CN103940140A - Shunting circulation first-class absorption heat pump - Google Patents

Shunting circulation first-class absorption heat pump Download PDF

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Publication number
CN103940140A
CN103940140A CN201410165941.0A CN201410165941A CN103940140A CN 103940140 A CN103940140 A CN 103940140A CN 201410165941 A CN201410165941 A CN 201410165941A CN 103940140 A CN103940140 A CN 103940140A
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newly
generator
increased
communicated
solution
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CN103940140B (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
    • F25B30/00—Heat pumps
    • F25B30/04—Heat pumps of the sorption type
    • 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
    • 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
    • F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
    • 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
    • F25B27/00—Machines, plants or systems, using particular sources of energy
    • F25B27/02—Machines, plants or systems, using particular sources of energy using waste heat, e.g. from internal-combustion engines
    • 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
    • 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
    • Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • 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 shunting circulation first-class absorption heat pump and belongs to the technical field of refrigeration and heat pumps. A generator, an absorber, a solution pump and a solution heat exchanger form a solution loop, and then a second generator, a throttling valve and an evaporator are additionally arranged to form a single-effect high temperature flow path; the second generator, a third generator, a fourth generator, a second absorber, a third absorber, a second solution pump, a third solution pump, a second solution heat exchanger, a third solution heat exchanger and a fourth solution heat exchanger form a solution loop, and then a condenser, a second evaporator, a second throttling valve and a third throttling valve are additionally arranged to form a double-effect low temperature flow path with a heat return flow path; the generator provides drive steam for the second generator, the absorber, the second absorber, the third absorber and the condenser supply heat outwards, and the shunting circulation first-class absorption heat pump is formed.

Description

First-class absorption type heat pump along separate routes circulates
Technical field:
The invention belongs to low temperature heat and absorption type heat pump.
Background technology:
Utilize angle from the temperature difference, first-class absorption type heat pump is using the temperature difference between driving thermal medium and heated medium as driving force, when drive the temperature difference should adopt twice when larger or repeatedly the temperature difference utilize flow process to improve the degree that the temperature difference is utilized, thereby realize the high efficiency of heat energy utilization; And from the angle of working media, the working media of absorption heat pump is solution, is subject to the restriction of physical property, each solution has its applicable working range; Like this, in the time driving the temperature of thermal medium and temperature drop to exceed the working range of single solution, should adopt different solution to carry out having circulated along separate routes to driving making full use of of the temperature difference, drive the temperature difference in pyrosol loop and cryogenic fluid loop, to be used respectively, realize the rationalization that drives the temperature difference to utilize.
In considering to make full use of the temperature difference, the circulation process of first-class absorption type heat pump also will be realized more requirement, and these requirements comprise: thermodynamic parameter smooth change, and heating parameter is adjustable, adaptation condition changes preferably, has best performance index; Can realize the deep exploitation to high temperature heat source, or utilize the thermal source of different grades to realize its comprehensive utilization etc.
In cryogenic fluid loop, double-effect process, in conjunction with single-action backheat and economic benefits and social benefits backheat, is the serial indispensable flow process of first-class absorption type heat pump that circulates along separate routes, is the important technology of realizing the required shunt circulation of above-mentioned requirements first-class absorption type heat pump.
Summary of the invention:
Main purpose of the present invention is that the serial first-class absorption type heat pump that circulates along separate routes will be provided, and adopts two-way solution circulation, progressively realizes making full use of of the temperature difference, and concrete summary of the invention subitem is described below:
1. the first-class absorption type heat pump that circulates along separate routes, is mainly made up of generator, the second generator, the 3rd generator, the 4th generator, absorber, the second absorber, the 3rd absorber, condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, the 3rd solution pump, choke valve, the second choke valve, the 3rd choke valve, solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and the 4th solution heat exchanger, absorber has weak solution pipeline to be communicated with generator through solution pump and solution heat exchanger, generator also has concentrated solution pipeline to be communicated with absorber through solution heat exchanger, after generator also has refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter through choke valve again---and generator provides refrigerant vapour to do to drive thermal medium to the second generator, and evaporimeter also has refrigerant vapour passage to be communicated with absorber, the 3rd absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution pump and the 4th solution heat exchanger, the second absorber also has weak solution pipeline to be communicated with the second generator through the second solution pump, the 3rd solution heat exchanger and the second solution heat exchanger, the second generator also has concentrated solution pipeline to be communicated with the 3rd generator through the second solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with the 4th generator through the 3rd solution heat exchanger, and the 4th generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger, the second generator also have refrigerant vapour passage be communicated with successively the 3rd generator and the 4th generator after the 4th generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve---the second generator provides refrigerant vapour do driving thermal medium to the 3rd generator and the 4th generator, the 3rd generator also has refrigerant vapour passage to be communicated with condenser, the 4th generator also has refrigerant vapour passage to be communicated with the second absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the 3rd choke valve, the second evaporimeter also has refrigerant vapour passage to be communicated with the 3rd absorber, generator drives thermal medium pipeline to be communicated with outside in addition, absorber, the second absorber, the 3rd absorber and condenser also have respectively heated medium pipeline to be communicated with outside, evaporimeter and the second evaporimeter medium pipeline that also has surplus heat is respectively communicated with outside, forms the shunt first-class absorption type heat pump that circulates.
2. the first-class absorption type heat pump that circulates along separate routes, is mainly made up of generator, the second generator, the 3rd generator, the 4th generator, absorber, the second absorber, the 3rd absorber, condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, the 3rd solution pump, the 4th solution pump, choke valve, the second choke valve, the 3rd choke valve, solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and the 4th solution heat exchanger, absorber has weak solution pipeline to be communicated with generator through solution pump and solution heat exchanger, generator also has concentrated solution pipeline to be communicated with absorber through solution heat exchanger, after generator also has refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter through choke valve again---and generator provides refrigerant vapour to do to drive thermal medium to the second generator, and evaporimeter also has refrigerant vapour passage to be communicated with absorber, the 3rd absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution pump and the 4th solution heat exchanger, the second absorber also has weak solution pipeline to be communicated with the 3rd generator through the second solution pump and the 3rd solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with the second generator through the 4th solution pump and the second solution heat exchanger, the second generator also has concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger and the 3rd solution heat exchanger, the 4th generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger, the second generator also have refrigerant vapour passage be communicated with successively the 3rd generator and the 4th generator after the 4th generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve---the second generator provides refrigerant vapour do driving thermal medium to the 3rd generator and the 4th generator, the 3rd generator also has refrigerant vapour passage to be communicated with condenser, the 4th generator also has refrigerant vapour passage to be communicated with the second absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the 3rd choke valve, the second evaporimeter also has refrigerant vapour passage to be communicated with the 3rd absorber, generator drives thermal medium pipeline to be communicated with outside in addition, absorber, the second absorber, the 3rd absorber and condenser also have respectively heated medium pipeline to be communicated with outside, evaporimeter and the second evaporimeter medium pipeline that also has surplus heat is respectively communicated with outside, forms the shunt first-class absorption type heat pump that circulates.
3. the first-class absorption type heat pump that circulates along separate routes, is mainly made up of generator, the second generator, the 3rd generator, the 4th generator, absorber, the second absorber, the 3rd absorber, condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, the 3rd solution pump, the 4th solution pump, choke valve, the second choke valve, the 3rd choke valve, solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and the 4th solution heat exchanger, absorber has weak solution pipeline to be communicated with generator through solution pump and solution heat exchanger, generator also has concentrated solution pipeline to be communicated with absorber through solution heat exchanger, after generator also has refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter through choke valve again---and generator provides refrigerant vapour to do to drive thermal medium to the second generator, and evaporimeter also has refrigerant vapour passage to be communicated with absorber, the 3rd absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution pump and the 4th solution heat exchanger, the second absorber also has weak solution pipeline to be communicated with the second generator through the second solution pump and the second solution heat exchanger, the second absorber also has weak solution pipeline to be communicated with the 3rd generator through the 4th solution pump and the 3rd solution heat exchanger, the second generator also has concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with the 4th generator through the 3rd solution heat exchanger, the 4th generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger, the second generator also have refrigerant vapour passage be communicated with successively the 3rd generator and the 4th generator after the 4th generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve---the second generator provides refrigerant vapour do driving thermal medium to the 3rd generator and the 4th generator, the 3rd generator also has refrigerant vapour passage to be communicated with condenser, the 4th generator also has refrigerant vapour passage to be communicated with the second absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the 3rd choke valve, the second evaporimeter also has refrigerant vapour passage to be communicated with the 3rd absorber, generator drives thermal medium pipeline to be communicated with outside in addition, absorber, the second absorber, the 3rd absorber and condenser also have respectively heated medium pipeline to be communicated with outside, evaporimeter and the second evaporimeter medium pipeline that also has surplus heat is respectively communicated with outside, forms the shunt first-class absorption type heat pump that circulates.
4. first-class absorption type heat pump along separate routes circulates, in the shunt circulation first-class absorption type heat pump described in the 1st, cancel the 4th generator, having concentrated solution pipeline to have concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 3rd generator through the 3rd solution heat exchanger and the 4th generator connected sum the 4th generator in the 3rd generator has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger and the 4th solution heat exchanger, by the second generator have refrigerant vapour passage be communicated with successively after the 3rd generator and the 4th generator the 4th generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve to be adjusted into the second generator have refrigerant vapour passage to be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into the 3rd generator to set up refrigerant vapour passage the second absorber in the 4th generator is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
5. first-class absorption type heat pump along separate routes circulates, in the shunt circulation first-class absorption type heat pump described in the 2nd, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger and the 3rd solution heat exchanger in the second generator, the 4th generator has concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the second generator has concentrated solution pipeline through the second solution heat exchanger, the 3rd solution heat exchanger and the 4th solution heat exchanger are communicated with the 4th generator, by the second generator have refrigerant vapour passage be communicated with successively after the 3rd generator and the 4th generator the 4th generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve to be adjusted into the second generator have refrigerant vapour passage to be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into the 3rd generator to set up refrigerant vapour passage the second absorber in the 4th generator is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
6. first-class absorption type heat pump along separate routes circulates, in the shunt circulation first-class absorption type heat pump described in the 3rd, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger in the second generator, the 3rd generator has concentrated solution pipeline to be communicated with the 4th generator through the 3rd solution heat exchanger, the 4th generator has concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the second generator has concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger and the 4th solution heat exchanger, the 3rd generator has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger and the 4th solution heat exchanger, by the second generator have refrigerant vapour passage be communicated with successively after the 3rd generator and the 4th generator the 4th generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve to be adjusted into the second generator have refrigerant vapour passage to be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into the 3rd generator to set up refrigerant vapour passage the second absorber in the 4th generator is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
7. first-class absorption type heat pump along separate routes circulates, in the shunt circulation first-class absorption type heat pump described in the 1st, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 4th solution pump, there is weak solution pipeline to be communicated with the second absorber and to be adjusted into the 3rd absorber and to have weak solution pipeline to be communicated with the 4th absorber through the 3rd solution pump and the 4th solution heat exchanger through the 3rd solution pump and the 4th solution heat exchanger the 3rd absorber, the 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution pump and the 5th solution heat exchanger again, there is concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 4th generator to have concentrated solution pipeline to be communicated with a point steam chest through solution choke valve and the second absorber in the 4th generator, divide steam chest to have again concentrated solution pipeline to be communicated with the 3rd absorber through the 5th solution heat exchanger and the 4th solution heat exchanger, divide steam chest to also have refrigerant vapour passage to be communicated with the 4th absorber, the 4th absorber also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
8. first-class absorption type heat pump along separate routes circulates, in the shunt circulation first-class absorption type heat pump described in the 1st, cancel the second absorber and the outside heated medium pipeline being communicated with, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 4th solution pump, there is weak solution pipeline to be communicated with the second absorber and to be adjusted into the 3rd absorber and to have weak solution pipeline to be communicated with the 4th absorber through the 3rd solution pump and the 4th solution heat exchanger through the 3rd solution pump and the 4th solution heat exchanger the 3rd absorber, the 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution pump and the 5th solution heat exchanger again, there is concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 4th generator to have concentrated solution pipeline to be communicated with a point steam chest through solution choke valve and the second absorber in the 4th generator, divide steam chest to have again concentrated solution pipeline to be communicated with the 3rd absorber through the 5th solution heat exchanger and the 4th solution heat exchanger, divide steam chest to also have refrigerant vapour passage to be communicated with the 4th absorber, the 4th absorber also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
9. first-class absorption type heat pump along separate routes circulates, in the shunt circulation first-class absorption type heat pump described in the 2nd, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 5th solution pump, there is weak solution pipeline to be communicated with the second absorber and to be adjusted into the 3rd absorber and to have weak solution pipeline to be communicated with the 4th absorber through the 3rd solution pump and the 4th solution heat exchanger through the 3rd solution pump and the 4th solution heat exchanger the 3rd absorber, the 4th absorber has weak solution pipeline to be communicated with the second absorber through the 5th solution pump and the 5th solution heat exchanger again, there is concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 4th generator to have concentrated solution pipeline to be communicated with a point steam chest through solution choke valve and the second absorber in the 4th generator, divide steam chest to have again concentrated solution pipeline to be communicated with the 3rd absorber through the 5th solution heat exchanger and the 4th solution heat exchanger, divide steam chest to also have refrigerant vapour passage to be communicated with the 4th absorber, the 4th absorber also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
10. first-class absorption type heat pump along separate routes circulates, in the shunt circulation first-class absorption type heat pump described in the 2nd, cancel the second absorber and the outside heated medium pipeline being communicated with, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 5th solution pump, there is weak solution pipeline to be communicated with the second absorber and to be adjusted into the 3rd absorber and to have weak solution pipeline to be communicated with the 4th absorber through the 3rd solution pump and the 4th solution heat exchanger through the 3rd solution pump and the 4th solution heat exchanger the 3rd absorber, the 4th absorber has weak solution pipeline to be communicated with the second absorber through the 5th solution pump and the 5th solution heat exchanger again, there is concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 4th generator to have concentrated solution pipeline to be communicated with a point steam chest through solution choke valve and the second absorber in the 4th generator, divide steam chest to have again concentrated solution pipeline to be communicated with the 3rd absorber through the 5th solution heat exchanger and the 4th solution heat exchanger, divide steam chest to also have refrigerant vapour passage to be communicated with the 4th absorber, the 4th absorber also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
11. first-class absorption type heat pumps that circulate along separate routes, in the shunt circulation first-class absorption type heat pump described in the 3rd, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 5th solution pump, there is weak solution pipeline to be communicated with the second absorber and to be adjusted into the 3rd absorber and to have weak solution pipeline to be communicated with the 4th absorber through the 3rd solution pump and the 4th solution heat exchanger through the 3rd solution pump and the 4th solution heat exchanger the 3rd absorber, the 4th absorber has weak solution pipeline to be communicated with the second absorber through the 5th solution pump and the 5th solution heat exchanger again, there is concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 4th generator to have concentrated solution pipeline to be communicated with a point steam chest through solution choke valve and the second absorber in the 4th generator, divide steam chest to have again concentrated solution pipeline to be communicated with the 3rd absorber through the 5th solution heat exchanger and the 4th solution heat exchanger, divide steam chest to also have refrigerant vapour passage to be communicated with the 4th absorber, the 4th absorber also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
