CN103940142A

CN103940142A - Branch circulation first-kind absorption heat pump

Info

Publication number: CN103940142A
Application number: CN201410138252.0A
Authority: CN
Inventors: 李华玉
Original assignee: Individual
Current assignee: Individual
Priority date: 2013-04-03
Filing date: 2014-03-30
Publication date: 2014-07-23
Anticipated expiration: 2034-03-30
Also published as: WO2014161367A1; CN103940142B

Abstract

The invention provides a branch circulation first-kind absorption heat pump, and belongs to the technical fields of refrigerating and heat pumps. An absorber is communicated with a generator through a solution pump and a solution heat exchanger, the generator is communicated with the absorber through the solution heat exchanger and communicated with a condenser through a refrigerant steam channel, the condenser is communicated with an evaporator through a throttling valve, the evaporator is communicated with the absorber through a refrigerant steam channel, a second absorber is communicated with a steam dividing chamber through a second solution pump, a second solution heat exchanger and the absorber, the steam dividing chamber is communicated with the second absorber through the second solution heat exchanger and communicated with a second condenser through a refrigerant steam channel, the second condenser is communicated with a second evaporator through a second throttling valve, the second evaporator is communicated with the second absorber through a refrigerant steam channel, the generator is communicated with a driving heat medium pipe, the second absorber, the condenser and the second condenser are respectively communicated with a heated medium pipe, the evaporator and the second evaporator are respectively communicated with a waste heat medium pipe, and the branch circulation first-kind 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 effect of the temperature difference in different solution circulation loop, to be embodied 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.

Summary of the invention:

Main purpose of the present invention is that the first-class absorption type heat pump that circulates along separate routes will be provided, and adopts two-way Huo San road 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, absorber, the second absorber, condenser, the second condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, choke valve, the second choke valve, solution heat exchanger, the second solution heat exchanger and a point steam chest; 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, generator also has refrigerant vapour passage to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through choke valve, and evaporimeter also has refrigerant vapour passage to be communicated with absorber; The second absorber has weak solution pipeline to be communicated with a point steam chest through the second solution pump, the second solution heat exchanger and absorber, divide steam chest to also have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, divide steam chest to also have refrigerant vapour passage to be communicated with the second condenser, the second condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve, and the second evaporimeter also has refrigerant vapour passage to be communicated with the second absorber; Generator drives thermal medium pipeline to be communicated with outside in addition, the second absorber, condenser and the second 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. 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 by the 3rd generator, the 3rd choke valve and the 3rd solution heat exchanger, solution pump is set up weak solution pipeline and is communicated with the 3rd generator through the 3rd solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with absorber through the 3rd solution heat exchanger, after having refrigerant vapour passage to be communicated with condenser to be adjusted into generator to have refrigerant vapour passage to be communicated with the 3rd generator in generator, the 3rd generator has cryogen liquid pipeline to be communicated with condenser through the 3rd choke valve again, the 3rd generator also has refrigerant vapour passage to be communicated with condenser, form the first-class absorption type heat pump that circulates along separate routes.

3. 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 by the 3rd generator, the 3rd choke valve and the 3rd 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, the 3rd 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 the 3rd generator through solution heat exchanger, the 3rd generator has concentrated solution pipeline to be communicated with absorber through the 3rd solution heat exchanger again, after having refrigerant vapour passage to be communicated with condenser to be adjusted into generator to have refrigerant vapour passage to be communicated with the 3rd generator in generator, the 3rd generator has cryogen liquid pipeline to be communicated with condenser through the 3rd choke valve again, the 3rd generator also has refrigerant vapour passage to be communicated with condenser, form the first-class absorption type heat pump that circulates along separate routes.

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, increase by the 3rd generator, the 3rd choke valve, the 3rd solution heat exchanger and the 3rd 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 the 3rd generator through solution pump and the second solution heat exchanger through solution pump and solution heat exchanger absorber, the 3rd generator has concentrated solution pipeline to be communicated with generator through the 3rd solution pump and the 3rd 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 absorber through the 3rd solution heat exchanger and solution heat exchanger, after having refrigerant vapour passage to be communicated with condenser to be adjusted into generator to have refrigerant vapour passage to be communicated with the 3rd generator in generator, the 3rd generator has cryogen liquid pipeline to be communicated with condenser through the 3rd choke valve again, the 3rd generator also has refrigerant vapour passage to be communicated with condenser, 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 1st, increase by the 3rd generator, the 3rd choke valve, the 3rd solution heat exchanger and the 3rd 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, the 3rd 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 the 3rd generator through solution heat exchanger, the 3rd generator has concentrated solution pipeline to be communicated with absorber through the 3rd solution heat exchanger again, the 3rd generator also has refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with evaporimeter through the 3rd choke valve, the 3rd generator drives thermal medium pipeline to be communicated with outside in addition, the 3rd 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, or condenser is had cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted into have cryogen liquid pipeline to be communicated with the 3rd condenser through choke valve condenser.

6. 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 by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd 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 the 3rd absorber through solution pump and the 3rd solution heat exchanger through solution pump and solution heat exchanger absorber, the 3rd absorber has weak solution pipeline to be communicated with generator through the 3rd 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 the 3rd generator through solution heat exchanger, the 3rd generator has concentrated solution pipeline to be communicated with absorber through the 3rd solution heat exchanger again, the 3rd generator also has refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd generator drives thermal medium pipeline to be communicated with outside in addition, the 3rd absorber also has heated medium pipeline to be communicated with outside, 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 by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd 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 the 3rd absorber through solution pump and the 3rd solution heat exchanger through solution pump and solution heat exchanger absorber, the 3rd absorber has weak solution pipeline to be communicated with generator through the 3rd 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 the 3rd generator through solution heat exchanger, the 3rd generator has concentrated solution pipeline to be communicated with absorber through the 3rd solution heat exchanger again, the 3rd generator also has refrigerant vapour passage to be communicated with the 3rd absorber, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest, the 3rd 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.

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, increase by the 3rd generator, the 3rd absorber, the 3rd solution pump, second point of steam chest, solution choke valve and 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 the 3rd absorber through solution pump and solution heat exchanger through solution pump and solution heat exchanger absorber, the 3rd absorber has weak solution pipeline to be communicated with generator through the second solution choke valve 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 the 3rd generator through the 3rd solution pump, the 3rd generator also has concentrated solution pipeline to be communicated with second point of steam chest through solution choke valve and the 3rd absorber, second point of steam chest has concentrated solution pipeline to be communicated with absorber through solution heat exchanger again, the 3rd generator also has refrigerant vapour passage to be communicated with the 3rd absorber, second point of steam chest also has refrigerant vapour passage to be communicated with condenser, the 3rd 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.

9. 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 by the 3rd generator, the 3rd absorber, second point of steam chest and 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 the 3rd absorber through solution pump and solution heat exchanger through solution pump and solution heat exchanger absorber, the 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator, the 3rd generator has concentrated solution pipeline to be communicated with generator through solution choke valve 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 second point of steam chest through the 3rd absorber, second point of steam chest has concentrated solution pipeline to be communicated with absorber through solution heat exchanger again, the 3rd generator also has refrigerant vapour passage to be communicated with the 3rd absorber, second point of steam chest also has refrigerant vapour passage to be communicated with condenser, the 3rd 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 by the 3rd solution pump, the 3rd absorber is had weak solution pipeline to be communicated with the 3rd generator to be adjusted into the 3rd absorber has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution pump.

10. 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 by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and 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 through solution pump through solution pump and solution heat exchanger absorber, solution heat exchanger and the 3rd solution heat exchanger are communicated with the 3rd absorber, the 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator, the 3rd generator has concentrated solution pipeline to be communicated with generator through the 3rd 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 second point of steam chest through the 3rd absorber, second point of steam chest has concentrated solution pipeline to be communicated with absorber through solution heat exchanger again, the 3rd generator also has refrigerant vapour passage to be communicated with the 3rd absorber, second point of steam chest also has refrigerant vapour passage to be communicated with condenser, the 3rd 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 by the 3rd solution pump, the 3rd absorber is had weak solution pipeline to be communicated with the 3rd generator to be adjusted into the 3rd absorber has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution pump.

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 1st, increase by the 3rd generator, the 3rd absorber, the 4th absorber, the 3rd solution pump, the 4th solution pump, the 3rd solution heat exchanger, the 4th solution heat exchanger, second point of steam chest and 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 the 4th absorber through solution pump and the 3rd solution heat exchanger through solution pump and solution heat exchanger absorber, the 4th absorber also has weak solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump and the 4th solution heat exchanger, the 3rd absorber has weak solution pipeline to be communicated with generator through the 4th 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 the 3rd generator through solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with second point of steam chest through solution choke valve and the 3rd absorber, second point of steam chest has concentrated solution pipeline to be communicated with absorber through the 4th solution heat exchanger and the 3rd solution heat exchanger again, the 3rd generator also has refrigerant vapour passage to be communicated with the 3rd absorber, second point of steam chest also has refrigerant vapour passage to be communicated with the 4th absorber, the 3rd generator drives thermal medium pipeline to be communicated with outside in addition, the 3rd absorber or in addition heated medium pipeline are communicated with outside, 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 1st, increase by the 3rd generator, the 3rd absorber, the 4th absorber, the 3rd solution pump, the 4th solution pump, the 3rd solution heat exchanger, the 4th solution heat exchanger, solution choke valve and 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 the 4th absorber through solution pump and the 3rd solution heat exchanger through solution pump and solution heat exchanger absorber, the 4th absorber also has weak solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump and the 4th solution heat exchanger, the 3rd absorber has weak solution pipeline to be communicated with generator through the 4th 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 the 3rd generator through solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with second point of steam chest through solution choke valve and the 3rd absorber, second point of steam chest has concentrated solution pipeline to be communicated with absorber through the 4th solution heat exchanger and the 3rd solution heat exchanger again, the 3rd generator also has refrigerant vapour passage to be communicated with the 3rd absorber, second point of steam chest also has refrigerant vapour passage to be communicated with the 4th absorber, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or are communicated with a point steam chest through the 3rd absorber, the 3rd 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.

13. first-class absorption type heat pumps that circulate along separate routes, in the shunt circulation first-class absorption type heat pump described in the 1st, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, generator is had refrigerant vapour passage to be communicated with condenser to be adjusted into generator has refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution pump and the 3rd solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, the 3rd generator also has refrigerant vapour passage to be communicated with condenser, the 3rd generator drives thermal medium pipeline to be communicated with outside in addition, the 3rd absorber also has heated medium pipeline to be communicated with outside, 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 shunt circulation first-class absorption type heat pump described in the 1st, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, generator is had refrigerant vapour passage to be communicated with condenser to be adjusted into generator has refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution pump and the 3rd solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, the 3rd generator also has refrigerant vapour passage to be communicated with condenser, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline through the second solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest, absorber is set up heated medium pipeline and is communicated with outside, the 3rd 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.

