentrated solution of minute steam chest 8 enters the first absorber 1 through the second solution pump 5; Another Lu Zhongwen refrigerant vapour enters the second absorber 2, by the concentrated solution from generator 3, absorbed and respectively heat release in another road solution of heated medium and second absorber 2 of flowing through, the weak solution of the second absorber 2 enters generator 3 through the first solution pump 4 and solution heat exchanger 7, the solution that the heating of driving thermal medium enters generator 3 externally discharges the high temperature refrigerant vapour, and the concentrated solution of generator 3 enters the second absorber 2 after solution heat exchanger 7 heat releases step-down.
Two-way circulation the 3rd class absorption-generation systems shown in Figure 2, with shown in Figure 1 comparing, change shown in Figure 3 has: 1. the second absorber 2 is communicated with outside without the heated medium pipeline, and the solution that enters the second absorber 2 absorbs refrigerant vapour and also heats another road solution of second absorber 2 of flowing through; 2. divide steam chest 8 to also have the cooling medium pipeline to be communicated with outside.
In the 3rd class absorption-generation systems shown in Figure 2, the effect of the second absorber 2 is: 1. heat its another the interior road solution of flowing through and achieve the part vaporization under low pressure, the weak solution concentration of such the second absorber 2 can be lower than the weak solution concentration of the first absorber 1, thereby the solution that makes to enter generator 3 can discharge the refrigerant vapour of higher temperature; 2. in conjunction with a minute steam chest 8, make to enter again the first absorber 1 after the solution raising concentration from the second absorber 2, this is conducive to improve the solution concentration that works in the first absorber 1, thereby thereby the refrigerant vapour or the afterheat steam that make the first absorber 1 can absorb lower temperature provide the thermic load of higher temperature to heated medium.Visible, utilize this 3rd class absorption-generation systems can improve the amplitude that waste heat supply temperature promotes, this raising does not propose extra demand to the high temperature driven thermal medium, but relies on the temperature difference between waste heat medium and cold environment to complete, thereby can improve the residual heat resources utilization rate.
Single channel circulation the 3rd class absorption-generation systems shown in Figure 3 is achieved in that
1. on structure, it is mainly by the first absorber, the second absorber, generator, the first solution pump, the second solution pump, solution heat exchanger and a minute steam chest form, the first absorber 1 has the weak solution pipeline to be communicated with the second absorber 2, the second absorber 2 also has the weak solution pipeline to be communicated with generator 3 through the first solution pump 4 and solution heat exchanger 7, generator 3 also has the concentrated solution pipeline to be communicated with a minute steam chest 8 through solution heat exchanger 7 and the second absorber 2, divide steam chest 8 to also have the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution pump 5, the first absorber 1 also has respectively heated medium pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, divide steam chest 8 to also have the refrigerant vapour passage to be communicated with outside, the second absorber 2 also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, generator 3 also has respectively the thermal medium of driving pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside.
2. on flow process, from warm refrigerant vapour in a road of outside (cryogen liquid absorbs remaining thermogenetic steam or afterheat steam), enter the first absorber 1, by the concentrated solution from minute steam chest 8, absorbed also heat release in heated medium, the weak solution of the first absorber 1 enters the second absorber 2, absorption from another Lu Zhongwen refrigerant vapour of outside and respectively heat release in heated medium and heat release in another road solution of second absorber 2 of flowing through, the weak solution of the second absorber 2 enters generator 3 through the first solution pump 4 and solution heat exchanger 7, driving the external high temperature refrigerant vapour that discharges under the thermal medium heating, the concentrated solution of generator 3 second absorber 2 of flowing through again after solution heat exchanger 7 heat releases step-down, heat absorption part vaporization, solution after vaporization enters minute steam chest 8 and carries out vapour, liquid separates and externally discharges low temperature (low pressure) refrigerant vapour and solution concentration is improved, divide the concentrated solution of steam chest 8 to enter the first absorber 1 through the second solution pump 5.
Single channel circulation the 3rd class absorption-generation systems shown in Figure 4, with shown in Figure 2 comparing, change shown in Figure 4 has: rectifying column has replaced generator, and minute steam chest 8 also has the cooling medium pipeline to be communicated with outside, and is required to meet distillation process.At this moment, can adopt such as ammoniacal liquor is that the solution of representative is as the working media that flows between the first absorber 1, the second absorber 2 and minute steam chest 8.
In the 3rd class absorption-generation systems shown in Figure 4, present two aspects of the acting body of the second absorber 2: 1. make solution from the first absorber 1 in the interior absorption of the second absorber 2 after warm refrigerant vapour concentration further reduce, thereby the weak solution that makes to enter generator 3 can discharge the refrigerant vapour of higher temperature; 2. after in conjunction with minute steam chest 8, making concentrated solution from generator 3 further improve concentration, enter the first absorber 1, be conducive to improve the solution concentration that works in the first absorber 1, thereby the refrigerant vapour or the afterheat steam that make the first absorber 1 can absorb lower temperature provide the higher temperature thermic load to heated medium.Visible, the 3rd class absorption-generation systems can improve the amplitude that waste heat supply temperature promotes, and to driving thermal medium, does not propose extra demand.
The driving force of carrying out from flow process, Fig. 1-the 3rd class absorption-generation systems shown in Figure 4 has not only utilized the temperature difference between high temperature driven thermal medium and heated medium, also having utilized simultaneously the temperature difference between waste heat (middle temperature refrigerant vapour) and cold environment (cryogenic coolant steam), is the 3rd class absorption-generation systems therefore name this absorption-generation systems.
Single-stage single-action based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 5 is achieved in that
1. on structure, in the 3rd class absorption-generation systems shown in Figure 1, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, cryogen liquid pump and choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator 3 and to have the refrigerant vapour passage to be communicated with the first condenser A in generator 3, the first condenser A also has the cryogen liquid pipeline to be communicated with the second evaporimeter D through choke valve E, to divide steam chest 8 to have refrigerant vapour passage and outside the connection to be defined as minute steam chest 8 and to have the refrigerant vapour passage to be communicated with the second condenser B, the second condenser B also has the cryogen liquid pipeline to be communicated with the first evaporimeter C through cryogen liquid pump F, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter C and to have the refrigerant vapour passage to be communicated with the first absorber 1 the first absorber 1, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter D and to have the refrigerant vapour passage to be communicated with the second absorber 2 the second absorber 2, the first condenser A also has the heated medium pipeline to be communicated with outside, the second condenser B also has the cooling medium pipeline to be communicated with outside, the first evaporimeter C and the second evaporimeter D medium pipeline that also has surplus heat respectively is communicated with outside.
2. on flow process, the refrigerant vapour that generator 3 produces enters the first condenser A, heat release and after heated medium, becomes cryogen liquid, and the cryogen liquid of the first condenser A enters the second evaporimeter D after choke valve E reducing pressure by regulating flow, the absorption waste heat becomes refrigerant vapour and provides to the second absorber 2; The refrigerant vapour that divides steam chest 8 to produce enters the second condenser B, heat release and after cooling medium, becomes cryogen liquid, the cryogen liquid of the second condenser B enters the first evaporimeter C after cryogen liquid pump F boosts, the absorption waste heat becomes refrigerant vapour and provides to the first absorber 1, forms single-stage single-action the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
In addition, second absorber 2 is suitable certain help can to the thermal performance that improves unit while bearing external heating demand; From angle corresponding to the external heating demand with the first condenser A, the first absorber 1 and the second absorber 2 can be regarded a heat supply end as.
Single-stage single-action based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 6 is achieved in that
1. on structure, in the 3rd class absorption-generation systems shown in Figure 1, increase by the first condenser, the second condenser, evaporimeter, choke valve and cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as generator 3 and to have the refrigerant vapour passage to be communicated with the first condenser A in generator 3, the first condenser A also has the cryogen liquid pipeline to be communicated with through choke valve E evaporimeter C, to divide steam chest 8 to have refrigerant vapour passage and outside the connection to be defined as minute steam chest 8 and to have the refrigerant vapour passage to be communicated with the second condenser B, the second condenser B also has the cryogen liquid pipeline to be communicated with evaporimeter C through cryogen liquid pump F, there are refrigerant vapour passage and outside the connection to be defined as evaporimeter C and to have the refrigerant vapour passage to be communicated with the first absorber 1 the first absorber 1, there are refrigerant vapour passage and outside the connection to be defined as evaporimeter C and to have the refrigerant vapour passage to be communicated with the second absorber 2 the second absorber 2, the first condenser A also has the heated medium pipeline to be communicated with outside, the second condenser B also has the cooling medium pipeline to be communicated with outside, the evaporimeter C medium pipeline that also has surplus heat is communicated with outside.
2. on flow process, the refrigerant vapour that generator 3 produces enters the first condenser A, heat release and after heated medium, becomes cryogen liquid, and the cryogen liquid of the first condenser A enters evaporimeter C after choke valve E reducing pressure by regulating flow; The refrigerant vapour that divides steam chest 8 to produce enters the second condenser B, heat release and after cooling medium, becomes cryogen liquid, and the cryogen liquid of the second condenser B enters evaporimeter C after cryogen liquid pump F boosts; The cryogen liquid that enters evaporimeter C absorbs waste heat and becomes refrigerant vapour and to the first absorber 1 and the second absorber 2, provide respectively, forms single-stage single-action the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage single-action based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 7 is achieved in that
1. on structure, in the 3rd class absorption-generation systems shown in Figure 2, increase by the 3rd solution pump, the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the cryogen liquid pump, first throttle valve and the second choke valve, the first absorber 1 is had the weak solution pipeline to be communicated with the second absorber 2 to be adjusted into the first absorber 1 has the weak solution pipeline to be communicated with the second absorber 2 through the 3rd solution pump 9, there are refrigerant vapour passage and outside the connection to be defined as generator 3 and to have the refrigerant vapour passage to be communicated with the first condenser A in generator 3, the first condenser A also has the cryogen liquid pipeline to be communicated with the first evaporimeter C through first throttle valve E, the first evaporimeter C has the cryogen liquid pipeline to be communicated with the second evaporimeter D through the second choke valve G again, to divide steam chest 8 to have refrigerant vapour passage and outside the connection to be defined as minute steam chest 8 and to have the refrigerant vapour passage to be communicated with the second condenser B, the second condenser B also has the cryogen liquid pipeline to be communicated with the first evaporimeter C through cryogen liquid pump F, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter D and to have the refrigerant vapour passage to be communicated with the first absorber 1 the first absorber 1, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter C and to have the refrigerant vapour passage to be communicated with the second absorber 2 the second absorber 2, the first condenser A also has the heated medium pipeline to be communicated with outside, the second condenser B also has the cooling medium pipeline to be communicated with outside, the first evaporimeter C and the second evaporimeter D medium pipeline that also has surplus heat respectively is communicated with outside.
2. on flow process, the refrigerant vapour that generator 3 produces enters the first condenser A, heat release and after heated medium, becomes cryogen liquid, and the cryogen liquid of the first condenser A enters the first evaporimeter C after first throttle valve E reducing pressure by regulating flow; The refrigerant vapour that divides steam chest 8 to produce enters the second condenser B, heat release and after cooling medium, becomes cryogen liquid, and the cryogen liquid of the second condenser B enters the first evaporimeter C after cryogen liquid pump F boosts; The cryogen liquid of the first evaporimeter C is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to the second absorber 2, second tunnel the second choke valve G throttling enters the second evaporimeter D, the absorption waste heat becomes refrigerant vapour and provides to the first absorber 1, forms single-stage single-action the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage single-action based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 8 is achieved in that
1. on structure, in the 3rd class absorption-generation systems shown in Figure 2, increase the solution choke valve, the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the cryogen liquid pump, first throttle valve and the second choke valve, the first absorber 1 is had the weak solution pipeline to be communicated with the second absorber 2 to be adjusted into the first absorber 1 has the weak solution pipeline to be communicated with the second absorber 2 through solution choke valve 6, there are refrigerant vapour passage and outside the connection to be defined as generator 3 and to have the refrigerant vapour passage to be communicated with the first condenser A in generator 3, the first condenser A has the cryogen liquid pipeline to be communicated with the first evaporimeter C through first throttle valve E, the first evaporimeter C also has the cryogen liquid pipeline to be communicated with the second evaporimeter D through the second choke valve G, to divide steam chest 8 to have refrigerant vapour passage and outside the connection to be defined as minute steam chest 8 and to have the refrigerant vapour passage to be communicated with the second condenser B, the second condenser B also has the cryogen liquid pipeline to be communicated with the first evaporimeter C through cryogen liquid pump F, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter C and to have the refrigerant vapour passage to be communicated with the first absorber 1 the first absorber 1, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter D and to have the refrigerant vapour passage to be communicated with the second absorber 2 the second absorber 2, the first condenser A also has the heated medium pipeline to be communicated with outside, the second condenser B also has the cooling medium pipeline to be communicated with outside, the first evaporimeter C and the second evaporimeter D medium pipeline that also has surplus heat respectively is communicated with outside.
Here it is to be noted, the cryogen liquid pipeline connects also can other two kinds of selection schemes: 1. the second condenser B being had the cryogen liquid pipeline to be communicated with the first evaporimeter C through cryogen liquid pump F to be adjusted into the second condenser B has the cryogen liquid pipeline to be communicated with the second evaporimeter D through cryogen liquid pump F; 2. the second condenser B being had the cryogen liquid pipeline to be communicated with the first evaporimeter C through cryogen liquid pump F to be adjusted into the second condenser B has the cryogen liquid pipeline to be communicated with the second evaporimeter D through cryogen liquid pump F, then the first evaporimeter C is had the cryogen liquid pipeline to be communicated with the second evaporimeter D through the second choke valve G to be adjusted into the first condenser A has the cryogen liquid pipeline to be communicated with the second evaporimeter D through the second choke valve G.
2. on flow process, the refrigerant vapour that generator 3 produces enters the first condenser A, heat release and after heated medium, becomes cryogen liquid, and this cryogen liquid enters the first evaporimeter C after first throttle valve E reducing pressure by regulating flow; The refrigerant vapour that divides steam chest 8 to produce enters the second condenser B, heat release and after cooling medium, becomes cryogen liquid, and the cryogen liquid of the second condenser B enters the first evaporimeter C after cryogen liquid pump F boosts; The cryogen liquid of the first evaporimeter C is divided into two parts---and a part absorbs waste heat and becomes refrigerant vapour and provide to the first absorber 1, another part enters the second evaporimeter D, absorbs waste heat and become refrigerant vapour and provide to the second absorber 2 through the second choke valve G throttling, forms single-stage single-action the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage single-action based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 9 is achieved in that
1. on structure, in the 3rd class absorption-generation systems shown in Figure 4, increase the solution choke valve, the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, choke valve and cryogen liquid pump, the first absorber 1 is had the weak solution pipeline to be communicated with the second absorber 2 to be adjusted into the first absorber 1 has the weak solution pipeline to be communicated with the second absorber 2 through solution choke valve 6, there are refrigerant vapour passage and outside the connection to be defined as rectifying column 3 and to have the refrigerant vapour passage to be communicated with the first condenser A on rectifying column 3, the first condenser A has the cryogen liquid pipeline to be communicated with the first evaporimeter C through choke valve E, to divide steam chest 8 to have refrigerant vapour passage and outside the connection to be defined as minute steam chest 8 and to have the refrigerant vapour passage to be communicated with the second condenser B, the second condenser B also has the cryogen liquid pipeline to be communicated with the second evaporimeter D through cryogen liquid pump F, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter C and to have the refrigerant vapour passage to be communicated with the first absorber 1 the first absorber 1, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter D and to have the refrigerant vapour passage to be communicated with the second absorber 2 the second absorber 2, the first condenser A also has the heated medium pipeline to be communicated with outside, the second condenser B also has the cooling medium pipeline to be communicated with outside, the first evaporimeter C and the second evaporimeter D medium pipeline that also has surplus heat respectively is communicated with outside.
2. on flow process, the refrigerant vapour that rectifying column 3 produces enters the first condenser A, heat release and after heated medium, becomes cryogen liquid, and this cryogen liquid enters the first evaporimeter C after choke valve E reducing pressure by regulating flow, the absorption waste heat becomes refrigerant vapour and provides to the first absorber 1; The refrigerant vapour that divides steam chest 8 to produce enters the second condenser B, heat release and after cooling medium, becomes cryogen liquid, the cryogen liquid of the second condenser B enters the second evaporimeter D after cryogen liquid pump F boosts, the absorption waste heat becomes refrigerant vapour and provides to the second absorber 2, forms single-stage single-action the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage parallel double-effect based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 10 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, increase by the second generator, the second solution heat exchanger and increase again choke valve, the first solution pump 4 is set up the weak solution pipeline and is communicated with the second generator H through the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline to be communicated with the second absorber 2 through the second solution heat exchanger I, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing choke valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator H also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the part weak solution of the second absorber 2 enters the second generator H through the first solution pump 4 and the second solution heat exchanger I, the refrigerant vapour that generator 3 the produces second generator H that flows through, the weak solution that heating enters the second generator H discharges refrigerant vapour and provides to the first condenser A, the refrigerant vapour heat release that enters the first condenser A becomes cryogen liquid after heated medium, the concentrated solution of the second generator H enters the second absorber 2 through the second solution heat exchanger I, flow through after the refrigerant vapour heat release of the second generator H forms cryogen liquid and through increasing again choke valve J throttling, enter the first condenser A again, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
Single-stage parallel double-effect based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 11 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, increase by the second generator, the second solution heat exchanger and increase again choke valve, the first solution pump 4 is set up the weak solution pipeline and is communicated with the second generator H through the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline, and the concentrated solution pipeline after solution heat exchanger 7 converges with generator 3 after the second solution heat exchanger I, through the second absorber 2, with a minute steam chest 8, be communicated with again, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing choke valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator H also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the part weak solution of the second absorber 2 enters the second generator H through the first solution pump 4 and the second solution heat exchanger I, the refrigerant vapour that generator 3 the produces second generator H that flows through, the weak solution that heating enters the second generator H discharges refrigerant vapour and provides to the first condenser A, the refrigerant vapour heat release that enters the first condenser A becomes cryogen liquid after heated medium, concentrated solution pipeline after solution heat exchanger 7 converges the concentrated solution of the second generator H with generator 3 after the second solution heat exchanger I, after the second absorber 2 heat absorbing part vaporizations, enter minute steam chest 8 again, flow through after the refrigerant vapour heat release of the second generator H forms cryogen liquid and through increasing again choke valve J throttling, enter the first condenser A again, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
Single-stage parallel double-effect based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 12 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, the first absorber 1 is set up the weak solution pipeline and is communicated with the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution heat exchanger I, generator 3 is had and drives the thermal medium pipeline and be defined as the second generator H and have the refrigerant vapour passage with generator 3, to be communicated with generator 3 afterwards to have the cryogen liquid pipeline to be communicated with the first condenser A through increasing choke valve J again again with outside the connection, the second generator H drives in addition the thermal medium pipeline and is communicated with outside.