12. first-class absorption type heat pumps that circulate along separate routes, in the shunt circulation first-class absorption type heat pump described in the 3rd, cancel the second absorber and the outside heated medium pipeline being communicated with, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 5th solution pump, there is weak solution pipeline to be communicated with the second absorber and to be adjusted into the 3rd absorber and to have weak solution pipeline to be communicated with the 4th absorber through the 3rd solution pump and the 4th solution heat exchanger through the 3rd solution pump and the 4th solution heat exchanger the 3rd absorber, the 4th absorber has weak solution pipeline to be communicated with the second absorber through the 5th solution pump and the 5th solution heat exchanger again, there is concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 4th generator to have concentrated solution pipeline to be communicated with a point steam chest through solution choke valve and the second absorber in the 4th generator, divide steam chest to have again concentrated solution pipeline to be communicated with the 3rd absorber through the 5th solution heat exchanger and the 4th solution heat exchanger, divide steam chest to also have refrigerant vapour passage to be communicated with the 4th absorber, the 4th absorber also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
13. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 7-8 item, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator through the 3rd solution heat exchanger in the 3rd generator, the 4th generator has concentrated solution pipeline to be communicated with a point steam chest through solution choke valve and the second absorber to be adjusted into the 3rd generator has concentrated solution pipeline through the 3rd solution heat exchanger, solution choke valve and the second absorber are communicated with a point steam chest, by the second generator have refrigerant vapour passage be communicated with successively after the 3rd generator and the 4th generator the 4th generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve to be adjusted into the second generator have refrigerant vapour passage to be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into the 3rd generator to set up refrigerant vapour passage the second absorber in the 4th generator is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
14. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 9-10 item, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger and the 3rd solution heat exchanger in the second generator, the 4th generator has concentrated solution pipeline to be communicated with a point steam chest through solution choke valve and the second absorber to be adjusted into the second generator has concentrated solution pipeline through the second solution heat exchanger, the 3rd solution heat exchanger, solution choke valve and the second absorber are communicated with a point steam chest, by the second generator have refrigerant vapour passage be communicated with successively after the 3rd generator and the 4th generator the 4th generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve to be adjusted into the second generator have refrigerant vapour passage to be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into the 3rd generator to set up refrigerant vapour passage the second absorber in the 4th generator is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
15. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 11-12 item, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger in the second generator, the 3rd generator has concentrated solution pipeline to be communicated with the 4th generator through the 3rd solution heat exchanger, the 4th generator has concentrated solution pipeline to be communicated with a point steam chest through solution choke valve and the second absorber to be adjusted into the second generator has concentrated solution pipeline to be communicated with solution choke valve through the second solution heat exchanger, the 3rd generator has concentrated solution pipeline to be communicated with solution choke valve through the 3rd solution heat exchanger, solution choke valve has solution pipeline to be communicated with a point steam chest through the second absorber again, by the second generator have refrigerant vapour passage be communicated with successively after the 3rd generator and the 4th generator the 4th generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve to be adjusted into the second generator have refrigerant vapour passage to be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline to be communicated with condenser through the second choke valve, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into the 3rd generator to set up refrigerant vapour passage the second absorber in the 4th generator is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
16. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline through solution pump through solution pump and solution heat exchanger absorber, newly-increased solution heat exchanger and solution heat exchanger are communicated with generator, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, after having refrigerant vapour passage to be communicated with the second generator in generator the second generator have again cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted into generator have refrigerant vapour passage to be communicated with newly-increased generator after newly-increased generator have again cryogen liquid pipeline warp to increase choke valve newly to be communicated with evaporimeter---generator provides refrigerant vapour do driving thermal medium to newly-increased generator, after newly-increased generator also has refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, form the first-class absorption type heat pump that circulates along separate routes.
17. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased generator through solution pump and solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased generator has concentrated solution pipeline to be communicated with generator through newly-increased solution pump and newly-increased solution heat exchanger again, there is concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator to have concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger and solution heat exchanger in generator, after having refrigerant vapour passage to be communicated with the second generator in generator the second generator have again cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted into generator have refrigerant vapour passage to be communicated with newly-increased generator after newly-increased generator have again cryogen liquid pipeline warp to increase choke valve newly to be communicated with evaporimeter---generator provides refrigerant vapour do driving thermal medium to newly-increased generator, after newly-increased generator also has refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, form the first-class absorption type heat pump that circulates along separate routes.
18. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, absorber is set up weak solution pipeline and is communicated with newly-increased generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger, after having refrigerant vapour passage to be communicated with the second generator in generator the second generator have again cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted into generator have refrigerant vapour passage to be communicated with newly-increased generator after newly-increased generator have again cryogen liquid pipeline warp to increase choke valve newly to be communicated with evaporimeter---generator provides refrigerant vapour do driving thermal medium to newly-increased generator, after newly-increased generator also has refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, form the first-class absorption type heat pump that circulates along separate routes.
19. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased condenser, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline through solution pump through solution pump and solution heat exchanger absorber, newly-increased solution heat exchanger and solution heat exchanger are communicated with generator, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased choke valve, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, newly-increased condenser also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
20. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-3 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger, newly-increased condenser, newly-increased solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline through solution pump through solution pump and solution heat exchanger absorber, newly-increased solution heat exchanger and solution heat exchanger are communicated with generator, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased choke valve, there is concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 4th generator to have concentrated solution pipeline to be communicated with the newly-increased steam chest that divides through newly-increased solution pump and newly-increased condenser in the 4th generator, a newly-increased point steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and a newly-increased point steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
21. first-class absorption type heat pumps that circulate along separate routes, in the shunt circulation first-class absorption type heat pump described in the 4th, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger, newly-increased condenser, newly-increased solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline through solution pump through solution pump and solution heat exchanger absorber, newly-increased solution heat exchanger and solution heat exchanger are communicated with generator, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased choke valve, there is concentrated solution pipeline to be communicated with the 3rd absorber and to be adjusted into the 3rd generator and to have concentrated solution pipeline to be communicated with the newly-increased steam chest that divides through newly-increased solution pump and newly-increased condenser through the 3rd solution heat exchanger and the 4th solution heat exchanger in the 3rd generator, a newly-increased point steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger and the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and a newly-increased point steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
22. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger, newly-increased condenser and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline through solution pump through solution pump and solution heat exchanger absorber, newly-increased solution heat exchanger and solution heat exchanger are communicated with generator, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased choke valve, there is concentrated solution pipeline to be communicated with the second solution heat exchanger to be adjusted into the second generator to have concentrated solution pipeline to be communicated with the newly-increased steam chest that divides through newly-increased condenser in the second generator, a newly-increased point steam chest has concentrated solution pipeline to be communicated with the second solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and a newly-increased point steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
23. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 7-15 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger, newly-increased condenser, newly-increased solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline through solution pump through solution pump and solution heat exchanger absorber, newly-increased solution heat exchanger and solution heat exchanger are communicated with generator, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased choke valve, to divide steam chest to have concentrated solution pipeline to be communicated with the 3rd absorber and to be adjusted into a point steam chest and to have concentrated solution pipeline to be communicated with the newly-increased steam chest that divides through newly-increased solution pump and newly-increased condenser through the 5th solution heat exchanger and the 4th solution heat exchanger, a newly-increased point steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 5th solution heat exchanger and the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and a newly-increased point steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
24. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
25. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-3 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, there is concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 4th generator to have concentrated solution pipeline to be communicated with the newly-increased steam chest that divides through newly-increased the second solution pump and newly-increased absorber in the 4th generator, a newly-increased point steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and a newly-increased point steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
26. first-class absorption type heat pumps that circulate along separate routes, in the shunt circulation first-class absorption type heat pump described in the 4th, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, there is concentrated solution pipeline to be communicated with the 3rd absorber and to be adjusted into the 3rd generator and to have concentrated solution pipeline to be communicated with the newly-increased steam chest that divides through newly-increased the second solution pump and newly-increased absorber through the 3rd solution heat exchanger and the 4th solution heat exchanger in the 3rd generator, a newly-increased point steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger and the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and a newly-increased point steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
27. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, there is concentrated solution pipeline to be communicated with the second solution heat exchanger to be adjusted into the second generator to have concentrated solution pipeline to be communicated with the newly-increased steam chest that divides through newly-increased absorber in the second generator, a newly-increased point steam chest has concentrated solution pipeline to be communicated with the second solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and a newly-increased point steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
28. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 7-15 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, to divide steam chest to have concentrated solution pipeline to be communicated with the 3rd absorber and to be adjusted into a point steam chest and to have concentrated solution pipeline to be communicated with the newly-increased steam chest that divides through newly-increased the second solution pump and newly-increased absorber through the 5th solution heat exchanger and the 4th solution heat exchanger, a newly-increased point steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 5th solution heat exchanger and the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and a newly-increased point steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
29. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased point steam chest, newly-increased solution choke valve and newly-increased the second solution choke valve, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased the second solution choke valve again, there is concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator to have concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution pump in generator, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, after having refrigerant vapour passage to be communicated with the second generator in generator the second generator have again cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted into generator and increase newly divide a steam chest to have refrigerant vapour passage to be communicated with the second generator after the second generator have again cryogen liquid pipeline to be communicated with evaporimeter through choke valve, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
30. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased absorber, newly-increased point steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator, newly-increased generator has concentrated solution pipeline to be communicated with generator through newly-increased solution choke valve again, there is concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator to have concentrated solution pipeline to be communicated with the newly-increased steam chest that divides through newly-increased absorber in generator, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, after having refrigerant vapour passage to be communicated with the second generator in generator the second generator have again cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted into generator and increase newly divide a steam chest to have refrigerant vapour passage to be communicated with the second generator after the second generator have again cryogen liquid pipeline to be communicated with evaporimeter through choke valve, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes, wherein, arrange for convenience of parts, or increase newly-increased solution pump, will increase absorber newly has weak solution pipeline to be communicated with newly-increased generator to be adjusted into newly-increased absorber to have weak solution pipeline warp to increase solution pump newly to be communicated with newly-increased generator.
31. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased absorber, newly-increased solution heat exchanger and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline through solution pump through solution pump and solution heat exchanger absorber, solution heat exchanger and newly-increased solution heat exchanger are communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator, newly-increased generator has concentrated solution pipeline to be communicated with generator through newly-increased solution heat exchanger again, there is concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator to have concentrated solution pipeline to be communicated with the newly-increased steam chest that divides through newly-increased absorber in generator, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, after having refrigerant vapour passage to be communicated with the second generator in generator the second generator have again cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted into generator and increase newly divide a steam chest to have refrigerant vapour passage to be communicated with the second generator after the second generator have again cryogen liquid pipeline to be communicated with evaporimeter through choke valve, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes, wherein, arrange for convenience of parts, or increase newly-increased solution pump, will increase absorber newly has weak solution pipeline to be communicated with newly-increased generator to be adjusted into newly-increased absorber to have weak solution pipeline warp to increase solution pump newly to be communicated with newly-increased generator.
32. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased choke valve, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased point steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased choke valve, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, newly-increased condenser also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes, wherein, newly-increased absorber or increase heated medium pipeline are communicated with outside.
33. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-3 item, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased throttling, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased point steam chest, newly-increased solution choke valve and newly-increased second point of steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased choke valve, there is concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 4th generator to have concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased the second solution pump and newly-increased condenser in the 4th generator, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
34. first-class absorption type heat pumps that circulate along separate routes, in the shunt circulation first-class absorption type heat pump described in the 4th, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased throttling, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased point steam chest, newly-increased solution choke valve and newly-increased second point of steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased choke valve, there is concentrated solution pipeline to be communicated with the 3rd absorber and to be adjusted into the 3rd generator and to have concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased the second solution pump and newly-increased condenser through the 3rd solution heat exchanger and the 4th solution heat exchanger in the 3rd generator, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger and the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
35. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased choke valve, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased point steam chest, newly-increased solution choke valve and newly-increased second point of steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased choke valve, there is concentrated solution pipeline to be communicated with the second solution heat exchanger to be adjusted into the second generator to have concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased condenser in the second generator, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the second solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
36. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 7-15 item, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased choke valve, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased point steam chest, newly-increased solution choke valve and newly-increased second point of steam chest, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased choke valve, to divide steam chest to have concentrated solution pipeline to be communicated with the 3rd absorber and to be adjusted into a point steam chest and to have concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased the second solution pump and newly-increased condenser through the 5th solution heat exchanger and the 4th solution heat exchanger, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 5th solution heat exchanger and the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
37. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased the second absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased the second absorber also has weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution pump and newly-increased the second solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased the second solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through newly-increased the second solution heat exchanger and newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased the second absorber, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, newly-increased the second absorber also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes, wherein, newly-increased absorber or increase heated medium pipeline are communicated with outside.
38. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-3 item, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased the 3rd solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest, newly-increased second point of steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased the second absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased the second absorber also has weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution pump and newly-increased the second solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased the second solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through newly-increased the second solution heat exchanger and newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased the second absorber, there is concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger to be adjusted into the 4th generator have concentrated solution pipeline through newly-increased the 3rd solution pump and newly-increased the second absorber or be communicated with newly-increased second point of steam chest through newly-increased absorber again in the 4th generator, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
39. first-class absorption type heat pumps that circulate along separate routes, in the shunt circulation first-class absorption type heat pump described in the 4th, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased the 3rd solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest, newly-increased second point of steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased the second absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased the second absorber also has weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution pump and newly-increased the second solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased the second solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through newly-increased the second solution heat exchanger and newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased the second absorber, there is concentrated solution pipeline to be communicated with the 3rd absorber and to be adjusted into the 3rd generator and to have concentrated solution pipeline through newly-increased the 3rd solution pump and newly-increased the second absorber or be communicated with newly-increased second point of steam chest through newly-increased absorber again through the 3rd solution heat exchanger and the 4th solution heat exchanger in the 3rd generator, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger and the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
40. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest, newly-increased second point of steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased the second absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased the second absorber also has weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution pump and newly-increased the second solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased the second solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through newly-increased the second solution heat exchanger and newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased the second absorber, there is concentrated solution pipeline to be communicated with the second solution heat exchanger to be adjusted into the second generator have concentrated solution pipeline through newly-increased the second absorber or be communicated with newly-increased second point of steam chest through newly-increased absorber again in the second generator, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the second solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
41. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in 7-15 item, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased the 3rd solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest, newly-increased second point of steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator and to be adjusted into absorber and to have weak solution pipeline to be communicated with newly-increased the second absorber through solution pump and newly-increased solution heat exchanger through solution pump and solution heat exchanger absorber, newly-increased the second absorber also has weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution pump and newly-increased the second solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with generator through newly-increased the second solution pump and solution heat exchanger again, generator is had concentrated solution pipeline to be communicated with absorber through solution heat exchanger to be adjusted into generator has concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest through newly-increased solution choke valve and newly-increased absorber, a newly-increased point steam chest has concentrated solution pipeline to be communicated with absorber through newly-increased the second solution heat exchanger and newly-increased solution heat exchanger again, newly-increased generator also has refrigerant vapour passage to be communicated with newly-increased absorber, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased the second absorber, to divide steam chest to have concentrated solution pipeline to be communicated with the 3rd absorber and to be adjusted into a point steam chest and to have concentrated solution pipeline through newly-increased the 3rd solution pump and newly-increased the second absorber or be communicated with newly-increased second point of steam chest through newly-increased absorber again through the 5th solution heat exchanger and the 4th solution heat exchanger, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber through the 5th solution heat exchanger and the 4th solution heat exchanger again, have refrigerant vapour passage to be communicated with the 3rd generator to be adjusted into the second generator and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator in the second generator---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
42. first-class absorption type heat pumps that circulate along separate routes, are in the arbitrary shunt circulation first-class absorption type heat pump described in 1-41 item, and evaporimeter and the second evaporimeter are united two into one, and form the first-class absorption type heat pump that circulates along separate routes.
Further illustrate the present invention below in conjunction with the first-class absorption type heat pump that circulates along separate routes shown in Fig. 1 and Figure 17:
(1) solution that drives heat medium flow to enter in it through generator 1, heating discharges and provides refrigerant vapour to the second generator 2, drives heat in pyrosol closed circuit, to carry out temperature drop for the first time; The refrigerant vapour that evaporimeter 9 produces enters absorber 5, is absorbed and heat up by concentrated solution, thereby realizes the utilization for the first time that drives the temperature difference.
(2) the refrigerant vapour solution that the second generator 2, heating enter in it of flowing through discharges and provides refrigerant vapour to the 3rd generator 3 and the 4th generator 4, drive heat in cryogenic fluid closed circuit, to realize temperature drop for the second time, realize the utilization for the second time that drives the temperature difference; Refrigerant vapour the 3rd generator 3 of flowing through heats again to solution, drives heat to realize temperature drop for the third time, realizes the utilization for the third time that drives the temperature difference.
(3) refrigerant vapour the 4th generator 4 heated solutions of flowing through, the refrigerant vapour discharging offers the second absorber 6 externally heat supply, the thermic load of the second absorber 6 is adjustable, be particularly suitable for the wide situation of heated medium range of temperature, the thermodynamics sophistication that is conducive to improve circulation, obtains higher performance index.
(4) be the occasion of sensible heat for driving heat, high-temperature part is for generator 1, driving heat after temperature reduces is for newly-increased generator A, and newly-increased generator A and newly-increased absorber G realize the temperature difference utilization that drives hot low temperature part, has further increased the degree of utilizing to driving heat.
Brief description of the drawings:
Fig. 1 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 1st kind of structure and schematic flow sheet.
Fig. 2 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 2nd kind of structure and schematic flow sheet.
Fig. 3 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 3rd kind of structure and schematic flow sheet.
Fig. 4 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 4th kind of structure and schematic flow sheet.
Fig. 5 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 5th kind of structure and schematic flow sheet.
Fig. 6 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 6th kind of structure and schematic flow sheet.
Fig. 7 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 7th kind of structure and schematic flow sheet.
Fig. 8 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 8th kind of structure and schematic flow sheet.
Fig. 9 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 9th kind of structure and schematic flow sheet.
Figure 10 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 10th kind of structure and schematic flow sheet.
Figure 11 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 11st kind of structure and schematic flow sheet.
Figure 12 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 12nd kind of structure and schematic flow sheet.
Figure 13 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 13rd kind of structure and schematic flow sheet.
Figure 14 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 14th kind of structure and schematic flow sheet.
Figure 15 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 15th kind of structure and schematic flow sheet.
Figure 16 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 16th kind of structure and schematic flow sheet.
Figure 17 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 17th kind of structure and schematic flow sheet.
Figure 18 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 18th kind of structure and schematic flow sheet.
Figure 19 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 19th kind of structure and schematic flow sheet.
Figure 20 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 20th kind of structure and schematic flow sheet.
Figure 21 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 21st kind of structure and schematic flow sheet.
Figure 22 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 22nd kind of structure and schematic flow sheet.
In figure, 1-generator, 2-the second generator, 3-the 3rd generator, 4-the 4th generator, 5-absorber, 6-the second absorber, 7-the 3rd absorber, 8-condenser, 9-evaporimeter, 10-the second evaporimeter, 11-solution pump, 12-the second solution pump, 13-the 3rd solution pump, 14-choke valve, 15-the second choke valve, 16-the 3rd choke valve, 17-solution heat exchanger, 18-the second solution heat exchanger, 19-the 3rd solution heat exchanger, 20-the 4th solution heat exchanger, 21-the 4th solution pump, 22-the 4th absorber, 23-solution choke valve, 24-the 5th solution heat exchanger, 25-divides steam chest, 26-the 5th solution pump, A-increases generator newly, B-increases choke valve newly, and C-increases solution heat exchanger newly, and D-increases solution pump newly, E-increases condenser newly, the newly-increased point steam chest of F-, G-increases absorber newly, and H-increases solution choke valve newly, I-increases the second solution choke valve newly, J-increases the second absorber newly, and K-increases the second solution heat exchanger newly, and L-increases the second solution pump newly.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, in inessential situation, do not repeat; Apparent flow process is not explained.Describe the present invention in detail below in conjunction with accompanying drawing and example.
Shunt circulation first-class absorption type heat pump shown in Fig. 1 is achieved in that
1. in structure, it is mainly made up of generator, the second generator, the 3rd generator, the 4th generator, absorber, the second absorber, the 3rd absorber, condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, the 3rd solution pump, choke valve, the second choke valve, the 3rd choke valve, solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and the 4th solution heat exchanger, absorber 5 has weak solution pipeline to be communicated with generator 1 through solution pump 11 and solution heat exchanger 17, generator 1 also has concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17, after generator 1 also has refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 again, and evaporimeter 9 also has refrigerant vapour passage to be communicated with absorber 5, the 3rd absorber 7 has weak solution pipeline to be communicated with the second absorber 6 through the 3rd solution pump 13 and the 4th solution heat exchanger 20, the second absorber 6 also has weak solution pipeline through the second solution pump 12, the 3rd solution heat exchanger 19 and the second solution heat exchanger 18 are communicated with the second generator 2, the second generator 2 also has concentrated solution pipeline to be communicated with the 3rd generator 3 through the second solution heat exchanger 18, the 3rd generator 3 also has concentrated solution pipeline to be communicated with the 4th generator 4 through the 3rd solution heat exchanger 19, the 4th generator 4 also has concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 4th solution heat exchanger 20, the second generator 2 also have refrigerant vapour passage be communicated with successively the 3rd generator 3 and the 4th generator 4 after the 4th generator 4 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15---the second generator provides refrigerant vapour to make driving thermal medium to the 3rd generator and the 4th generator, the 3rd generator 3 also has refrigerant vapour passage to be communicated with condenser 8, the 4th generator 4 also has refrigerant vapour passage to be communicated with the second absorber 6, condenser 8 also has cryogen liquid pipeline to be communicated with the second evaporimeter 10 through the 3rd choke valve 16, the second evaporimeter 10 also has refrigerant vapour passage to be communicated with the 3rd absorber 7, generator 1 drives thermal medium pipeline to be communicated with outside in addition, absorber 5, the second absorber 6, the 3rd absorber 7 and condenser 8 also have respectively heated medium pipeline to be communicated with outside, and evaporimeter 9 and the second evaporimeter 10 medium pipeline that also has surplus heat is respectively communicated with outside.
2. in flow process, the weak solution of absorber 5 enters generator 1 through solution pump 11 and solution heat exchanger 17, driving heat medium flow to enter solution in it through generator 1, heating discharges and provides refrigerant vapour to the second generator 2---and refrigerant vapour that generator 1 produces is as the driving thermal medium of the second generator 2, and the concentrated solution of generator 1 enters absorber 5, absorbs refrigerant vapour heat release in heated medium through solution heat exchanger 17, the weak solution of the 3rd absorber 7 enters the second absorber 6 through the 3rd solution pump 13 and the 4th solution heat exchanger 20, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 6 is through the second solution pump 12, the 3rd solution heat exchanger 19 and the second solution heat exchanger 18 enter the second generator 2, refrigerant vapour second generator 2 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to the 3rd generator 3 and the 4th generator 4, flow through after the refrigerant vapour heat release of the second generator 2 becomes cryogen liquid and enter evaporimeter 9 through choke valve 14 throttlings, absorbing waste heat becomes refrigerant vapour and provides to absorber 5, the concentrated solution of the second generator 2 enters the 3rd generator 3 through the second solution heat exchanger 18, refrigerant vapour the 3rd generator 3 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to condenser 8, the concentrated solution of the 3rd generator 3 enters the 4th generator 4 through the 3rd solution heat exchanger 19, the refrigerant vapour heat release of the 3rd generator 3 of flowing through becomes backward the 4th generator 4 of moist steam to provide, wet steam flow is through the 4th generator 4, the solution that heating enters in it discharges and provides refrigerant vapour to the second absorber 6, the concentrated solution of the 4th generator 4 enters the 3rd absorber 7 through the 4th solution heat exchanger 20, absorb refrigerant vapour heat release in heated medium, flow through after the moist steam heat release of the 4th generator 4 becomes cryogen liquid and enter condenser 8 through the second choke valve 15 throttlings again, the refrigerant vapour heat release of condenser 8 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 8 enters the second evaporimeter 10, absorbs waste heat and become refrigerant vapour and provide to the 3rd absorber 7 through the 3rd choke valve 16 throttling, forms the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Fig. 2 is achieved in that
1. in structure, it is mainly made up of generator, the second generator, the 3rd generator, the 4th generator, absorber, the second absorber, the 3rd absorber, condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, the 3rd solution pump, the 4th solution pump, choke valve, the second choke valve, the 3rd choke valve, solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and the 4th solution heat exchanger, absorber 5 has weak solution pipeline to be communicated with generator 1 through solution pump 11 and solution heat exchanger 17, generator 1 also has concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17, after generator 1 also has refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 again, and evaporimeter 9 also has refrigerant vapour passage to be communicated with absorber 5, the 3rd absorber 7 has weak solution pipeline to be communicated with the second absorber 6 through the 3rd solution pump 13 and the 4th solution heat exchanger 20, the second absorber 6 also has weak solution pipeline to be communicated with the 3rd generator 3 through the second solution pump 12 and the 3rd solution heat exchanger 19, the 3rd generator 3 also has concentrated solution pipeline to be communicated with the second generator 2 through the 4th solution pump 21 and the second solution heat exchanger 18, the second generator 2 also has concentrated solution pipeline to be communicated with the 4th generator 4 through the second solution heat exchanger 18 and the 3rd solution heat exchanger 19, the 4th generator 4 also has concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 4th solution heat exchanger 20, the second generator 2 also have refrigerant vapour passage be communicated with successively the 3rd generator 3 and the 4th generator 4 after the 4th generator 4 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15---the second generator provides refrigerant vapour to make driving thermal medium to the 3rd generator and the 4th generator, the 3rd generator 3 also has refrigerant vapour passage to be communicated with condenser 8, the 4th generator 4 also has refrigerant vapour passage to be communicated with the second absorber 6, condenser 8 also has cryogen liquid pipeline to be communicated with the second evaporimeter 10 through the 3rd choke valve 16, the second evaporimeter 10 also has refrigerant vapour passage to be communicated with the 3rd absorber 7, generator 1 drives thermal medium pipeline to be communicated with outside in addition, absorber 5, the second absorber 6, the 3rd absorber 7 and condenser 8 also have respectively heated medium pipeline to be communicated with outside, and evaporimeter 9 and the second evaporimeter 10 medium pipeline that also has surplus heat is respectively communicated with outside.