15. first-class absorption type heat pumps that circulate along separate routes, in the shunt circulation first-class absorption type heat pump described in the 1st, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, generator is had refrigerant vapour passage to be communicated with condenser to be adjusted into generator has refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution pump and the 3rd solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, the 3rd generator also has refrigerant vapour passage to be communicated with condenser, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest, the 3rd 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.

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, the second solution pump is set up weak solution pipeline and is communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger, after dividing steam chest to have refrigerant vapour passage to be communicated with the second condenser to be adjusted into a point steam chest to have refrigerant vapour passage to be communicated with newly-increased generator, newly-increased generator has cryogen liquid pipeline to be communicated with the second condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the second condenser, 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, at 1-6, 8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline through the second solution pump, newly-increased solution heat exchanger, the second solution heat exchanger and absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger again, after dividing steam chest to have refrigerant vapour passage to be communicated with the second condenser to be adjusted into a point steam chest to have refrigerant vapour passage to be communicated with newly-increased generator, newly-increased generator has cryogen liquid pipeline to be communicated with the second condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the second condenser, 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, the 7th, in arbitrary shunt circulation first-class absorption type heat pump described in 15, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline through the second solution pump, newly-increased solution heat exchanger, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger again, after dividing steam chest to have refrigerant vapour passage to be communicated with the second condenser to be adjusted into a point steam chest to have refrigerant vapour passage to be communicated with newly-increased generator, newly-increased generator has cryogen liquid pipeline to be communicated with the second condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the second condenser, 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 the 12nd, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or have weak solution pipeline through the second solution pump through the 3rd absorber with dividing a steam chest to be communicated with to be adjusted into the second absorber again, newly-increased solution heat exchanger, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or are communicated with a point steam chest through the 3rd absorber, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger again, after dividing steam chest to have refrigerant vapour passage to be communicated with the second condenser to be adjusted into a point steam chest to have refrigerant vapour passage to be communicated with newly-increased generator, newly-increased generator has cryogen liquid pipeline to be communicated with the second condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the second condenser, 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 the 14th, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline through the second solution pump, newly-increased solution heat exchanger, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger again, after dividing steam chest to have refrigerant vapour passage to be communicated with the second condenser to be adjusted into a point steam chest to have refrigerant vapour passage to be communicated with newly-increased generator, newly-increased generator has cryogen liquid pipeline to be communicated with the second condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the second condenser, 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, at 1-6, 8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased generator through the second solution pump and the second solution heat exchanger, newly-increased generator has concentrated solution pipeline again through newly-increased solution pump, newly-increased solution heat exchanger and absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest to have concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger and the second solution heat exchanger, after dividing steam chest to have refrigerant vapour passage to be communicated with the second condenser to be adjusted into a point steam chest to have refrigerant vapour passage to be communicated with newly-increased generator, newly-increased generator has cryogen liquid pipeline to be communicated with the second condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the second condenser, 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, the 7th, in arbitrary shunt circulation first-class absorption type heat pump described in 15, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased generator through the second solution pump and the second solution heat exchanger, newly-increased generator has concentrated solution pipeline again through newly-increased solution pump, newly-increased solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest to have concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger and the second solution heat exchanger, after dividing steam chest to have refrigerant vapour passage to be communicated with the second condenser to be adjusted into a point steam chest to have refrigerant vapour passage to be communicated with newly-increased generator, newly-increased generator has cryogen liquid pipeline to be communicated with the second condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the second condenser, 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 the 12nd, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or have weak solution pipeline to be communicated with newly-increased generator through the second solution pump and the second solution heat exchanger through the 3rd absorber with dividing a steam chest to be communicated with to be adjusted into the second absorber again, newly-increased generator has concentrated solution pipeline again through newly-increased solution pump, newly-increased solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or are communicated with a point steam chest through the 3rd absorber, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest to have concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger and the second solution heat exchanger, after dividing steam chest to have refrigerant vapour passage to be communicated with the second condenser to be adjusted into a point steam chest to have refrigerant vapour passage to be communicated with newly-increased generator, newly-increased generator has cryogen liquid pipeline to be communicated with the second condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the second condenser, 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 the 14th, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased generator through the second solution pump and the second solution heat exchanger, newly-increased generator has concentrated solution pipeline again through newly-increased solution pump, newly-increased solution heat exchanger and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest to have concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger and the second solution heat exchanger, after dividing steam chest to have refrigerant vapour passage to be communicated with the second condenser to be adjusted into a point steam chest to have refrigerant vapour passage to be communicated with newly-increased generator, newly-increased generator has cryogen liquid pipeline to be communicated with the second condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the second condenser, 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 1-15 item, increase newly-increased point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second evaporimeter is had refrigerant vapour passage to be communicated with the second absorber to be adjusted into the second evaporimeter has refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline through newly-increased solution pump, newly-increased solution heat exchanger and absorber are communicated with a newly-increased point steam chest, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with the second absorber, 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.

26. first-class absorption type heat pumps that circulate along separate routes, at 1-6, 8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, increase newly-increased point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline again through newly-increased solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest to have concentrated solution pipeline to be communicated with a newly-increased point steam chest through the second solution heat exchanger and absorber, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased absorber, 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.

27. first-class absorption type heat pumps that circulate along separate routes, the 7th, in arbitrary shunt circulation first-class absorption type heat pump described in 15, increase newly-increased point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline again through newly-increased solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline through the second solution heat exchanger, absorber and the 3rd absorber are communicated with a newly-increased point steam chest, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased absorber, 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.

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 the 12nd, increase newly-increased point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, be communicated with a point steam chest with absorber and the 4th absorber or have weak solution pipeline to be communicated with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger through the 3rd absorber with dividing a steam chest to be communicated with to be adjusted into the second absorber again, newly-increased absorber has weak solution pipeline again through newly-increased solution pump, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or are communicated with a point steam chest through the 3rd absorber, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline through the second solution heat exchanger, absorber and the 4th absorber are communicated with a newly-increased point steam chest or are communicated with a newly-increased point steam chest through the 3rd absorber, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased absorber, 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.

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 the 14th, increase newly-increased point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline again through newly-increased solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest to have concentrated solution pipeline to be communicated with a newly-increased point steam chest through the second solution heat exchanger and the 3rd absorber, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with the second absorber through newly-increased solution heat exchanger, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased absorber, 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.

30. first-class absorption type heat pumps that circulate along separate routes, at 1-6, 8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, increase 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 solution choke valve, newly-increased point steam chest and newly-increased second point of steam chest, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased the second absorber through the second solution pump and newly-increased solution heat exchanger, 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 again through newly-increased the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest to have concentrated solution pipeline to be communicated with a newly-increased point steam chest through the second solution heat exchanger and absorber, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased solution choke valve and newly-increased absorber, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the second absorber through newly-increased the second solution heat exchanger and newly-increased solution heat exchanger again, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased second point of steam chest also has refrigerant vapour passage to be communicated with newly-increased the second absorber, newly-increased absorber or in addition heated medium pipeline are communicated with outside, 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.

31. first-class absorption type heat pumps that circulate along separate routes, the 7th, in arbitrary shunt circulation first-class absorption type heat pump described in 15, increase 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 solution choke valve, newly-increased point steam chest and newly-increased second point of steam chest, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased the second absorber through the second solution pump and newly-increased solution heat exchanger, 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 again through newly-increased the second solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline through the second solution heat exchanger, absorber and the 3rd absorber are communicated with a newly-increased point steam chest, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased solution choke valve and newly-increased absorber, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the second absorber through newly-increased the second solution heat exchanger and newly-increased solution heat exchanger again, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased second point of steam chest also has refrigerant vapour passage to be communicated with newly-increased the second absorber, newly-increased absorber or in addition heated medium pipeline are communicated with outside, 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.

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 the 12nd, increase 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 solution choke valve, newly-increased point steam chest and newly-increased second point of steam chest, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or have weak solution pipeline to be communicated with newly-increased the second absorber through the second solution pump and newly-increased solution heat exchanger through the 3rd absorber with dividing a steam chest to be communicated with to be adjusted into the second absorber again, 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 again through newly-increased the second solution pump, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or are communicated with a point steam chest through the 3rd absorber, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline through the second solution heat exchanger, absorber and the 4th absorber are communicated with a newly-increased point steam chest or are communicated with a newly-increased point steam chest through the 3rd absorber, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased solution choke valve and newly-increased absorber, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the second absorber through newly-increased the second solution heat exchanger and newly-increased solution heat exchanger again, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased second point of steam chest also has refrigerant vapour passage to be communicated with newly-increased the second absorber, newly-increased absorber or in addition heated medium pipeline are communicated with outside, 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.

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 the 14th, increase 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 solution choke valve, newly-increased point steam chest and newly-increased second point of steam chest, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased the second absorber through the second solution pump and newly-increased solution heat exchanger, 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 again through newly-increased the second solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest to have concentrated solution pipeline to be communicated with a newly-increased point steam chest through the second solution heat exchanger and the 3rd absorber, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased second point of steam chest through newly-increased solution choke valve and newly-increased absorber, newly-increased second point of steam chest has concentrated solution pipeline to be communicated with the second absorber through newly-increased the second solution heat exchanger and newly-increased solution heat exchanger again, a newly-increased point steam chest also has refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased second point of steam chest also has refrigerant vapour passage to be communicated with newly-increased the second absorber, newly-increased absorber or in addition heated medium pipeline are communicated with outside, 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.

34. first-class absorption type heat pumps that circulate along separate routes, at 1-6, 8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline again through newly-increased solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with the second 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.

35. first-class absorption type heat pumps that circulate along separate routes, the 7th, in arbitrary shunt circulation first-class absorption type heat pump described in 15, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline again through newly-increased solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with the second 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.

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 the 12nd, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or have weak solution pipeline to be communicated with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger through the 3rd absorber with dividing a steam chest to be communicated with to be adjusted into the second absorber again, newly-increased absorber has weak solution pipeline again through newly-increased solution pump, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or are communicated with a point steam chest through the 3rd absorber, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with the second 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.

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 the 14th, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline again through newly-increased solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with the second 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.

38. first-class absorption type heat pumps that circulate along separate routes, at 1-6, 8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, 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 solution choke valve and newly-increased point steam chest, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased the second absorber through the second solution pump and newly-increased solution heat exchanger, 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 again through newly-increased the second solution pump, the second solution heat exchanger and absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second 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 the second 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 absorber or in addition heated medium pipeline are communicated with outside, 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.