2. on flow process, the part weak solution of the first absorber 1 enters the second generator H through the first solution pump 4 and the second solution heat exchanger I, driving the thermal medium heating enters the solution release refrigerant vapour of the second generator H and provides and using as its driving thermal medium to generator 3, the concentrated solution of the second generator H enters the first absorber 1 through the second solution heat exchanger I, flow through after the refrigerant vapour heat release of generator 3 forms cryogen liquid and through increasing again choke valve J throttling, enter the first condenser A again, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
Single-stage parallel double-effect based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 13 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, cancel the second evaporimeter, the second choke valve and solution choke valve, the first absorber 1 has the weak solution pipeline to be communicated with the second absorber 2, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, the first absorber 1 is set up the weak solution pipeline and is communicated with the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution heat exchanger I, the second generator H has the cryogen liquid pipeline with the first condenser A, to be communicated with the driving thermal medium of the refrigerant vapour of generator generation one by one as the second generator through increasing choke valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H, the second generator H also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the part weak solution of the first absorber 1 enters the second generator H through the first solution pump 4 and the second solution heat exchanger I, refrigerant vapour heating from generator 3 enters the solution release refrigerant vapour of the second generator H and provides to the first condenser A, the concentrated solution of the second generator H enters the first absorber 1 through the second solution heat exchanger I, flow through after the refrigerant vapour heat release of the second generator H forms cryogen liquid and through increasing again choke valve J throttling, enter the first condenser A again, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
Single-stage based on the 3rd class absorption-generation systems series connection economic benefits and social benefits the 3rd class absorption heat pump shown in Figure 14 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, increase by the second generator, increase again choke valve and the second solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and the weak solution pipeline to be arranged through the first solution pump 4 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, solution heat exchanger 7 and the second solution heat exchanger I are communicated with generator 3, generator 3 is had the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with the second generator H through the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing choke valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator H also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the weak solution of the second absorber 2 enters generator 3 through the first solution pump 4, solution heat exchanger 7 and the second solution heat exchanger I, the refrigerant vapour that generator 3 produces provides to using to the second generator H and drives thermal medium as it, and the concentrated solution of generator 3 enters the second generator H through the second solution heat exchanger I; The weak solution that the refrigerant vapour heating of the second generator H of flowing through enters the second generator H discharges refrigerant vapour and provides to the first condenser A, the concentrated solution of the second generator H enters the second absorber 2 through solution heat exchanger 7, after refrigerant vapour heat release formation cryogen liquid as the second generator H driving thermal medium, through increasing again choke valve J throttling, enter the first condenser A again, form single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage connection in series-parallel based on the 3rd class absorption-generation systems economic benefits and social benefits the 3rd class absorption heat pump shown in Figure 15 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, cancel the second evaporimeter, the second choke valve and solution choke valve, the first absorber 1 has the weak solution pipeline to be communicated with the second absorber 2, increase by the second generator, increase again choke valve and the second solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and to have the weak solution pipeline directly with the second generator H connected sum, through the second solution heat exchanger I, with generator 3, to be communicated with again respectively after the first solution pump 4 and solution heat exchanger 7 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, generator 3 is had the concentrated solution pipeline to be communicated with a minute steam chest 8 through solution heat exchanger 7 and the second absorber 2 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with the second generator H through the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline to be communicated with a minute steam chest 8 through solution heat exchanger 7 and the second absorber 2, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing choke valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator H also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the weak solution of the second absorber 2 directly enters respectively the second generator H and through the second solution heat exchanger I, enters generator 3 again after the first solution pump 4 and solution heat exchanger 7, the refrigerant vapour that generator 3 discharges provides to using to the second generator H and drives thermal medium as it, and the concentrated solution of generator 3 enters the second generator H through the second solution heat exchanger I; The solution release refrigerant vapour that the refrigerant vapour heating enters the second generator H provides to the first condenser A, the concentrated solution of the second generator H enters minute steam chest 8 through solution heat exchanger 7 and the second absorber 2, flow through after the refrigerant vapour heat release of the second generator H forms cryogen liquid and through increasing again choke valve J throttling, enter the first condenser A again, form single-stage connection in series-parallel economic benefits and social benefits the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage based on the 3rd class absorption-generation systems series connection economic benefits and social benefits the 3rd class absorption heat pump shown in Figure 16 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 6, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and to have the weak solution pipeline to be communicated with the second generator H through the first solution pump 4 and solution heat exchanger 7 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, the second generator H also has the concentrated solution pipeline to be communicated with generator 3 through resolubilization liquid pump K and the second solution heat exchanger I, generator 3 is had the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with the second absorber 2 through the second solution heat exchanger I and solution heat exchanger 7, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing choke valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator H also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the refrigerant vapour that generator 3 discharges provides to using to the second generator H and drives thermal medium as it, the weak solution of the second absorber 2 enters the second generator H through the first solution pump 4 and solution heat exchanger 7, solution that the refrigerant vapour heating of the second generator H of flowing through enters in it discharges refrigerant vapour, the refrigerant vapour that the second generator H produces enters the first condenser A, and the concentrated solution of the second generator H enters generator through resolubilization liquid pump K and the second solution heat exchanger I; The concentrated solution of generator 3 enters the second absorber 2 through the second solution heat exchanger I and solution heat exchanger 7, after refrigerant vapour heat release formation cryogen liquid as the second generator H driving thermal medium, through increasing again choke valve J throttling, enter the first condenser A again, form single-stage connection in series-parallel economic benefits and social benefits the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage connection in series-parallel based on the 3rd class absorption-generation systems economic benefits and social benefits the 3rd class absorption heat pump shown in Figure 17 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and to have the weak solution pipeline with the second generator H connected sum, with generator 3, to be communicated with respectively after the first solution pump 4 and solution heat exchanger 7 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, the second generator H also has the concentrated solution pipeline to be communicated with generator 3 through resolubilization liquid pump K and the second solution heat exchanger I, generator 3 there is is the concentrated solution pipeline to be communicated with a minute steam chest 8 through solution heat exchanger 7 and the second absorber 2 to be adjusted into generator 3 and the concentrated solution pipeline is arranged through the second solution heat exchanger I, solution heat exchanger 7 and the second absorber 2 are communicated with a minute steam chest 8, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing choke valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator H also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the weak solution of the second absorber 2 enters respectively the second generator H and generator 3 after the first solution pump 4 and solution heat exchanger 7, the refrigerant vapour that generator 3 discharges provides to using to the second generator H and drives thermal medium as it, solution that the refrigerant vapour heating of the second generator H of flowing through enters in it discharges refrigerant vapour, the refrigerant vapour that the second generator H produces enters the first condenser A, and the concentrated solution of the second generator H enters generator through resolubilization liquid pump K and the second solution heat exchanger I; The concentrated solution of generator 3 enters minute steam chest 8 through the second solution heat exchanger I, solution heat exchanger 7 and the second absorber 2, after refrigerant vapour heat release formation cryogen liquid as the second generator H driving thermal medium, through increasing again choke valve J throttling, enter the first condenser A again, form single-stage connection in series-parallel economic benefits and social benefits the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage based on the 3rd class absorption-generation systems shown in Figure 180 triple effect the 3rd class absorption heat pump in parallel is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, the first solution pump 4 is set up the weak solution pipeline and through the second solution heat exchanger I, with the second generator H connected sum, through the 3rd solution heat exchanger M, with the 3rd generator L, is communicated with respectively, the second generator H also has the concentrated solution pipeline to be communicated with the second absorber 2 through the second solution heat exchanger I, the 3rd generator L also has the concentrated solution pipeline to be communicated with the second absorber 2 through the 3rd solution heat exchanger M, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing first throttle valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator H also had the refrigerant vapour passage to be communicated with the 3rd generator L, the 3rd generator L had the cryogen liquid pipeline to be communicated with the first condenser A through increasing the second choke valve N more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator L also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the release refrigerant vapour of generator 3 provides to using to the second generator H and drives thermal medium as it, the refrigerant vapour heating discharges refrigerant vapour by the second absorber 2 through the solution that the first solution pump 4, the second solution heat exchanger I enter the second generator H, the refrigerant vapour that the second generator H produces offers the 3rd generator L and drives thermal medium as it, and the concentrated solution of the second generator H enters the second absorber 2 through the second solution heat exchanger I; The refrigerant vapour heating discharges refrigerant vapour by the second absorber 2 through the solution that the first solution pump 4, the 3rd solution heat exchanger M enter the 3rd generator L, the concentrated solution of the 3rd generator L enters the first condenser A through the refrigerant vapour that the 3rd solution heat exchanger M enters the second absorber 2, the three generator L generations; The cryogen liquid that the refrigerant vapour heat release of the second generator H of flowing through forms enters the first condenser A through increasing first throttle valve J again, the cryogen liquid that the refrigerant vapour heat release of the 3rd generator L of flowing through forms enters the first condenser A through increasing the second choke valve N again, the refrigerant vapour heat release that enters the first condenser A becomes cryogen liquid in heated medium, forms based on the single-stage of the 3rd class absorption-generation systems triple effect the 3rd class absorption heat pump in parallel.
Single-stage based on the 3rd class absorption-generation systems shown in Figure 19 triple effect the 3rd class absorption heat pump in parallel is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, the first solution pump 4 is set up the weak solution pipeline and through the second solution heat exchanger I, with the second generator H connected sum, through the 3rd solution heat exchanger M, with the 3rd generator L, is communicated with respectively, the second generator H has the concentrated solution pipeline with the 3rd generator L, the concentrated solution pipeline to be arranged after the second solution heat exchanger I, and all the concentrated solution pipeline after solution heat exchanger 7 converges with generator 3 after the 3rd solution heat exchanger M, through the second absorber 2, with a minute steam chest 8, be communicated with again, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing first throttle valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator H also had the refrigerant vapour passage to be communicated with the 3rd generator L, the 3rd generator L had the cryogen liquid pipeline to be communicated with the first condenser A through increasing the second choke valve N more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator L also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the release refrigerant vapour of generator 3 provides to using to the second generator H and drives thermal medium as it, refrigerant vapour heats by the second absorber 2 through the first solution pump 4, the solution that the second solution heat exchanger I enters the second generator H discharges refrigerant vapour, the refrigerant vapour that the second generator H produces offers the 3rd generator L and drives thermal medium as it, refrigerant vapour heats by the second absorber 2 through the first solution pump 4, the solution that the 3rd solution heat exchanger M enters the 3rd generator L discharges refrigerant vapour, the refrigerant vapour that the 3rd generator L produces enters the first condenser A, the concentrated solution of the second generator H is converged with the concentrated solution of generator 3 after solution heat exchanger 7 after the second solution heat exchanger I, the concentrated solution of the 3rd generator L is converged with the concentrated solution of generator 3 after solution heat exchanger 7 after the 3rd solution heat exchanger M, the solution that three tunnels merge enters minute steam chest 8 again after the second absorber 2 heat absorbing part vaporizations, the cryogen liquid that the refrigerant vapour heat release of the second generator H of flowing through forms enters the first condenser A through increasing first throttle valve J again, the cryogen liquid that the refrigerant vapour heat release of the 3rd generator L of flowing through forms enters the first condenser A through increasing the second choke valve N again, forms single-stage parallel connection triple effect the 3rd class absorption heat pump based on the 3rd class absorptions-generation systems.
Single-stage based on the 3rd class absorption-generation systems shown in Figure 20 triple effect the 3rd class absorption heat pump in parallel is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber 1 is set up the weak solution pipeline and through the second solution heat exchanger I, with the second generator H connected sum, through the 3rd solution heat exchanger M, with the 3rd generator L, is communicated with respectively after resolubilization liquid pump K again again, the second generator H also has the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution heat exchanger I, the 3rd generator L also has the concentrated solution pipeline to be communicated with the first absorber 1 through the 3rd solution heat exchanger M, generator 3 is had and drives the thermal medium pipeline and be defined as the second generator H and have the refrigerant vapour passage with generator 3, to be communicated with generator 3 afterwards to have the cryogen liquid pipeline to be communicated with the first condenser A through increasing first throttle valve J again again with outside the connection---the refrigerant vapour of the second generator generation is as the driving thermal medium of generator, the 3rd generator L has the cryogen liquid pipeline to be communicated with the first condenser A through increasing the second choke valve N more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the 3rd generator L---and the refrigerant vapour of generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator L also has the refrigerant vapour passage to be communicated with the first condenser A, the second generator H drives in addition the thermal medium pipeline and is communicated with outside.
2. on flow process, drive the thermal medium heating and by the first absorber 1, through resolubilization liquid pump K and the second solution heat exchanger I, entered the solution release refrigerant vapour of the second generator H, the refrigerant vapour that the second generator H produces offers generator 3 and drives thermal medium as it, and the concentrated solution of the second generator H enters the first absorber 1 through the second solution heat exchanger I; The release refrigerant vapour of generator 3 provides to using to the 3rd generator L and drives thermal medium as it, the refrigerant vapour heating is entered the solution release refrigerant vapour of the 3rd generator L through resolubilization liquid pump K and the 3rd solution heat exchanger M by the first absorber 1, the refrigerant vapour that the 3rd generator L produces provides to the first condenser A, and the concentrated solution of the 3rd generator L enters the first absorber 1 through the 3rd solution heat exchanger M; The cryogen liquid that the refrigerant vapour heat release of generator 3 of flowing through forms enters the first condenser A through increasing first throttle valve J again, the cryogen liquid that the refrigerant vapour heat release of the 3rd generator L of flowing through forms enters the first condenser A through increasing the second choke valve N again, forms single-stage parallel connection triple effect the 3rd class absorption heat pump based on the 3rd class absorptions-generation systems.
Single-stage based on the 3rd class absorption-generation systems shown in Figure 21 triple effect the 3rd class absorption heat pump in parallel is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber 1 is set up the weak solution pipeline and through the second solution heat exchanger I, with the second generator H connected sum, through the 3rd solution heat exchanger M, with the 3rd generator L, is communicated with respectively after resolubilization liquid pump K again again, the second generator H also has the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution heat exchanger I, the 3rd generator L also has the concentrated solution pipeline to be communicated with the first absorber 1 through the 3rd solution heat exchanger M, generator 3 is had and drives the thermal medium pipeline and be defined as the 3rd generator L and have the refrigerant vapour passage with generator 3, to be communicated with generator 3 afterwards to have the cryogen liquid pipeline to be communicated with the first condenser A through increasing the second choke valve N again again with outside the connection---the refrigerant vapour of the 3rd generator generation is as the driving thermal medium of generator, after the second generator H also had the refrigerant vapour passage to be communicated with the 3rd generator L, the 3rd generator L had the cryogen liquid pipeline to be communicated with the first condenser A through increasing first throttle valve J more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the second generator H drives in addition the thermal medium pipeline and is communicated with outside.
2. on flow process, drive the thermal medium heating and by the first absorber 1, through resolubilization liquid pump K and the second solution heat exchanger I, entered the solution release refrigerant vapour of the second generator H, the refrigerant vapour that the second generator H produces offers the 3rd generator L and drives thermal medium as it, and the concentrated solution of the second generator H enters the first absorber 1 through the second solution heat exchanger I; The refrigerant vapour heating is entered the solution release refrigerant vapour of the 3rd generator L through resolubilization liquid pump K and the 3rd solution heat exchanger M by the first absorber 1, the refrigerant vapour that the 3rd generator L discharges provides to using to generator 3 and drives thermal medium as it, the refrigerant vapour that generator 3 produces provides to the first condenser A, and the concentrated solution of the 3rd generator L enters the first absorber 1 through the 3rd solution heat exchanger M; The cryogen liquid that the refrigerant vapour heat release of the 3rd generator L of flowing through forms enters the first condenser A through increasing first throttle valve J again, the cryogen liquid that the refrigerant vapour heat release of generator 3 of flowing through forms enters the first condenser A through increasing the second choke valve N again, forms single-stage parallel connection triple effect the 3rd class absorption heat pump based on the 3rd class absorptions-generation systems.
Single-stage serially connected three-effect based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 22 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 6, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and the weak solution pipeline to be arranged through the first solution pump 4 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, solution heat exchanger 7, the second solution heat exchanger I and the 3rd solution heat exchanger M are communicated with generator 3, generator 3 is had the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with the second generator H through the 3rd solution heat exchanger M, the second generator H also has the concentrated solution pipeline to be communicated with the 3rd generator L through the second solution heat exchanger I, the 3rd generator L also has the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing first throttle valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator 3 generations is as the driving thermal medium of the second generator H, after the second generator H also had the refrigerant vapour passage to be communicated with the 3rd generator L, the 3rd generator L had the cryogen liquid pipeline to be communicated with the first condenser A through increasing the second choke valve N more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator L also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the weak solution of the second absorber 2 enters generator 3 through the first solution pump 4, solution heat exchanger 7, the second solution heat exchanger I and the 3rd solution heat exchanger M, the refrigerant vapour that generator 3 produces offers the second generator H usings as its driving thermal medium, and the concentrated solution of generator 3 enters the second generator H through the 3rd solution heat exchanger M; Solution that the refrigerant vapour heating of the second generator H of flowing through enters in it discharges refrigerant vapour, the refrigerant vapour that the second generator H produces offers the 3rd generator L usings as its driving thermal medium, and the concentrated solution of the second generator H enters the 3rd generator L through the second solution heat exchanger I; Solution that the refrigerant vapour heating of the 3rd generator L of flowing through enters in it discharges refrigerant vapour, and the concentrated solution of the 3rd generator L enters through solution heat exchanger 7 refrigerant vapour that the second absorber 2, the three generator L produce and enters the first condenser A; The cryogen liquid that the refrigerant vapour heat release of the second generator H of flowing through forms enters the first condenser A through increasing first throttle valve J again, the cryogen liquid that the refrigerant vapour heat release of the 3rd generator L of flowing through forms enters the first condenser A through increasing the second choke valve N again, forms single-stage serially connected three-effect the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage serially connected three-effect based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 23 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and the weak solution pipeline to be arranged through the first solution pump 4 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, solution heat exchanger 7, the second solution heat exchanger I and the 3rd solution heat exchanger M are communicated with generator 3, generator 3 is had the concentrated solution pipeline to be communicated with a minute steam chest 8 through solution heat exchanger 7 and the second absorber 2 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with the second generator H through the 3rd solution heat exchanger M, the second generator H also has the concentrated solution pipeline to be communicated with the 3rd generator L through the second solution heat exchanger I, the 3rd generator L also has the concentrated solution pipeline to be communicated with a minute steam chest 8 through solution heat exchanger 7 and the second absorber 2, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing first throttle valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator H also had the refrigerant vapour passage to be communicated with the 3rd generator L, the 3rd generator L had the cryogen liquid pipeline to be communicated with the first condenser A through increasing the second choke valve N more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator L also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the weak solution of the second absorber 2 enters generator 3 through the first solution pump 4, solution heat exchanger 7, the second solution heat exchanger I and the 3rd solution heat exchanger M, the refrigerant vapour that generator 3 produces offers the second generator H usings as its driving thermal medium, and the concentrated solution of generator 3 enters the second generator H through the 3rd solution heat exchanger M; Solution that the refrigerant vapour heating of the second generator H of flowing through enters in it discharges refrigerant vapour, the refrigerant vapour that the second generator H produces offers the 3rd generator L usings as its driving thermal medium, and the concentrated solution of the second generator H enters the 3rd generator L through the second solution heat exchanger I; Solution that the refrigerant vapour heating of the 3rd generator L of flowing through enters in it discharges refrigerant vapour, and the concentrated solution of the 3rd generator L enters the first condenser A through the refrigerant vapour that solution heat exchanger 7 and the second absorber 2 enter 8, the three generator L generations of minute steam chest; The cryogen liquid that the refrigerant vapour heat release of the second generator H of flowing through forms enters the first condenser A through increasing first throttle valve J again, the cryogen liquid that the refrigerant vapour heat release of the 3rd generator L of flowing through forms enters the first condenser A through increasing the second choke valve N again, forms single-stage serially connected three-effect the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage serially connected three-effect based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 24 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, increase again the first solution pump, increase again the second solution pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and to have the weak solution pipeline to be communicated with the 3rd generator L through the first solution pump 4 and solution heat exchanger 7 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, the 3rd generator L also has the concentrated solution pipeline to be communicated with the second generator H through increasing the first solution pump K and the second solution heat exchanger I again, the second generator H also has the concentrated solution pipeline through increasing the second solution pump O and the 3rd solution heat exchanger M is communicated with generator 3 again, generator 3 there is is the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7 to be adjusted into generator 3 and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger M, the second solution heat exchanger I and solution heat exchanger 7 are communicated with the second absorber 2, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing first throttle valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator H also had the refrigerant vapour passage to be communicated with the 3rd generator L, the 3rd generator L had the cryogen liquid pipeline to be communicated with the first condenser A through increasing the second choke valve N more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator L also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the weak solution of the second absorber 2 enters the 3rd generator L through the first solution pump 4 and solution heat exchanger 7, the concentrated solution of the 3rd generator L is through increasing the first solution pump K and the second solution heat exchanger I enters the second generator H again, the concentrated solution of the second generator H is through increasing the second solution pump O and the 3rd solution heat exchanger M enters generator 3 again, and the concentrated solution of generator 3 enters the second absorber 2 through the 3rd solution heat exchanger M, the second solution heat exchanger I and solution heat exchanger 7; The refrigerant vapour that generator 3 produces offers the second generator H and usings as its driving thermal medium, solution that the refrigerant vapour heating of the second generator H of flowing through enters in it discharges refrigerant vapour, and the refrigerant vapour that the second generator H produces offers the 3rd generator L and usings and drive thermal medium as it; Solution that the refrigerant vapour heating of the 3rd generator L of flowing through enters in it discharges refrigerant vapour, and the refrigerant vapour that the 3rd generator L produces enters the first condenser A; The cryogen liquid that the refrigerant vapour heat release of the second generator H of flowing through forms enters the first condenser A through increasing first throttle valve J again, the cryogen liquid that the refrigerant vapour heat release of the 3rd generator L of flowing through forms enters the first condenser A through increasing the second choke valve N again, forms single-stage serially connected three-effect the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
Single-stage serially connected three-effect based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 25 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, cancel the second evaporimeter, the second choke valve and solution choke valve, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, increase again the first solution pump, increase again the second solution pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and to have the weak solution pipeline to be communicated with the 3rd generator L through the first solution pump 4 and solution heat exchanger 7 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, the 3rd generator L also has the concentrated solution pipeline to be communicated with the second generator H through increasing the first solution pump K and the second solution heat exchanger I again, the second generator H also has the concentrated solution pipeline through increasing the second solution pump O and the 3rd solution heat exchanger M is communicated with generator 3 again, generator 3 there is is the concentrated solution pipeline to be communicated with a minute steam chest 8 through solution heat exchanger 7 and the second absorber 2 to be adjusted into generator 3 and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger M, the second solution heat exchanger I, solution heat exchanger 7 and the second absorber 2 are communicated with a minute steam chest 8 and are communicated with, the second generator H has the cryogen liquid pipeline to be communicated with the first condenser A through increasing first throttle valve J more again after generator 3 has the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 to have the refrigerant vapour passage to be communicated with the second generator H---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, after the second generator H also had the refrigerant vapour passage to be communicated with the 3rd generator L, the 3rd generator L had the cryogen liquid pipeline to be communicated with the first condenser A through increasing the second choke valve N more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator L also has the refrigerant vapour passage to be communicated with the first condenser A.