2. in flow process, the weak solution of absorber 5 enters generator 1 through solution pump 11 and solution heat exchanger 17, driving heat medium flow to enter solution in it through generator 1, heating discharges and provides refrigerant vapour to the second generator 2---and refrigerant vapour that generator 1 produces is as the driving thermal medium of the second generator 2, and the concentrated solution of generator 1 enters absorber 5, absorbs refrigerant vapour heat release in heated medium through solution heat exchanger 17, the weak solution of the 3rd absorber 7 enters the second absorber 6 through the 3rd solution pump 13 and the 4th solution heat exchanger 20, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 6 enters the 3rd generator 3 through the second solution pump 12 and the 3rd solution heat exchanger 19, refrigerant vapour the 3rd generator 3 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to condenser 8, the concentrated solution of the 3rd generator 3 enters the second generator 2 through the 4th solution pump 21 and the second solution heat exchanger 18, the refrigerant vapour heat release of the 3rd generator 3 of flowing through becomes backward the 4th generator 4 of moist steam to provide, refrigerant vapour second generator 2 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to the 3rd generator 3 and the 4th generator 4, flow through after the refrigerant vapour heat release of the second generator 2 becomes cryogen liquid and enter evaporimeter 9 through choke valve 14 throttlings, absorbing waste heat becomes refrigerant vapour and provides to absorber 5, the concentrated solution of the second generator 2 enters the 4th generator 4 through the second solution heat exchanger 18 and the 3rd solution heat exchanger 19, wet steam flow is through the 4th generator 4, the solution that heating enters in it discharges and provides refrigerant vapour to the second absorber 6, the concentrated solution of the 4th generator 4 enters the 3rd absorber 7 through the 4th solution heat exchanger 20, absorb refrigerant vapour heat release in heated medium, flow through after the moist steam heat release of the 4th generator 4 becomes cryogen liquid and enter condenser 8 through the second choke valve 15 throttlings again, the refrigerant vapour heat release of condenser 8 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 8 enters the second evaporimeter 10, absorbs waste heat and become refrigerant vapour and provide to the 3rd absorber 7 through the 3rd choke valve 16 throttling, forms the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Fig. 3 is achieved in that
1. in structure, it is mainly made up of generator, the second generator, the 3rd generator, the 4th generator, absorber, the second absorber, the 3rd absorber, condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, the 3rd solution pump, the 4th solution pump, choke valve, the second choke valve, the 3rd choke valve, solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and the 4th solution heat exchanger, absorber 5 has weak solution pipeline to be communicated with generator 1 through solution pump 11 and solution heat exchanger 17, generator 1 also has concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17, after generator 1 also has refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 again, and evaporimeter 9 also has refrigerant vapour passage to be communicated with absorber 5, the 3rd absorber 7 has weak solution pipeline to be communicated with the second absorber 6 through the 3rd solution pump 13 and the 4th solution heat exchanger 20, the second absorber 6 also has weak solution pipeline to be communicated with the second generator 2 through the second solution pump 12 and the second solution heat exchanger 18, the second absorber 6 also has weak solution pipeline to be communicated with the 3rd generator 3 through the 4th solution pump 21 and the 3rd solution heat exchanger 19, the second generator 2 also has concentrated solution pipeline to be communicated with the 4th generator 4 through the second solution heat exchanger 18, the 3rd generator 3 also has concentrated solution pipeline to be communicated with the 4th generator 4 through the 3rd solution heat exchanger 19, the 4th generator 4 also has concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 4th solution heat exchanger 20, the second generator 2 also have refrigerant vapour passage be communicated with successively the 3rd generator 3 and the 4th generator 4 after the 4th generator 4 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15---the second generator provides refrigerant vapour to make driving thermal medium to the 3rd generator and the 4th generator, the 3rd generator 3 also has refrigerant vapour passage to be communicated with condenser 8, the 4th generator 4 also has refrigerant vapour passage to be communicated with the second absorber 6, condenser 8 also has cryogen liquid pipeline to be communicated with the second evaporimeter 10 through the 3rd choke valve 16, the second evaporimeter 10 also has refrigerant vapour passage to be communicated with the 3rd absorber 7, generator 1 drives thermal medium pipeline to be communicated with outside in addition, absorber 5, the second absorber 6, the 3rd absorber 7 and condenser 8 also have respectively heated medium pipeline to be communicated with outside, and evaporimeter 9 and the second evaporimeter 10 medium pipeline that also has surplus heat is respectively communicated with outside.
2. in flow process, the weak solution of absorber 5 enters generator 1 through solution pump 11 and solution heat exchanger 17, driving heat medium flow to enter solution in it through generator 1, heating discharges and provides refrigerant vapour to the second generator 2---and refrigerant vapour that generator 1 produces is as the driving thermal medium of the second generator 2, and the concentrated solution of generator 1 enters absorber 5, absorbs refrigerant vapour heat release in heated medium through solution heat exchanger 17; The weak solution of the 3rd absorber 7 enters the second absorber 6, absorption refrigerant vapour heat release in heated medium through the 3rd solution pump 13 and the 4th solution heat exchanger 20, the weak solution of the second absorber 6 is divided into two-way---and the first via is through the second solution pump 12 and the second solution heat exchanger 18 enters the second generator 2, the second tunnels the 4th solution pump 21 and the 3rd solution heat exchanger 19 enters the 3rd generator 3; The refrigerant vapour solution that the second generator 2, heating enter in it of flowing through discharges and provides refrigerant vapour to the 3rd generator 3 and the 4th generator 4, and the refrigerant vapour heat release of second generator 2 of flowing through becomes after cryogen liquid through choke valve 14 throttlings to enter evaporimeter 9, absorb waste heat and become refrigerant vapour and provide to absorber 5; The refrigerant vapour solution that the 3rd generator 3, heating enter in it of flowing through discharges and provides refrigerant vapour to condenser 8, and the refrigerant vapour heat release of the 3rd generator 3 of flowing through becomes backward the 4th generator 4 of moist steam to provide; The concentrated solution of the second generator 2 enters the 4th generator 4 through the second solution heat exchanger 18, the concentrated solution of the 3rd generator 3 enters the 4th generator 4 through the 3rd solution heat exchanger 19, the solution that wet steam flow enters in it through the 4th generator 4, heating discharges and provides refrigerant vapour to the second absorber 6, the concentrated solution of the 4th generator 4 enters the 3rd absorber 7, absorption refrigerant vapour heat release in heated medium through the 4th solution heat exchanger 20, and the moist steam heat release of the 4th generator 4 of flowing through enters condenser 8 through the second choke valve 15 throttlings after becoming cryogen liquid again; The refrigerant vapour heat release of condenser 8 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 8 enters the second evaporimeter 10, absorbs waste heat and become refrigerant vapour and provide to the 3rd absorber 7 through the 3rd choke valve 16 throttling, forms the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Fig. 4 is achieved in that
In the shunt circulation first-class absorption type heat pump shown in Fig. 1, cancel the 4th generator, having concentrated solution pipeline to have concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 4th solution heat exchanger 20 to be adjusted into the 3rd generator 3 through the 3rd solution heat exchanger 19 and the 4th generator 4 connected sums the 4th generator 4 in the 3rd generator 3 has concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 3rd solution heat exchanger 19 and the 4th solution heat exchanger 20, by the second generator 2 have refrigerant vapour passage be communicated with successively after the 3rd generator 3 and the 4th generator 4 the 4th generator 4 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15 to be adjusted into the second generator 2 have refrigerant vapour passage to be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15, having refrigerant vapour passage to be communicated with the second absorber 6 to be adjusted into the 3rd generator 3 to set up refrigerant vapour passage the second absorber 6 in the 4th generator 4 is communicated with, the refrigerant vapour solution that the 3rd generator 3, heating enter in it of flowing through discharges and provides refrigerant vapour to condenser 8 and the second absorber 6 respectively, the concentrated solution of the 3rd generator 3 enters the 3rd absorber 7 through the 3rd solution heat exchanger 19 and the 4th solution heat exchanger 20, forms the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Fig. 5 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, cancel the second absorber 6 and the outside heated medium pipeline being communicated with, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 4th solution pump, there is weak solution pipeline to be communicated with the second absorber 6 and to be adjusted into the 3rd absorber 7 and to have weak solution pipeline to be communicated with the 4th absorber 22 through the 3rd solution pump 13 and the 4th solution heat exchanger 20 through the 3rd solution pump 13 and the 4th solution heat exchanger 20 the 3rd absorber 7, the 4th absorber 22 has weak solution pipeline to be communicated with the second absorber 6 through the 4th solution pump 21 and the 5th solution heat exchanger 24 again, there is concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 4th solution heat exchanger 20 to be adjusted into the 4th generator 4 to have concentrated solution pipeline to be communicated with a point steam chest 25 through solution choke valve 23 and the second absorber 6 in the 4th generator 4, divide steam chest 25 to have again concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 5th solution heat exchanger 24 and the 4th solution heat exchanger 20, divide steam chest 25 to also have refrigerant vapour passage to be communicated with the 4th absorber 22, the 4th absorber 22 also has heated medium pipeline to be communicated with outside.
2. in flow process, the weak solution of the 3rd absorber 7 enters the 4th absorber 22, absorbs refrigerant vapour heat release in heated medium through the 3rd solution pump 13 and the 4th solution heat exchanger 20, and the weak solution of the 4th absorber 22 enters the second absorber 6, absorbs refrigerant vapour heat release in the solution of flowing through in it through the 4th solution pump 21 and the 5th solution heat exchanger 24; The concentrated solution of the 4th generator 4 enters point steam chest 25 after second absorber 6 of flowing through after solution choke valve 23 reducing pressure by regulating flows, heat absorbing part vaporization, divide the concentrated solution of steam chest 25 to enter the 3rd absorber 7 through the 5th solution heat exchanger 24 and the 4th solution heat exchanger 20, divide the refrigerant vapour of steam chest 25 to enter the 4th absorber 22, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Fig. 6 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, cancel the second absorber 6 and the outside heated medium pipeline being communicated with, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 5th solution pump, there is weak solution pipeline to be communicated with the second absorber 6 and to be adjusted into the 3rd absorber 7 and to have weak solution pipeline to be communicated with the 4th absorber 22 through the 3rd solution pump 13 and the 4th solution heat exchanger 20 through the 3rd solution pump 13 and the 4th solution heat exchanger 20 the 3rd absorber 7, the 4th absorber 22 has weak solution pipeline to be communicated with the second absorber 6 through the 5th solution pump 26 and the 5th solution heat exchanger 24 again, there is concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 4th solution heat exchanger 20 to be adjusted into the 4th generator 4 to have concentrated solution pipeline to be communicated with a point steam chest 25 through solution choke valve 23 and the second absorber 6 in the 4th generator 4, divide steam chest 25 to have again concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 5th solution heat exchanger 24 and the 4th solution heat exchanger 20, divide steam chest 25 to also have refrigerant vapour passage to be communicated with the 4th absorber 22, the 4th absorber 22 also has heated medium pipeline to be communicated with outside.
2. in flow process, the weak solution of the 3rd absorber 7 enters the 4th absorber 22, absorbs refrigerant vapour heat release in heated medium through the 3rd solution pump 13 and the 4th solution heat exchanger 20, and the weak solution of the 4th absorber 22 enters the second absorber 6, absorbs refrigerant vapour heat release in the solution of flowing through in it through the 5th solution pump 26 and the 5th solution heat exchanger 24; The concentrated solution of the 4th generator 4 enters point steam chest 25 after second absorber 6 of flowing through after solution choke valve 23 reducing pressure by regulating flows, heat absorbing part vaporization, divide the concentrated solution of steam chest 25 to enter the 3rd absorber 7 through the 5th solution heat exchanger 24 and the 4th solution heat exchanger 20, divide the refrigerant vapour of steam chest 25 to enter the 4th absorber 22, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Fig. 7 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, cancel the second absorber 6 and the outside heated medium pipeline being communicated with, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 5th solution pump, there is weak solution pipeline to be communicated with the second absorber 6 and to be adjusted into the 3rd absorber 7 and to have weak solution pipeline to be communicated with the 4th absorber 22 through the 3rd solution pump 13 and the 4th solution heat exchanger 20 through the 3rd solution pump 13 and the 4th solution heat exchanger 20 the 3rd absorber 7, the 4th absorber 22 has weak solution pipeline to be communicated with the second absorber 6 through the 5th solution pump 26 and the 5th solution heat exchanger 24 again, there is concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 4th solution heat exchanger 20 to be adjusted into the 4th generator 4 to have concentrated solution pipeline to be communicated with a point steam chest 25 through solution choke valve 23 and the second absorber 6 in the 4th generator 4, divide steam chest 25 to have again concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 5th solution heat exchanger 24 and the 4th solution heat exchanger 20, divide steam chest 25 to also have refrigerant vapour passage to be communicated with the 4th absorber 22, the 4th absorber 22 also has heated medium pipeline to be communicated with outside.
2. in flow process, the weak solution of the 3rd absorber 7 enters the 4th absorber 22, absorbs refrigerant vapour heat release in heated medium through the 3rd solution pump 13 and the 4th solution heat exchanger 20, and the weak solution of the 4th absorber 22 enters the second absorber 6, absorbs refrigerant vapour heat release in the solution of flowing through in it through the 5th solution pump 26 and the 5th solution heat exchanger 24; The concentrated solution of the 4th generator 4 enters point steam chest 25 after second absorber 6 of flowing through after solution choke valve 23 reducing pressure by regulating flows, heat absorbing part vaporization, divide the concentrated solution of steam chest 25 to enter the 3rd absorber 7 through the 5th solution heat exchanger 24 and the 4th solution heat exchanger 20, divide the refrigerant vapour of steam chest 25 to enter the 4th absorber 22, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Fig. 8 is achieved in that
In the shunt circulation first-class absorption type heat pump shown in Fig. 5, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator 4 through the 3rd solution heat exchanger 19 in the 3rd generator 3, the 4th generator 4 has concentrated solution pipeline to be communicated with a point steam chest 25 through solution choke valve 23 and the second absorber 6 to be adjusted into the 3rd generator 3 has concentrated solution pipeline through the 3rd solution heat exchanger 19, solution choke valve 23 and the second absorber 6 are communicated with a point steam chest 25, by the second generator 2 have refrigerant vapour passage be communicated with successively after the 3rd generator 3 and the 4th generator 4 the 4th generator 4 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15 to be adjusted into the second generator 2 have refrigerant vapour passage to be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15, having refrigerant vapour passage to be communicated with the second absorber 6 to be adjusted into the 3rd generator 3 to set up refrigerant vapour passage the second absorber 6 in the 4th generator 4 is communicated with.