39. first-class absorption type heat pumps that circulate along separate routes, the 7th, in arbitrary shunt circulation first-class absorption type heat pump described in 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 solution choke valve and newly-increased point steam chest, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased the second absorber through the second solution pump and newly-increased solution heat exchanger, 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 again through newly-increased the second solution pump, the second solution heat exchanger, absorber and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second 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 the second 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 absorber or in addition heated medium pipeline are communicated with outside, 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.

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 the 12nd, 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 solution choke valve and newly-increased point steam chest, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or have weak solution pipeline to be communicated with newly-increased the second absorber through the second solution pump and newly-increased solution heat exchanger through the 3rd absorber with dividing a steam chest to be communicated with to be adjusted into the second absorber again, 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 again through newly-increased the second solution pump, the second solution heat exchanger, absorber and the 4th absorber are communicated with a point steam chest or are communicated with a point steam chest through the 3rd absorber, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second 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 the second 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 absorber or in addition heated medium pipeline are communicated with outside, 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.

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 the 14th, 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 solution choke valve and newly-increased point steam chest, the second absorber is had to weak solution pipeline through the second solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest and are adjusted into the second absorber and have weak solution pipeline to be communicated with newly-increased the second absorber through the second solution pump and newly-increased solution heat exchanger, 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 again through newly-increased the second solution pump, the second solution heat exchanger and the 3rd absorber are communicated with a point steam chest, to divide steam chest to have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger to be adjusted into a point steam chest has concentrated solution pipeline to be communicated with newly-increased generator through the second 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 the second 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 absorber or in addition heated medium pipeline are communicated with outside, 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.

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.

43. 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 1-42 item, and condenser and the second condenser are united two into one, and form the first-class absorption type heat pump that circulates along separate routes.

44. 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 choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second evaporimeter is had refrigerant vapour passage to be communicated with the second absorber to be adjusted into the second evaporimeter has refrigerant vapour passage to be communicated with newly-increased absorber, after dividing steam chest to have refrigerant vapour passage to be communicated with the second condenser to be adjusted into a point steam chest to have refrigerant vapour passage to be communicated with newly-increased generator, newly-increased generator has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve again, newly-increased evaporimeter also has refrigerant vapour passage to be communicated with the second absorber, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased generator also has refrigerant vapour passage to be communicated with the second condenser, newly-increased absorber also has heated medium pipeline to be communicated with outside, the newly-increased evaporimeter medium pipeline that also has surplus heat is communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.

45. 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 choke valve, newly-increased solution heat exchanger, newly-increased solution pump, newly-increased absorber, newly-increased point steam chest, newly-increased condenser and newly-increased evaporimeter, cancel the second absorber and the outside heated medium pipeline being communicated with, newly-increased absorber has weak solution pipeline through newly-increased solution pump, newly-increased solution heat exchanger and the second absorber are communicated with a newly-increased point steam chest, a newly-increased point steam chest also has concentrated solution to be communicated with newly-increased absorber through newly-increased solution heat exchanger, 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 newly-increased evaporimeter through newly-increased choke valve, newly-increased evaporimeter also has refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber and newly-increased condenser also have respectively heated medium pipeline to be communicated with outside, the newly-increased evaporimeter medium pipeline that also has surplus heat is communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.

46. 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 44-45 item, and it is one that evaporimeter, the second evaporimeter and newly-increased evaporimeter are closed to three, forms the first-class absorption type heat pump that circulates along separate routes.

47. 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 the 44th, and condenser and the second condenser are united two into one, and form the first-class absorption type heat pump that circulates along separate routes.

48. first-class absorption type heat pumps that circulate along separate routes, are that it is one that condenser, the second condenser and newly-increased condenser are closed to three in the arbitrary shunt circulation first-class absorption type heat pump described in the 45th, form the first-class absorption type heat pump that circulates along separate routes.

Further illustrate feature of the present invention and essence below in conjunction with the first-class absorption type heat pump that circulates along separate routes shown in Fig. 1, Fig. 7 and Figure 22:

1. the solution that drives heat medium flow to enter in it through generator 1, heating discharges and provides refrigerant vapour to condensation 4, drives heat in first solution circulation loop, to carry out temperature drop for the first time; The refrigerant vapour that evaporimeter 6 produces enters absorber 3, is absorbed and heat up by concentrated solution, after intensification, for the generating process of another road solution, is equal to high temperature driven thermic load and brings into play twice effect, has improved the value of high temperature driven thermal medium.

2. the second absorber 3, condenser 4 and the common externally heat supply of the second condenser 5, condenser 4 is the heat supply of single-action flow process, the second absorber 3 and the second condenser 5 are simple double-effect process heat supply, 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.

3. be the occasion of sensible heat for driving heat, high-temperature part is for generator 1, and the driving heat after temperature reduces forms temperature difference utilization for the second time for the 3rd generator 15, the three generators 15 and the 3rd absorber 20, has further increased the degree of utilizing to driving heat.

4. Fig. 7 combines with Figure 22, the backheat flow process that the 3rd generator 15 and the 3rd absorber 20 form, and it provides driving thermic load to driving the utilization of the temperature difference to be embodied in by absorber 2 to another road solution; The backheat flow process that newly-increased generator A and newly-increased absorber E form, still can make to drive the temperature difference to be further utilized again, thereby realizes driving making full use of of the temperature difference.

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.

Figure 23 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 23rd kind of structure and schematic flow sheet.

Figure 24 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 24th kind of structure and schematic flow sheet.

Figure 25 is according to shunt circulation first-class absorption type heat pump provided by the present invention the 25th kind of structure and schematic flow sheet.

In figure, 1-generator, 2-absorber, 3-the second absorber, 4-condenser, 5-the second condenser, 6-evaporimeter, 7-the second evaporimeter, 8-solution pump, 9-the second solution pump, 10-choke valve, 11-the second choke valve, 12-solution heat exchanger, 13-the second solution heat exchanger, 14-divides steam chest, 15-the 3rd generator, 16-the 3rd choke valve, 17-the 3rd solution heat exchanger, 18-the 3rd solution pump, 19-the 3rd condenser, 20-the 3rd absorber, 21-solution choke valve, 22-the second solution choke valve, second point of steam chest of 23-, 24-the 4th absorber, 25-the 4th solution pump, 26-the 4th solution heat exchanger, A-increases generator newly, and B-increases choke valve newly, and C-increases solution heat exchanger newly, D-increases solution pump newly, E-increases absorber newly, the newly-increased point steam chest of F-, and G-increases the second solution pump newly, H-increases the second solution heat exchanger newly, I-increases second point of steam chest newly, and J-increases solution choke valve newly, and K-increases the second absorber newly, L-increases condenser newly, and M-increases evaporimeter 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, absorber, the second absorber, condenser, the second condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, choke valve, the second choke valve, solution heat exchanger, the second solution heat exchanger and a point steam chest; Absorber 2 has weak solution pipeline to be communicated with generator 1 through solution pump 8 and solution heat exchanger 12, generator 1 also has concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12, generator 1 also has refrigerant vapour passage to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through choke valve 10, and evaporimeter 6 also has refrigerant vapour passage to be communicated with absorber 2; The second absorber 3 has weak solution pipeline to be communicated with a point steam chest 14 through the second solution pump 9, the second solution heat exchanger 13 and absorber 2, divide steam chest 14 to also have concentrated solution pipeline to be communicated with the second absorber 3 through the second solution heat exchanger 13, divide steam chest 14 to also have refrigerant vapour passage to be communicated with the second condenser 5, the second condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 7 through the second choke valve 11, and the second evaporimeter 7 also has refrigerant vapour passage to be communicated with the second absorber 3; Generator 1 drives thermal medium pipeline to be communicated with outside in addition, and the second absorber 3, condenser 4 and the second condenser 5 also have respectively heated medium pipeline to be communicated with outside, and evaporimeter 6 and the second evaporimeter 7 medium pipeline that also has surplus heat is respectively communicated with outside.

2. in flow process, the weak solution of absorber 2 enters generator 1 through solution pump 8 and solution heat exchanger 12, the solution that drives heat medium flow to enter in it through generator 1, heating discharges and provides refrigerant vapour to condenser 4, the concentrated solution of generator 1 enters absorber 2, absorbs refrigerant vapour heat release in the solution of flowing through in it through solution heat exchanger 12, the refrigerant vapour heat release of condenser 4 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 4 through choke valve 10 reducing pressure by regulating flows enter evaporimeter 6, absorb waste heat become refrigerant vapour and provide to absorber 2, the weak solution of the second absorber 3 absorber 2 of flowing through after the second solution pump 9 and the second solution heat exchanger 13, after heat absorbing part vaporization, enter point steam chest 14, divide the concentrated solution of steam chest 14 to enter the second absorber 3 through the second solution heat exchanger 13, absorb refrigerant vapour heat release in heated medium, divide the refrigerant vapour of steam chest 14 to enter the second condenser 5, heat release becomes cryogen liquid in heated medium, the cryogen liquid of the second condenser 5 enters the second evaporimeter 7 through the second choke valve 11 throttlings, absorbing waste heat becomes refrigerant vapour and provides to the second absorber 3, form 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, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase by the 3rd generator, the 3rd choke valve and the 3rd solution heat exchanger, solution pump 8 is set up weak solution pipeline and is communicated with the 3rd generator 15 through the 3rd solution heat exchanger 17, the 3rd generator 15 also has concentrated solution pipeline to be communicated with absorber 2 through the 3rd solution heat exchanger 17, after having refrigerant vapour passage to be communicated with condenser 4 to be adjusted into generator 1 to have refrigerant vapour passage to be communicated with the 3rd generator 15 in generator 1, the 3rd generator 15 has cryogen liquid pipeline to be communicated with condenser 4 through the 3rd choke valve 16 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with condenser 4.

2. in flow process, the refrigerant vapour that generator 1 produces offers the 3rd generator 15 and makes to drive thermal medium, the part weak solution of absorber 2 enters the 3rd generator 15 through solution pump 8 and the 3rd solution heat exchanger 17, refrigerant vapour the 3rd generator 15 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to condenser 4, the concentrated solution of the 3rd generator 15 enters absorber 2 through the 3rd solution heat exchanger 17, flow through after the refrigerant vapour heat release of the 3rd generator 15 becomes cryogen liquid and enter condenser 4 through the 3rd choke valve 16 throttlings again, form 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, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase by the 3rd generator, the 3rd choke valve and the 3rd solution heat exchanger, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 2 and to have weak solution pipeline through solution pump 8 through solution pump 8 and solution heat exchanger 12 absorber 2, the 3rd solution heat exchanger 17 and solution heat exchanger 12 are communicated with generator 1, generator 1 is had concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with the 3rd generator 15 through solution heat exchanger 12, the 3rd generator 15 has concentrated solution pipeline to be communicated with absorber 2 through the 3rd solution heat exchanger 17 again, after having refrigerant vapour passage to be communicated with condenser 4 to be adjusted into generator 1 to have refrigerant vapour passage to be communicated with the 3rd generator 15 in generator 1, the 3rd generator 15 has cryogen liquid pipeline to be communicated with condenser 4 through the 3rd choke valve 16 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with condenser 4.