2. on flow process, the weak solution of the second absorber 2 enters the 3rd generator L through the first solution pump 4 and solution heat exchanger 7, the concentrated solution of the 3rd generator L is through increasing the first solution pump K and the second solution heat exchanger I enters the second generator H again, the concentrated solution of the second generator H is through increasing the second solution pump O and the 3rd solution heat exchanger M enters generator 3 again, and the concentrated solution of generator 3 enters minute steam chest 8 through the 3rd solution heat exchanger M, the second solution heat exchanger I, solution heat exchanger 7 and the second absorber 2; The refrigerant vapour that generator 3 produces offers the second generator H and usings as its driving thermal medium, solution that the refrigerant vapour heating of the second generator H of flowing through enters in it discharges refrigerant vapour, and the refrigerant vapour that the second generator H produces offers the 3rd generator L and usings and drive thermal medium as it; Solution that the refrigerant vapour heating of the 3rd generator L of flowing through enters in it discharges refrigerant vapour, and the refrigerant vapour that the 3rd generator L produces enters the first condenser A; The cryogen liquid that the refrigerant vapour heat release of the second generator H of flowing through forms enters the first condenser A through increasing first throttle valve J again, the cryogen liquid that the refrigerant vapour heat release of the 3rd generator L of flowing through forms enters the first condenser A through increasing the second choke valve N again, forms single-stage serially connected three-effect the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
One generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 26 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 6, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase absorption-evaporimeter, the second cryogen liquid pump and the second solution heat exchanger, to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) and the second solution heat exchanger (I), the first absorber (1) is had the weak solution pipeline to be communicated with a minute steam chest (8) through solution choke valve (6) and the second absorber (2) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with absorption-evaporimeter (Q) through the second solution heat exchanger (I), absorption-evaporimeter (Q) also has the weak solution pipeline to be communicated with a minute steam chest (8) through solution choke valve (6) and the second absorber (2), evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into evaporimeter (C) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (Q), evaporimeter (C) is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P) with absorption-evaporimeter (Q) after absorption-evaporimeter (Q) is communicated with again.
2. on flow process, the cryogen liquid of evaporimeter C after the second cryogen liquid pump P pressurization, flow through absorption-evaporimeter Q, absorb heat into refrigerant vapour and provide to the first absorber 1, divide the concentrated solution of steam chest 8 to enter the first absorber 1 through the second solution pump 5 and the second solution heat exchanger I, absorb the refrigerant vapour of self-absorption-evaporimeter Q heat release in heated medium, the weak solution of the first absorber 1 enters absorption-evaporimeter Q through the second solution heat exchanger I, absorb the refrigerant vapour of flash-pot C heat release in the cryogen liquid of the absorption of flowing through-evaporimeter Q, the weak solution of absorption-evaporimeter Q enters minute steam chest 8 through solution choke valve 6 and the second absorber 2, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
One generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 27 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, cancel the solution choke valve, increase absorption-evaporimeter, the resolubilization liquid pump, the second cryogen liquid pump and the second solution heat exchanger, to divide steam chest 8 to have the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution pump 5 to be adjusted into minute steam chest 8 has the concentrated solution pipeline to be communicated with absorption-evaporimeter Q through the second solution pump 5, absorption-evaporimeter Q also has the weak solution pipeline to be communicated with the first absorber 1 through resolubilization liquid pump K and the second solution heat exchanger I, the first absorber 1 is had the weak solution pipeline to be communicated with a minute steam chest 8 through solution choke valve 6 and the second absorber 2 to be adjusted into the first absorber 1 has the weak solution pipeline to be communicated with dividing a steam chest 8 through the second solution heat exchanger I and the second absorber 2, the first evaporimeter C is had the refrigerant vapour passage to be communicated with the first absorber 1 to be adjusted into the first evaporimeter C has the refrigerant vapour passage to be communicated with absorption-evaporimeter Q, the first evaporimeter C sets up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with the first absorber 1 through the second cryogen liquid pump P with absorption-evaporimeter Q after absorption-evaporimeter Q is communicated with again.
2. on flow process, the cryogen liquid of the first evaporimeter C after the second cryogen liquid pump P pressurization, flow through absorption-evaporimeter Q, absorb heat into refrigerant vapour and provide to the first absorber 1, divide the concentrated solution of steam chest 8 to enter absorption-evaporimeter Q through the second solution pump 5, absorption from the refrigerant vapour of the first evaporimeter C heat release in the cryogen liquid of the absorption of flowing through-evaporimeter Q, the weak solution of absorption-evaporimeter Q enters the first absorber 1 through resolubilization liquid pump K and the second solution heat exchanger I, absorb the refrigerant vapour of self-absorption-evaporimeter Q heat release in heated medium, the weak solution of the first absorber 1 enters minute steam chest 8 through the second absorber 2 again after the second solution heat exchanger I decrease temperature and pressure, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
One generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 28 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase and increase again choke valve, absorption-evaporimeter and the second solution heat exchanger, to divide steam chest 8 to have the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution pump 5 to be adjusted into minute steam chest 8 has the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution pump 5 and the second solution heat exchanger I, the first absorber 1 is had the weak solution pipeline to be communicated with the second absorber 2 through solution choke valve 6 to be adjusted into the first absorber 1 has the weak solution pipeline to be communicated with absorption-evaporimeter Q through the second solution heat exchanger I, absorption-evaporimeter Q also has the weak solution pipeline to be communicated with the second absorber 2 through solution choke valve 6, the first evaporimeter C is had the refrigerant vapour passage to be communicated with the first absorber 1 to be adjusted into the first evaporimeter C has the refrigerant vapour passage to be communicated with absorption-evaporimeter Q, the first condenser A sets up cryogen liquid pipeline absorption-evaporimeter Q after increasing choke valve J again and absorption-evaporimeter Q is communicated with has the refrigerant vapour passage to be communicated with the first absorber 1 again.
2. on flow process, the cryogen liquid of the first condenser A after increasing again choke valve J reducing pressure by regulating flow, flow through absorption-evaporimeter Q, absorb heat into refrigerant vapour and provide to the first absorber 1, divide the concentrated solution of steam chest 8 to enter the first absorber 1 through the second solution pump 5 and the second solution heat exchanger I, absorb the refrigerant vapour of self-absorption-evaporimeter Q heat release in heated medium, the weak solution of the first absorber 1 enters absorption-evaporimeter Q through the second solution heat exchanger I, absorption from the refrigerant vapour of the first evaporimeter C heat release in the cryogen liquid of the absorption of flowing through-evaporimeter Q, the weak solution of absorption-evaporimeter Q enters the second absorber 2 through solution choke valve 6, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
One generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 29 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, cancel the solution choke valve, increase by the second cryogen liquid pump, absorption-evaporimeter, resolubilization liquid pump and the second solution heat exchanger, to divide steam chest 8 to have the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution pump 5 to be adjusted into minute steam chest 8 has the concentrated solution pipeline to be communicated with absorption-evaporimeter Q through the second solution pump 5, absorption-evaporimeter Q also has the weak solution pipeline to be communicated with the first absorber 1 through resolubilization liquid pump K and the second solution heat exchanger I, the first absorber 1 is had the weak solution pipeline to be communicated with the second absorber 2 through solution choke valve 6 to be adjusted into the first absorber 1 has the weak solution pipeline to be communicated with the second absorber 2 through the second solution heat exchanger I, the first evaporimeter C is had the refrigerant vapour passage to be communicated with the first absorber 1 to be adjusted into the first evaporimeter C has the refrigerant vapour passage to be communicated with absorption-evaporimeter Q, the first evaporimeter C sets up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with the first absorber 1 through the second cryogen liquid pump P with absorption-evaporimeter Q after absorption-evaporimeter Q is communicated with again.
2. on flow process, the cryogen liquid of the first evaporimeter C after the second cryogen liquid pump P pressurization, flow through absorption-evaporimeter Q, absorb heat into refrigerant vapour and provide to the first absorber 1, divide the concentrated solution of steam chest 8 to enter absorption-evaporimeter Q through the second solution pump 5, absorption from the refrigerant vapour of the first evaporimeter C heat release in the cryogen liquid of the absorption of flowing through-evaporimeter Q, the weak solution of absorption-evaporimeter Q enters the first absorber 1 through resolubilization liquid pump K and the second solution heat exchanger I, absorb the refrigerant vapour of self-absorption-evaporimeter Q heat release in heated medium, the weak solution of the first absorber 1 enters the second absorber 2 through the second solution heat exchanger I, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
Here it is to be noted, shown in Figure 28-29 in the 3rd class absorption heat pump, optional disappear the second choke valve G and the first evaporimeter C of selecting is communicated with the second evaporimeter D through the second choke valve G, and the second condenser B is had the cryogen liquid pipeline to be communicated with the first evaporimeter C through cryogen liquid pump F to be adjusted into the second condenser B has the cryogen liquid pipeline to be communicated with the second evaporimeter D through cryogen liquid pump F.
One generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 30 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase and increase again choke valve, the 3rd absorber and the second solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and the weak solution pipeline to be arranged through the first solution pump 4 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, solution heat exchanger 7 and the second solution heat exchanger I are communicated with generator 3, generator 3 is had the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with the 3rd absorber R through the second solution heat exchanger I, the 3rd absorber R also has the weak solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7, there are heated medium pipeline and outside the connection to be adjusted into the first condenser A and to have cryogen liquid pipeline first absorber 1 after increasing again choke valve J and the first absorber 1 is communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber R the first absorber 1, the 3rd absorber R also has the heated medium pipeline to be communicated with outside.
2. on flow process, the cryogen liquid of the first condenser A after increasing again choke valve J throttling, flow through again the first absorber 1, absorb heat into refrigerant vapour and provide to the 3rd absorber R; The concentrated solution of generator 3 enters the 3rd absorber R, absorbs from the refrigerant vapour of the first absorber 1 heat release in heated medium through the second solution heat exchanger I, the weak solution of the 3rd absorber R enters the second absorber 2 through solution heat exchanger 7, the weak solution of the second absorber 2 enters generator 3 through the first solution pump 4, solution heat exchanger 7 and the second solution heat exchanger I, forms one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber based on the 3rd class absorption-generation systems, by the first absorber.
One generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 31 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase by the second cryogen liquid pump, the 3rd absorber, resolubilization liquid pump and the second solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and to have the weak solution pipeline to be communicated with the 3rd absorber R through the first solution pump 4 and solution heat exchanger 7 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, the 3rd absorber R also has the weak solution pipeline to be communicated with generator 3 through resolubilization liquid pump K and the second solution heat exchanger I, generator 3 is had the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with the second absorber 2 through the second solution heat exchanger I and solution heat exchanger 7, there are heated medium pipeline and outside the connection to be adjusted into the second evaporimeter D and to have the cryogen liquid pipeline with the first absorber 1 after the first absorber 1 is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber R through the second cryogen liquid pump P the first absorber 1, the 3rd absorber R also has the heated medium pipeline to be communicated with outside.
2. on flow process, the cryogen liquid of the second evaporimeter D after the second cryogen liquid pump P pressurization, flow through again the first absorber 1, absorb heat into refrigerant vapour and provide to the 3rd absorber R; The weak solution of the second absorber 2 enters the 3rd absorber R, absorbs from the refrigerant vapour of the first absorber 1 heat release in heated medium through the first solution pump 4 and solution heat exchanger 7, the weak solution of the 3rd absorber R enters generator 3 through resolubilization liquid pump K and the second solution heat exchanger I, the concentrated solution of generator 3 enters the second absorber 2 through the second solution heat exchanger I and solution heat exchanger 7, forms one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber based on the 3rd class absorption-generation systems, by the first absorber.
One generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 32 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, cancel the second evaporimeter, the second choke valve and solution choke valve, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, the first absorber 1 has the weak solution pipeline to be communicated with the second absorber 2, increase by the second cryogen liquid pump, the 3rd absorber and the second solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and the weak solution pipeline to be arranged through the first solution pump 4 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, solution heat exchanger 7 and the second solution heat exchanger I are communicated with generator 3, generator 3 is had the concentrated solution pipeline to be communicated with a minute steam chest 8 through solution heat exchanger 7 and the second absorber 2 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with the 3rd absorber R through the second solution heat exchanger I, the 3rd absorber R also has the weak solution pipeline to be communicated with a minute steam chest 8 through solution heat exchanger 7 and the second absorber 2, there are heated medium pipeline and outside the connection to be adjusted into evaporimeter C and to have the cryogen liquid pipeline with the first absorber 1 after the first absorber 1 is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber R through the second cryogen liquid pump P the first absorber 1, the 3rd absorber R also has the heated medium pipeline to be communicated with outside.
2. on flow process, the cryogen liquid of evaporimeter C after the second cryogen liquid pump P pressurization, flow through again the first absorber 1, absorb heat into refrigerant vapour and provide to the 3rd absorber R; The concentrated solution of generator 3 enters the 3rd absorber R, absorbs from the refrigerant vapour of the first absorber 1 heat release in heated medium through the second solution heat exchanger I, the weak solution of the 3rd absorber R enters minute steam chest 8 through solution heat exchanger 7 and the second absorber 2, the weak solution of the second absorber 2 enters generator 3 through the first solution pump 4, solution heat exchanger 7 and the second solution heat exchanger I, forms one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber based on the 3rd class absorption-generation systems, by the first absorber.
One generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 33 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, cancel the second choke valve G, cancel the cryogen liquid pipeline that the first evaporimeter C is communicated with the second evaporimeter D through the second choke valve G, the second condenser B is had the cryogen liquid pipeline to be communicated with the first evaporimeter C through the first cryogen liquid pump F to be adjusted into the second condenser B has the cryogen liquid pipeline to be communicated with the second evaporimeter D through the first cryogen liquid pump F; increase by the second cryogen liquid pump, the 3rd absorber, resolubilization liquid pump and the second solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and to have the weak solution pipeline to be communicated with the 3rd absorber R through the first solution pump 4 and solution heat exchanger 7 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, the 3rd absorber R also has the weak solution pipeline to be communicated with generator 3 through resolubilization liquid pump K and the second solution heat exchanger I, generator 3 there is is the concentrated solution pipeline to be communicated with a minute steam chest 8 through solution heat exchanger 7 and the second absorber 2 to be adjusted into generator 3 and the concentrated solution pipeline is arranged through the second solution heat exchanger I, solution heat exchanger 7 and the second absorber 2 are communicated with a minute steam chest 8, there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter C and to have the cryogen liquid pipeline with the first absorber 1 after the first absorber 1 is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber R through the second cryogen liquid pump P the first absorber 1, the 3rd absorber R also has the heated medium pipeline to be communicated with outside.
2. on flow process, the cryogen liquid of the first evaporimeter C after the second cryogen liquid pump P pressurization, flow through the first absorber 1, absorb heat into refrigerant vapour and provide to the 3rd absorber R; The weak solution of the second absorber 2 enters the 3rd absorber R, absorbs from the refrigerant vapour of the first absorber 1 heat release in heated medium through the first solution pump 4 and solution heat exchanger 7, the weak solution of the 3rd absorber R enters generator 3 through resolubilization liquid pump K and the second solution heat exchanger I, the concentrated solution of generator 3 enters minute steam chest 8 through the second solution heat exchanger I, solution heat exchanger 7 and the second absorber 2, forms one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber based on the 3rd class absorption-generation systems, by the first absorber.
One generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 34 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase by the second cryogen liquid pump, the 3rd cryogen liquid pump, the 3rd condenser, the 3rd evaporimeter, the 3rd absorber, the 4th absorber, the second solution heat exchanger, the second solution choke valve, resolubilization liquid pump and second minute steam chest, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and to have the weak solution pipeline to be communicated with second minute steam chest U through the second solution choke valve V and the 4th absorber T through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, steam chest U also had the concentrated solution pipeline to be communicated with the 3rd absorber R through resolubilization liquid pump K and solution heat exchanger 7 in second minute, the 3rd absorber R also has the weak solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7, generator 3 is had the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with the 4th absorber T through the second solution heat exchanger I, the 4th absorber T also has the weak solution pipeline to be communicated with generator 3 through the first solution pump 4 and the second solution heat exchanger I, the first condenser A is had the cryogen liquid pipeline to be communicated with the second evaporimeter D through choke valve E to be adjusted into the first condenser A has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter X through choke valve E, the 3rd evaporimeter X also has the refrigerant vapour passage to be communicated with the 4th absorber T, steam chest U also had the refrigerant vapour passage to be communicated with the 3rd condenser W in second minute, the 3rd condenser W also has the cryogen liquid pipeline to be communicated with the second evaporimeter D through the 3rd cryogen liquid pump S, there are heated medium pipeline and outside the connection to be adjusted into the second evaporimeter D and to have the cryogen liquid pipeline with the first absorber 1 after the first absorber 1 is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber R through the second cryogen liquid pump P the first absorber 1, the 3rd absorber R also has the heated medium pipeline to be communicated with outside, the 3rd condenser W also has the cooling medium pipeline to be communicated with outside, the 3rd evaporimeter X medium pipeline that also has surplus heat is communicated with outside.