2. in flow process, the refrigerant vapour solution that the 3rd generator 3, heating enter in it of flowing through discharges and provides refrigerant vapour to condenser 8 and the second absorber 6 respectively, the concentrated solution of the 3rd generator 3 is through the 3rd solution heat exchanger 19 heat exchange and after second absorber 6 of flowing through after solution choke valve 23 reducing pressure by regulating flows, heat absorbing part vaporization, enter point steam chest 25 again, forms the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Fig. 9 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 6, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator 4 through the second solution heat exchanger 18 and the 3rd solution heat exchanger 19 in the second generator 2, the 4th generator 4 has concentrated solution pipeline to be communicated with a point steam chest 25 through solution choke valve 23 and the second absorber 6 to be adjusted into the second generator 2 has concentrated solution pipeline through the second solution heat exchanger 18, the 3rd solution heat exchanger 19, solution choke valve 23 and the second absorber 6 are communicated with a point steam chest 25, by the second generator 2 have refrigerant vapour passage be communicated with successively after the 3rd generator 3 and the 4th generator 4 the 4th generator 4 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15 to be adjusted into the second generator 2 have refrigerant vapour passage to be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15, having refrigerant vapour passage to be communicated with the second absorber 6 to be adjusted into the 3rd generator 3 to set up refrigerant vapour passage the second absorber 6 in the 4th generator 4 is communicated with.
2. in flow process, the refrigerant vapour solution that the 3rd generator 3, heating enter in it of flowing through discharges and provides refrigerant vapour to condenser 8 and the second absorber 6 respectively, the concentrated solution of the second generator 2 is through the second solution heat exchanger 18 and the 3rd solution heat exchanger 19 heat exchange and after second absorber 6 of flowing through after solution choke valve 23 reducing pressure by regulating flows, heat absorbing part vaporization, enter point steam chest 25 again, forms the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 10 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 7, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator 4 through the second solution heat exchanger 18 in the second generator 2, the 3rd generator 3 has concentrated solution pipeline to be communicated with the 4th generator 4 through the 3rd solution heat exchanger 19, the 4th generator 4 has concentrated solution pipeline to be communicated with a point steam chest 25 through solution choke valve 23 and the second absorber 6 to be adjusted into the second generator 2 has concentrated solution pipeline to be communicated with solution choke valve 23 through the second solution heat exchanger 18, the 3rd generator 3 has concentrated solution pipeline to be communicated with solution choke valve 23 through the 3rd solution heat exchanger 19, solution choke valve 23 has solution pipeline to be communicated with a point steam chest 25 through the second absorber 6 again, by the second generator 2 have refrigerant vapour passage be communicated with successively after the 3rd generator 3 and the 4th generator 4 the 4th generator 4 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15 to be adjusted into the second generator 2 have refrigerant vapour passage to be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline to be communicated with condenser 8 through the second choke valve 15, having refrigerant vapour passage to be communicated with the second absorber 6 to be adjusted into the 3rd generator 3 to set up refrigerant vapour passage the second absorber 6 in the 4th generator 4 is communicated with.
2. in flow process, the refrigerant vapour solution that the 3rd generator 3, heating enter in it of flowing through discharges and provides refrigerant vapour to condenser 8 and the second absorber 6 respectively, the second generator 2, through converging and enter point steam chest 25 again after second absorber 6 of flowing through after solution choke valve 23 reducing pressure by regulating flows, heat absorbing part vaporization through the concentrated solution after the 3rd solution heat exchanger 19 with the 3rd generator 3 after the concentrated solution of the second solution heat exchanger 18, forms the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 11 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline through solution pump 11 through solution pump 11 and solution heat exchanger 17 absorber 5, newly-increased solution heat exchanger C and solution heat exchanger 17 are communicated with generator 1, generator 1 is had concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 17, newly-increased generator A has concentrated solution pipeline to be communicated with absorber 5 through newly-increased solution heat exchanger C again, after having refrigerant vapour passage to be communicated with the second generator 2 in generator 1, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 to be adjusted into generator 1 again and increases generator A after having refrigerant vapour passage to be communicated with newly-increased generator A newly and have cryogen liquid pipeline warp to increase choke valve B newly to be communicated with evaporimeter 9 again, after newly-increased generator A also has refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 again.
2. in flow process, the refrigerant vapour that generator 1 produces offers newly-increased generator A and makes to drive thermal medium, the weak solution of absorber 5 is through solution pump 11, newly-increased solution heat exchanger C and solution heat exchanger 17 enter generator 1, the concentrated solution of generator 1 enters newly-increased generator A through solution heat exchanger 17, refrigerant vapour is flowed through and is increased generator A newly, the solution that heating enters in it discharges and provides refrigerant vapour to make to drive thermal medium to the second generator 2, the concentrated solution of newly-increased generator A enters absorber 5 through newly-increased solution heat exchanger C, flow through after the refrigerant vapour heat release of newly-increased generator A becomes cryogen liquid and enter evaporimeter 9 through newly-increased choke valve B throttling, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 12 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased choke valve, newly-increased solution pump and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline to be communicated with newly-increased generator A through solution pump 11 and solution heat exchanger 17 through solution pump 11 and solution heat exchanger 17 absorber 5, newly-increased generator A has concentrated solution pipeline to be communicated with generator 1 through newly-increased solution pump D and newly-increased solution heat exchanger C again, there is concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 to have concentrated solution pipeline to be communicated with absorber 5 through newly-increased solution heat exchanger C and solution heat exchanger 17 in generator 1, after having refrigerant vapour passage to be communicated with the second generator 2 in generator 1, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 to be adjusted into generator 1 again and increases generator A after having refrigerant vapour passage to be communicated with newly-increased generator A newly and have cryogen liquid pipeline warp to increase choke valve B newly to be communicated with evaporimeter 9 again, after newly-increased generator A also has refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 again.
2. in flow process, the refrigerant vapour that generator 1 produces offers newly-increased generator A and makes to drive thermal medium, the weak solution of absorber 5 enters newly-increased generator A through solution pump 11 and solution heat exchanger 17, refrigerant vapour is flowed through and is increased generator A newly, the solution that heating enters in it discharges and provides refrigerant vapour to make to drive thermal medium to the second generator 2, flow through after the refrigerant vapour heat release of newly-increased generator A becomes cryogen liquid and enter evaporimeter 9 through newly-increased choke valve B throttling, the concentrated solution of newly-increased generator A enters generator 1 through newly-increased solution pump D and newly-increased solution heat exchanger C, the concentrated solution of generator 1 enters absorber 5 through newly-increased solution heat exchanger C and solution heat exchanger 17, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 13 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased choke valve, newly-increased solution pump and newly-increased solution heat exchanger, absorber 5 is set up weak solution pipeline and is communicated with newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, newly-increased generator A also has concentrated solution pipeline to be communicated with absorber 5 through newly-increased solution heat exchanger C, after having refrigerant vapour passage to be communicated with the second generator 2 in generator 1, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 to be adjusted into generator 1 again and increases generator A after having refrigerant vapour passage to be communicated with newly-increased generator A newly and have cryogen liquid pipeline warp to increase choke valve B newly to be communicated with evaporimeter 9 again, after newly-increased generator A also has refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 again.
2. in flow process, the refrigerant vapour that generator 1 produces offers newly-increased generator A and makes to drive thermal medium, the part weak solution of absorber 5 enters newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, refrigerant vapour is flowed through and is increased generator A newly, the solution that heating enters in it discharges and provides refrigerant vapour to make to drive thermal medium to the second generator 2, the concentrated solution of newly-increased generator A enters absorber 5 through newly-increased solution heat exchanger C, flow through after the refrigerant vapour heat release of newly-increased generator A becomes cryogen liquid and enter evaporimeter 9 through newly-increased choke valve B throttling, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 14 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased condenser, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline through solution pump 11 through solution pump 11 and solution heat exchanger 17 absorber 5, newly-increased solution heat exchanger C and solution heat exchanger 17 are communicated with generator 1, generator 1 is had concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 17, newly-increased generator A has concentrated solution pipeline to be communicated with absorber 5 through newly-increased solution heat exchanger C again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased condenser E, newly-increased condenser E also has cryogen liquid pipeline to be communicated with evaporimeter 9 through newly-increased choke valve B, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition, newly-increased condenser E also has heated medium pipeline to be communicated with outside.
2. in flow process, the weak solution of absorber 5 enters generator 1 through solution pump 11, newly-increased solution heat exchanger C and solution heat exchanger 17, the concentrated solution of generator 1 enters newly-increased generator A through solution heat exchanger 17, the solution that drives heat medium flow to enter in it through newly-increased generator A, heating discharges and provides refrigerant vapour to newly-increased condenser E, and the concentrated solution of newly-increased generator A enters absorber 5 through newly-increased solution heat exchanger C; The refrigerant vapour heat release of newly-increased condenser E becomes cryogen liquid in heated medium, and the cryogen liquid of newly-increased condenser E enters evaporimeter 9 through newly-increased choke valve B throttling, forms the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 15 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger, newly-increased condenser, newly-increased solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline through solution pump 11 through solution pump 11 and solution heat exchanger 17 absorber 5, newly-increased solution heat exchanger C and solution heat exchanger 17 are communicated with generator 1, generator 1 is had concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 17, newly-increased generator A has concentrated solution pipeline to be communicated with absorber 5 through newly-increased solution heat exchanger C again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased condenser E, newly-increased condenser E also has cryogen liquid pipeline to be communicated with evaporimeter 9 through newly-increased choke valve B, there is concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 4th solution heat exchanger 20 to be adjusted into the 4th generator 4 to have concentrated solution pipeline to be communicated with the newly-increased steam chest F of dividing through newly-increased solution pump D and newly-increased condenser E in the 4th generator 4, a newly-increased point steam chest F has concentrated solution pipeline to be communicated with the 3rd absorber 7 through the 4th solution heat exchanger 20 again, having refrigerant vapour passage to be communicated with the 3rd generator 3 to be adjusted into the second generator 2 and a newly-increased point steam chest F to have refrigerant vapour passage to be communicated with the 3rd generator 3 in the second generator 2---the second generator and the newly-increased steam chest that divides provide driving thermal medium to the 3rd generator jointly, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition.
2. in flow process, the weak solution of absorber 5 is through solution pump 11, newly-increased solution heat exchanger C and solution heat exchanger 17 enter generator 1, the concentrated solution of generator 1 enters newly-increased generator A through solution heat exchanger 17, drive heat medium flow through newly-increased generator A, the solution that heating enters in it discharges and provides refrigerant vapour to newly-increased condenser E, the concentrated solution of newly-increased generator A enters absorber 5 through newly-increased solution heat exchanger C, the refrigerant vapour heat release of newly-increased condenser E becomes cryogen liquid in the solution of flowing through in it, the cryogen liquid of newly-increased condenser E enters evaporimeter 9 through newly-increased choke valve B throttling, the concentrated solution of the 4th generator 4 enters newly-increased point steam chest F after flow through after newly-increased solution pump D pressurization newly-increased condenser E, heat absorbing part vaporization, the concentrated solution of newly-increased point steam chest F enters the 3rd absorber 7 through the 4th solution heat exchanger 20, the refrigerant vapour of newly-increased point steam chest F is flowed through after the 3rd generator 3 becomes cryogen liquid with the 4th generator 4, heat release and is entered condenser 8 through the second choke valve 15 throttlings again, forms the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 16 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline to be communicated with newly-increased absorber G through solution pump 11 and newly-increased solution heat exchanger C through solution pump 11 and solution heat exchanger 17 absorber 5, newly-increased absorber G has weak solution pipeline to be communicated with generator 1 through newly-increased solution pump D and solution heat exchanger 17 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 17, newly-increased generator A has concentrated solution pipeline to be communicated with absorber 5 through newly-increased solution heat exchanger C again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased absorber G, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber G also has heated medium pipeline to be communicated with outside.
2. in flow process, the weak solution of absorber 5 enters newly-increased absorber G through solution pump 11 and newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in heated medium, the weak solution of newly-increased absorber G enters generator 1 through newly-increased solution pump D and solution heat exchanger 17, the concentrated solution of generator 1 enters newly-increased generator A through solution heat exchanger 17, drive heat medium flow through newly-increased generator A, the solution that heating enters in it discharges and provides refrigerant vapour to newly-increased absorber G, the concentrated solution of newly-increased generator A enters absorber 5 through newly-increased solution heat exchanger C, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 17 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline to be communicated with newly-increased absorber G through solution pump 11 and newly-increased solution heat exchanger C through solution pump 11 and solution heat exchanger 17 absorber 5, newly-increased absorber G has weak solution pipeline to be communicated with generator 1 through newly-increased solution pump D and solution heat exchanger 17 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 17, newly-increased generator A has concentrated solution pipeline to be communicated with absorber 5 through newly-increased solution heat exchanger C again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased absorber G, there is concentrated solution pipeline to be communicated with the second solution heat exchanger 18 to be adjusted into the second generator 2 to have concentrated solution pipeline to be communicated with the newly-increased steam chest F of dividing through newly-increased absorber G in the second generator 2, a newly-increased point steam chest F has concentrated solution pipeline to be communicated with the second solution heat exchanger 18 again, having refrigerant vapour passage to be communicated with the 3rd generator 3 to be adjusted into the second generator 2 and a newly-increased point steam chest F to have refrigerant vapour passage to be communicated with the 3rd generator 3 in the second generator 2---the second generator and the newly-increased steam chest that divides provide driving thermal medium to the 3rd generator jointly, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition.