2. in flow process, the refrigerant vapour that generator 1 produces offers the 3rd generator 15 and makes to drive thermal medium, the weak solution of absorber 2 is through solution pump 8, the 3rd solution heat exchanger 17 and solution heat exchanger 12 enter generator 1, the concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12, refrigerant vapour the 3rd generator 15 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to condenser 4, the concentrated solution of the 3rd generator 15 enters absorber 2 through the 3rd solution heat exchanger 17, flow through after the refrigerant vapour heat release of the 3rd generator 15 becomes cryogen liquid and enter condenser 4 through the 3rd choke valve 16 throttlings again, form 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

1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase by the 3rd generator, the 3rd choke valve, the 3rd solution heat exchanger and the 3rd solution pump, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 2 and to have weak solution pipeline to be communicated with the 3rd generator 15 through solution pump 8 and the second solution heat exchanger 12 through solution pump 8 and solution heat exchanger 12 absorber 2, the 3rd generator 15 has concentrated solution pipeline to be communicated with generator 1 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with absorber 2 through the 3rd solution heat exchanger 17 and solution heat exchanger 12, after having refrigerant vapour passage to be communicated with condenser 4 to be adjusted into generator 1 to have refrigerant vapour passage to be communicated with the 3rd generator 15 in generator 1, the 3rd generator 15 has cryogen liquid pipeline to be communicated with condenser 4 through the 3rd choke valve 16 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with condenser 4.

2. in flow process, the refrigerant vapour that generator 1 produces offers the 3rd generator 15 and makes to drive thermal medium, the weak solution of absorber 2 enters the 3rd generator 15 through solution pump 8 and solution heat exchanger 12, refrigerant vapour the 3rd generator 15 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to condenser 4, the concentrated solution of the 3rd generator 15 enters generator 1 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, the concentrated solution of generator 1 enters absorber 2 through the 3rd solution heat exchanger 17 and solution heat exchanger 12, flow through after the refrigerant vapour heat release of the 3rd generator 15 becomes cryogen liquid and enter condenser 4 through the 3rd choke valve 16 throttlings again, form 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, increase by the 3rd generator, the 3rd choke valve, the 3rd solution heat exchanger and the 3rd condenser, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 2 and to have weak solution pipeline through solution pump 8 through solution pump 8 and solution heat exchanger 12 absorber 2, the 3rd solution heat exchanger 17 and solution heat exchanger 12 are communicated with generator 1, generator 1 is had concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with the 3rd generator 15 through solution heat exchanger 12, the 3rd generator 15 has concentrated solution pipeline to be communicated with absorber 2 through the 3rd solution heat exchanger 17 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with the 3rd condenser 19, the 3rd condenser 19 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through the 3rd choke valve 16, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition, the 3rd condenser 19 also has heated medium pipeline to be communicated with outside.

2. in flow process, the weak solution of absorber 2 enters generator 1 through solution pump 8, the 3rd solution heat exchanger 17 and solution heat exchanger 12, the concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12, the solution that drives heat medium flow to enter in it through the 3rd generator 15, heating discharges and provides refrigerant vapour to the 3rd condenser 19, and the concentrated solution of the 3rd generator 15 enters absorber 2 through the 3rd solution heat exchanger 17; The refrigerant vapour heat release of the 3rd condenser 19 becomes cryogen liquid in heated medium, and the cryogen liquid of the 3rd condenser 19 enters evaporimeter 6 through the 3rd choke valve 16 throttlings, forms 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, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 2 and to have weak solution pipeline to be communicated with the 3rd absorber 20 through solution pump 8 and the 3rd solution heat exchanger 17 through solution pump 8 and solution heat exchanger 12 absorber 2, the 3rd absorber 20 has weak solution pipeline to be communicated with generator 1 through the 3rd solution pump 18 and solution heat exchanger 12 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with the 3rd generator 15 through solution heat exchanger 12, the 3rd generator 15 has concentrated solution pipeline to be communicated with absorber 2 through the 3rd solution heat exchanger 17 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition, the 3rd absorber 20 also has heated medium pipeline to be communicated with outside.

2. in flow process, the weak solution of absorber 2 enters the 3rd absorber 20 through solution pump 8 and the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 20 enters generator 1 through the 3rd solution pump 18 and solution heat exchanger 12, the concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12, drive heat medium flow through the 3rd generator 15, the solution that heating enters in it discharges and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 enters absorber 2 through the 3rd 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 Fig. 7 is achieved in that

1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 2 and to have weak solution pipeline to be communicated with the 3rd absorber 20 through solution pump 8 and the 3rd solution heat exchanger 17 through solution pump 8 and solution heat exchanger 12 absorber 2, the 3rd absorber 20 has weak solution pipeline to be communicated with generator 1 through the 3rd solution pump 18 and solution heat exchanger 12 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with the 3rd generator 15 through solution heat exchanger 12, the 3rd generator 15 has concentrated solution pipeline to be communicated with absorber 2 through the 3rd solution heat exchanger 17 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, the second absorber 3 is had to weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14 and are adjusted into the second absorber 3 and have weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13, absorber 2 and the 3rd absorber 20 are communicated with a point steam chest 14, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition.

2. in flow process, the weak solution of absorber 2 enters the 3rd absorber 20 through solution pump 8 and the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of the 3rd absorber 20 enters generator 1 through the 3rd solution pump 18 and solution heat exchanger 12, the concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12, drive heat medium flow through the 3rd generator 15, the solution that heating enters in it discharges and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 enters absorber 2 through the 3rd solution heat exchanger 17, the weak solution of the second absorber 3 enters point steam chest 14 after flow through successively after the second solution pump 9 and the second solution heat exchanger 13 absorber 2 and the 3rd absorber 20, heat absorbing part vaporization, forms 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

1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase by the 3rd generator, the 3rd absorber, the 3rd solution pump, second point of steam chest, solution choke valve and the second solution choke valve, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 2 and to have weak solution pipeline to be communicated with the 3rd absorber 20 through solution pump 8 and solution heat exchanger 12 through solution pump 8 and solution heat exchanger 12 absorber 2, the 3rd absorber 20 has weak solution pipeline to be communicated with generator 1 through the second solution choke valve 22 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution pump 18, the 3rd generator 15 also has concentrated solution pipeline to be communicated with second point of steam chest 23 through solution choke valve 21 and the 3rd absorber 20, second point of steam chest 23 has concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, second point of steam chest 23 also has refrigerant vapour passage to be communicated with condenser 4, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition.

2. in flow process, the weak solution of absorber 2 enters the 3rd absorber 20 through solution pump 8 and solution heat exchanger 12, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of the 3rd absorber 20 enters generator 1 through the second solution choke valve 22 reducing pressure by regulating flows, the concentrated solution of generator 1 enters the 3rd generator 15 through the 3rd solution pump 18, drive heat medium flow through the 3rd generator 15, the solution that heating enters in it discharges and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 the 3rd absorber 20 of flowing through after solution choke valve 21 reducing pressure by regulating flows, after heat absorbing part vaporization, enter second point of steam chest 23, the concentrated solution of second point of steam chest 23 enters absorber 3 through solution heat exchanger 12, the refrigerant vapour of second point of steam chest 23 enters condenser 4, form 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. 1, increase by the 3rd generator, the 3rd absorber, second point of steam chest and solution choke valve, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 2 and to have weak solution pipeline to be communicated with the 3rd absorber 20 through solution pump 8 and solution heat exchanger 12 through solution pump 8 and solution heat exchanger 12 absorber 2, the 3rd absorber 20 also has weak solution pipeline to be communicated with the 3rd generator 15, the 3rd generator 15 has concentrated solution pipeline to be communicated with generator 1 through solution choke valve 21 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with second point of steam chest 23 through the 3rd absorber 20, second point of steam chest 23 has concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, second point of steam chest 23 also has refrigerant vapour passage to be communicated with condenser 4, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition.

2. in flow process, the weak solution of absorber 2 enters the 3rd absorber 20 through solution pump 8 and solution heat exchanger 12, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of the 3rd absorber 20 enters the 3rd generator 15, drive heat medium flow through the 3rd generator 15, the solution that heating enters in it discharges and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 enters generator 1 through solution choke valve 21 reducing pressure by regulating flows, the concentrated solution of generator 1 the 3rd absorber 20 of flowing through, after heat absorbing part vaporization, enter second point of steam chest 23, the concentrated solution of second point of steam chest 23 enters absorber 2 through solution heat exchanger 12, the refrigerant vapour of second point of steam chest 23 enters condenser 4, form 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. 1, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and second point of steam chest, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 2 and to have weak solution pipeline through solution pump 8 through solution pump 8 and solution heat exchanger 12 absorber 2, solution heat exchanger 12 and the 3rd solution heat exchanger 17 are communicated with the 3rd absorber 20, the 3rd absorber 20 also has weak solution pipeline to be communicated with the 3rd generator 15, the 3rd generator 15 has concentrated solution pipeline to be communicated with generator 1 through the 3rd solution heat exchanger 17 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with second point of steam chest 23 through the 3rd absorber 20, second point of steam chest 23 has concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, second point of steam chest 23 also has refrigerant vapour passage to be communicated with condenser 4, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition.

2. in flow process, the weak solution of absorber 2 is through solution pump 8, solution heat exchanger 12 and the 3rd solution heat exchanger 17 enter the 3rd absorber 20, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of the 3rd absorber 20 enters the 3rd generator 15, drive heat medium flow through the 3rd generator 15, the solution that heating enters in it discharges and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 enters generator 1 through the 3rd solution heat exchanger 17, the concentrated solution of generator 1 the 3rd absorber 20 of flowing through, after heat absorbing part vaporization, enter second point of steam chest 23, the concentrated solution of second point of steam chest 23 enters absorber 2 through solution heat exchanger 12, the refrigerant vapour of second point of steam chest 23 enters condenser 4, form 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 by the 3rd generator, the 3rd absorber, the 4th absorber, the 3rd solution pump, the 4th solution pump, the 3rd solution heat exchanger, the 4th solution heat exchanger, second point of steam chest and solution choke valve, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 2 and to have weak solution pipeline to be communicated with the 4th absorber 24 through solution pump 8 and the 3rd solution heat exchanger 17 through solution pump 8 and solution heat exchanger 12 absorber 2, the 4th absorber 24 also has weak solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18 and the 4th solution heat exchanger 26, the 3rd absorber 20 has weak solution pipeline to be communicated with generator 1 through the 4th solution pump 25 and solution heat exchanger 12 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with the 3rd generator 15 through solution heat exchanger 12, the 3rd generator 15 also has concentrated solution pipeline to be communicated with second point of steam chest 23 through solution choke valve 21 and the 3rd absorber 20, second point of steam chest 23 has concentrated solution pipeline to be communicated with absorber 2 through the 4th solution heat exchanger 26 and the 3rd solution heat exchanger 17 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, second point of steam chest 23 also has refrigerant vapour passage to be communicated with the 4th absorber 24, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition, the 4th absorber 24 also has heated medium pipeline to be communicated with outside.