2. on flow process, the cryogen liquid of the first condenser A enters the 3rd evaporimeter X, absorbs waste heat and become refrigerant vapour and provide to the 4th absorber T through first throttle valve E throttling, the refrigerant vapour of steam chest U release in second minute enters the 3rd condenser W, heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of the 3rd condenser W enters the second evaporimeter D through the 3rd cryogen liquid pump S; The cryogen liquid that enters evaporimeter D is divided into two-way---the first via absorbs waste heat and becomes refrigerant vapour and provide to the second absorber 2, the second tunnel after the second cryogen liquid pump P pressurization, flow through again the first absorber 1, absorb heat into refrigerant vapour and provide to the 3rd absorber R; The concentrated solution of generator 3 enters the 4th absorber T, absorbs from the refrigerant vapour of the 3rd evaporimeter X heat release in the solution of the 4th absorber T that flows through through the second solution heat exchanger I, and the weak solution of the 4th absorber T enters generator 3 through the first solution pump 4 and the second solution heat exchanger I; The weak solution of the second absorber 2 is flowed through after the vaporization of the 4th absorber T, heat absorbing part again and is entered second minute steam chest U after the second solution choke valve V throttling; The solution that enters second minute steam chest U discharges refrigerant vapour and provides to the 3rd condenser W, concentrated solution enters the 3rd absorber R, absorbs from the refrigerant vapour of the first absorber 1 heat release in heated medium through resolubilization liquid pump K and solution heat exchanger 7, the weak solution of the 3rd absorber R enters the second absorber 2 through solution heat exchanger 7, forms one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber based on the 3rd class absorption-generation systems, by the first absorber.
One generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 35 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, cancel the second choke valve G, cancel the cryogen liquid pipeline that the first evaporimeter C is communicated with the second evaporimeter D through the second choke valve G, the second condenser B is had the cryogen liquid pipeline to be communicated with the first evaporimeter C through the first cryogen liquid pump F to be adjusted into the second condenser B has the cryogen liquid pipeline to be communicated with the second evaporimeter D through the first cryogen liquid pump F, increase by the second cryogen liquid pump, the 3rd cryogen liquid pump, the 3rd condenser, the 3rd evaporimeter, the 3rd absorber, the 4th absorber, the second solution heat exchanger, the second solution choke valve, resolubilization liquid pump and second minute steam chest, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and to have the weak solution pipeline to be communicated with the 4th absorber T through the second solution choke valve V through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, the 4th absorber T also has the weak solution pipeline to be communicated with generator 3 through the first solution pump 4 and the second solution heat exchanger I, generator 3 is had the concentrated solution pipeline to be communicated with first minute steam chest 8 through solution heat exchanger 7 and the second absorber 2 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with second minute steam chest U through the second solution heat exchanger I and the 4th absorber T, steam chest U also had the concentrated solution pipeline to be communicated with the 3rd absorber R through resolubilization liquid pump K and solution heat exchanger 7 in second minute, the 3rd absorber R also has the weak solution pipeline to be communicated with first minute steam chest 8 through solution heat exchanger 7 and the second absorber 2, steam chest U also had the refrigerant vapour passage to be communicated with the 3rd condenser W in second minute, the 3rd condenser W also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter X through the 3rd cryogen liquid pump S, the 3rd evaporimeter X also has the refrigerant vapour passage to be communicated with the 4th absorber T, there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter C and to have the cryogen liquid pipeline with the first absorber 1 after the first absorber 1 is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber R through the second cryogen liquid pump P the first absorber 1, the 3rd absorber R also has the heated medium pipeline to be communicated with outside, the 3rd condenser W also has the cooling medium pipeline to be communicated with outside, the 3rd evaporimeter X medium pipeline that also has surplus heat is communicated with outside.
2. on flow process, the cryogen liquid of the first condenser A is divided into two-way again after first throttle valve E throttling enters the first evaporimeter C---the first via absorbs waste heat and becomes refrigerant vapour to provide to the first absorber 1, the second tunnel after the second cryogen liquid pump P pressurization, flow through again the first absorber 1, absorb heat into refrigerant vapour and provide to the 3rd absorber R, the refrigerant vapour that second minute steam chest U discharges enters the 3rd condenser W, heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of the 3rd condenser W enters the 3rd evaporimeter X, absorbs waste heat and become refrigerant vapour and provide to the 4th minute steam chest T through the 3rd cryogen liquid pump S, the weak solution of the second absorber 2 enters the 4th absorber T after the second solution choke valve V throttling, absorb from the refrigerant vapour of the 3rd evaporimeter X heat release in the solution of the 4th absorber T that flows through, and the weak solution of the 4th absorber T enters generator 3 through the first solution pump 4 and the second solution heat exchanger I, the concentrated solution of generator 3 is through the second solution heat exchanger I the 4th absorber T that flows through again, after the heat absorbing part vaporization, enter second minute steam chest U, the solution that enters second minute steam chest U discharges refrigerant vapour and provides to the 3rd condenser W, concentrated solution enters the 3rd absorber R through resolubilization liquid pump K and solution heat exchanger 7, absorption from the refrigerant vapour of the first absorber 1 heat release in heated medium, the weak solution of the 3rd absorber R enters first minute steam chest 8 through solution heat exchanger 7 and the second absorber 2, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber.
Double-generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 36 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase by the second generator, the 3rd absorber, resolubilization liquid pump and the second solution heat exchanger, generator 3 is had the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 has the refrigerant vapour passage to be communicated with the 3rd absorber R, the 3rd absorber R also has the weak solution pipeline to be communicated with the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline to be communicated with the 3rd absorber R through the second solution heat exchange I, the second generator H also has respectively refrigerant vapour passage and the first condenser A connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber R also has the heated medium pipeline to be communicated with outside.
2. on flow process, the refrigerant vapour that generator 3 discharges enters the 3rd absorber R, by solution, absorbed also heat release in heated medium, the weak solution of the 3rd absorber R enters the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, driving the thermal medium heating enters the solution release refrigerant vapour of the second generator H and provides to the first condenser A, the concentrated solution of the second generator H enters the 3rd absorber R through the second solution heat exchanger I, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by generator.
Double-generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 37 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 6, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator 3, to be communicated with and to be adjusted into the second absorber 2 and the weak solution pipeline to be arranged through the first solution pump 4 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, solution heat exchanger 7 and the second solution heat exchanger I are communicated with the second generator H, the second generator H also has the concentrated solution pipeline to be communicated with the 3rd absorber R through the second solution heat exchanger I, the 3rd absorber R also has the weak solution pipeline to be communicated with generator 3 through resolubilization liquid pump K and the 3rd solution heat exchanger M, generator 3 is had the concentrated solution pipeline to be communicated with the second absorber 2 through solution heat exchanger 7 to be adjusted into generator 3 has the concentrated solution pipeline to be communicated with the second absorber 2 through the 3rd solution heat exchanger M and solution heat exchanger 7, generator 3 is had the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into generator 3 has the refrigerant vapour passage to be communicated with the 3rd absorber R, the second generator H also has respectively refrigerant vapour passage and the first condenser A connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber R also has the heated medium pipeline to be communicated with outside.
2. on flow process, the weak solution of the second absorber 2 enters the second generator H through the first solution pump 4, solution heat exchanger 7 and the second solution heat exchanger I, drives the thermal medium heating and enters the solution release refrigerant vapour of the second generator H and provide to the first condenser A; The concentrated solution of the second generator H enters the 3rd absorber R, absorbs from the refrigerant vapour of generator 3 heat release in heated medium through the second solution volume interchanger I, the weak solution of the 3rd absorber R enters generator 3 through resolubilization liquid pump K and the 3rd solution heat exchanger M, the concentrated solution of generator 3 enters the second absorber 2 through the 3rd solution heat exchanger M and solution heat exchanger 7, forms double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber based on the 3rd class absorption-generation systems, by generator.
Double-generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 38 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, cancel the second absorber 2 and the outside heated medium pipeline that is communicated with, cancel the second evaporimeter D and the second choke valve G, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger, the second condenser and increase again choke valve, generator 3 is set up the refrigerant vapour passage and is communicated with the 3rd absorber R, the 3rd absorber R also has the weak solution pipeline to be communicated with the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline to be communicated with the 3rd absorber R through the second solution heat exchange I, the second generator H also has the refrigerant vapour passage to be communicated with the 3rd condenser W, the 3rd condenser W also has the cryogen liquid pipeline to be communicated with the first condenser A through increasing choke valve J again, the second generator H drives in addition the thermal medium pipeline and is communicated with outside, the 3rd absorber R and the 3rd condenser W also have respectively the heated medium pipeline to be communicated with outside.
2. on flow process, the part refrigerant vapour that generator 3 discharges enters the 3rd absorber R, by the solution from the second generator H, absorbed also heat release in heated medium, the weak solution of the 3rd absorber R enters the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, driving the thermal medium heating enters the solution release refrigerant vapour of the second generator H and provides to the 3rd condenser W, the concentrated solution of the second generator H enters the 3rd absorber R through the second solution heat exchanger I, the refrigerant vapour heat release that enters the 3rd condenser W enters the first condenser A through increasing choke valve J more again after heated medium becomes cryogen liquid, formation is based on the 3rd class absorption-generation systems, by generator, to the first condenser and the 3rd absorber, provide respectively double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
Here be noted that, in Figure 38, the first condenser A, the second condenser B are connected with the pipeline of evaporimeter C with outside waste heat medium and shown in Figure 8 having any different, but be identical in essence, therefore Figure 38 still regards as take the 3rd class absorption heat pump shown in Figure 8 as basis.
Double-generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 39 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger, the second condenser and increase again choke valve, generator 3 is set up the refrigerant vapour passage and is communicated with the 3rd absorber R, the 3rd absorber R also has the weak solution pipeline to be communicated with the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline to be communicated with the 3rd absorber R through the second solution heat exchange I, the second generator H also has the refrigerant vapour passage to be communicated with the 3rd condenser W, the 3rd condenser W also has the cryogen liquid pipeline to be communicated with the first condenser A through increasing choke valve J again, the second generator H drives in addition the thermal medium pipeline and is communicated with outside, the 3rd absorber R and the 3rd condenser W also have respectively the heated medium pipeline to be communicated with outside.
2. on flow process, the part refrigerant vapour that generator 3 discharges enters the 3rd absorber R, by the solution from the second generator H, absorbed also heat release in heated medium, the weak solution of the 3rd absorber R enters the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, driving the thermal medium heating enters the solution release refrigerant vapour of the second generator H and provides to the 3rd condenser W, the concentrated solution of the second generator H enters the 3rd absorber R through the second solution heat exchanger I, the refrigerant vapour heat release that enters the 3rd condenser W enters the first condenser A through increasing choke valve J more again after heated medium becomes cryogen liquid, formation is based on the 3rd class absorption-generation systems, by generator, to the first condenser and the 3rd absorber, provide respectively double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
Double-generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 40 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 5, increase by the second generator, the 3rd absorber, resolubilization liquid pump and the second solution heat exchanger, the first absorber 1 is had the weak solution pipeline to be communicated with a minute steam chest 8 through solution choke valve 6 and the second absorber 2 to be adjusted into the first absorber 1 has the weak solution pipeline to be communicated with dividing a steam chest 8 through the 3rd solution heat exchanger M and the second absorber 2, to divide steam chest 8 to have the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution pump 5 to be adjusted into minute steam chest 8 has the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution pump 5 and the 3rd solution heat exchanger M, the first evaporimeter C is had the refrigerant vapour passage to be communicated with the first absorber 1 to be adjusted into the first evaporimeter C has the refrigerant vapour passage to be communicated with the 3rd absorber R, the 3rd absorber R also has the weak solution pipeline to be communicated with the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline to be communicated with the 3rd absorber R through the second solution heat exchanger I, the second generator H also has respectively refrigerant vapour passage and the first absorber 1 connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber R also has the heated medium pipeline to be communicated with outside.
2. on flow process, the refrigerant vapour that the first evaporimeter C produces enters the 3rd absorber R, by solution, absorbed also heat release in heated medium, the weak solution of the 3rd absorber R enters the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, driving the thermal medium heating enters the solution release refrigerant vapour of the second generator H and provides to the first absorber 1, the concentrated solution of the second generator H enters the 3rd absorber R through the second solution heat exchanger I, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by the second generator.
Double-generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 41 is achieved in that
1. on structure, in the 3rd class sorption type heat pump shown in Figure 8, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger, the 3rd condenser and increase again choke valve, cancel solution choke valve 6, the first absorber 1 is had the weak solution pipeline to be communicated with the second absorber 2 through solution choke valve 6 to be adjusted into the first absorber 1 has the weak solution pipeline to be communicated with the second absorber 2 through the 3rd solution heat exchanger M, to divide steam chest 8 to have the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution pump 5 to be adjusted into minute steam chest 8 has the concentrated solution pipeline to be communicated with the first absorber 1 through the second solution pump 5 and the 3rd solution heat exchanger M, the first evaporimeter C is had the refrigerant vapour passage to be communicated with the first absorber 1 to be adjusted into the first evaporimeter C has the refrigerant vapour passage to be communicated with the 3rd absorber R, the 3rd absorber R also has the weak solution pipeline to be communicated with the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, the second generator H also has the concentrated solution pipeline to be communicated with the 3rd absorber R through the second solution heat exchanger I, the second generator H also has the refrigerant vapour passage with the 3rd condenser W and the first absorber 1, to be communicated with respectively, the 3rd condenser W also has the cryogen liquid pipeline to be communicated with the first evaporimeter C through increasing choke valve J again, the second generator H drives in addition the thermal medium pipeline and is communicated with outside, the 3rd condenser W and the 3rd absorber R also have respectively the heated medium pipeline to be communicated with outside.
2. on flow process, the refrigerant vapour that the first evaporimeter produces C enters the 3rd absorber R, by solution, is absorbed also heat release in heated medium, the weak solution of the 3rd absorber R enters the second generator H through resolubilization liquid pump K and the second solution heat exchanger I, drive the thermal medium heating and enter the solution release refrigerant vapour of the second generator H and to the 3rd condenser W and the first absorber 1, provide respectively, the concentrated solution of the second generator H enters the 3rd absorber R through the second solution heat exchanger I; The refrigerant vapour heat release that enters the 3rd condenser W becomes cryogen liquid in heated medium, this cryogen liquid enters the first evaporimeter C through increasing choke valve J more again, forms based on the 3rd class absorption-generation systems, by generator, to the 3rd condenser and the 3rd absorber, provides respectively double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
Double-generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 42 is achieved in that
In the 3rd class sorption type heat pump shown in Figure 40, increase by the second cryogen liquid pump, have heated medium pipeline and outside the connection to be adjusted into the first evaporimeter C and to set up the cryogen liquid pipeline and with the 3rd absorber R after the 3rd absorber R is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber 1 through the second cryogen liquid pump P the 3rd absorber R; The cryogen liquid of the first evaporimeter C after the second cryogen liquid pump P pressurization, flow through again the 3rd absorber R, absorb heat into refrigerant vapour and provide to the first absorber 1, form based on the 3rd class absorption-generation systems, by the 3rd absorber and the second generator, jointly to the first absorber, provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.Wherein, can come as the case may be to determine whether the second absorber 2 bears external thermal loads.
Double-generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 43 is achieved in that
In the 3rd class sorption type heat pump shown in Figure 41, increase and to increase choke valve again, having the heated medium pipeline to be communicated with outside to be adjusted into the first condenser A to set up cryogen liquid pipeline the 3rd absorber R after increasing choke valve J again and the 3rd absorber R is communicated with the 3rd absorber R has the refrigerant vapour passage to be communicated with the first absorber 1 again; The cryogen liquid of the first condenser A after increasing again choke valve J throttling, flow through again the 3rd absorber R, absorb heat into refrigerant vapour and provide to the first absorber 1, form based on the 3rd class absorption-generation systems, by the 3rd absorber and the second generator, jointly to the first absorber, provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.Wherein, can come as the case may be to determine whether the second absorber 2 bears external thermal loads.
Double-generator two-stage based on the 3rd class absorption-generation systems the 3rd class absorption heat pump shown in Figure 44 is achieved in that
In the 3rd class sorption type heat pump shown in Figure 36, increase and to increase choke valve again, having the heated medium pipeline to be communicated with outside to be adjusted into the first condenser A to set up cryogen liquid pipeline first absorber 1 after increasing choke valve J again and the first absorber 1 is communicated with the first absorber 1 has the refrigerant vapour passage to be communicated with the 3rd absorber R again; The road cryogen liquid of the first condensation A after increasing again choke valve J throttling, flow through again the first absorber 1, absorb heat into refrigerant vapour and provide to the 3rd absorber R, form based on the 3rd class absorption-generation systems, by the first absorber and generator, jointly to the 3rd absorber, provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
Shown in Figure 45 economic benefits and social benefits the 3rd class absorption heat pump of connecting based on the 3rd class absorption-generation systems, take newly-increased absorber as the single-stage of adding high-temperature heat supply end is achieved in that
1. on structure, in single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump shown in Figure 16, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger and newly-increased choke valve, there is the weak solution pipeline with the second generator H, to be communicated with and to be adjusted into the second absorber 2 and to have the weak solution pipeline to be communicated with newly-increased absorber b1 through the first solution pump 4 and solution heat exchanger 7 through the first solution pump 4 and solution heat exchanger 7 the second absorber 2, newly-increased absorber b1 also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter a1 through newly-increased the first solution heat exchanger d1, newly-increased absorption-evaporimeter a1 also has the weak solution pipeline through newly-increased solution pump c1, newly-increased the first solution heat exchanger d1 and newly-increased the second solution heat exchanger e1 are communicated with the second generator H, there is the concentrated solution pipeline with the second absorber 2, to be communicated with and to be adjusted into generator 3 and the concentrated solution pipeline to be arranged through the second solution heat exchanger I through the second solution heat exchanger I and solution heat exchanger 7 in generator 3, newly-increased the second solution heat exchanger e1 and solution heat exchanger 7 are communicated with the second absorber 2, evaporimeter C sets up the refrigerant vapour passage and is communicated with newly-increased absorption-evaporimeter a1, the first condenser A sets up cryogen liquid pipeline newly-increased absorption-evaporimeter a1 after increasing choke valve f1 newly and newly-increased absorption-evaporimeter a1 is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber b1 again, newly-increased absorber b1 also has the heated medium pipeline to be communicated with outside.