2. in flow process, the weak solution of absorber 5 enters newly-increased absorber G, absorbs refrigerant vapour heat release in the solution of flowing through in it through solution pump 11 and newly-increased solution heat exchanger C, the weak solution of newly-increased absorber G enters generator 1 through newly-increased solution pump D and solution heat exchanger 17, the concentrated solution of generator 1 enters newly-increased generator A through solution heat exchanger 17, the solution that drives heat medium flow to enter in it through newly-increased generator A, heating discharges and provides refrigerant vapour to newly-increased absorber G, and the concentrated solution of newly-increased generator A enters absorber 5 through newly-increased solution heat exchanger C; The concentrated solution of the second generator 2 enters a newly-increased point steam chest F after flowing through and increasing absorber G, heat absorbing part vaporization newly, the concentrated solution of newly-increased point steam chest F enters the 3rd generator 3 through the second solution heat exchanger 18, the refrigerant vapour of newly-increased point of steam chest F the 3rd generator 3 of flowing through enters condenser 8 through the second choke valve 15 throttlings become cryogen liquid with the 4th generator 4, heat release after, forms the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 18 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased point steam chest, newly-increased solution choke valve and newly-increased the second solution choke valve, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline to be communicated with newly-increased absorber G through solution pump 11 and solution heat exchanger 17 through solution pump 11 and solution heat exchanger 17 absorber 5, newly-increased absorber G has weak solution pipeline to be communicated with generator 1 through newly-increased the second solution choke valve I again, there is concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 to have concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased solution pump D in generator 1, newly-increased generator A also has concentrated solution pipeline to be communicated with a newly-increased point steam chest F through newly-increased solution choke valve H and newly-increased absorber G, a newly-increased point steam chest F has concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased absorber G, after having refrigerant vapour passage to be communicated with the second generator 2 in generator 1 the second generator 2 have again cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 to be adjusted into generator 1 and increase newly divide a steam chest F to have refrigerant vapour passage to be communicated with the second generator 2 after the second generator 2 have again cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition.
2. in flow process, the weak solution of absorber 5 enters newly-increased absorber G through solution pump 11 and solution heat exchanger 17, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of newly-increased absorber G enters generator 1 through newly-increased the second solution choke valve I reducing pressure by regulating flow, the concentrated solution of generator 1 enters newly-increased generator A through newly-increased solution pump D pressurization, drive heat medium flow through newly-increased generator A, the solution that heating enters in it discharges and provides refrigerant vapour to newly-increased absorber G, the concentrated solution of newly-increased generator A is flowed through and is increased absorber G newly after solution choke valve H reducing pressure by regulating flow, after heat absorbing part vaporization, enter newly-increased point steam chest F, the concentrated solution of newly-increased point steam chest F enters absorber 5 through solution heat exchanger 17, the refrigerant vapour of newly-increased point of steam chest F second generator 2 of flowing through, heat release enters evaporimeter 9 through choke valve 14 throttlings after becoming cryogen liquid again, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 19 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased point steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline to be communicated with newly-increased absorber G through solution pump 11 and solution heat exchanger 17 through solution pump 11 and solution heat exchanger 17 absorber 5, newly-increased absorber G also has weak solution pipeline to be communicated with newly-increased generator A, newly-increased generator A has concentrated solution pipeline to be communicated with generator 1 through newly-increased solution choke valve H again, there is concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 to have concentrated solution pipeline to be communicated with the newly-increased steam chest F of dividing through newly-increased absorber G in generator 1, a newly-increased point steam chest F has concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased absorber G, after having refrigerant vapour passage to be communicated with the second generator 2 in generator 1 the second generator 2 have again cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 to be adjusted into generator 1 and increase newly divide a steam chest F to have refrigerant vapour passage to be communicated with the second generator 2 after the second generator 2 have again cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition.
2. in flow process, the weak solution of absorber 5 enters newly-increased absorber G through solution pump 11 and solution heat exchanger 17, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of newly-increased absorber G enters newly-increased generator A, drive heat medium flow through newly-increased generator A, the solution that heating enters in it discharges and provides refrigerant vapour to newly-increased absorber G, the concentrated solution of newly-increased generator A enters generator 1 through solution choke valve H reducing pressure by regulating flow, the concentrated solution of generator 1 is flowed through and is increased absorber G newly, after heat absorbing part vaporization, enter newly-increased point steam chest F, the concentrated solution of newly-increased point steam chest F enters absorber 5 through solution heat exchanger 17, the refrigerant vapour of newly-increased point of steam chest F second generator 2 of flowing through, heat release enters evaporimeter 9 through choke valve 14 throttlings after becoming cryogen liquid again, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 20 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased solution heat exchanger and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline through solution pump 11 through solution pump 11 and solution heat exchanger 17 absorber 5, solution heat exchanger 17 and newly-increased solution heat exchanger C are communicated with newly-increased absorber G, newly-increased absorber G also has weak solution pipeline to be communicated with newly-increased generator A, newly-increased generator A has concentrated solution pipeline to be communicated with generator 1 through newly-increased solution heat exchanger C again, there is concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 to have concentrated solution pipeline to be communicated with the newly-increased steam chest F of dividing through newly-increased absorber G in generator 1, a newly-increased point steam chest F has concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased absorber G, after having refrigerant vapour passage to be communicated with the second generator 2 in generator 1 the second generator 2 have again cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14 to be adjusted into generator 1 and increase newly divide a steam chest F to have refrigerant vapour passage to be communicated with the second generator 2 after the second generator 2 have again cryogen liquid pipeline to be communicated with evaporimeter 9 through choke valve 14, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition.
2. in flow process, the weak solution of absorber 5 is through solution pump 11, solution heat exchanger 17 and newly-increased solution heat exchanger C enter newly-increased absorber G, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of newly-increased absorber G enters newly-increased generator A, drive heat medium flow through newly-increased generator A, the solution that heating enters in it discharges and provides refrigerant vapour to newly-increased absorber G, the concentrated solution of newly-increased generator A enters generator 1 through newly-increased solution heat exchanger C, the concentrated solution of generator 1 is flowed through and is increased absorber G newly, after heat absorbing part vaporization, enter newly-increased point steam chest F, the concentrated solution of newly-increased point steam chest F enters absorber 5 through solution heat exchanger 17, the refrigerant vapour of newly-increased point of steam chest F second generator 2 of flowing through, heat release enters evaporimeter 9 through choke valve 14 throttlings after becoming cryogen liquid again, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 21 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased choke valve, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased point steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline to be communicated with newly-increased absorber G through solution pump 11 and newly-increased solution heat exchanger C through solution pump 11 and solution heat exchanger 17 absorber 5, newly-increased absorber G has weak solution pipeline to be communicated with generator 1 through newly-increased solution pump D and solution heat exchanger 17 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 17, newly-increased generator A also has concentrated solution pipeline to be communicated with a newly-increased point steam chest F through newly-increased solution choke valve H and newly-increased absorber G, a newly-increased point steam chest F has concentrated solution pipeline to be communicated with absorber 5 through newly-increased solution heat exchanger C again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased absorber G, a newly-increased point steam chest F also has refrigerant vapour passage to be communicated with newly-increased condenser E, newly-increased condenser E also has cryogen liquid pipeline to be communicated with evaporimeter 9 through newly-increased choke valve B, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition, newly-increased condenser E also has heated medium pipeline to be communicated with outside.
2. in flow process, the weak solution of absorber 5 enters newly-increased absorber G through solution pump 11 and newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of newly-increased absorber G enters generator 1 through newly-increased solution pump D and solution heat exchanger 17, the concentrated solution of generator 1 enters newly-increased generator A through solution heat exchanger 17, drive heat medium flow through newly-increased generator A, the solution that heating enters in it discharges and provides refrigerant vapour to newly-increased absorber G, the concentrated solution of newly-increased generator A is flowed through and is increased absorber G newly after solution choke valve H reducing pressure by regulating flow, after heat absorbing part vaporization, enter newly-increased point steam chest F, the concentrated solution of newly-increased point steam chest F enters absorber 5 through newly-increased solution heat exchanger C, the refrigerant vapour of newly-increased point steam chest F enters newly-increased condenser E, heat release becomes cryogen liquid in heated medium, the cryogen liquid of newly-increased condenser E enters evaporimeter 9 through newly-increased choke valve B throttling, form the first-class absorption type heat pump that circulates along separate routes.
Shunt circulation first-class absorption type heat pump shown in Figure 22 is achieved in that
1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 5 and to have weak solution pipeline to be communicated with newly-increased the second absorber J through solution pump 11 and newly-increased solution heat exchanger C through solution pump 11 and solution heat exchanger 17 absorber 5, newly-increased the second absorber J also has weak solution pipeline to be communicated with newly-increased absorber G through newly-increased solution pump D and newly-increased the second solution heat exchanger K, newly-increased absorber G has weak solution pipeline to be communicated with generator 1 through newly-increased the second solution pump L and solution heat exchanger 17 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 5 through solution heat exchanger 17 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 17, newly-increased generator A also has concentrated solution pipeline to be communicated with a newly-increased point steam chest F through newly-increased solution choke valve H and newly-increased absorber G, a newly-increased point steam chest F has concentrated solution pipeline to be communicated with absorber 5 through newly-increased the second solution heat exchanger K and newly-increased solution heat exchanger C again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased absorber G, a newly-increased point steam chest F also has refrigerant vapour passage to be communicated with newly-increased the second absorber J, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition, newly-increased the second absorber J also has heated medium pipeline to be communicated with outside.
2. in flow process, the weak solution of absorber 5 enters newly-increased the second absorber J through solution pump 11 and newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in heated medium, the weak solution of newly-increased the second absorber J enters newly-increased absorber G through newly-increased solution pump D and newly-increased the second solution heat exchanger K, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of newly-increased absorber G enters generator 1 through newly-increased the second solution pump L and solution heat exchanger 17, the concentrated solution of generator 1 enters newly-increased generator A through solution heat exchanger 17, drive heat medium flow through newly-increased generator A, the solution that heating enters in it discharges and provides refrigerant vapour to newly-increased absorber G, the concentrated solution of newly-increased generator A is flowed through and is increased absorber G newly after solution choke valve H reducing pressure by regulating flow, after heat absorbing part vaporization, enter newly-increased point steam chest F, the concentrated solution of newly-increased point steam chest F enters absorber 5 through newly-increased the second solution heat exchanger K and newly-increased solution heat exchanger C, the refrigerant vapour of newly-increased point steam chest F enters newly-increased the second absorber J, form the first-class absorption type heat pump that circulates along separate routes.
The effect that the technology of the present invention can realize---shunt circulation first-class absorption type heat pump proposed by the invention has following effect and advantage:
(1) circulation substep are realized temperature drop along separate routes, can adopt different operating solution, are conducive to drive selection and coupling between thermal medium, circulation solution and flow process, overcome the restriction of single working media, improve the temperature difference and utilize level.
(2) comprise single-action and supply thermal flow process for thermal flow process, economic benefits and social benefits for thermal flow process and backheat, multiterminal heat supply, adapts to the wide occasion of heated medium range of temperature, is conducive to improve heat utilization rate.
(3) there is the flow process of backheat heat supply end and there is single-action-economic benefits and social benefits backheat or there is the flow process of economic benefits and social benefits backheat, thermodynamic parameter smooth change, heating parameter is adjustable, and adaptation condition changes preferably, obtains higher thermodynamics sophistication.
(4) enrich the type of first-class absorption type heat pump, expanded the range of application of first-class absorption type heat pump, be conducive to adopt better first-class absorption type heat pump to realize temperature difference utilization, improved utilization efficiency of heat energy.

Claims (42)

1. the first-class absorption type heat pump that circulates along separate routes, is mainly made up of generator, the second generator, the 3rd generator, the 4th generator, absorber, the second absorber, the 3rd absorber, condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, the 3rd solution pump, choke valve, the second choke valve, the 3rd choke valve, solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and the 4th solution heat exchanger, absorber (5) has weak solution pipeline to be communicated with generator (1) through solution pump (11) and solution heat exchanger (17), generator (1) also has concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17), after generator (1) also has refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) again---and generator provides refrigerant vapour to make to drive thermal medium to the second generator, evaporimeter (9) also has refrigerant vapour passage to be communicated with absorber (5), the 3rd absorber (7) has weak solution pipeline to be communicated with the second absorber (6) through the 3rd solution pump (13) and the 4th solution heat exchanger (20), the second absorber (6) also has weak solution pipeline through the second solution pump (12), the 3rd solution heat exchanger (19) and the second solution heat exchanger (18) are communicated with the second generator (2), the second generator (2) also has concentrated solution pipeline to be communicated with the 3rd generator (3) through the second solution heat exchanger (18), the 3rd generator (3) also has concentrated solution pipeline to be communicated with the 4th generator (4) through the 3rd solution heat exchanger (19), the 4th generator (4) also has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20), the second generator (2) also have refrigerant vapour passage be communicated with successively the 3rd generator (3) and the 4th generator (4) afterwards the 4th generator (4) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15)---the second generator provides refrigerant vapour do driving thermal medium to the 3rd generator and the 4th generator, the 3rd generator (3) also has refrigerant vapour passage to be communicated with condenser (8), the 4th generator (4) also has refrigerant vapour passage to be communicated with the second absorber (6), condenser (8) also has cryogen liquid pipeline to be communicated with the second evaporimeter (10) through the 3rd choke valve (16), the second evaporimeter (10) also has refrigerant vapour passage to be communicated with the 3rd absorber (7), generator (1) drives thermal medium pipeline to be communicated with outside in addition, absorber (5), the second absorber (6), the 3rd absorber (7) and condenser (8) also have respectively heated medium pipeline to be communicated with outside, evaporimeter (9) and the second evaporimeter (10) medium pipeline that also has surplus heat is respectively communicated with outside, forms the shunt first-class absorption type heat pump that circulates.