2. in flow process, the weak solution of absorber 2 enters the 4th absorber 24 through solution pump 8 and the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in heated medium, the weak solution of the 4th absorber 24 enters the 3rd absorber 20 through the 3rd solution pump 18 and the 4th solution heat exchanger 26, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of the 3rd absorber 20 enters generator 1 through the 4th solution pump 25 and solution heat exchanger 12, the concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12, drive heat medium flow through the 3rd generator 15, the solution that heating enters in it discharges and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 the 3rd absorber 20 of flowing through after solution choke valve 21 reducing pressure by regulating flows, after heat absorbing part vaporization, enter second point of steam chest 23, the concentrated solution of second point of steam chest 23 enters absorber 2 through the 4th solution heat exchanger 26 and the 3rd solution heat exchanger 17, the refrigerant vapour of second point of steam chest 23 enters the 4th absorber 24, 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 by the 3rd generator, the 3rd absorber, the 4th absorber, the 3rd solution pump, the 4th solution pump, the 3rd solution heat exchanger, the 4th solution heat exchanger, solution choke valve and second point of steam chest, there is weak solution pipeline to be communicated with generator 1 and to be adjusted into absorber 2 and to have weak solution pipeline to be communicated with the 4th absorber 24 through solution pump 8 and the 3rd solution heat exchanger 17 through solution pump 8 and solution heat exchanger 12 absorber 2, the 4th absorber 24 also has weak solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18 and the 4th solution heat exchanger 26, the 3rd absorber 20 has weak solution pipeline to be communicated with generator 1 through the 4th solution pump 25 and solution heat exchanger 12 again, generator 1 is had concentrated solution pipeline to be communicated with absorber 2 through solution heat exchanger 12 to be adjusted into generator 1 has concentrated solution pipeline to be communicated with the 3rd generator 15 through solution heat exchanger 12, the 3rd generator 15 also has concentrated solution pipeline to be communicated with second point of steam chest 23 through solution choke valve 21 and the 3rd absorber 20, second point of steam chest 23 has concentrated solution pipeline to be communicated with absorber 2 through the 4th solution heat exchanger 26 and the 3rd solution heat exchanger 17 again, the 3rd generator 15 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, second point of steam chest 23 also has refrigerant vapour passage to be communicated with the 4th absorber 24, the second absorber 3 is had to weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14 and are adjusted into the second absorber 3 and have weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13, absorber 2 and the 4th absorber 24 are communicated with a point steam chest 14, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition.

2. in flow process, the weak solution of absorber 2 enters the 4th absorber 24 through solution pump 8 and the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of the 4th absorber 24 enters the 3rd absorber 20 through the 3rd solution pump 18 and the 4th solution heat exchanger 26, absorb refrigerant vapour heat release in the solution of flowing through in it, the weak solution of the 3rd absorber 20 enters generator 1 through the 4th solution pump 25 and solution heat exchanger 12, the concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12, drive heat medium flow through the 3rd generator 15, the solution that heating enters in it discharges and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 the 3rd absorber 20 of flowing through after solution choke valve 21 reducing pressure by regulating flows, after heat absorbing part vaporization, enter second point of steam chest 23, the concentrated solution of second point of steam chest 23 enters absorber 2 through the 4th solution heat exchanger 26 and the 3rd solution heat exchanger 17, the refrigerant vapour of second point of steam chest 23 enters the 4th absorber 24, the weak solution of the second absorber 3 enters point steam chest 14 after flow through successively after the second solution pump 9 and the second solution heat exchanger 13 absorber 2 and the 4th absorber 24, heat absorbing part vaporization, forms 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 by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, generator 1 is had refrigerant vapour passage to be communicated with condenser 4 to be adjusted into generator 1 has refrigerant vapour passage to be communicated with the 3rd absorber 20, the 3rd absorber 20 also has weak solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, the 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution heat exchanger 17, the 3rd generator 15 also has refrigerant vapour passage to be communicated with condenser 4, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition, the 3rd absorber 20 also has heated medium pipeline to be communicated with outside.

2. in flow process, the refrigerant vapour of generator 1 enters the 3rd absorber 20, is absorbed also heat release in heated medium by concentrated solution, the weak solution of the 3rd absorber 20 enters the 3rd generator 15 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, the solution that drives heat medium flow to enter in it through the 3rd generator 15, heating discharges and provides refrigerant vapour to condenser 4, the concentrated solution of the 3rd generator 15 enters the 3rd absorber 20 through the 3rd solution heat exchanger 17, forms 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 by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, generator 1 is had refrigerant vapour passage to be communicated with condenser 4 to be adjusted into generator 1 has refrigerant vapour passage to be communicated with the 3rd absorber 20, the 3rd absorber 20 also has weak solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, the 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution heat exchanger 17, the 3rd generator 15 also has refrigerant vapour passage to be communicated with condenser 4, the second absorber 3 is had to weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14 and are adjusted into the second absorber 3 and have weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and the 3rd absorber 20 are communicated with a point steam chest 14, absorber 2 is set up heated medium pipeline and is communicated with outside, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition.

2. in flow process, the refrigerant vapour of generator 1 enters the 3rd absorber 20, absorbed by concentrated solution and heat release in the solution of flowing through in it, the weak solution of the 3rd absorber 20 enters the 3rd generator 15 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, drive heat medium flow through the 3rd generator 15, the solution that heating enters in it discharges and provides refrigerant vapour to condenser 4, the concentrated solution of the 3rd generator 15 enters the 3rd absorber 20 through the 3rd solution heat exchanger 17, the cryogen liquid of condenser 4 enters evaporimeter 6 through choke valve 10 reducing pressure by regulating flows, absorbing waste heat becomes refrigerant vapour and passes through to absorber 2, the concentrated solution of generator 1 enters absorber 2 through solution heat exchanger 12, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 3 enters point steam chest 14 after flow through after the second solution pump 9 and the second solution heat exchanger 13 the 3rd absorber 20, heat absorbing part vaporization, 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 by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, generator 1 is had refrigerant vapour passage to be communicated with condenser 4 to be adjusted into generator 1 has refrigerant vapour passage to be communicated with the 3rd absorber 20, the 3rd absorber 20 also has weak solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, the 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution heat exchanger 17, the 3rd generator 15 also has refrigerant vapour passage to be communicated with condenser 4, the second absorber 3 is had to weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14 and are adjusted into the second absorber 3 and have weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13, absorber 2 and the 3rd absorber 20 are communicated with a point steam chest 14, the 3rd generator 15 drives thermal medium pipeline to be communicated with outside in addition.

2. in flow process, the refrigerant vapour of generator 1 enters the 3rd absorber 20, absorbed by concentrated solution and heat release in the solution of flowing through in it, the weak solution of the 3rd absorber 20 enters the 3rd generator 15 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, the solution that drives heat medium flow to enter in it through the 3rd generator 15, heating discharges and provides refrigerant vapour to condenser 4, and the concentrated solution of the 3rd generator 15 enters the 3rd absorber 20 through the 3rd solution heat exchanger 17; The weak solution of the second absorber 3 enters point steam chest 14 after flow through successively after the second solution pump 9 and the second solution heat exchanger 13 absorber 2 and the 3rd absorber 20, heat absorbing part vaporization, 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 choke valve and newly-increased solution heat exchanger, the second solution pump 9 is set up weak solution pipeline and is communicated with newly-increased generator A through newly-increased solution heat exchanger C, newly-increased generator A also has concentrated solution pipeline to be communicated with the second absorber 3 through newly-increased solution heat exchanger C, after dividing steam chest 14 to have refrigerant vapour passage to be communicated with the second condenser 5 to be adjusted into point steam chest 14 to have refrigerant vapour passage to be communicated with newly-increased generator A, newly-increased generator A has cryogen liquid pipeline to be communicated with the second condenser 5 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the second condenser 5.

2. in flow process, the refrigerant vapour that divides steam chest 14 to discharge offers newly-increased generator A and makes to drive thermal medium, the part weak solution of the second absorber 3 enters newly-increased generator A through the second solution pump 9 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 the second condenser 5, the concentrated solution of newly-increased generator A enters the second absorber 3 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 the second condenser 5 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 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 choke valve and newly-increased solution heat exchanger, the second absorber 3 is had to weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14 and are adjusted into the second absorber 3 and have weak solution pipeline through the second solution pump 9, newly-increased solution heat exchanger C, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14, to divide steam chest 14 to have concentrated solution pipeline to be communicated with the second absorber 3 through the second solution heat exchanger 13 to be adjusted into point steam chest 14 has concentrated solution pipeline to be communicated with newly-increased generator A through the second solution heat exchanger 13, newly-increased generator A has concentrated solution pipeline to be communicated with the second absorber 3 through newly-increased solution heat exchanger C again, after dividing steam chest 14 to have refrigerant vapour passage to be communicated with the second condenser 5 to be adjusted into point steam chest 14 to have refrigerant vapour passage to be communicated with newly-increased generator A, newly-increased generator A has cryogen liquid pipeline to be communicated with the second condenser 5 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the second condenser 5.

2. in flow process, the refrigerant vapour that divides steam chest 14 to discharge offers newly-increased generator A and makes to drive thermal medium, the weak solution of the second absorber 3 is through the second solution pump 9, the absorber 2 of flowing through after newly-increased solution heat exchanger C and the second solution heat exchanger 13, after heat absorbing part vaporization, enter point steam chest 14, divide the concentrated solution of steam chest 14 to enter newly-increased generator A through the second solution heat exchanger 13, refrigerant vapour is flowed through and is increased generator A newly, the solution that heating enters in it discharges and provides refrigerant vapour to the second condenser 5, the concentrated solution of newly-increased generator A enters the second absorber 3 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 the second condenser 5 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 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 choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second absorber 3 is had to weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14 and are adjusted into the second absorber 3 and have weak solution pipeline to be communicated with newly-increased generator A through the second solution pump 9 and the second solution heat exchanger 13, newly-increased generator A has concentrated solution pipeline again through newly-increased solution pump D, newly-increased solution heat exchanger C and absorber 2 are communicated with a point steam chest 14, to divide steam chest 14 to have concentrated solution pipeline to be communicated with the second absorber 3 through the second solution heat exchanger 13 to be adjusted into point steam chest 14 to have concentrated solution pipeline to be communicated with the second absorber 3 through newly-increased solution heat exchanger C and the second solution heat exchanger 13, after dividing steam chest 14 to have refrigerant vapour passage to be communicated with the second condenser 5 to be adjusted into point steam chest 14 to have refrigerant vapour passage to be communicated with newly-increased generator A, newly-increased generator A has cryogen liquid pipeline to be communicated with the second condenser 5 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the second condenser 5.