2. on flow process, realize that the flow process of additional high-temperature heat supply end is performed such: the second absorber 2 enters the solution of newly-increased absorber b1 through the first solution pump 4 and solution heat exchanger 7, absorbs from the refrigerant vapour of newly-increased absorption-evaporimeter a1 heat release in heated medium; The weak solution warp of newly-increased absorber b1 increases the first solution heat exchanger d1 newly and enters newly-increased absorption-evaporimeter a1, absorbs the refrigerant vapour of flash-pot C and heat the cryogen liquid that increases absorption-evaporimeter a1 newly of flowing through to become refrigerant vapour; The weak solution of newly-increased absorption-evaporimeter a1 enters the second generator H through newly-increased solution pump c1, newly-increased the first solution heat exchanger d1 and newly-increased the second solution heat exchanger e1; Discharged by the second generator H that aforementioned two parts refrigerant vapour enters the first condenser A, heat release becomes cryogen liquid in heated medium, this cryogen liquid is divided into two-way---and the first via enters evaporimeter C, absorbs waste heat and become refrigerant vapour and provide to newly-increased absorption-evaporimeter a1 through choke valve E, the second tunnel is flowed through again and is increased absorption-evaporimeter a1 newly, absorbs heat into refrigerant vapour and provide to newly-increased absorber b1 after newly-increased choke valve f1 throttling, form single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump take newly-increased absorber as additional high-temperature heat supply end.
Shown in Figure 46 based on the 3rd class absorption-generation systems, take newly-increased absorber, for single-stage single-action the 3rd class absorption heat pump that adds high-temperature heat supply end, be achieved in that
1. on structure, in the 3rd class absorption heat pump shown in Figure 5, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased the first solution heat exchanger, newly-increased the second solution heat exchanger and newly-increased cryogen liquid pump, generator 3 is set up the concentrated solution pipeline and is communicated with newly-increased absorber b1 through newly-increased the second solution heat exchanger e1, newly-increased absorber b1 also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter a1 through newly-increased the first solution heat exchanger d1, newly-increased absorption-evaporimeter a1 also has the weak solution pipeline through newly-increased solution pump c1, newly-increased the first solution heat exchanger d1 and newly-increased the second solution heat exchanger e1 are communicated with generator 3, the second evaporimeter D sets up the refrigerant vapour passage and is communicated with newly-increased absorption-evaporimeter a1, the second evaporimeter D sets up cryogen liquid pipeline newly-increased absorption-evaporimeter a1 after increasing cryogen liquid pump g1 newly and newly-increased absorption-evaporimeter a1 is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber b1 again, newly-increased absorber b1 also has the heated medium pipeline to be communicated with outside.
2. on flow process, realize that the flow process of additional high-temperature heat supply end is performed such: generator 3 enters the solution of newly-increased absorber b1 through newly-increased the second solution heat exchanger e1, absorbs from the refrigerant vapour of newly-increased absorption-evaporimeter a1 heat release in heated medium; The weak solution of newly-increased absorber b1 enters newly-increased absorptions-evaporimeter a1 through newly-increased the first solution heat exchanger d1, absorbs from the refrigerant vapour of the second evaporimeter D the heating cryogen liquid that increases absorption-evaporimeter a1 newly of flowing through and becomes refrigerant vapour; The weak solution of newly-increased absorption-evaporimeter a1 enters generator 3 through newly-increased solution pump c1, newly-increased the first solution heat exchanger d1 and newly-increased the second solution heat exchanger e1; Generator 3 discharges that aforementioned two parts refrigerant vapour enters the first condenser A, heat release becomes cryogen liquid in heated medium, and this cryogen liquid enters the second evaporimeter D through first throttle valve E; This cryogen liquid that enters the second evaporimeter D is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to newly-increased absorption-evaporimeter a1, the second tunnel is flowed through again and is increased absorption-evaporimeter a1 newly, absorbs heat into refrigerant vapour and provide to newly-increased absorber b1 after newly-increased cryogen liquid pump g1 pressurization, form single-stage single-action the 3rd class absorption heat pump take newly-increased absorber as additional high-temperature heat supply end.
Shown in Figure 47 based on the 3rd class absorption-generation systems, take single-stage parallel double-effect three class absorption heat pump of high temperature condenser as additional high-temperature heat supply end, be achieved in that
In single-stage parallel double-effect shown in Figure 10 the 3rd class absorption heat pump, increase high temperature condenser a2 and high temperature choke valve b2, high pressure generator 3 is set up the refrigerant vapour passage and is communicated with high temperature condenser a2, high temperature condenser a2 also has the cryogen liquid pipeline to be communicated with the first condenser A through high temperature choke valve b2, and high temperature condenser a2 also has the heated medium pipeline to be communicated with outside; A part of refrigerant vapour that high pressure generator 3 discharges enters high temperature condenser a2, heat release becomes cryogen liquid in heated medium, the cryogen liquid of high temperature condenser a2 enters the first condenser A through high temperature choke valve b2 throttling, forms the 3rd class absorption heat pump as additional high-temperature heat supply end take high temperature condenser a2.
Shown in Figure 48 based on the 3rd class absorption-generation systems, take single-stage parallel double-effect three class absorption heat pump of high temperature condenser as additional high-temperature heat supply end, be achieved in that
in the 3rd class absorption heat pump shown in Figure 47, increase first flow control valve and second adjustable valve, having respectively heated medium pipeline and outside the connection to be adjusted into outside and the heated medium pipeline to be arranged and be divided into two-way after the first condenser A is communicated with the first condenser A and high temperature condenser a2---the first via has the heated medium pipeline to be communicated with outside through first flow choke valve c2 with high temperature condenser a2 after high temperature condenser a2 is communicated with again, second tunnel the second flow throttle valve d2 is communicated with outside, formation is take adjustable type three class absorption heat pump of high temperature condenser a2 as additional high-temperature heat supply end.
Shown in Figure 49ly based on the 3rd class absorption-generation systems two-stage the 3rd class absorption heat pump take single-stage series connection economic benefits and social benefits as the first order, be achieved in that
1. on structure, in single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump shown in Figure 14, increase secondary absorber, second-stage generator, secondary solution pump and secondary solution heat exchanger, there is the cryogen liquid pipeline with the first condenser A, to be communicated with and to be adjusted into low pressure generator H and to have the cryogen liquid pipeline to be communicated with the second evaporimeter D through increasing again choke valve J through increasing again choke valve J low pressure generator H, low pressure generator H is had the refrigerant vapour passage to be communicated with the first condenser A to be adjusted into low pressure generator H has the refrigerant vapour passage to be communicated with secondary absorber a3, secondary absorber a3 also has the weak solution pipeline to be communicated with second-stage generator b3 through secondary solution pump c3 and secondary solution heat exchanger d3, second-stage generator b3 also has the concentrated solution pipeline to be communicated with secondary absorber a3 through secondary solution heat exchanger d3, second-stage generator b3 also has the refrigerant vapour passage to be communicated with the first condenser A, secondary absorber a3 also has the heated medium pipeline to be communicated with outside, second-stage generator b3 drives in addition the thermal medium pipeline and is communicated with outside.
2. on flow process, the second level flow process of lifting waste heat supply temperature is performed such: a part of refrigerant vapour that low pressure generator H produces enters secondary absorber a3, by the concentrated solution from second-stage generator b3, absorbed also heat release in heated medium, the weak solution of secondary absorber a3 enters second-stage generator b3 through secondary solution pump c3 and secondary solution heat exchanger d3, driving the thermal medium heating enters the solution release refrigerant vapour of second-stage generator b3 and provides to the first condenser A, the concentrated solution of second-stage generator b3 enters secondary absorber a3 through secondary solution heat exchanger d3, formation is take the single-stage economic benefits and social benefits as the first order, two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to secondary absorber by low pressure generator.
Shown in Figure 50ly based on the 3rd class absorption-generation systems the 3rd class absorption heat pump of the two-stage take the single-stage parallel double-effect as the first order, be achieved in that
1. on structure, in single-stage parallel double-effect shown in Figure 11 the 3rd class absorption heat pump, increase secondary absorber, second-stage generator, the secondary solution pump, the secondary solution heat exchanger, secondary condenser and two-step throttle valve, low pressure generator H sets up the refrigerant vapour passage and is communicated with secondary absorber a3, secondary absorber a3 also has the weak solution pipeline to be communicated with second-stage generator b3 through secondary solution pump c3 and secondary solution heat exchanger d3, second-stage generator b3 also has the concentrated solution pipeline to be communicated with secondary absorber a3 through secondary solution heat exchanger d3, second-stage generator b3 also has the refrigerant vapour passage to be communicated with secondary condenser e3, secondary condenser e3 also has the cryogen liquid pipeline to be communicated with the first condenser A through two-step throttle valve f3, secondary absorber a3 and secondary condenser e3 also have respectively the heated medium pipeline to be communicated with outside, second-stage generator b3 drives in addition the thermal medium pipeline and is communicated with outside.
2. on flow process, the second level flow process of lifting waste heat supply temperature is performed such: a part of refrigerant vapour that low pressure generator H produces enters secondary absorber a3, by the concentrated solution from second-stage generator b3, is absorbed also heat release in heated medium, the weak solution of secondary absorber a3 enters second-stage generator b3 through secondary solution pump c3 and secondary solution heat exchanger d3, drive the thermal medium heating and enter the solution release refrigerant vapour of second-stage generator b3 and provide to secondary condenser e3, the concentrated solution of second-stage generator b3 enters secondary absorber a3 through secondary solution heat exchanger d3; The refrigerant vapour heat release that enters secondary condenser e3 becomes cryogen liquid in heated medium, the cryogen liquid of secondary condenser e3 enters the first condenser A through two-step throttle valve f3 throttling, forms take the single-stage economic benefits and social benefits as the first order, by low pressure generator, to the first condenser and secondary absorber, provides respectively two-stage the 3rd class absorption heat pump of refrigerant vapour.
The effect that the technology of the present invention can realize---the 3rd class absorption-generation systems and the 3rd class absorption heat pump proposed by the invention have following effect and advantage:
1. the 3rd class absorption-generation systems, structure and the flow process advantages of simple that propose.With the first kind absorption-generation systems that is comprised of absorber, solution pump, solution heat exchanger and generator, compare, the 3rd class absorption-generation systems that the present invention proposes has mainly increased the second absorber and solution pump, and simple in structure, flow process is reasonable.
2. the 3rd class absorption-generation systems that proposes,---temperature difference between the temperature difference between high temperature driven thermal medium and heated medium and waste heat medium and cooling medium (environment)---, for same absorption-generation systems, is that the generation of the 3rd class absorption heat pump provides the foundation simultaneously by two kinds of driving forces.
3. the 3rd class absorption heat pump that proposes, have first-class absorption type heat pump heat supply temperature height and the excellent double grading of second-kind absorption-type heat pump performance index, can improve the residual heat resources utilization rate.
4. series the 3rd class absorption heat pump that proposes, realized the diversity of absorption heat pump kind having good creativeness, novelty and practicality, can realize better the mutual coupling between heat pump heat supply and user's request.
5. utilize the 3rd class absorption heat pump of the present invention, in residual heat resources than horn of plenty, especially exist take latent heat and while enriching residual heat resources, can realize the further lifting of waste heat supply temperature as main; Can utilize the waste heat of lower temperature and the heat supply of higher temperature is provided to the user, enlarge the temperature operation interval of absorption heat pump, expand and enriched the range of application of absorption heat pump.

Claims (85)

1. the 3rd class absorption-generation systems, mainly by the first absorber, the second absorber, generator, the first solution pump, the second solution pump, the solution choke valve, solution heat exchanger and minute steam chest form, the first absorber (1) has the weak solution pipeline to be communicated with a minute steam chest (8) through solution choke valve (6) and the second absorber (2), divide steam chest (8) to also have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5), the second absorber (2) has the weak solution pipeline to be communicated with generator (3) through the first solution pump (4) and solution heat exchanger (7), generator (3) also has the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7), the first absorber (1) also has respectively heated medium pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, divide steam chest (8) to also have the refrigerant vapour passage be communicated with or have respectively the refrigerant vapour passage to be communicated with outside with outside connected sum cooling medium pipeline with outside, the second absorber (2) also has the refrigerant vapour passage be communicated with or also have respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside with outside, generator (3) also has respectively the thermal medium of driving pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, form two-way circulation the 3rd class absorption-generation systems.
2. the 3rd class absorption-generation systems, in the 3rd class absorption-generation systems claimed in claim 1, when generator is rectifying column, the second absorber (2) has the weak solution pipeline to be communicated with rectifying column through the first solution pump (4) and solution heat exchanger (7), rectifying column also has the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7), rectifying column also has respectively the thermal medium of driving pipeline to be communicated with, to have heated medium pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside with outside, forms two-way circulation the 3rd class absorption-generation systems.
3. the 3rd class absorption-generation systems, mainly by the first absorber, the second absorber, generator, the first solution pump, the second solution pump, solution heat exchanger and a minute steam chest form, the first absorber (1) has the weak solution pipeline to be communicated with the second absorber (2), the second absorber (2) also has the weak solution pipeline to be communicated with generator (3) through the first solution pump (4) and solution heat exchanger (7), generator (3) also has the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2), divide steam chest (8) to also have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5), the first absorber (1) also has respectively heated medium pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, divide steam chest (8) to also have the refrigerant vapour passage to be communicated with outside, the second absorber (2) also has the refrigerant vapour passage be communicated with or also have respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside with outside, generator (3) also has respectively the thermal medium of driving pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, form single channel circulation the 3rd class absorption-generation systems.
4. the 3rd class absorption-generation systems, in the 3rd class absorption-generation systems claimed in claim 3, when generator is rectifying column, the second absorber (2) has the weak solution pipeline to be communicated with rectifying column through the first solution pump (4) and solution heat exchanger (7), rectifying column also has the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2), rectifying column also has respectively the thermal medium of driving pipeline to be communicated with outside, there are heated medium pipeline and outside connected sum to have the refrigerant vapour passage to be communicated with outside, divide steam chest to also have the cooling medium pipeline to be communicated with outside, form single channel circulation the 3rd class absorption-generation systems.
5. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption-generation systems of claim 1-2, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, cryogen liquid pump and choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator (3) and to have the refrigerant vapour passage to be communicated with the first condenser (A) in generator (3), the first condenser (A) also has the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through choke valve (E), to divide steam chest (8) to have refrigerant vapour passage and outside the connection to be defined as a minute steam chest (8) and to have the refrigerant vapour passage to be communicated with the second condenser (B), the second condenser (B) also has the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through cryogen liquid pump (F), there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (C) and to have the refrigerant vapour passage to be communicated with the first absorber (1) the first absorber (1), there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter (D) and to have the refrigerant vapour passage to be communicated with the second absorber (2) the second absorber (2), the first condenser (A) also has the heated medium pipeline to be communicated with outside, the second condenser (B) also has the cooling medium pipeline to be communicated with outside, the first evaporimeter (C) and the second evaporimeter (D) medium pipeline that also has surplus heat respectively is communicated with outside, formation is based on single-stage single-action the 3rd class absorption heat pump of the 3rd class absorption-generation systems, wherein, during without the second evaporimeter (D), the first condenser (A) has the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through choke valve (E), and the first evaporimeter (C) also has the refrigerant vapour passage to be communicated with the second absorber (2).
6. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption-generation systems of claim 3-4, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the cryogen liquid pump, first throttle valve or add the second choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator (3) and to have the refrigerant vapour passage to be communicated with the first condenser (A) in generator (3), to divide steam chest (8) to have refrigerant vapour passage and outside the connection to be defined as a minute steam chest (8) and to have the refrigerant vapour passage to be communicated with the second condenser (B), the second condenser (B) has the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through cryogen liquid pump (F) and the first condenser (A) has the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through first throttle valve (E) and the first evaporimeter (C) connected sum the first evaporimeter (C), or second condenser (B) have the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through cryogen liquid pump (F) and the first condenser (A) has respectively the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through the second choke valve (G) through first throttle valve (E) and the second evaporimeter (D) connected sum, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (C) and to have the refrigerant vapour passage to be communicated with the first absorber (1) the first absorber (1), there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter (D) and to have the refrigerant vapour passage to be communicated with the second absorber (2) the second absorber (2), the first condenser (A) also has the heated medium pipeline to be communicated with outside, the second condenser (B) also has the cooling medium pipeline to be communicated with outside, the first evaporimeter (C) and the second evaporimeter (D) medium pipeline that also has surplus heat respectively is communicated with outside, formation is based on single-stage single-action the 3rd class absorption heat pump of the 3rd class absorption-generation systems, wherein: during 1. without the second evaporimeter (D) and the second choke valve (G), the first condenser (A) has the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through first throttle valve (E), and the first evaporimeter (C) also has the refrigerant vapour passage to be communicated with the second absorber (2), 2. the second absorber (2) is communicated with and while having the second evaporimeter (D) with outside without the heated medium pipeline, cancel the second choke valve (G), the second condenser (B) has the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through cryogen liquid pump (F) and the first condenser (A) has the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through first throttle valve (E) and the first evaporimeter (C) connected sum the first evaporimeter (C), or second condenser (B) have the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through first throttle valve (E) through cryogen liquid pump (F) and the second evaporimeter (D) connected sum the first condenser (A).
7 The third absorption heat pump , is claimed in any one of claim 3-4 wherein the third class of absorption - generating system , throttle solution increases , the first condenser , second condenser , a first evaporator , the second evaporator , the refrigerant pump, the first throttle valve and a second throttle valve, the first absorber ( 1 ) with a dilute solution of the second absorber pipe ( 2 ) is adjusted to the first absorption communicating device ( 1 ) with a dilute solution from the solution line throttle valve ( 6 ) and the second absorber ( 2 ) communicates the generator ( 3 ) with the refrigerant passage communicates with the outside vapor generator identified as ( 3 ) of cold refrigerant vapor passage of the first condenser (A) communicates , the points steam chamber ( 8 ) with the refrigerant vapor passage communicates with the outside of steam determined chamber ( 8) and a second steam passage of the refrigerant condenser (B) communicating , the second condenser (B) a liquid refrigerant through the refrigerant piping pump (F) and the first evaporator (C) and the first condenser communicating (A) a liquid refrigerant through the first flow line valve (E) and the first evaporator (C) and a first evaporator connected (C) with the refrigerant liquid line via a second throttle valve (G) and the second evaporator (D) communicates , or the second condenser device (B) with liquid refrigerant in the refrigerant piping by the pump (F) and the second evaporator (D) and the first condenser communicating (A) a liquid refrigerant line through a first throttle valve (E) the first evaporator (C) and a first evaporator connected (C) with the refrigerant liquid line via a second throttle valve (G) and the second evaporator (D) connecting the first absorber ( 1 ) a refrigerant vapor passage communicating with the outside determined as the first evaporator (C) with the refrigerant vapor passage of the first absorber ( 1 ) communicates , and the second absorber ( 2 ) with the refrigerant vapor passage communicates with the outside determined second evaporator (D) with a second refrigerant vapor passage and the absorber ( 2 ) communicates a first condenser (A) and the heating medium pipe communicates with the outside , the second condenser (B) and cooling medium line communicates with the outside , a first evaporator (C) and the second evaporator (D) were further heat medium pipe communicates with the outside , forming the third type of absorption - generating system efficiency single-stage III absorption heat pump ; wherein : a second absorber ( 2 ) without being heated and the medium line communicates with the outside there is a second evaporator (D) , the second condenser (B) a liquid refrigerant through the refrigerant liquid line pump (F) and the first evaporator (C) and the first condenser communicating (A) a liquid refrigerant line through a first throttle valve (E) and the first evaporator (C) and a first evaporator connected (C) with the refrigerant liquid line via a second throttle valve (G) and the second evaporator (D) communicates , or the second condenser (B) a liquid refrigerant through the refrigerant piping pump (F) and the second evaporator (D) and the first condenser communicating (A) a liquid refrigerant line through a first throttle valve (E) and the first evaporator (C) connected.
8. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption-generation systems of claim 3-4, increase by the 3rd solution pump, the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the cryogen liquid pump, first throttle valve and the second choke valve, the first absorber (1) is had the weak solution pipeline to be communicated with the second absorber (2) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with the second absorber (2) through the 3rd solution pump (9), there are refrigerant vapour passage and outside the connection to be defined as generator (3) and to have the refrigerant vapour passage to be communicated with the first condenser (A) in generator (3), to divide steam chest (8) to have refrigerant vapour passage and outside the connection to be defined as a minute steam chest (8) and to have the refrigerant vapour passage to be communicated with the second condenser (B), the second condenser (B) has the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through cryogen liquid pump (F), the first condenser (A) has the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through the second choke valve (G) through first throttle valve (E) and the first evaporimeter (C) connected sum the first evaporimeter (C), or first condenser (A) have respectively the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through the second choke valve (G) through first throttle valve (E) and the first evaporimeter (C) connected sum, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter (D) and to have the refrigerant vapour passage to be communicated with the first absorber (1) the first absorber (1), there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (C) and to have the refrigerant vapour passage to be communicated with the second absorber (2) the second absorber (2), the first condenser (A) also has the heated medium pipeline to be communicated with outside, the second condenser (B) also has the cooling medium pipeline to be communicated with outside, the first evaporimeter (C) and the second evaporimeter (D) medium pipeline that also has surplus heat respectively is communicated with outside, formation is based on single-stage single-action the 3rd class absorption heat pump of the 3rd class absorption-generation systems, wherein: during 1. without the second evaporimeter (D) and the second choke valve (G), the first condenser (A) has the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through first throttle valve (E), and the first evaporimeter (C) also has the refrigerant vapour passage to be communicated with the first absorber (1), 2. the second absorber (2) is communicated with and while having the second evaporimeter (D) with outside without the heated medium pipeline, and the first condenser (A) has the cryogen liquid pipeline to have the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through the second choke valve (G) or the first condenser (A) has the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through first throttle valve (E) through first throttle valve (E) and the first evaporimeter (C) connected sum the first evaporimeter (C).
9. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase by the second generator, the second solution heat exchanger and increase again choke valve, the first solution pump (4) is set up the weak solution pipeline and is communicated with the second generator (H) through the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline to be communicated with the second absorber (2) through the second solution heat exchanger (I), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator (H) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
10. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase by the second generator, the second solution heat exchanger and increase again choke valve, the first solution pump (4) is set up the weak solution pipeline and is communicated with the second generator (H) through the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline with generator (3), through solution heat exchanger (7) concentrated solution pipeline afterwards, to converge afterwards through the second solution heat exchanger (I), through the second absorber (2), with a minute steam chest (8), be communicated with again, the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator (H) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
11. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, the first absorber (1) is set up the weak solution pipeline and is communicated with the second generator (H) through resolubilization liquid pump (K) and the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution heat exchanger (I), generator (3) is had and drives the thermal medium pipeline and be defined as the second generator (H) and have the refrigerant vapour passage with generator (3), to be communicated with generator (3) afterwards to have the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) again again with outside the connection, the second generator (H) drives in addition the thermal medium pipeline and is communicated with outside, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
12. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, the first absorber (1) is set up the weak solution pipeline and is communicated with the second generator (H) through resolubilization liquid pump (K) and the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution heat exchanger (I), generator (3) is had and drives the thermal medium pipeline and be defined as the second generator (H) and have the refrigerant vapour passage with generator (3), to be communicated with generator (3) afterwards to have the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) again again with outside the connection, the second generator (H) drives in addition the thermal medium pipeline and is communicated with outside, formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
13. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, the first absorber (1) is set up the weak solution pipeline and is communicated with the second generator (H) through resolubilization liquid pump (K) and the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution heat exchanger (I), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator (H) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
14. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, the first absorber (1) is set up the weak solution pipeline and is communicated with the second generator (H) through resolubilization liquid pump (K) and the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution heat exchanger (I), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator (H) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage parallel double-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
15. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 3, increase by the second generator, increase again choke valve and the second solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and the weak solution pipeline to be arranged through the first solution pump (4) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with generator (3), generator (3) is had the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7) to be adjusted into generator (3) has the concentrated solution pipeline to be communicated with the second generator (H) through the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator (H) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
16. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase by the second generator, increase again choke valve and the second solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and the weak solution pipeline to be arranged through the first solution pump (4) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with generator (3), generator (3) is had the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2) to be adjusted into generator (3) has the concentrated solution pipeline to be communicated with the second generator (H) through the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator (H) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
17. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 15-16, the second absorber (2) is had to the weak solution pipeline through the first solution pump (4), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with generator (3) and are adjusted into the second absorber (2) and the weak solution pipeline are arranged through the first solution pump (4), solution heat exchanger (7) directly is communicated with generator (3) through the second solution heat exchanger (I) with the second generator (H) connected sum respectively afterwards again, formation is based on single-stage connection in series-parallel economic benefits and social benefits the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
18. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with the second generator (H) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), the second generator (H) also has the concentrated solution pipeline to be communicated with generator (3) through resolubilization liquid pump (K) and the second solution heat exchanger (I), generator (3) is had the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7) to be adjusted into generator (3) has the concentrated solution pipeline to be communicated with the second absorber (2) through the second solution heat exchanger (I) and solution heat exchanger (7), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator (H) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
19. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase by the second generator, the second solution heat exchanger, increase again choke valve and resolubilization liquid pump, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with the second generator (H) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), the second generator (H) also has the concentrated solution pipeline to be communicated with generator (3) through resolubilization liquid pump (K) and the second solution heat exchanger (I), generator (3) there is is the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2) to be adjusted into generator (3) and the concentrated solution pipeline is arranged through the second solution heat exchanger (I), solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator (H) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage series connection economic benefits and social benefits the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
20. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 18-19, there is the weak solution pipeline with the second generator (H), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline with generator (3) connected sum, with the second generator (H), to be communicated with respectively afterwards through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), form single-stage connection in series-parallel economic benefits and social benefits the 3rd class absorption heat pump based on the 3rd class absorption-generation systems.
21. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, the first solution pump (4) is set up the weak solution pipeline and through the second solution heat exchanger (I), with the second generator (H) connected sum, through the 3rd solution heat exchanger (M), with the 3rd generator (L), is communicated with respectively, the second generator (H) also has the concentrated solution pipeline to be communicated with the second absorber (2) through the second solution heat exchanger (I), the 3rd generator (L) also has the concentrated solution pipeline to be communicated with the second absorber (2) through the 3rd solution heat exchanger (M), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing first throttle valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator (H) also has the refrigerant vapour passage with the 3rd generator (L), to be communicated with the 3rd generator (L) afterwards has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing the second choke valve (N) more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (L) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on the single-stage of the 3rd class absorption-generation systems triple effect the 3rd class absorption heat pump in parallel.
22. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, the first solution pump (4) is set up the weak solution pipeline and through the second solution heat exchanger (I), with the second generator (H) connected sum, through the 3rd solution heat exchanger (M), with the 3rd generator (L), is communicated with respectively, the second generator (H) has the concentrated solution pipeline to have the concentrated solution pipeline all with generator (3), through solution heat exchanger (7) concentrated solution pipeline afterwards, to converge afterwards through the 3rd solution heat exchanger (M) through the second solution heat exchanger (I) the afterwards with three generator (L), through the second absorber (2), with a minute steam chest (8), be communicated with again, the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing first throttle valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator generation is as the driving thermal medium of the second generator, the second generator (H) also has the refrigerant vapour passage with the 3rd generator (L), to be communicated with the 3rd generator (L) afterwards has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing the second choke valve (N) more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (L) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on the single-stage of the 3rd class absorption-generation systems triple effect the 3rd class absorption heat pump in parallel.
23. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 5-8, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber (1) is set up the weak solution pipeline and through the second solution heat exchanger (I), with the second generator (H) connected sum, through the 3rd solution heat exchanger (M), with the 3rd generator (L), is communicated with respectively afterwards through resolubilization liquid pump (K) again again, the second generator (H) also has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution heat exchanger (I), the 3rd generator (L) also has the concentrated solution pipeline to be communicated with the first absorber (1) through the 3rd solution heat exchanger (M), generator (3) is had and drives the thermal medium pipeline and be defined as the second generator (H) and have the refrigerant vapour passage with generator (3), to be communicated with generator (3) afterwards to have the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing first throttle valve (J) again again with outside the connection---the refrigerant vapour of the second generator generation is as the driving thermal medium of generator, the 3rd generator (L) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing the second choke valve (N) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the 3rd generator (L)---and the refrigerant vapour of generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (L) also has the refrigerant vapour passage to be communicated with the first condenser (A), the second generator (H) drives in addition the thermal medium pipeline and is communicated with outside, formation is based on the single-stage of the 3rd class absorption-generation systems triple effect the 3rd class absorption heat pump in parallel.
24. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 5-8, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber (1) is set up the weak solution pipeline and through the second solution heat exchanger (I), with the second generator (H) connected sum, through the 3rd solution heat exchanger (M), with the 3rd generator (L), is communicated with respectively afterwards through resolubilization liquid pump (K) again again, the second generator (H) also has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution heat exchanger (I), the 3rd generator (L) also has the concentrated solution pipeline to be communicated with the first absorber (1) through the 3rd solution heat exchanger (M), generator (3) is had and drives the thermal medium pipeline and be defined as the 3rd generator (L) and have the refrigerant vapour passage with generator (3), to be communicated with generator (3) afterwards to have the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing the second choke valve (N) again again with outside the connection---the refrigerant vapour of the 3rd generator generation is as the driving thermal medium of generator, the second generator (H) also has the refrigerant vapour passage with the 3rd generator (L), to be communicated with the 3rd generator (L) afterwards has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing first throttle valve (J) more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the second generator (H) drives in addition the thermal medium pipeline and is communicated with outside, formation is based on the single-stage of the 3rd class absorption-generation systems triple effect the 3rd class absorption heat pump in parallel.
25. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and the weak solution pipeline to be arranged through the first solution pump (4) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), solution heat exchanger (7), the second solution heat exchanger (I) and the 3rd solution heat exchanger (M) are communicated with generator (3), generator (3) is had the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7) to be adjusted into generator (3) has the concentrated solution pipeline to be communicated with the second generator (H) through the 3rd solution heat exchanger (M), the second generator (H) also has the concentrated solution pipeline to be communicated with the 3rd generator (L) through the second solution heat exchanger (I), the 3rd generator (L) also has the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing first throttle valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator (3) generation is as the driving thermal medium of the second generator (H), the second generator (H) also has the refrigerant vapour passage with the 3rd generator (L), to be communicated with the 3rd generator (L) afterwards has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing the second choke valve (N) more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (L) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage serially connected three-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
26. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and the weak solution pipeline to be arranged through the first solution pump (4) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), solution heat exchanger (7), the second solution heat exchanger (I) and the 3rd solution heat exchanger (M) are communicated with generator (3), generator (3) is had the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2) to be adjusted into generator (3) has the concentrated solution pipeline to be communicated with the second generator (H) through the 3rd solution heat exchanger (M), the second generator (H) also has the concentrated solution pipeline to be communicated with the 3rd generator (L) through the second solution heat exchanger (I), the 3rd generator (L) also has the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing first throttle valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator (3) generation is as the driving thermal medium of the second generator (H), the second generator (H) also has the refrigerant vapour passage with the 3rd generator (L), to be communicated with the 3rd generator (L) afterwards has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing the second choke valve (N) more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (L) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage serially connected three-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
27. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, increase again the first solution pump, increase again the second solution pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with the 3rd generator (L) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), the 3rd generator (L) also has the concentrated solution pipeline to be communicated with the second generator (H) through increasing the first solution pump (K) and the second solution heat exchanger (I) again, the second generator (H) also has the concentrated solution pipeline through increasing the second solution pump (O) and the 3rd solution heat exchanger (M) is communicated with generator (3) again, generator (3) there is is the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7) to be adjusted into generator (3) and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger (M), the second solution heat exchanger (I) and solution heat exchanger (7) are communicated with the second absorber (2), the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing first throttle valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator (3) generation is as the driving thermal medium of the second generator (H), the second generator (H) also has the refrigerant vapour passage with the 3rd generator (L), to be communicated with the 3rd generator (L) afterwards has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing the second choke valve (N) more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (L) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage serially connected three-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
28. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase by the second generator, the 3rd generator, increase again the first throttle valve, increase again the second choke valve, increase again the first solution pump, increase again the second solution pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with the 3rd generator (L) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), the 3rd generator (L) also has the concentrated solution pipeline to be communicated with the second generator (H) through increasing the first solution pump (K) and the second solution heat exchanger (I) again, the second generator (H) also has the concentrated solution pipeline through increasing the second solution pump (O) and the 3rd solution heat exchanger (M) is communicated with generator (3) again, generator (3) there is is the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2) to be adjusted into generator (3) and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger (M), the second solution heat exchanger (I), solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8) and are communicated with, the second generator (H) has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing first throttle valve (J) more again after generator (3) has the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) to have the refrigerant vapour passage to be communicated with the second generator (H)---and the refrigerant vapour of generator (3) generation is as the driving thermal medium of the second generator (H), the second generator (H) also has the refrigerant vapour passage with the 3rd generator (L), to be communicated with the 3rd generator (L) afterwards has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing the second choke valve (N) more again---and the refrigerant vapour of the second generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (L) also has the refrigerant vapour passage to be communicated with the first condenser (A), formation is based on single-stage serially connected three-effect the 3rd class absorption heat pump of the 3rd class absorption-generation systems.
29. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase absorption-evaporimeter, the second cryogen liquid pump and the second solution heat exchanger, to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) and the second solution heat exchanger (I), the first absorber (1) is had the weak solution pipeline to be communicated with a minute steam chest (8) through solution choke valve (6) and the second absorber (2) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with absorption-evaporimeter (Q) through the second solution heat exchanger (I), absorption-evaporimeter (Q) also has the weak solution pipeline to be communicated with a minute steam chest (8) through solution choke valve (6) and the second absorber (2), the first evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into the first evaporimeter (C) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (Q), the first evaporimeter (C) is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P) with absorption-evaporimeter (Q) after absorption-evaporimeter (Q) is communicated with again, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
30. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, cancel the solution choke valve, increase absorption-evaporimeter, the resolubilization liquid pump, the second cryogen liquid pump and the second solution heat exchanger, to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with absorption-evaporimeter (Q) through the second solution pump (5), absorption-evaporimeter (Q) also has the weak solution pipeline to be communicated with the first absorber (1) through resolubilization liquid pump (K) and the second solution heat exchanger (I), the first absorber (1) is had the weak solution pipeline to be communicated with a minute steam chest (8) through solution choke valve (6) and the second absorber (2) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with dividing a steam chest (8) through the second solution heat exchanger (I) and the second absorber (2), the first evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into the first evaporimeter (C) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (Q), the first evaporimeter (C) is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P) with absorption-evaporimeter (Q) after absorption-evaporimeter (Q) is communicated with again, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
31. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 6, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter and the second solution heat exchanger, to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) and the second solution heat exchanger (I), the first absorber (1) is had the weak solution pipeline to be communicated with the second absorber (2) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with absorption-evaporimeter (Q) through the second solution heat exchanger (I), absorption-evaporimeter (Q) also has the weak solution pipeline to be communicated with the second absorber (2), the first evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into the first evaporimeter (C) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (Q), the first condenser (A) is set up cryogen liquid pipeline absorption-evaporimeter (Q) after increasing choke valve (J) again and absorption-evaporimeter (Q) is communicated with has the refrigerant vapour passage to be communicated with the first absorber (1) again, or first evaporimeter (C) set up the cryogen liquid pipeline and with absorption-evaporimeter (Q) after absorption-evaporimeter (Q) is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P), formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
32. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 6, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter, resolubilization liquid pump and the second solution heat exchanger, to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with absorption-evaporimeter (Q) through the second solution pump (5), absorption-evaporimeter (Q) also has the weak solution pipeline to be communicated with the first absorber (1) through resolubilization liquid pump (K) and the second solution heat exchanger (I), the first absorber (1) is had the weak solution pipeline to be communicated with the second absorber (2) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with the second absorber (2) through the second solution heat exchanger (I), the first evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into the first evaporimeter (C) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (Q), the first condenser (A) is set up cryogen liquid pipeline absorption-evaporimeter (Q) after increasing choke valve (J) again and absorption-evaporimeter (Q) is communicated with has the refrigerant vapour passage to be communicated with the first absorber (1) again, or first evaporimeter (C) set up the cryogen liquid pipeline and with absorption-evaporimeter (Q) after absorption-evaporimeter (Q) is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P), formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
33. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 7, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter and the second solution heat exchanger, to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) and the second solution heat exchanger (I), the first absorber (1) is had the weak solution pipeline to be communicated with the second absorber (2) through solution choke valve (6) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with absorption-evaporimeter (Q) through the second solution heat exchanger (I), absorption-evaporimeter (Q) also has the weak solution pipeline to be communicated with the second absorber (2) through solution choke valve (6), the first evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into the first evaporimeter (C) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (Q), the first condenser (A) is set up cryogen liquid pipeline absorption-evaporimeter (Q) after increasing choke valve (J) again and absorption-evaporimeter (Q) is communicated with has the refrigerant vapour passage to be communicated with the first absorber (1) again, or first evaporimeter (C) set up the cryogen liquid pipeline and with absorption-evaporimeter (Q) after absorption-evaporimeter (Q) is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P), formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
34. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 7, cancel the solution choke valve, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter, resolubilization liquid pump and the second solution heat exchanger, to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with absorption-evaporimeter (Q) through the second solution pump (5), absorption-evaporimeter (Q) also has the weak solution pipeline to be communicated with the first absorber (1) through resolubilization liquid pump (K) and the second solution heat exchanger (I), the first absorber (1) is had the weak solution pipeline to be communicated with the second absorber (2) through solution choke valve (6) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with the second absorber (2) through the second solution heat exchanger (I), the first evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into the first evaporimeter (C) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (Q), the first condenser (A) is set up cryogen liquid pipeline absorption-evaporimeter (Q) after increasing choke valve (J) again and absorption-evaporimeter (Q) is communicated with has the refrigerant vapour passage to be communicated with the first absorber (1) again, or first evaporimeter (C) set up the cryogen liquid pipeline and with absorption-evaporimeter (Q) after absorption-evaporimeter (Q) is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P), formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
35. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 8, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter and the second solution heat exchanger, to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) and the second solution heat exchanger (I), the first absorber (1) is had the weak solution pipeline to be communicated with the second absorber (2) through the 3rd solution pump (9) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with absorption-evaporimeter (Q) through the second solution heat exchanger (I), absorption-evaporimeter (Q) also has the weak solution pipeline to be communicated with the second absorber (2) through the 3rd solution pump (9), the first evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into the first evaporimeter (C) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (Q), the first condenser (A) is set up cryogen liquid pipeline absorption-evaporimeter (Q) after increasing choke valve (J) again and absorption-evaporimeter (Q) is communicated with has the refrigerant vapour passage to be communicated with the first absorber (1) again, or first evaporimeter (C) set up the cryogen liquid pipeline and with absorption-evaporimeter (Q) after absorption-evaporimeter (Q) is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P), formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
36. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 8, increase and increase again choke valve or the second cryogen liquid pump, absorption-evaporimeter and the second solution heat exchanger, to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with absorption-evaporimeter (Q) through the second solution pump (5), the first absorber (1) is had the weak solution pipeline to be communicated with the second absorber (2) through the 3rd solution pump (9) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with the second absorber (2) through the second solution heat exchanger (I), absorption-evaporimeter (Q) also has the weak solution pipeline to be communicated with the first absorber (1) through the 3rd solution pump (9) and the second solution heat exchanger (I), the first evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into the first evaporimeter (C) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (Q), the first condenser (A) is set up cryogen liquid pipeline absorption-evaporimeter (Q) after increasing choke valve (J) again and absorption-evaporimeter (Q) is communicated with has the refrigerant vapour passage to be communicated with the first absorber (1) again, or first evaporimeter (C) set up the cryogen liquid pipeline and with absorption-evaporimeter (Q) after absorption-evaporimeter (Q) is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P), formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by absorption-evaporimeter.
37. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase and increase again choke valve or the second cryogen liquid pump, the 3rd absorber and the second solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and the weak solution pipeline to be arranged through the first solution pump (4) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with generator (3), generator (3) is had the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7) to be adjusted into generator (3) has the concentrated solution pipeline to be communicated with the 3rd absorber (R) through the second solution heat exchanger (I), the 3rd absorber (R) also has the weak solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7), there are heated medium pipeline and outside the connection to be adjusted into the first condenser (A) and to have cryogen liquid pipeline first absorber (1) after increasing again choke valve (J) and the first absorber (1) is communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) the first absorber (1), or be adjusted into the second evaporimeter (D) and have the cryogen liquid pipeline with the first absorber (1) after the first absorber (1) is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P), the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber, wherein, when the second evaporimeter, the first condenser (A) has the cryogen liquid pipeline through increasing choke valve (J) and the first absorber (1) after the first absorber (1) is communicated with again and have the refrigerant vapour passage to be communicated with the 3rd absorber (R) again or the first evaporimeter (C) having the cryogen liquid pipeline with the first absorber (1) after the first absorber (1) is communicated with, to have the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P) again.
38. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase and increase again choke valve or the second cryogen liquid pump, the 3rd absorber, resolubilization liquid pump and the second solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with the 3rd absorber (R) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), the 3rd absorber (R) also has the weak solution pipeline to be communicated with generator (3) through resolubilization liquid pump (K) and the second solution heat exchanger (I), generator (3) is had the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7) to be adjusted into generator (3) has the concentrated solution pipeline to be communicated with the second absorber (2) through the second solution heat exchanger (I) and solution heat exchanger (7), there are heated medium pipeline and outside the connection to be adjusted into the first condenser (A) and to have cryogen liquid pipeline first absorber (1) after increasing again choke valve (J) and the first absorber (1) is communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) the first absorber (1), or be adjusted into the second evaporimeter (D) and have the cryogen liquid pipeline with the first absorber (1) after the first absorber (1) is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P), the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber, wherein, when the second evaporimeter, the first condenser (A) has the cryogen liquid pipeline through increasing choke valve (J) and the first absorber (1) after the first absorber (1) is communicated with again and have the refrigerant vapour passage to be communicated with the 3rd absorber (R) again or the first evaporimeter (C) having the cryogen liquid pipeline with the first absorber (1) after the first absorber (1) is communicated with, to have the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P) again.
39. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase and increase again choke valve or the second cryogen liquid pump, the 3rd absorber and the second solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and the weak solution pipeline to be arranged through the first solution pump (4) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with generator (3), generator (3) is had the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2) to be adjusted into generator (3) has the concentrated solution pipeline to be communicated with the 3rd absorber (R) through the second solution heat exchanger (I), the 3rd absorber (R) also has the weak solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2), there are heated medium pipeline and outside the connection to be adjusted into the first condenser (A) and to have cryogen liquid pipeline first absorber (1) after increasing again choke valve (J) and the first absorber (1) is communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) the first absorber (1), or be adjusted into the first evaporimeter (C) and have the cryogen liquid pipeline with the first absorber (1) after the first absorber (1) is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P), the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber.
40. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase and increase again choke valve or the second cryogen liquid pump, the 3rd absorber, resolubilization liquid pump and the second solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with the 3rd absorber (R) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), the 3rd absorber (R) also has the weak solution pipeline to be communicated with generator (3) through resolubilization liquid pump (K) and the second solution heat exchanger (I), generator (3) there is is the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2) to be adjusted into generator (3) and the concentrated solution pipeline is arranged through the second solution heat exchanger (I), solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8), there are heated medium pipeline and outside the connection to be adjusted into the first condenser (A) and to have cryogen liquid pipeline first absorber (1) after increasing again choke valve (J) and the first absorber (1) is communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) the first absorber (1), or be adjusted into the first evaporimeter (C) and have the cryogen liquid pipeline with the first absorber (1) after the first absorber (1) is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P), the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber.
41. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase by the second cryogen liquid pump, the 3rd cryogen liquid pump, the 3rd condenser, the 3rd evaporimeter, the 3rd absorber, the 4th absorber, the second solution heat exchanger, the second solution choke valve, resolubilization liquid pump and second minute steam chest, by the second absorber (2) have the weak solution pipeline through the first solution pump (4) and solution heat exchanger (7) with generator (3), be communicated be adjusted into the second absorber (2) have the weak solution pipeline through the second solution choke valve (V) and the 4th absorber (T) with second minute steam chest (U) be communicated with, second minute steam chest (U) also have the concentrated solution pipeline to be communicated with the 3rd absorber (R) through resolubilization liquid pump (K) and solution heat exchanger (7), the 3rd absorber (R) also has the weak solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7), generator (3) is had the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7) to be adjusted into generator (3) has the concentrated solution pipeline to be communicated with the 4th absorber (T) through the second solution heat exchanger (I), the 4th absorber (T) also has the weak solution pipeline to be communicated with generator (3) through the first solution pump (4) and the second solution heat exchanger (I), the first condenser (A) is had the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through choke valve (E) to be adjusted into the first condenser (A) has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter (X) through choke valve (E), the 3rd evaporimeter (X) also has the refrigerant vapour passage to be communicated with the 4th absorber (T), second minute steam chest (U) also have the refrigerant vapour passage to be communicated with the 3rd condenser (W), the 3rd condenser (W) also has the cryogen liquid pipeline to be communicated with the second evaporimeter (D) through the 3rd cryogen liquid pump (S), there are heated medium pipeline and outside the connection to be adjusted into the second evaporimeter (D) and to have the cryogen liquid pipeline with the first absorber (1) after the first absorber (1) is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P) the first absorber (1), the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, the 3rd condenser (W) also has the cooling medium pipeline to be communicated with outside, the 3rd evaporimeter (X) medium pipeline that also has surplus heat is communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber, wherein, during without the second evaporimeter (D) and the 3rd evaporimeter (X), the first condenser (A) has the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through choke valve (E), the 3rd condenser (W) has the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through the 3rd cryogen liquid pump (S), the first evaporimeter (C) has the cryogen liquid pipeline with the first absorber (1) after the first absorber (1) is communicated with, to have the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P) again, the first evaporimeter (C) also has the refrigerant vapour passage with the second absorber (2) and the 4th absorber (T), to be communicated with respectively.
42. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 7, increase by the second cryogen liquid pump or increase again choke valve, the 3rd cryogen liquid pump, the 3rd condenser, the 3rd evaporimeter, the 3rd absorber, the 4th absorber, the second solution heat exchanger, the second solution choke valve, resolubilization liquid pump and second minute steam chest, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with the 4th absorber (T) through the second solution choke valve (V) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), the 4th absorber (T) also has the weak solution pipeline to be communicated with generator (3) through the first solution pump (4) and the second solution heat exchanger (I), by generator (3) have the concentrated solution pipeline through solution heat exchanger (7) and the second absorber (2) with first minute steam chest (8) be communicated be adjusted into generator (3) have the concentrated solution pipeline through the second solution heat exchanger (I) and the 4th absorber (T) with second minute steam chest (U) be communicated with, second minute steam chest (U) also have the concentrated solution pipeline to be communicated with the 3rd absorber (R) through resolubilization liquid pump (K) and solution heat exchanger (7), the 3rd absorber (R) also have the weak solution pipeline through solution heat exchanger (7) and the second absorber (2) with first minute steam chest (8) be communicated with, second minute steam chest (U) also have the refrigerant vapour passage to be communicated with the 3rd condenser (W), the 3rd condenser (W) also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter (X) through the 3rd cryogen liquid pump (S), the 3rd evaporimeter (X) also has the refrigerant vapour passage to be communicated with the 4th absorber (T), there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter (C) and to have the cryogen liquid pipeline with the first absorber (1) after the first absorber (1) is communicated with, to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P) the first absorber (1), or be adjusted into the first condenser (A) and have cryogen liquid pipeline first absorber (1) after increasing again choke valve (J) the first absorber (1) and being communicated with to have again the refrigerant vapour passage to be communicated with the 3rd absorber (R), the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, the 3rd condenser (W) also has the cooling medium pipeline to be communicated with outside, the 3rd evaporimeter (X) medium pipeline that also has surplus heat is communicated with outside, formation is based on the 3rd class absorption-generation systems, one generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by the first absorber.
43. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 5-8, increase by the second generator, the 3rd absorber, resolubilization liquid pump and the second solution heat exchanger, generator (3) is had the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) has the refrigerant vapour passage to be communicated with the 3rd absorber (R), the 3rd absorber (R) also has the weak solution pipeline to be communicated with the second generator (H) through resolubilization liquid pump (K) and the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline to be communicated with the 3rd absorber (R) through the second solution heat exchange (I), the second generator (H) also has respectively refrigerant vapour passage and the first condenser (A) connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by generator.
44. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and the weak solution pipeline to be arranged through the first solution pump (4) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with the second generator (H), the second generator (H) also has the concentrated solution pipeline to be communicated with the 3rd absorber (R) through the second solution heat exchanger (I), the 3rd absorber (R) also has the weak solution pipeline to be communicated with generator (3) through resolubilization liquid pump (K) and the 3rd solution heat exchanger (M), generator (3) is had the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7) to be adjusted into generator (3) has the concentrated solution pipeline to be communicated with the second absorber (2) through the 3rd solution heat exchanger (M) and solution heat exchanger (7), generator (3) is had the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) has the refrigerant vapour passage to be communicated with the 3rd absorber (R), the second generator (H) also has respectively refrigerant vapour passage and the first condenser (A) connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by generator.
45. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and the weak solution pipeline to be arranged through the first solution pump (4) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with the second generator (H), the second generator (H) also has the concentrated solution pipeline to be communicated with the 3rd absorber (R) through the second solution heat exchanger (I), the 3rd absorber (R) also has the weak solution pipeline to be communicated with generator (3) through resolubilization liquid pump (K) and the 3rd solution heat exchanger (M), generator (3) there is is the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2) to be adjusted into generator (3) and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger (M), solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8), generator (3) is had the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into generator (3) has the refrigerant vapour passage to be communicated with the 3rd absorber (R), the second generator (H) also has respectively refrigerant vapour passage and the first condenser (A) connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the 3rd absorber by generator.
46. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 43, increase by the 3rd condenser and increase again choke valve, the second generator (H) is had the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into the second generator (H) has the refrigerant vapour passage to be communicated with the 3rd condenser (W), generator (3) is set up the refrigerant vapour passage and is communicated with the first condenser (A), the 3rd condenser (W) also has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) again, the 3rd condenser (W) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, by generator, to the first condenser and the 3rd absorber, provide respectively double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
47. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 44-45, increase by the 3rd condenser and increase again choke valve, the second generator (H) is had the refrigerant vapour passage to be communicated with the first condenser (A) to be adjusted into the second generator (H) has the refrigerant vapour passage to be communicated with the 3rd condenser (W), generator (3) is set up the refrigerant vapour passage and is communicated with the first condenser (A), the 3rd condenser (W) also has the cryogen liquid pipeline to be communicated with the first condenser (A) through increasing choke valve (J) again, the 3rd condenser (W) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, by generator, to the first condenser and the 3rd absorber, provide respectively double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
48. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 5, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber (1) is had the weak solution pipeline to be communicated with a minute steam chest (8) through solution choke valve (6) and the second absorber (2) to be adjusted into the first absorber (1) has the weak solution pipeline to be communicated with dividing a steam chest (8) through the 3rd solution heat exchanger (M) and the second absorber (2), to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) and the 3rd solution heat exchanger (M), the first evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into the first evaporimeter (C) has the refrigerant vapour passage to be communicated with the 3rd absorber (R), the 3rd absorber (R) also has the weak solution pipeline to be communicated with the second generator (H) through resolubilization liquid pump (K) and the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline to be communicated with the 3rd absorber (R) through the second solution heat exchanger (I), the second generator (H) also has respectively refrigerant vapour passage and the first absorber (1) connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by the second generator.
49. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 6-8, increase by the second generator, the 3rd absorber, the resolubilization liquid pump, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber (1) is had to the weak solution pipeline directly or be communicated with the second absorber (2) through solution choke valve (6) or through resolubilization liquid pump (K) and all be adjusted into the first absorber (1) and have the weak solution pipeline to be communicated with the second absorber (2) through the 3rd solution heat exchanger (M), to divide steam chest (8) to have the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) to be adjusted into a minute steam chest (8) has the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution pump (5) and the 3rd solution heat exchanger (M), the first evaporimeter (C) is had the refrigerant vapour passage to be communicated with the first absorber (1) to be adjusted into the first evaporimeter (C) has the refrigerant vapour passage to be communicated with the 3rd absorber (R), the 3rd absorber (R) also has the weak solution pipeline to be communicated with the second generator (H) through resolubilization liquid pump (K) and the second solution heat exchanger (I), the second generator (H) also has the concentrated solution pipeline to be communicated with the 3rd absorber (R) through the second solution heat exchanger (I), the second generator (H) also has respectively refrigerant vapour passage and the first absorber (1) connected sum to have the thermal medium of driving pipeline to be communicated with outside, the 3rd absorber (R) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to the first absorber by the second generator.
50. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 48-49, increase by the 3rd condenser and increase again choke valve, the second generator (H) is set up the refrigerant vapour passage and is communicated with the 3rd condenser (W), the 3rd condenser (W) also has the cryogen liquid pipeline to be communicated with the first evaporimeter (C) through increasing choke valve (J) again, the 3rd condenser (W) also has the heated medium pipeline to be communicated with outside, formation is based on the 3rd class absorption-generation systems, by the second generator, to the 3rd condenser and the first absorber, provide respectively double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
51. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 48, increase by the second cryogen liquid pump, there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter (C) and to set up the cryogen liquid pipeline and with the 3rd absorber (R) after the 3rd absorber (R) is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P) the 3rd absorber (R), formation is based on the 3rd class absorption-generation systems, by the 3rd absorber and the second generator, jointly to the first absorber, provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
52. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 49, increase by the second cryogen liquid pump or increase again choke valve, there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter (C) and to set up the cryogen liquid pipeline and with the 3rd absorber (R) after the 3rd absorber (R) is communicated with, have again the refrigerant vapour passage to be communicated with the first absorber (1) through the second cryogen liquid pump (P) the 3rd absorber (R), or be adjusted into the first condenser (A) and set up cryogen liquid pipeline the 3rd absorber (R) after increasing again choke valve (J) and the 3rd absorber (R) is communicated with and have again the refrigerant vapour passage to be communicated with the first absorber (1), formation is based on the 3rd class absorption-generation systems, by the 3rd absorber and the second generator, jointly to the first absorber, provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour.
53. the 3rd class absorption heat pump, described in claim 43, the second absorber is without in heated medium pipeline and outside arbitrary the 3rd class absorption heat pump that is communicated with, increase by the second cryogen liquid pump or increase again choke valve, there are heated medium pipeline and outside the connection to be adjusted into the second evaporimeter (D) and to set up the cryogen liquid pipeline and with the first absorber (1) after the first absorber (1) is communicated with, have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P) the first absorber (1), or be adjusted into the first condenser (A) and set up cryogen liquid pipeline first absorber (1) after increasing again choke valve (J) and the first absorber (1) is communicated with and have again the refrigerant vapour passage to be communicated with the 3rd absorber (R), formation is based on the 3rd class absorption-generation systems, by the first absorber and generator, jointly to the 3rd absorber, provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour, wherein, when the second evaporimeter, having the heated medium pipeline to be communicated with outside to be adjusted into the first evaporimeter (C) to set up the cryogen liquid pipeline the first absorber (1) has the refrigerant vapour passage to be communicated with the 3rd absorber (R) again or is adjusted into the first condenser (A) through the second cryogen liquid pump (P) and the first absorber (1) after the first absorber (1) is communicated with and set up cryogen liquid pipeline first absorber (1) after increasing choke valve (J) again and the first absorber (1) is communicated with and have the refrigerant vapour passage to be communicated with the 3rd absorber (R) again.
54. the 3rd class absorption heat pump, described at claim 44-45, the second absorber is without in heated medium pipeline and outside arbitrary the 3rd class absorption heat pump that is communicated with, increase by the second cryogen liquid pump or increase again choke valve, there are heated medium pipeline and outside the connection to be adjusted into the second evaporimeter (D) and to set up the cryogen liquid pipeline and with the first absorber (1) after the first absorber (1) is communicated with, have again the refrigerant vapour passage to be communicated with the 3rd absorber (R) through the second cryogen liquid pump (P) the first absorber (1), or be adjusted into the first condenser (A) and set up cryogen liquid pipeline first absorber (1) after increasing again choke valve (J) and the first absorber (1) is communicated with and have again the refrigerant vapour passage to be communicated with the 3rd absorber (R), formation is based on the 3rd class absorption-generation systems, by the first absorber and generator, jointly to the 3rd absorber, provide double-generator two-stage the 3rd class absorption heat pump of refrigerant vapour, wherein, when the second evaporimeter, having the heated medium pipeline to be communicated with outside to be adjusted into the first evaporimeter (C) to set up the cryogen liquid pipeline the first absorber (1) has the refrigerant vapour passage to be communicated with the 3rd absorber (R) again or is adjusted into the first condenser (A) through the second cryogen liquid pump (P) and the first absorber (1) after the first absorber (1) is communicated with and set up cryogen liquid pipeline first absorber (1) after increasing choke valve (J) again and the first absorber (1) is communicated with and have the refrigerant vapour passage to be communicated with the 3rd absorber (R) again.