2. the first-class absorption type heat pump that circulates along separate routes, is mainly made up of generator, the second generator, the 3rd generator, the 4th generator, absorber, the second absorber, the 3rd absorber, condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, the 3rd solution pump, the 4th solution pump, choke valve, the second choke valve, the 3rd choke valve, solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and the 4th solution heat exchanger, absorber (5) has weak solution pipeline to be communicated with generator (1) through solution pump (11) and solution heat exchanger (17), generator (1) also has concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17), after generator (1) also has refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) again---and generator provides refrigerant vapour to make to drive thermal medium to the second generator, evaporimeter (9) also has refrigerant vapour passage to be communicated with absorber (5), the 3rd absorber (7) has weak solution pipeline to be communicated with the second absorber (6) through the 3rd solution pump (13) and the 4th solution heat exchanger (20), the second absorber (6) also has weak solution pipeline to be communicated with the 3rd generator (3) through the second solution pump (12) and the 3rd solution heat exchanger (19), the 3rd generator (3) also has concentrated solution pipeline to be communicated with the second generator (2) through the 4th solution pump (21) and the second solution heat exchanger (18), the second generator (2) also has concentrated solution pipeline to be communicated with the 4th generator (4) through the second solution heat exchanger (18) and the 3rd solution heat exchanger (19), the 4th generator (4) also has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20), the second generator (2) also have refrigerant vapour passage be communicated with successively the 3rd generator (3) and the 4th generator (4) afterwards the 4th generator (4) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15)---the second generator provides refrigerant vapour do driving thermal medium to the 3rd generator and the 4th generator, the 3rd generator (3) also has refrigerant vapour passage to be communicated with condenser (8), the 4th generator (4) also has refrigerant vapour passage to be communicated with the second absorber (6), condenser (8) also has cryogen liquid pipeline to be communicated with the second evaporimeter (10) through the 3rd choke valve (16), the second evaporimeter (10) also has refrigerant vapour passage to be communicated with the 3rd absorber (7), generator (1) drives thermal medium pipeline to be communicated with outside in addition, absorber (5), the second absorber (6), the 3rd absorber (7) and condenser (8) also have respectively heated medium pipeline to be communicated with outside, evaporimeter (9) and the second evaporimeter (10) medium pipeline that also has surplus heat is respectively communicated with outside, forms the shunt first-class absorption type heat pump that circulates.
3. the first-class absorption type heat pump that circulates along separate routes, is mainly made up of generator, the second generator, the 3rd generator, the 4th generator, absorber, the second absorber, the 3rd absorber, condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, the 3rd solution pump, the 4th solution pump, choke valve, the second choke valve, the 3rd choke valve, solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and the 4th solution heat exchanger, absorber (5) has weak solution pipeline to be communicated with generator (1) through solution pump (11) and solution heat exchanger (17), generator (1) also has concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17), after generator (1) also has refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) again---and generator provides refrigerant vapour to make to drive thermal medium to the second generator, evaporimeter (9) also has refrigerant vapour passage to be communicated with absorber (5), the 3rd absorber (7) has weak solution pipeline to be communicated with the second absorber (6) through the 3rd solution pump (13) and the 4th solution heat exchanger (20), the second absorber (6) also has weak solution pipeline to be communicated with the second generator (2) through the second solution pump (12) and the second solution heat exchanger (18), the second absorber (6) also has weak solution pipeline to be communicated with the 3rd generator (3) through the 4th solution pump (21) and the 3rd solution heat exchanger (19), the second generator (2) also has concentrated solution pipeline to be communicated with the 4th generator (4) through the second solution heat exchanger (18), the 3rd generator (3) also has concentrated solution pipeline to be communicated with the 4th generator (4) through the 3rd solution heat exchanger (19), the 4th generator (4) also has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20), the second generator (2) also have refrigerant vapour passage be communicated with successively the 3rd generator (3) and the 4th generator (4) afterwards the 4th generator (4) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15)---the second generator provides refrigerant vapour do driving thermal medium to the 3rd generator and the 4th generator, the 3rd generator (3) also has refrigerant vapour passage to be communicated with condenser (8), the 4th generator (4) also has refrigerant vapour passage to be communicated with the second absorber (6), condenser (8) also has cryogen liquid pipeline to be communicated with the second evaporimeter (10) through the 3rd choke valve (16), the second evaporimeter (10) also has refrigerant vapour passage to be communicated with the 3rd absorber (7), generator (1) drives thermal medium pipeline to be communicated with outside in addition, absorber (5), the second absorber (6), the 3rd absorber (7) and condenser (8) also have respectively heated medium pipeline to be communicated with outside, evaporimeter (9) and the second evaporimeter (10) medium pipeline that also has surplus heat is respectively communicated with outside, forms the shunt first-class absorption type heat pump that circulates.
4. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 1, cancel the 4th generator, having concentrated solution pipeline to have concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 3rd generator (3) through the 3rd solution heat exchanger (19) and the 4th generator (4) connected sum the 4th generator (4) in the 3rd generator (3) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20), by the second generator (2) have refrigerant vapour passage be communicated with successively the 3rd generator (3) and the 4th generator (4) afterwards the 4th generator (4) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15) to be adjusted into the second generator (2) have refrigerant vapour passage to be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15), having refrigerant vapour passage to be communicated with the second absorber (6) to be adjusted into the 3rd generator (3) to set up refrigerant vapour passage the second absorber (6) in the 4th generator (4) is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
5. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 2, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator (4) through the second solution heat exchanger (18) and the 3rd solution heat exchanger (19) in the second generator (2), the 4th generator (4) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the second generator (2) has concentrated solution pipeline through the second solution heat exchanger (18), the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20) are communicated with the 4th generator (4), by the second generator (2) have refrigerant vapour passage be communicated with successively the 3rd generator (3) and the 4th generator (4) afterwards the 4th generator (4) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15) to be adjusted into the second generator (2) have refrigerant vapour passage to be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15), having refrigerant vapour passage to be communicated with the second absorber (6) to be adjusted into the 3rd generator (3) to set up refrigerant vapour passage the second absorber (6) in the 4th generator (4) is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
6. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 3, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator (4) through the second solution heat exchanger (18) in the second generator (2), the 3rd generator (3) has concentrated solution pipeline to be communicated with the 4th generator (4) through the 3rd solution heat exchanger (19), the 4th generator (4) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the second generator (2) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the second solution heat exchanger (18) and the 4th solution heat exchanger (20), the 3rd generator (3) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20), by the second generator (2) have refrigerant vapour passage be communicated with successively the 3rd generator (3) and the 4th generator (4) afterwards the 4th generator (4) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15) to be adjusted into the second generator (2) have refrigerant vapour passage to be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15), having refrigerant vapour passage to be communicated with the second absorber (6) to be adjusted into the 3rd generator (3) to set up refrigerant vapour passage the second absorber (6) in the 4th generator (4) is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
7. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 1, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 4th solution pump, there is weak solution pipeline to be communicated with the second absorber (6) and to be adjusted into the 3rd absorber (7) and to have weak solution pipeline to be communicated with the 4th absorber (22) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) the 3rd absorber (7), the 4th absorber (22) has weak solution pipeline to be communicated with the second absorber (6) through the 4th solution pump (21) and the 5th solution heat exchanger (24) again, there is concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 4th generator (4) to have concentrated solution pipeline to be communicated with a point steam chest (25) through solution choke valve (23) and the second absorber (6) in the 4th generator (4), divide steam chest (25) to have again concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20), divide steam chest (25) to also have refrigerant vapour passage to be communicated with the 4th absorber (22), the 4th absorber (22) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
8. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 1, cancel the second absorber (6) and the outside heated medium pipeline being communicated with, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 4th solution pump, there is weak solution pipeline to be communicated with the second absorber (6) and to be adjusted into the 3rd absorber (7) and to have weak solution pipeline to be communicated with the 4th absorber (22) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) the 3rd absorber (7), the 4th absorber (22) has weak solution pipeline to be communicated with the second absorber (6) through the 4th solution pump (21) and the 5th solution heat exchanger (24) again, there is concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 4th generator (4) to have concentrated solution pipeline to be communicated with a point steam chest (25) through solution choke valve (23) and the second absorber (6) in the 4th generator (4), divide steam chest (25) to have again concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20), divide steam chest (25) to also have refrigerant vapour passage to be communicated with the 4th absorber (22), the 4th absorber (22) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
9. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 2, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 5th solution pump, there is weak solution pipeline to be communicated with the second absorber (6) and to be adjusted into the 3rd absorber (7) and to have weak solution pipeline to be communicated with the 4th absorber (22) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) the 3rd absorber (7), the 4th absorber (22) has weak solution pipeline to be communicated with the second absorber (6) through the 5th solution pump (26) and the 5th solution heat exchanger (24) again, there is concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 4th generator (4) to have concentrated solution pipeline to be communicated with a point steam chest (25) through solution choke valve (23) and the second absorber (6) in the 4th generator (4), divide steam chest (25) to have again concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20), divide steam chest (25) to also have refrigerant vapour passage to be communicated with the 4th absorber (22), the 4th absorber (22) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
10. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 2, cancel the second absorber (6) and the outside heated medium pipeline being communicated with, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 5th solution pump, there is weak solution pipeline to be communicated with the second absorber (6) and to be adjusted into the 3rd absorber (7) and to have weak solution pipeline to be communicated with the 4th absorber (22) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) the 3rd absorber (7), the 4th absorber (22) has weak solution pipeline to be communicated with the second absorber (6) through the 5th solution pump (26) and the 5th solution heat exchanger (24) again, there is concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 4th generator (4) to have concentrated solution pipeline to be communicated with a point steam chest (25) through solution choke valve (23) and the second absorber (6) in the 4th generator (4), divide steam chest (25) to have again concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20), divide steam chest (25) to also have refrigerant vapour passage to be communicated with the 4th absorber (22), the 4th absorber (22) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
11. first-class absorption type heat pumps that circulate along separate routes, in shunt circulation first-class absorption type heat pump claimed in claim 3, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 5th solution pump, there is weak solution pipeline to be communicated with the second absorber (6) and to be adjusted into the 3rd absorber (7) and to have weak solution pipeline to be communicated with the 4th absorber (22) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) the 3rd absorber (7), the 4th absorber (22) has weak solution pipeline to be communicated with the second absorber (6) through the 5th solution pump (26) and the 5th solution heat exchanger (24) again, there is concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 4th generator (4) to have concentrated solution pipeline to be communicated with a point steam chest (25) through solution choke valve (23) and the second absorber (6) in the 4th generator (4), divide steam chest (25) to have again concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20), divide steam chest (25) to also have refrigerant vapour passage to be communicated with the 4th absorber (22), the 4th absorber (22) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
12. first-class absorption type heat pumps that circulate along separate routes, in shunt circulation first-class absorption type heat pump claimed in claim 3, cancel the second absorber (6) and the outside heated medium pipeline being communicated with, increase solution choke valve, divide steam chest, the 5th solution heat exchanger, the 4th absorber and the 5th solution pump, there is weak solution pipeline to be communicated with the second absorber (6) and to be adjusted into the 3rd absorber (7) and to have weak solution pipeline to be communicated with the 4th absorber (22) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) through the 3rd solution pump (13) and the 4th solution heat exchanger (20) the 3rd absorber (7), the 4th absorber (22) has weak solution pipeline to be communicated with the second absorber (6) through the 5th solution pump (26) and the 5th solution heat exchanger (24) again, there is concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 4th generator (4) to have concentrated solution pipeline to be communicated with a point steam chest (25) through solution choke valve (23) and the second absorber (6) in the 4th generator (4), divide steam chest (25) to have again concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20), divide steam chest (25) to also have refrigerant vapour passage to be communicated with the 4th absorber (22), the 4th absorber (22) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
13. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 7-8, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator (4) through the 3rd solution heat exchanger (19) in the 3rd generator (3), the 4th generator (4) has concentrated solution pipeline to be communicated with a point steam chest (25) through solution choke valve (23) and the second absorber (6) to be adjusted into the 3rd generator (3) has concentrated solution pipeline through the 3rd solution heat exchanger (19), solution choke valve (23) and the second absorber (6) are communicated with a point steam chest (25), by the second generator (2) have refrigerant vapour passage be communicated with successively the 3rd generator (3) and the 4th generator (4) afterwards the 4th generator (4) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15) to be adjusted into the second generator (2) have refrigerant vapour passage to be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15), having refrigerant vapour passage to be communicated with the second absorber (6) to be adjusted into the 3rd generator (3) to set up refrigerant vapour passage the second absorber (6) in the 4th generator (4) is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
14. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 9-10, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator (4) through the second solution heat exchanger (18) and the 3rd solution heat exchanger (19) in the second generator (2), the 4th generator (4) has concentrated solution pipeline to be communicated with a point steam chest (25) through solution choke valve (23) and the second absorber (6) to be adjusted into the second generator (2) has concentrated solution pipeline through the second solution heat exchanger (18), the 3rd solution heat exchanger (19), solution choke valve (23) and the second absorber (6) are communicated with a point steam chest (25), by the second generator (2) have refrigerant vapour passage be communicated with successively the 3rd generator (3) and the 4th generator (4) afterwards the 4th generator (4) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15) to be adjusted into the second generator (2) have refrigerant vapour passage to be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15), having refrigerant vapour passage to be communicated with the second absorber (6) to be adjusted into the 3rd generator (3) to set up refrigerant vapour passage the second absorber (6) in the 4th generator (4) is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
15. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 11-12, cancel the 4th generator, there is concentrated solution pipeline to be communicated with the 4th generator (4) through the second solution heat exchanger (18) in the second generator (2), the 3rd generator (3) has concentrated solution pipeline to be communicated with the 4th generator (4) through the 3rd solution heat exchanger (19), the 4th generator (4) has concentrated solution pipeline to be communicated with a point steam chest (25) through solution choke valve (23) and the second absorber (6) to be adjusted into the second generator (2) has concentrated solution pipeline to be communicated with solution choke valve (23) through the second solution heat exchanger (18), the 3rd generator (3) has concentrated solution pipeline to be communicated with solution choke valve (23) through the 3rd solution heat exchanger (19), solution choke valve (23) has solution pipeline to be communicated with a point steam chest (25) through the second absorber (6) again, by the second generator (2) have refrigerant vapour passage be communicated with successively the 3rd generator (3) and the 4th generator (4) afterwards the 4th generator (4) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15) to be adjusted into the second generator (2) have refrigerant vapour passage to be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline to be communicated with condenser (8) through the second choke valve (15), having refrigerant vapour passage to be communicated with the second absorber (6) to be adjusted into the 3rd generator (3) to set up refrigerant vapour passage the second absorber (6) in the 4th generator (4) is communicated with, form the first-class absorption type heat pump that circulates along separate routes.
16. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline through solution pump (11) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased solution heat exchanger (C) and solution heat exchanger (17) are communicated with generator (1), generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, after having refrigerant vapour passage to be communicated with the second generator (2) in generator (1), the second generator (2) has cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) to be adjusted into generator (1) again and increases generator (A) after having refrigerant vapour passage to be communicated with newly-increased generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly to be communicated with evaporimeter (9) again---and generator provides refrigerant vapour do driving thermal medium to newly-increased generator, after newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) again, form the first-class absorption type heat pump that circulates along separate routes.
17. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased generator (A) through solution pump (11) and solution heat exchanger (17) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased generator (A) has concentrated solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C) again, there is concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) to have concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) and solution heat exchanger (17) in generator (1), after having refrigerant vapour passage to be communicated with the second generator (2) in generator (1), the second generator (2) has cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) to be adjusted into generator (1) again and increases generator (A) after having refrigerant vapour passage to be communicated with newly-increased generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly to be communicated with evaporimeter (9) again---and generator provides refrigerant vapour do driving thermal medium to newly-increased generator, after newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) again, form the first-class absorption type heat pump that circulates along separate routes.
18. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, absorber (5) is set up weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C), after having refrigerant vapour passage to be communicated with the second generator (2) in generator (1), the second generator (2) has cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) to be adjusted into generator (1) again and increases generator (A) after having refrigerant vapour passage to be communicated with newly-increased generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly to be communicated with evaporimeter (9) again---and generator provides refrigerant vapour do driving thermal medium to newly-increased generator, after newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) again, form the first-class absorption type heat pump that circulates along separate routes.
19. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased condenser, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline through solution pump (11) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased solution heat exchanger (C) and solution heat exchanger (17) are communicated with generator (1), generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (9) through newly-increased choke valve (B), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased condenser (E) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
20. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-3, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger, newly-increased condenser, newly-increased solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline through solution pump (11) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased solution heat exchanger (C) and solution heat exchanger (17) are communicated with generator (1), generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (9) through newly-increased choke valve (B), there is concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 4th generator (4) to have concentrated solution pipeline to divide a steam chest (F) to be communicated with through newly-increased solution pump (D) and newly-increased condenser (E) with increasing newly in the 4th generator (4), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and a newly-increased point steam chest (F) to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
21. first-class absorption type heat pumps that circulate along separate routes, in shunt circulation first-class absorption type heat pump claimed in claim 4, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger, newly-increased condenser, newly-increased solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline through solution pump (11) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased solution heat exchanger (C) and solution heat exchanger (17) are communicated with generator (1), generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (9) through newly-increased choke valve (B), there is concentrated solution pipeline to be communicated with the 3rd absorber (7) and to be adjusted into the 3rd generator (3) and to have concentrated solution pipeline to divide a steam chest (F) to be communicated with through newly-increased solution pump (D) and newly-increased condenser (E) with increasing newly through the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20) in the 3rd generator (3), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and a newly-increased point steam chest (F) to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
22. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger, newly-increased condenser and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline through solution pump (11) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased solution heat exchanger (C) and solution heat exchanger (17) are communicated with generator (1), generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (9) through newly-increased choke valve (B), there is concentrated solution pipeline to be communicated with the second solution heat exchanger (18) to be adjusted into the second generator (2) to have concentrated solution pipeline to be communicated with the newly-increased steam chest (F) that divides through newly-increased condenser (E) in the second generator (2), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the second solution heat exchanger (18) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and a newly-increased point steam chest (F) to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
23. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 7-15, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger, newly-increased condenser, newly-increased solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline through solution pump (11) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased solution heat exchanger (C) and solution heat exchanger (17) are communicated with generator (1), generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (9) through newly-increased choke valve (B), to divide steam chest (25) to have concentrated solution pipeline to be communicated with the 3rd absorber (7) and to be adjusted into a point steam chest (25) and to have concentrated solution pipeline to divide a steam chest (F) to be communicated with through newly-increased solution pump (D) and newly-increased condenser (E) with increasing newly through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and a newly-increased point steam chest (F) to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
24. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber (G) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.
25. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-3, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), there is concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 4th generator (4) to have concentrated solution pipeline to divide a steam chest (F) to be communicated with through newly-increased the second solution pump (L) and newly-increased absorber (G) with increasing newly in the 4th generator (4), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and a newly-increased point steam chest (F) to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
26. first-class absorption type heat pumps that circulate along separate routes, in shunt circulation first-class absorption type heat pump claimed in claim 4, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), there is concentrated solution pipeline to be communicated with the 3rd absorber (7) and to be adjusted into the 3rd generator (3) and to have concentrated solution pipeline to divide a steam chest (F) to be communicated with through newly-increased the second solution pump (L) and newly-increased absorber (G) with increasing newly through the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20) in the 3rd generator (3), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and a newly-increased point steam chest (F) to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
27. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), there is concentrated solution pipeline to be communicated with the second solution heat exchanger (18) to be adjusted into the second generator (2) to have concentrated solution pipeline to be communicated with the newly-increased steam chest (F) that divides through newly-increased absorber (G) in the second generator (2), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the second solution heat exchanger (18) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and a newly-increased point steam chest (F) to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
28. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 7-15, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased the second solution pump and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), to divide steam chest (25) to have concentrated solution pipeline to be communicated with the 3rd absorber (7) and to be adjusted into a point steam chest (25) and to have concentrated solution pipeline to divide a steam chest (F) to be communicated with through newly-increased the second solution pump (L) and newly-increased absorber (G) with increasing newly through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and a newly-increased point steam chest (F) to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator and increase newly and divide a steam chest jointly to provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
29. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased point steam chest, newly-increased solution choke valve and newly-increased the second solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and solution heat exchanger (17) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased the second solution choke valve (I) again, there is concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) to have concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (D) in generator (1), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), after having refrigerant vapour passage to be communicated with the second generator (2) in generator (1) the second generator (2) have again cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) to be adjusted into generator (1) and increase newly divide a steam chest (F) to have refrigerant vapour passage to be communicated with the second generator (2) after the second generator (2) have again cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
30. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased absorber, newly-increased point steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and solution heat exchanger (17) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) also has weak solution pipeline to be communicated with newly-increased generator (A), newly-increased generator (A) has concentrated solution pipeline to be communicated with generator (1) through newly-increased solution choke valve (H) again, there is concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) to have concentrated solution pipeline to be communicated with the newly-increased steam chest (F) that divides through newly-increased absorber (G) in generator (1), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), after having refrigerant vapour passage to be communicated with the second generator (2) in generator (1) the second generator (2) have again cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) to be adjusted into generator (1) and increase newly divide a steam chest (F) to have refrigerant vapour passage to be communicated with the second generator (2) after the second generator (2) have again cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes, wherein, arrange for convenience of parts, or increase newly-increased solution pump, will increase absorber (G) newly has weak solution pipeline to be communicated with newly-increased generator (A) to be adjusted into newly-increased absorber (G) to have weak solution pipeline warp to increase solution pump (D) newly to be communicated with newly-increased generator (A).
31. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased absorber, newly-increased solution heat exchanger and newly-increased point steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline through solution pump (11) through solution pump (11) and solution heat exchanger (17) absorber (5), solution heat exchanger (17) and newly-increased solution heat exchanger (C) are communicated with newly-increased absorber (G), newly-increased absorber (G) also has weak solution pipeline to be communicated with newly-increased generator (A), newly-increased generator (A) has concentrated solution pipeline to be communicated with generator (1) through newly-increased solution heat exchanger (C) again, there is concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) to have concentrated solution pipeline to be communicated with the newly-increased steam chest (F) that divides through newly-increased absorber (G) in generator (1), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), after having refrigerant vapour passage to be communicated with the second generator (2) in generator (1) the second generator (2) have again cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14) to be adjusted into generator (1) and increase newly divide a steam chest (F) to have refrigerant vapour passage to be communicated with the second generator (2) after the second generator (2) have again cryogen liquid pipeline to be communicated with evaporimeter (9) through choke valve (14), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes, wherein, arrange for convenience of parts, or increase newly-increased solution pump, will increase absorber (G) newly has weak solution pipeline to be communicated with newly-increased generator (A) to be adjusted into newly-increased absorber (G) to have weak solution pipeline warp to increase solution pump (D) newly to be communicated with newly-increased generator (A).
32. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased choke valve, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased point steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (9) through newly-increased choke valve (B), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased condenser (E) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes, wherein, newly-increased absorber (G) or increase heated medium pipeline are communicated with outside.
33. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-3, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased throttling, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased point steam chest, newly-increased solution choke valve and newly-increased second point of steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (9) through newly-increased choke valve (B), there is concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 4th generator (4) to have concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased the second solution pump (L) and newly-increased condenser (E) in the 4th generator (4), newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
34. first-class absorption type heat pumps that circulate along separate routes, in shunt circulation first-class absorption type heat pump claimed in claim 4, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased throttling, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased point steam chest, newly-increased solution choke valve and newly-increased second point of steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (9) through newly-increased choke valve (B), there is concentrated solution pipeline to be communicated with the 3rd absorber (7) and to be adjusted into the 3rd generator (3) and to have concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased the second solution pump (L) and newly-increased condenser (E) through the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20) in the 3rd generator (3), newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
35. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased choke valve, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased point steam chest, newly-increased solution choke valve and newly-increased second point of steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (9) through newly-increased choke valve (B), there is concentrated solution pipeline to be communicated with the second solution heat exchanger (18) to be adjusted into the second generator (2) to have concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased condenser (E) in the second generator (2), newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the second solution heat exchanger (18) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
36. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 7-15, increase newly-increased generator, newly-increased absorber, newly-increased condenser, newly-increased choke valve, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased point steam chest, newly-increased solution choke valve and newly-increased second point of steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased absorber (G) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased solution pump (D) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (9) through newly-increased choke valve (B), to divide steam chest (25) to have concentrated solution pipeline to be communicated with the 3rd absorber (7) and to be adjusted into a point steam chest (25) and to have concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased the second solution pump (L) and newly-increased condenser (E) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20), newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
37. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased the second absorber (J) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased the second absorber (J) also has weak solution pipeline to be communicated with newly-increased absorber (G) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (K), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased the second solution pump (L) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased the second solution heat exchanger (K) and newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (J), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased the second absorber (J) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes, wherein, newly-increased absorber (G) or increase heated medium pipeline are communicated with outside.
38. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-3, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased the 3rd solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest, newly-increased second point of steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased the second absorber (J) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased the second absorber (J) also has weak solution pipeline to be communicated with newly-increased absorber (G) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (K), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased the second solution pump (L) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased the second solution heat exchanger (K) and newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (J), there is concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) to be adjusted into the 4th generator (4) have concentrated solution pipeline through newly-increased the 3rd solution pump and newly-increased the second absorber (J) or be communicated with newly-increased second point of steam chest through newly-increased absorber (G) again in the 4th generator (4), newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
39. first-class absorption type heat pumps that circulate along separate routes, in shunt circulation first-class absorption type heat pump claimed in claim 4, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased the 3rd solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest, newly-increased second point of steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased the second absorber (J) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased the second absorber (J) also has weak solution pipeline to be communicated with newly-increased absorber (G) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (K), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased the second solution pump (L) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased the second solution heat exchanger (K) and newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (J), there is concentrated solution pipeline to be communicated with the 3rd absorber (7) and to be adjusted into the 3rd generator (3) and to have concentrated solution pipeline through newly-increased the 3rd solution pump and newly-increased the second absorber (J) or be communicated with newly-increased second point of steam chest through newly-increased absorber (G) again through the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20) in the 3rd generator (3), newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
40. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-15, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest, newly-increased second point of steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased the second absorber (J) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased the second absorber (J) also has weak solution pipeline to be communicated with newly-increased absorber (G) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (K), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased the second solution pump (L) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased the second solution heat exchanger (K) and newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (J), there is concentrated solution pipeline to be communicated with the second solution heat exchanger (18) to be adjusted into the second generator (2) have concentrated solution pipeline through newly-increased the second absorber (J) or be communicated with newly-increased second point of steam chest through newly-increased absorber (G) again in the second generator (2), newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the second solution heat exchanger (18) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
41. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 7-15, increase newly-increased generator, newly-increased absorber, newly-increased the second absorber, newly-increased solution pump, newly-increased the second solution pump, newly-increased the 3rd solution pump, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased point steam chest, newly-increased second point of steam chest and newly-increased solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (5) and to have weak solution pipeline to be communicated with newly-increased the second absorber (J) through solution pump (11) and newly-increased solution heat exchanger (C) through solution pump (11) and solution heat exchanger (17) absorber (5), newly-increased the second absorber (J) also has weak solution pipeline to be communicated with newly-increased absorber (G) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (K), newly-increased absorber (G) has weak solution pipeline to be communicated with generator (1) through newly-increased the second solution pump (L) and solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (5) through solution heat exchanger (17) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (17), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through newly-increased solution choke valve (H) and newly-increased absorber (G), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with absorber (5) through newly-increased the second solution heat exchanger (K) and newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (G), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (J), to divide steam chest (25) to have concentrated solution pipeline to be communicated with the 3rd absorber (7) and to be adjusted into a point steam chest (25) and to have concentrated solution pipeline through newly-increased the 3rd solution pump and newly-increased the second absorber (J) or be communicated with newly-increased second point of steam chest through newly-increased absorber (G) again through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20), newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the 3rd absorber (7) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (20) again, have refrigerant vapour passage to be communicated with the 3rd generator (3) to be adjusted into the second generator (2) and newly-increased second point of steam chest to have refrigerant vapour passage to be communicated with the 3rd generator (3) in the second generator (2)---the second generator with increase second point of steam chest newly and jointly provide driving thermal medium to the 3rd generator, newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, form the first-class absorption type heat pump that circulates along separate routes.
42. first-class absorption type heat pumps that circulate along separate routes, in the arbitrary shunt circulation first-class absorption type heat pump described in claim 1-41, evaporimeter (9) and the second evaporimeter (10) are united two into one, form the first-class absorption type heat pump that circulates along separate routes.
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