2. in flow process, the refrigerant vapour that divides steam chest 14 to discharge offers newly-increased generator A and makes to drive thermal medium, the weak solution of the second absorber 3 enters newly-increased generator A through the second solution pump 9 and the second solution heat exchanger 13, refrigerant vapour is flowed through and is increased generator A newly, the solution that heating enters in it discharges and provides refrigerant vapour to the second condenser 5, the concentrated solution of the newly-increased generator A absorber 2 of flowing through after newly-increased solution pump D and newly-increased solution heat exchanger C, after heat absorbing part gasification, enter point steam chest 14, divide the concentrated solution of steam chest 14 to enter the second absorber 3 through newly-increased solution heat exchanger C and the second solution heat exchanger 13, flow through after the refrigerant vapour heat release of newly-increased generator A becomes cryogen liquid and enter the second condenser 5 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 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 point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second evaporimeter 7 is had refrigerant vapour passage to be communicated with the second absorber 3 to be adjusted into the second evaporimeter 7 has refrigerant vapour passage to be communicated with newly-increased absorber E, newly-increased absorber E also has weak solution pipeline through newly-increased solution pump D, newly-increased solution heat exchanger C and absorber 2 are communicated with a newly-increased point steam chest F, a newly-increased point steam chest F also has concentrated solution pipeline to be communicated with newly-increased absorber E through newly-increased solution heat exchanger C, a newly-increased point steam chest F also has refrigerant vapour passage to be communicated with the second absorber 3, newly-increased absorber E also has heated medium pipeline to be communicated with outside.

2. in flow process, the refrigerant vapour that the second evaporimeter 7 produces enters newly-increased absorber E, is absorbed also heat release in heated medium by concentrated solution, flow through after newly-increased solution pump D and newly-increased solution heat exchanger C absorber 2, heat absorbing part gasification of the weak solution of newly-increased absorber E enters a newly-increased point steam chest F, the concentrated solution of newly-increased point steam chest F enters newly-increased absorber E through newly-increased solution heat exchanger C, the refrigerant vapour that newly-increased point steam chest F discharges enters the second absorber 3, forms 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 point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber 3 is had to weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14 and are adjusted into the second absorber 3 and have weak solution pipeline to be communicated with newly-increased absorber E through the second solution pump 9 and newly-increased solution heat exchanger C, newly-increased absorber E has weak solution pipeline again through newly-increased solution pump D, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14, to divide steam chest 14 to have concentrated solution pipeline to be communicated with the second absorber 3 through the second solution heat exchanger 13 to be adjusted into point steam chest 14 to have concentrated solution pipeline to be communicated with a newly-increased point steam chest F through the second solution heat exchanger 13 and absorber 2, a newly-increased point steam chest F also has concentrated solution pipeline to be communicated with the second absorber 3 through newly-increased solution heat exchanger C, a newly-increased point steam chest F also has refrigerant vapour passage to be communicated with newly-increased absorber E, newly-increased absorber E also has heated medium pipeline to be communicated with outside.

2. in flow process, the weak solution of the second absorber 3 enters newly-increased absorber E through the second solution pump 9 and newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in heated medium, the weak solution of the newly-increased absorber E absorber 2 of flowing through after newly-increased solution pump D and the second solution heat exchanger 13, after heat absorbing part gasification, enter point steam chest 14, the concentrated solution of point steam chest 14 absorber 2 of flowing through after the second solution heat exchanger 13, after heat absorbing part gasification, enter newly-increased point steam chest F, the concentrated solution of newly-increased point steam chest F enters the second absorber 3 through newly-increased solution heat exchanger C, the refrigerant vapour of newly-increased point steam chest F enters newly-increased absorber E, 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 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 solution choke valve, newly-increased point steam chest and newly-increased second point of steam chest, the second absorber 3 is had to weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14 and are adjusted into the second absorber 3 and have weak solution pipeline to be communicated with newly-increased the second absorber K through the second solution pump 9 and newly-increased solution heat exchanger C, newly-increased the second absorber K also has weak solution pipeline to be communicated with newly-increased absorber E through newly-increased solution pump D and newly-increased the second solution heat exchanger H, newly-increased absorber E has weak solution pipeline again through newly-increased the second solution pump G, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14, to divide steam chest 14 to have concentrated solution pipeline to be communicated with the second absorber 3 through the second solution heat exchanger 13 to be adjusted into point steam chest 14 to have concentrated solution pipeline to be communicated with a newly-increased point steam chest F through the second solution heat exchanger 13 and absorber 2, a newly-increased point steam chest F also has concentrated solution pipeline to be communicated with newly-increased second point of steam chest I through newly-increased solution choke valve J and newly-increased absorber E, newly-increased second point of steam chest I has concentrated solution pipeline to be communicated with the second absorber 3 through newly-increased the second solution heat exchanger H and newly-increased solution heat exchanger C again, a newly-increased point steam chest F also has refrigerant vapour passage to be communicated with newly-increased absorber E, newly-increased second point of steam chest I also has refrigerant vapour passage to be communicated with newly-increased the second absorber K, newly-increased absorber E and newly-increased the second absorber K also have respectively heated medium pipeline to be communicated with outside.

2. in flow process, the weak solution of the second absorber 3 enters newly-increased the second absorber K through the second solution pump 9 and newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in heated medium, the weak solution of newly-increased the second absorber K enters newly-increased absorber E through newly-increased solution pump D and newly-increased the second solution heat exchanger H, absorption refrigerant vapour respectively heat release are in heated medium and the solution of flowing through in it, the weak solution of the newly-increased absorber E absorber 2 of flowing through after newly-increased the second solution pump G and the second solution heat exchanger 13, after heat absorbing part gasification, enter point steam chest 14, the concentrated solution of point steam chest 14 absorber 2 of flowing through after the second solution heat exchanger 13, after heat absorbing part gasification, enter newly-increased point steam chest F, newly-increased absorber E flows through after the newly-increased solution choke valve J reducing pressure by regulating flow of concentrated solution warp of newly-increased point steam chest F, after heat absorbing part vaporization, enter newly-increased second point of steam chest I, the concentrated solution of newly-increased second point of steam chest I enters the second absorber 3 through newly-increased the second solution heat exchanger H and newly-increased solution heat exchanger C, the refrigerant vapour of newly-increased point steam chest F enters newly-increased absorber E, the refrigerant vapour of newly-increased point steam chest I enters newly-increased the second absorber K, 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 solution pump and newly-increased solution heat exchanger, the second absorber 3 is had to weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14 and are adjusted into the second absorber 3 and have weak solution pipeline to be communicated with newly-increased absorber E through the second solution pump 9 and newly-increased solution heat exchanger C, newly-increased absorber E has weak solution pipeline again through newly-increased solution pump D, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14, to divide steam chest 14 to have concentrated solution pipeline to be communicated with the second absorber 3 through the second solution heat exchanger 13 to be adjusted into point steam chest 14 has concentrated solution pipeline to be communicated with newly-increased generator A through the second solution heat exchanger 13, newly-increased generator A has concentrated solution pipeline to be communicated with the second absorber 3 through newly-increased solution heat exchanger C again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased absorber E, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber E also has heated medium pipeline to be communicated with outside.

2. in flow process, the weak solution of the second absorber 3 enters newly-increased absorber E through the second solution pump 9 and newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in heated medium, the weak solution of the newly-increased absorber E absorber 2 of flowing through after newly-increased solution pump D and the second solution heat exchanger 13, after heat absorbing part gasification, enter point steam chest 14, divide the concentrated solution of steam chest 14 to enter newly-increased generator A through the second solution heat exchanger 13, 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 E, the concentrated solution of newly-increased generator A enters the second absorber 3 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 23 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 solution choke valve and newly-increased point steam chest, the second absorber 3 is had to weak solution pipeline through the second solution pump 9, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14 and are adjusted into the second absorber 3 and have weak solution pipeline to be communicated with newly-increased the second absorber K through the second solution pump 9 and newly-increased solution heat exchanger C, newly-increased the second absorber K also has weak solution pipeline to be communicated with newly-increased absorber E through newly-increased solution pump D and newly-increased the second solution heat exchanger H, newly-increased absorber E has weak solution pipeline again through newly-increased the second solution pump G, the second solution heat exchanger 13 and absorber 2 are communicated with a point steam chest 14, to divide steam chest 14 to have concentrated solution pipeline to be communicated with the second absorber 3 through the second solution heat exchanger 13 to be adjusted into point steam chest 14 has concentrated solution pipeline to be communicated with newly-increased generator A through the second solution heat exchanger 13, 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 J and newly-increased absorber E, a newly-increased point steam chest F has concentrated solution pipeline to be communicated with the second absorber 3 through newly-increased the second solution heat exchanger H and newly-increased solution heat exchanger C again, newly-increased generator A also has refrigerant vapour passage to be communicated with newly-increased absorber E, a newly-increased point steam chest F also has refrigerant vapour passage to be communicated with newly-increased the second absorber K, newly-increased generator A drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber E and newly-increased the second absorber K also have respectively heated medium pipeline to be communicated with outside.

2. in flow process, the weak solution of the second absorber 3 enters newly-increased the second absorber K through the second solution pump 9 and newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in heated medium, the weak solution of newly-increased the second absorber K enters newly-increased absorber E through newly-increased solution pump D and newly-increased the second solution heat exchanger H, absorption refrigerant vapour respectively heat release are in heated medium and the solution of flowing through in it, the weak solution of the newly-increased absorber E absorber 2 of flowing through after newly-increased the second solution pump G and the second solution heat exchanger 13, after heat absorbing part gasification, enter point steam chest 14, divide the concentrated solution of steam chest 14 to enter newly-increased generator A through the second solution heat exchanger 13, 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 E, the concentrated solution of newly-increased generator A is flowed through and is increased absorber E newly after newly-increased solution choke valve J 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 the second absorber 3 through newly-increased the second solution heat exchanger H and newly-increased solution heat exchanger C, the refrigerant vapour of newly-increased point steam chest F enters newly-increased the second absorber K, form the first-class absorption type heat pump that circulates along separate routes.