55. the 3rd class absorption heat pump, in claim 5, 11, 29-30, 48, 51 and based on the claim 24 of two-way circulation the 3rd class absorption-generation systems, in 50 described arbitrary the 3rd class absorption heat pumps, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with generator (3), there is the concentrated solution pipeline to be communicated with the second absorber (2) through solution heat exchanger (7) to be adjusted into generator (3) to have the concentrated solution pipeline to be communicated with the second absorber (2) through newly-increased the second solution heat exchanger (e1) and solution heat exchanger (7) in generator (3), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
56. the 3rd class absorption heat pump, at claim 6-8, 12, 31-36, 49, 52 and based on the claim 24 of single channel circulation the 3rd class absorption-generation systems, in 50 described arbitrary the 3rd class absorption heat pumps, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with generator (3), generator (3) there is is the concentrated solution pipeline to be communicated with a minute steam chest (8) through solution heat exchanger (7) and the second absorber (2) to be adjusted into generator (3) and the concentrated solution pipeline is arranged through increasing the second solution heat exchanger (e1) newly, solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
57. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 9, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator (H), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and the second solution heat exchanger (I) through the first solution pump (4) and the second solution heat exchanger (I) the second absorber (2), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the second generator (H), there is the concentrated solution pipeline to be communicated with the second absorber (2) through the second solution heat exchanger (I) to be adjusted into the second generator (H) to have the concentrated solution pipeline to be communicated with the second absorber (2) through newly-increased the second solution heat exchanger (e1) and the second solution heat exchanger (I) in the second generator (H), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (a1) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
58. the 3rd class absorption heat pump, in arbitrary the 3rd class absorption heat pump claimed in claim 10, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator (H), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and the second solution heat exchanger (I) through the first solution pump (4) and the second solution heat exchanger (I) the second absorber (2), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the second generator (H), the second generator (H) there is is the concentrated solution pipeline to be communicated with a minute steam chest (8) through the second solution heat exchanger (I) and the second absorber (2) to be adjusted into the second generator (H) and the concentrated solution pipeline is arranged through increasing the second solution heat exchanger (e1) newly, the second solution heat exchanger (I) and the second absorber (2) are communicated with a minute steam chest (8), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
59. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 13-14, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator (H), to be communicated with and to be adjusted into the first absorber (1) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through resolubilization liquid pump (K) and the second solution heat exchanger (I) through resolubilization liquid pump (K) and the second solution heat exchanger (I) the first absorber (1), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the second generator (H), there is the concentrated solution pipeline to be communicated with the first absorber (1) through the second solution heat exchanger (I) to be adjusted into the second generator (H) to have the concentrated solution pipeline to be communicated with the first absorber (1) through newly-increased the second solution heat exchanger (e1) and the second solution heat exchanger (I) in the second generator (H), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (a1) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
60. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 15-17, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, the second absorber (2) is had to the weak solution pipeline through the first solution pump (4), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with generator (3) and are adjusted into the second absorber (2) and the weak solution pipeline are arranged through the first solution pump (4), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with generator (3), there is the concentrated solution pipeline to be communicated with the second generator (H) through the second solution heat exchanger (I) to be adjusted into generator (3) the concentrated solution pipeline to be arranged through newly-increased the second solution heat exchanger (e1) in generator (3), the second solution heat exchanger (I) is communicated with the second generator (H), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
61. the 3rd class absorption heat pump, in claim 18 and described arbitrary the 3rd class absorption heat pump of claim 20 based on two-way circulation the 3rd class absorption-generation systems, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator (H), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the second generator (H), there is the concentrated solution pipeline with the second absorber (2), to be communicated with and to be adjusted into generator (3) and the concentrated solution pipeline to be arranged through the second solution heat exchanger (I) through the second solution heat exchanger (I) and solution heat exchanger (7) in generator (3), newly-increased the second solution heat exchanger (e1) and solution heat exchanger (7) are communicated with the second absorber (2), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
62. the 3rd class absorption heat pump, in claim 19 and described arbitrary the 3rd class absorption heat pump of claim 20 based on single channel circulation the 3rd class absorption-generation systems, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator (H), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the second generator (H), generator (3) is had to the concentrated solution pipeline through the second solution heat exchanger (I), solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8) and are adjusted into generator (3) and the concentrated solution pipeline are arranged through the second solution heat exchanger (I), newly-increased the second solution heat exchanger (e1), solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
63. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 21, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the 3rd generator (L), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and the 3rd solution heat exchanger (M) through the first solution pump (4) and the 3rd solution heat exchanger (M) the second absorber (2), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the 3rd generator (L), there is the concentrated solution pipeline to be communicated with the second absorber (2) through the 3rd solution heat exchanger (M) to be adjusted into the 3rd generator (L) to have the concentrated solution pipeline to be communicated with the second absorber (2) through newly-increased the second solution heat exchanger (e1) and the 3rd solution heat exchanger (M) in the 3rd generator (L), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
64. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 22, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the 3rd generator (L), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and the 3rd solution heat exchanger (M) through the first solution pump (4) and the 3rd solution heat exchanger (M) the second absorber (2), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the 3rd generator (L), the 3rd generator (L) there is is the concentrated solution pipeline to be communicated with a minute steam chest (8) through the 3rd solution heat exchanger (M) and the second absorber (2) to be adjusted into the 3rd generator (L) and the concentrated solution pipeline is arranged through increasing the second solution heat exchanger (e1) newly, the 3rd solution heat exchanger (M) and the second absorber (2) are communicated with a minute steam chest (8), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
65. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 23, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the 3rd generator (L), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through resolubilization liquid pump (K) and the 3rd solution heat exchanger (M) through resolubilization liquid pump (K) and the 3rd solution heat exchanger (M) the first absorber (1), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the 3rd generator (L), there is the concentrated solution pipeline to be communicated with the first absorber (1) through the 3rd solution heat exchanger (M) to be adjusted into the 3rd generator (L) to have the concentrated solution pipeline to be communicated with the first absorber (1) through newly-increased the second solution heat exchanger (e1) and the 3rd solution heat exchanger (M) in the 3rd generator (L), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
66. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 25-26, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, the second absorber (2) is had to the weak solution pipeline through the first solution pump (4), solution heat exchanger (7), the second solution heat exchanger (I) and the 3rd solution heat exchanger (M) are communicated with generator (3) and are adjusted into the second absorber (2) and the weak solution pipeline are arranged through the first solution pump (4), solution heat exchanger (7), the second solution heat exchanger (I) and the 3rd solution heat exchanger (M) are communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with generator (3), there is the concentrated solution pipeline to be communicated with the second generator (H) through the 3rd solution heat exchanger (M) to be adjusted into generator (3) to have the concentrated solution pipeline to be communicated with the second generator (H) through newly-increased the second solution heat exchanger (e1) and the 3rd solution heat exchanger (M) in generator (3), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
67. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 27, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the 3rd generator (L), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the 3rd generator (L), generator (3) is had to the concentrated solution pipeline through the 3rd solution heat exchanger (M), the second solution heat exchanger (I) and solution heat exchanger (7) are communicated with the second absorber (2) and are adjusted into the 3rd generator (L) and the concentrated solution pipeline are arranged through the 3rd solution heat exchanger (M), the second solution heat exchanger (I), newly-increased the second solution heat exchanger (e1) and solution heat exchanger (7) are communicated with the second absorber (2), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
68. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 28, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the 3rd generator (L), to be communicated with and to be adjusted into the second absorber (2) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and solution heat exchanger (7) through the first solution pump (4) and solution heat exchanger (7) the second absorber (2), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the 3rd generator (L), generator (3) is had to the concentrated solution pipeline through the 3rd solution heat exchanger (M), the second solution heat exchanger (I), solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8) and are adjusted into the 3rd generator (L) and the concentrated solution pipeline are arranged through the 3rd solution heat exchanger (M), the second solution heat exchanger (I), newly-increased the second solution heat exchanger (e1), solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
69. the 3rd class absorption heat pump, in claim 37, in 39 described arbitrary the 3rd class absorption heat pumps, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, the second absorber (2) is had to the weak solution pipeline through the first solution pump (4), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with generator (3) and are adjusted into the second absorber (2) and the weak solution pipeline are arranged through the first solution pump (4), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with generator (3), there is the concentrated solution pipeline to be communicated with the 3rd absorber (R) through the second solution heat exchanger (I) to be adjusted into generator (3) to have the concentrated solution pipeline to be communicated with the 3rd absorber (R) through newly-increased the second solution heat exchanger (e1) and the second solution heat exchanger (I) in generator (3), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
70. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 38, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the 3rd absorber (R) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through resolubilization liquid pump (K) and the second solution heat exchanger (I) through resolubilization liquid pump (K) and the second solution heat exchanger (I) the 3rd absorber (R), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with generator (3), there is the concentrated solution pipeline with the second absorber (2), to be communicated with and to be adjusted into generator (3) and the concentrated solution pipeline to be arranged through newly-increased the second solution heat exchanger (e1) through the second solution heat exchanger (I) and solution heat exchanger (7) in generator (3), the second solution heat exchanger (I) and solution heat exchanger (7) are communicated with the second absorber (2), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
71. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 40, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the 3rd absorber (R) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through resolubilization liquid pump (K) and the second solution heat exchanger (I) through resolubilization liquid pump (K) and the second solution heat exchanger (I) the 3rd absorber (R), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with generator (3), generator (3) is had to the concentrated solution pipeline through the second solution heat exchanger (I), solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8) and are adjusted into generator (3) and the concentrated solution pipeline are arranged through increasing the second solution heat exchanger (e1) newly, the second solution heat exchanger (I), solution heat exchanger (7) and the second absorber (2) are communicated with a minute steam chest (8), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
72. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 41, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the 4th absorber (T) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and the second solution heat exchanger (I) through the first solution pump (4) and the second solution heat exchanger (I) the 4th absorber (T), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with generator (3), there is the concentrated solution pipeline to be communicated with the 4th absorber (T) through the second solution heat exchanger (I) to be adjusted into generator (3) to have the concentrated solution pipeline to be communicated with the 4th absorber (T) through newly-increased the second solution heat exchanger (e1) and the second solution heat exchanger (I) in generator (3), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
73. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 42, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with generator (3), to be communicated with and to be adjusted into the 4th absorber (T) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through the first solution pump (4) and the second solution heat exchanger (I) through the first solution pump (4) and the second solution heat exchanger (I) the 4th absorber (T), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with generator (3), by generator (3) have the concentrated solution pipeline through the second solution heat exchanger (I) and the 4th absorber (T) with second minute steam chest (U) be communicated with and be adjusted into generator (3) and the concentrated solution pipeline arranged through newly-increased the second solution heat exchanger (e1), the second solution heat exchanger (I) and the 4th absorber (T) with second minute steam chest (U) be communicated with, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
74. the 3rd class absorption heat pump, in claim 43, 46, in 53 described arbitrary the 3rd class absorption heat pumps, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, there is the weak solution pipeline with the second generator (H), to be communicated with and to be adjusted into the 3rd absorber (R) and to have the weak solution pipeline to be communicated with newly-increased absorber (b1) through resolubilization liquid pump (K) and the second solution heat exchanger (I) through resolubilization liquid pump (K) and the second solution heat exchanger (I) the 3rd absorber (R), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the second generator (H), there is the concentrated solution pipeline to be communicated with the 3rd absorber (R) through the second solution heat exchanger (I) to be adjusted into the second generator (H) to have the concentrated solution pipeline to be communicated with the 3rd absorber (R) through newly-increased the second solution heat exchanger (e1) and the second solution heat exchanger (I) in the second generator (H), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
75. the 3rd class absorption heat pump, at claim 44-45, 47, in 54 described arbitrary the 3rd class absorption heat pumps, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, the second absorber (2) is had to the weak solution pipeline through the first solution pump (4), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with the second generator (H) and are adjusted into the second absorber (2) and the weak solution pipeline are arranged through the first solution pump (4), solution heat exchanger (7) and the second solution heat exchanger (I) are communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the second generator (H), there is the concentrated solution pipeline to be communicated with the 3rd absorber (R) through the second solution heat exchanger (I) to be adjusted into the second generator (H) to have the concentrated solution pipeline to be communicated with the 3rd absorber (R) through newly-increased the second solution heat exchanger (e1) and the second solution heat exchanger (I) in the second generator (H), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser (A) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
76. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 9-28, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, low pressure generator is set up the concentrated solution pipeline and is communicated with newly-increased absorber (b1) through newly-increased the second solution heat exchanger (e1), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with low pressure generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
77. the 3rd class absorption heat pump, at claim 5-8, 29-42, in described arbitrary the 3rd class absorption heat pump of 48-52, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, generator (3) is set up the concentrated solution pipeline and is communicated with newly-increased absorber (b1) through newly-increased the second solution heat exchanger (e1), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with generator (3), refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
78. the 3rd class absorption heat pump, at claim 43-47, in described arbitrary the 3rd class absorption heat pump of 53-54, increase newly-increased absorption-evaporimeter, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased choke valve or newly-increased cryogen liquid pump, the second generator is set up the concentrated solution pipeline and is communicated with newly-increased absorber (b1) through newly-increased the second solution heat exchanger (e1), newly-increased absorber (b1) also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (a1) through newly-increased solution heat exchanger (d1), newly-increased absorption-evaporimeter (a1) also has the weak solution pipeline through newly-increased solution pump (c1), newly-increased solution heat exchanger (d1) and newly-increased the second solution heat exchanger (e1) are communicated with the second generator, refrigerant vapour provides device to set up the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (a1), the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (a1) after increasing choke valve (f1) newly and newly-increased absorption-evaporimeter (a1) is communicated with has the refrigerant vapour passage to be communicated with newly-increased absorber (b1) again, or cryogen liquid provide device set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (g1) with increase absorption-evaporimeter (a1) newly after newly-increased absorption-evaporimeter (a1) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (b1), newly-increased absorber (b1) also has the heated medium pipeline to be communicated with outside, three class absorption heat pump of formation take newly-increased absorber (b1) as additional high-temperature heat supply end.
79. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 9-28, increase high temperature condenser (a2) and high temperature choke valve (b2), high pressure generator is set up the refrigerant vapour passage and is communicated with high temperature condenser (a2), high temperature condenser (a2) also has the cryogen liquid pipeline to be communicated with the first condenser (A) through high temperature choke valve (b2), high temperature condenser (a2) also has the heated medium pipeline to be communicated with outside, forms take three class absorption heat pump of high temperature condenser (a2) as additional high-temperature heat supply end.
80. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 21-28, increase high temperature condenser (a2) and high temperature choke valve (b2), middle pressure generator is set up the refrigerant vapour passage and is communicated with high temperature condenser (a2), high temperature condenser (a2) also has the cryogen liquid pipeline to be communicated with the first condenser (A) through high temperature choke valve (b2), high temperature condenser (a2) also has the heated medium pipeline to be communicated with outside, forms take three class absorption heat pump of high temperature condenser (a2) as additional high-temperature heat supply end.
81. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 79-80, increase first flow control valve and second adjustable valve, having respectively heated medium pipeline and outside the connection to be adjusted into outside and the heated medium pipeline to be arranged and be divided into two-way after the first condenser (A) is communicated with the first condenser (A) and high temperature condenser (a2)---the first via has the heated medium pipeline to be communicated with outside through first flow choke valve (c2) with high temperature condenser (a2) after high temperature condenser (a2) is communicated with again, second tunnel the second flow throttle valve (d2) is communicated with outside, formation is take adjustable type three class absorption heat pump of high temperature condenser (a2) as additional high-temperature heat supply end.
82. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 9-20, increase secondary absorber, second-stage generator, secondary solution pump and secondary solution heat exchanger, there is the cryogen liquid pipeline with the first condenser, to be communicated with and to be adjusted into low pressure generator and to have the cryogen liquid pipeline to be communicated with the second evaporimeter through increasing again choke valve through increasing again choke valve low pressure generator, low pressure generator is had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into low pressure generator has the refrigerant vapour passage to be communicated with secondary absorber (a3), secondary absorber (a3) also has the weak solution pipeline to be communicated with second-stage generator (b3) through secondary solution pump (c3) and secondary solution heat exchanger (d3), second-stage generator (b3) also has the concentrated solution pipeline to be communicated with secondary absorber (a3) through secondary solution heat exchanger (d3), second-stage generator (b3) also has the refrigerant vapour passage to be communicated with the first condenser, secondary absorber (a3) also has the heated medium pipeline to be communicated with outside, second-stage generator (b3) drives in addition the thermal medium pipeline and is communicated with outside, formation is take the single-stage economic benefits and social benefits as the first order, two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to secondary absorber by low pressure generator, wherein, while only having the first evaporimeter, low pressure generator has the cryogen liquid pipeline to be communicated with the first evaporimeter through increasing choke valve again.
83. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 9-20, increase secondary absorber, second-stage generator, the secondary solution pump, the secondary solution heat exchanger, secondary condenser and two-step throttle valve, low pressure generator is set up refrigerant vapour and is communicated with secondary absorber (a3), secondary absorber (a3) also has the weak solution pipeline to be communicated with second-stage generator (b3) through secondary solution pump (c3) and secondary solution heat exchanger (d3), second-stage generator (b3) also has the concentrated solution pipeline to be communicated with secondary absorber (a3) through secondary solution heat exchanger (d3), second-stage generator (b3) also has the refrigerant vapour passage to be communicated with secondary condenser (e3), secondary condenser (e3) also has the cryogen liquid pipeline to be communicated with the first condenser through two-step throttle valve (f3), secondary absorber (a3) and secondary condenser (e3) also have respectively the heated medium pipeline to be communicated with outside, second-stage generator (b3) drives in addition the thermal medium pipeline and is communicated with outside, formation is take the single-stage economic benefits and social benefits as the first order, by low pressure generator, to the first condenser and secondary absorber, provide respectively two-stage the 3rd class absorption heat pump of refrigerant vapour.
84. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 21-28, increase secondary absorber, second-stage generator, secondary solution pump and secondary solution heat exchanger, there is the cryogen liquid pipeline with the first condenser, to be communicated with and to be adjusted into middle pressure generator and to have the cryogen liquid pipeline to be communicated with the second evaporimeter through increasing again the first throttle valve through increasing again the first throttle valve in middle pressure generator, there is the cryogen liquid pipeline with the first condenser, to be communicated with and to be adjusted into low pressure generator and to have the cryogen liquid pipeline to be communicated with the second evaporimeter through increasing again the second choke valve through increasing again the second choke valve low pressure generator, low pressure generator is had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into low pressure generator has the refrigerant vapour passage to be communicated with secondary absorber (a3), secondary absorber (a3) also has the weak solution pipeline to be communicated with second-stage generator (b3) through secondary solution pump (c3) and secondary solution heat exchanger (d3), second-stage generator (b3) also has the concentrated solution pipeline to be communicated with secondary absorber (a3) through secondary solution heat exchanger (d3), second-stage generator (b3) also has the refrigerant vapour passage to be communicated with the first condenser, secondary absorber (a3) also has the heated medium pipeline to be communicated with outside, second-stage generator (b3) drives in addition the thermal medium pipeline and is communicated with outside, formation is take the single-stage triple effect as the first order, two-stage the 3rd class absorption heat pump of refrigerant vapour is provided to secondary absorber by low pressure generator, wherein, while only having the first evaporimeter, middle pressure generator has the cryogen liquid pipeline to be communicated with the first evaporimeter through increasing choke valve again, and low pressure generator has the cryogen liquid pipeline to be communicated with the first evaporimeter through increasing the second choke valve again.
85. the 3rd class absorption heat pump, in described arbitrary the 3rd class absorption heat pump of claim 21-28, increase secondary absorber, second-stage generator, the secondary solution pump, the secondary solution heat exchanger, secondary condenser and two-step throttle valve, low pressure generator is set up refrigerant vapour and is communicated with secondary absorber (a3), secondary absorber (a3) also has the weak solution pipeline to be communicated with second-stage generator (b3) through secondary solution pump (c3) and secondary solution heat exchanger (d3), second-stage generator (b3) also has the concentrated solution pipeline to be communicated with secondary absorber (a3) through secondary solution heat exchanger (d3), second-stage generator (b3) also has the refrigerant vapour passage to be communicated with secondary condenser (e3), secondary condenser (e3) also has the cryogen liquid pipeline to be communicated with the first condenser through two-step throttle valve (f3), secondary absorber (a3) and secondary condenser (e3) also have respectively the heated medium pipeline to be communicated with outside, second-stage generator (b3) drives in addition the thermal medium pipeline and is communicated with outside, formation is take the single-stage triple effect as the first order, by low pressure generator, to the first condenser and secondary absorber, provide respectively two-stage the 3rd class absorption heat pump of refrigerant vapour.
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