Shunt circulation first-class absorption type heat pump shown in Figure 24 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 choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second evaporimeter 7 is had refrigerant vapour passage to be communicated with the second absorber 3 to be adjusted into the second evaporimeter 7 has refrigerant vapour passage to be communicated with newly-increased absorber E, after dividing steam chest 14 to have refrigerant vapour passage to be communicated with the second condenser 5 to be adjusted into point steam chest 14 to have refrigerant vapour passage to be communicated with newly-increased generator A, newly-increased generator A has cryogen liquid pipeline to be communicated with newly-increased evaporimeter M through newly-increased choke valve B again, newly-increased evaporimeter M also has refrigerant vapour passage to be communicated with the second absorber 3, newly-increased generator A also has concentrated solution pipeline to be communicated with newly-increased absorber E through newly-increased solution heat exchanger C, newly-increased absorber E also has weak solution pipeline to be 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 refrigerant vapour passage to be communicated with the second condenser 5, newly-increased absorber E also has heated medium pipeline to be communicated with outside, the newly-increased evaporimeter M medium pipeline that also has surplus heat is communicated with outside.

2. in flow process, the refrigerant vapour that divides steam chest 14 to produce offers newly-increased generator A and makes to drive thermal medium, the weak solution of newly-increased absorber E 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 the second condenser 5, the concentrated solution of newly-increased generator A enters newly-increased absorber E 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 newly-increased evaporimeter M through newly-increased choke valve B reducing pressure by regulating flow, absorbing waste heat becomes refrigerant vapour and provides to the second absorber 3, the cryogen liquid of the second condenser 5 enters the second evaporimeter 7 through the second choke valve 11 reducing pressure by regulating flows, absorbing waste heat becomes refrigerant vapour and provides to newly-increased absorber E, form the first-class absorption type heat pump that circulates along separate routes.

Shunt circulation first-class absorption type heat pump shown in Figure 25 is achieved in that

1. in structure, in the shunt circulation first-class absorption type heat pump shown in Fig. 1, increase newly-increased choke valve, newly-increased solution heat exchanger, newly-increased solution pump, newly-increased absorber, newly-increased point steam chest, newly-increased condenser and newly-increased evaporimeter, cancel the second absorber 3 and the outside heated medium pipeline being communicated with, newly-increased absorber E has weak solution pipeline through newly-increased solution pump D, newly-increased solution heat exchanger C and the second absorber 3 are communicated with a newly-increased point steam chest F, a newly-increased point steam chest F also has concentrated solution to be communicated with newly-increased absorber E through newly-increased solution heat exchanger C, a newly-increased point steam chest F also has refrigerant vapour passage to be communicated with newly-increased condenser L, newly-increased condenser L also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter M through newly-increased choke valve B, newly-increased evaporimeter M also has refrigerant vapour passage to be communicated with newly-increased absorber E, newly-increased absorber E and newly-increased condenser L also have respectively heated medium pipeline to be communicated with outside, the newly-increased evaporimeter M medium pipeline that also has surplus heat is communicated with outside.

2. in flow process, the second evaporimeter 7 produces refrigerant vapour and enters the second absorber 3, absorbed by concentrated solution and heat release in the solution of flowing through in it, the weak solution of newly-increased absorber E second absorber 3 of flowing through after newly-increased solution pump D and newly-increased solution heat exchanger C, after heat absorbing part gasification, enter newly-increased point steam chest F, the concentrated solution of newly-increased point steam chest F enters newly-increased absorber E through newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour of newly-increased point steam chest F enters newly-increased condenser L, heat release becomes cryogen liquid in heated medium, the cryogen liquid of newly-increased condenser L enters newly-increased evaporimeter M through newly-increased choke valve B reducing pressure by regulating flow, absorbing waste heat becomes refrigerant vapour and provides to newly-increased absorber E, 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) two-way or multichannel solution circulation, for the generating process of other circulation solution, is conducive to drive selection and coupling between thermal medium, circulation solution and flow process after waste heat lifting temperature, overcomes the restriction of single working media, improves the temperature difference and utilizes level.

(2) multiterminal heat supply, can adapt to the wider operating mode of range of temperature of heated medium preferably, obtains rational thermodynamics sophistication.

(3) there is the flow process of backheat heat supply end, thermodynamic parameter smooth change, heating parameter is adjustable, and adaptation condition changes preferably, obtains higher thermodynamics sophistication.

(4) there is the flow process of backheat heat supply end, can realize the deep exploitation of driving heat source or can increase the lifting amplitude of waste heat supply temperature, improve heat utilization rate.

(5) comprise single-action and supply thermal flow process for thermal flow process and economic benefits and social benefits, substep is realized temperature difference utilization, is conducive to improve performance index and the thermodynamics sophistication of circulation.

(6) 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 performance index and thermodynamics sophistication.

(7) 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

1. the first-class absorption type heat pump that circulates along separate routes, is mainly made up of generator, absorber, the second absorber, condenser, the second condenser, evaporimeter, the second evaporimeter, solution pump, the second solution pump, choke valve, the second choke valve, solution heat exchanger, the second solution heat exchanger and a point steam chest, absorber (2) has weak solution pipeline to be communicated with generator (1) through solution pump (8) and solution heat exchanger (12), generator (1) also has concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12), generator (1) also has refrigerant vapour passage to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (10), and evaporimeter (6) also has refrigerant vapour passage to be communicated with absorber (2), the second absorber (3) has weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14), divide steam chest (14) to also have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13), divide steam chest (14) to also have refrigerant vapour passage to be communicated with the second condenser (5), the second condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (7) through the second choke valve (11), the second evaporimeter (7) also has refrigerant vapour passage to be communicated with the second absorber (3), generator (1) drives thermal medium pipeline to be communicated with outside in addition, the second absorber (3), condenser (4) and the second condenser (5) also have respectively heated medium pipeline to be communicated with outside, evaporimeter (6) and the second evaporimeter (7) medium pipeline that also has surplus heat is respectively communicated with outside, forms the shunt first-class absorption type heat pump that circulates.

2. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 1, increase by the 3rd generator, the 3rd choke valve and the 3rd solution heat exchanger, solution pump (8) is set up weak solution pipeline and is communicated with the 3rd generator (15) through the 3rd solution heat exchanger (17), the 3rd generator (15) also has concentrated solution pipeline to be communicated with absorber (2) through the 3rd solution heat exchanger (17), after having refrigerant vapour passage to be communicated with condenser (4) to be adjusted into generator (1) to have refrigerant vapour passage to be communicated with the 3rd generator (15) in generator (1), the 3rd generator (15) has cryogen liquid pipeline to be communicated with condenser (4) through the 3rd choke valve (16) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with condenser (4), form the first-class absorption type heat pump that circulates along separate routes.

3. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 1, increase by the 3rd generator, the 3rd choke valve and the 3rd solution heat exchanger, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (2) and to have weak solution pipeline through solution pump (8) through solution pump (8) and solution heat exchanger (12) absorber (2), the 3rd solution heat exchanger (17) and solution heat exchanger (12) are communicated with generator (1), generator (1) is had concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with the 3rd generator (15) through solution heat exchanger (12), the 3rd generator (15) has concentrated solution pipeline to be communicated with absorber (2) through the 3rd solution heat exchanger (17) again, after having refrigerant vapour passage to be communicated with condenser (4) to be adjusted into generator (1) to have refrigerant vapour passage to be communicated with the 3rd generator (15) in generator (1), the 3rd generator (15) has cryogen liquid pipeline to be communicated with condenser (4) through the 3rd choke valve (16) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with condenser (4), form the first-class absorption type heat pump that circulates along separate routes.

4. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 1, increase by the 3rd generator, the 3rd choke valve, the 3rd solution heat exchanger and the 3rd solution pump, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (2) and to have weak solution pipeline to be communicated with the 3rd generator (15) through solution pump (8) and the second solution heat exchanger (12) through solution pump (8) and solution heat exchanger (12) absorber (2), the 3rd generator (15) has concentrated solution pipeline to be communicated with generator (1) through the 3rd solution pump (18) and the 3rd solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with absorber (2) through the 3rd solution heat exchanger (17) and solution heat exchanger (12), after having refrigerant vapour passage to be communicated with condenser (4) to be adjusted into generator (1) to have refrigerant vapour passage to be communicated with the 3rd generator (15) in generator (1), the 3rd generator (15) has cryogen liquid pipeline to be communicated with condenser (4) through the 3rd choke valve (16) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with condenser (4), 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 1, increase by the 3rd generator, the 3rd choke valve, the 3rd solution heat exchanger and the 3rd condenser, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (2) and to have weak solution pipeline through solution pump (8) through solution pump (8) and solution heat exchanger (12) absorber (2), the 3rd solution heat exchanger (17) and solution heat exchanger (12) are communicated with generator (1), generator (1) is had concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with the 3rd generator (15) through solution heat exchanger (12), the 3rd generator (15) has concentrated solution pipeline to be communicated with absorber (2) through the 3rd solution heat exchanger (17) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with the 3rd condenser (19), the 3rd condenser (19) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through the 3rd choke valve (16), the 3rd generator (15) drives thermal medium pipeline to be communicated with outside in addition, the 3rd condenser (19) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes, wherein, or condenser (4) is had cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (10) to be adjusted into have cryogen liquid pipeline to be communicated with the 3rd condenser (19) through choke valve (10) condenser (4).

6. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 1, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (2) and to have weak solution pipeline to be communicated with the 3rd absorber (20) through solution pump (8) and the 3rd solution heat exchanger (17) through solution pump (8) and solution heat exchanger (12) absorber (2), the 3rd absorber (20) has weak solution pipeline to be communicated with generator (1) through the 3rd solution pump (18) and solution heat exchanger (12) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with the 3rd generator (15) through solution heat exchanger (12), the 3rd generator (15) has concentrated solution pipeline to be communicated with absorber (2) through the 3rd solution heat exchanger (17) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 3rd generator (15) drives thermal medium pipeline to be communicated with outside in addition, the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, 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 by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (2) and to have weak solution pipeline to be communicated with the 3rd absorber (20) through solution pump (8) and the 3rd solution heat exchanger (17) through solution pump (8) and solution heat exchanger (12) absorber (2), the 3rd absorber (20) has weak solution pipeline to be communicated with generator (1) through the 3rd solution pump (18) and solution heat exchanger (12) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with the 3rd generator (15) through solution heat exchanger (12), the 3rd generator (15) has concentrated solution pipeline to be communicated with absorber (2) through the 3rd solution heat exchanger (17) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14), the 3rd generator (15) drives thermal medium pipeline to be communicated with outside in addition, 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, increase by the 3rd generator, the 3rd absorber, the 3rd solution pump, second point of steam chest, solution choke valve and the second solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (2) and to have weak solution pipeline to be communicated with the 3rd absorber (20) through solution pump (8) and solution heat exchanger (12) through solution pump (8) and solution heat exchanger (12) absorber (2), the 3rd absorber (20) has weak solution pipeline to be communicated with generator (1) through the second solution choke valve (22) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution pump (18), the 3rd generator (15) also has concentrated solution pipeline to be communicated with second point of steam chest (23) through solution choke valve (21) and the 3rd absorber (20), second point of steam chest (23) has concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), second point of steam chest (23) also has refrigerant vapour passage to be communicated with condenser (4), the 3rd generator (15) drives thermal medium pipeline to be communicated with outside in addition, 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 1, increase by the 3rd generator, the 3rd absorber, second point of steam chest and solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (2) and to have weak solution pipeline to be communicated with the 3rd absorber (20) through solution pump (8) and solution heat exchanger (12) through solution pump (8) and solution heat exchanger (12) absorber (2), the 3rd absorber (20) also has weak solution pipeline to be communicated with the 3rd generator (15), the 3rd generator (15) has concentrated solution pipeline to be communicated with generator (1) through solution choke valve (21) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with second point of steam chest (23) through the 3rd absorber (20), second point of steam chest (23) has concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), second point of steam chest (23) also has refrigerant vapour passage to be communicated with condenser (4), the 3rd generator (15) 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 increasing by the 3rd solution pump, the 3rd absorber (20) is had weak solution pipeline to be communicated with the 3rd generator (15) to be adjusted into the 3rd absorber (20) has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution pump (18).

10. first-class absorption type heat pump along separate routes circulates, in shunt circulation first-class absorption type heat pump claimed in claim 1, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and second point of steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (2) and to have weak solution pipeline through solution pump (8) through solution pump (8) and solution heat exchanger (12) absorber (2), solution heat exchanger (12) and the 3rd solution heat exchanger (17) are communicated with the 3rd absorber (20), the 3rd absorber (20) also has weak solution pipeline to be communicated with the 3rd generator (15), the 3rd generator (15) has concentrated solution pipeline to be communicated with generator (1) through the 3rd solution heat exchanger (17) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with second point of steam chest (23) through the 3rd absorber (20), second point of steam chest (23) has concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), second point of steam chest (23) also has refrigerant vapour passage to be communicated with condenser (4), the 3rd generator (15) 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 increasing by the 3rd solution pump, the 3rd absorber (20) is had weak solution pipeline to be communicated with the 3rd generator (15) to be adjusted into the 3rd absorber (20) has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution pump (18).

11. first-class absorption type heat pumps that circulate along separate routes, in shunt circulation first-class absorption type heat pump claimed in claim 1, increase by the 3rd generator, the 3rd absorber, the 4th absorber, the 3rd solution pump, the 4th solution pump, the 3rd solution heat exchanger, the 4th solution heat exchanger, second point of steam chest and solution choke valve, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (2) and to have weak solution pipeline to be communicated with the 4th absorber (24) through solution pump (8) and the 3rd solution heat exchanger (17) through solution pump (8) and solution heat exchanger (12) absorber (2), the 4th absorber (24) also has weak solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18) and the 4th solution heat exchanger (26), the 3rd absorber (20) has weak solution pipeline to be communicated with generator (1) through the 4th solution pump (25) and solution heat exchanger (12) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with the 3rd generator (15) through solution heat exchanger (12), the 3rd generator (15) also has concentrated solution pipeline to be communicated with second point of steam chest (23) through solution choke valve (21) and the 3rd absorber (20), second point of steam chest (23) has concentrated solution pipeline to be communicated with absorber (2) through the 4th solution heat exchanger (26) and the 3rd solution heat exchanger (17) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), second point of steam chest (23) also has refrigerant vapour passage to be communicated with the 4th absorber (24), the 3rd generator (15) drives thermal medium pipeline to be communicated with outside in addition, the 3rd absorber (20) or in addition heated medium pipeline are communicated with outside, the 4th absorber (24) 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 1, increase by the 3rd generator, the 3rd absorber, the 4th absorber, the 3rd solution pump, the 4th solution pump, the 3rd solution heat exchanger, the 4th solution heat exchanger, solution choke valve and second point of steam chest, there is weak solution pipeline to be communicated with generator (1) and to be adjusted into absorber (2) and to have weak solution pipeline to be communicated with the 4th absorber (24) through solution pump (8) and the 3rd solution heat exchanger (17) through solution pump (8) and solution heat exchanger (12) absorber (2), the 4th absorber (24) also has weak solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18) and the 4th solution heat exchanger (26), the 3rd absorber (20) has weak solution pipeline to be communicated with generator (1) through the 4th solution pump (25) and solution heat exchanger (12) again, generator (1) is had concentrated solution pipeline to be communicated with absorber (2) through solution heat exchanger (12) to be adjusted into generator (1) has concentrated solution pipeline to be communicated with the 3rd generator (15) through solution heat exchanger (12), the 3rd generator (15) also has concentrated solution pipeline to be communicated with second point of steam chest (23) through solution choke valve (21) and the 3rd absorber (20), second point of steam chest (23) has concentrated solution pipeline to be communicated with absorber (2) through the 4th solution heat exchanger (26) and the 3rd solution heat exchanger (17) again, the 3rd generator (15) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), second point of steam chest (23) also has refrigerant vapour passage to be communicated with the 4th absorber (24), the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or are communicated with a point steam chest (14) through the 3rd absorber (20), the 3rd generator (15) drives thermal medium pipeline to be communicated with outside in addition, 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 shunt circulation first-class absorption type heat pump claimed in claim 1, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, generator (1) is had refrigerant vapour passage to be communicated with condenser (4) to be adjusted into generator (1) has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 3rd absorber (20) also has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution pump (18) and the 3rd solution heat exchanger (17), the 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution heat exchanger (17), the 3rd generator (15) also has refrigerant vapour passage to be communicated with condenser (4), the 3rd generator (15) drives thermal medium pipeline to be communicated with outside in addition, the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, 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 shunt circulation first-class absorption type heat pump claimed in claim 1, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, generator (1) is had refrigerant vapour passage to be communicated with condenser (4) to be adjusted into generator (1) has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 3rd absorber (20) also has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution pump (18) and the 3rd solution heat exchanger (17), the 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution heat exchanger (17), the 3rd generator (15) also has refrigerant vapour passage to be communicated with condenser (4), the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14), absorber (2) is set up heated medium pipeline and is communicated with outside, the 3rd generator (15) drives thermal medium pipeline to be communicated with outside in addition, 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 shunt circulation first-class absorption type heat pump claimed in claim 1, increase by the 3rd generator, the 3rd absorber, the 3rd solution heat exchanger and the 3rd solution pump, generator (1) is had refrigerant vapour passage to be communicated with condenser (4) to be adjusted into generator (1) has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 3rd absorber (20) also has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution pump (18) and the 3rd solution heat exchanger (17), the 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution heat exchanger (17), the 3rd generator (15) also has refrigerant vapour passage to be communicated with condenser (4), the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14), the 3rd generator (15) drives thermal medium pipeline to be communicated with outside in addition, 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, the second solution pump (9) is set up weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C), after dividing steam chest (14) to have refrigerant vapour passage to be communicated with the second condenser (5) to be adjusted into a point steam chest (14) to have refrigerant vapour passage to be communicated with newly-increased generator (A), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the second condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second condenser (5), 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, at claim 1-6,8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline through the second solution pump (9), newly-increased solution heat exchanger (C), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) again, after dividing steam chest (14) to have refrigerant vapour passage to be communicated with the second condenser (5) to be adjusted into a point steam chest (14) to have refrigerant vapour passage to be communicated with newly-increased generator (A), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the second condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second condenser (5), 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 claim 7, in arbitrary shunt circulation first-class absorption type heat pump described in 15, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline through the second solution pump (9), newly-increased solution heat exchanger (C), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) again, after dividing steam chest (14) to have refrigerant vapour passage to be communicated with the second condenser (5) to be adjusted into a point steam chest (14) to have refrigerant vapour passage to be communicated with newly-increased generator (A), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the second condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second condenser (5), 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 12, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or have weak solution pipeline through the second solution pump (9) through the 3rd absorber (20) with dividing a steam chest (14) to be communicated with to be adjusted into the second absorber (3) again, newly-increased solution heat exchanger (C), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or are communicated with a point steam chest (14) through the 3rd absorber (20), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) again, after dividing steam chest (14) to have refrigerant vapour passage to be communicated with the second condenser (5) to be adjusted into a point steam chest (14) to have refrigerant vapour passage to be communicated with newly-increased generator (A), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the second condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second condenser (5), 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 14, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline through the second solution pump (9), newly-increased solution heat exchanger (C), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) again, after dividing steam chest (14) to have refrigerant vapour passage to be communicated with the second condenser (5) to be adjusted into a point steam chest (14) to have refrigerant vapour passage to be communicated with newly-increased generator (A), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the second condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second condenser (5), 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, at claim 1-6,8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased generator (A) through the second solution pump (9) and the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline again through newly-increased solution pump (D), newly-increased solution heat exchanger (C) and absorber (2) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) and the second solution heat exchanger (13), after dividing steam chest (14) to have refrigerant vapour passage to be communicated with the second condenser (5) to be adjusted into a point steam chest (14) to have refrigerant vapour passage to be communicated with newly-increased generator (A), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the second condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second condenser (5), 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 claim 7, in arbitrary shunt circulation first-class absorption type heat pump described in 15, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased generator (A) through the second solution pump (9) and the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline again through newly-increased solution pump (D), newly-increased solution heat exchanger (C), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) and the second solution heat exchanger (13), after dividing steam chest (14) to have refrigerant vapour passage to be communicated with the second condenser (5) to be adjusted into a point steam chest (14) to have refrigerant vapour passage to be communicated with newly-increased generator (A), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the second condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second condenser (5), 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 12, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or have weak solution pipeline to be communicated with newly-increased generator (A) through the second solution pump (9) and the second solution heat exchanger (13) through the 3rd absorber (20) with dividing a steam chest (14) to be communicated with to be adjusted into the second absorber (3) again, newly-increased generator (A) has concentrated solution pipeline again through newly-increased solution pump (D), newly-increased solution heat exchanger (C), absorber (2) and the 4th absorber (20) are communicated with a point steam chest (14) or are communicated with a point steam chest (14) through the 3rd absorber (20), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) and the second solution heat exchanger (13), after dividing steam chest (14) to have refrigerant vapour passage to be communicated with the second condenser (5) to be adjusted into a point steam chest (14) to have refrigerant vapour passage to be communicated with newly-increased generator (A), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the second condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second condenser (5), 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 14, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased generator (A) through the second solution pump (9) and the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline again through newly-increased solution pump (D), newly-increased solution heat exchanger (C) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) and the second solution heat exchanger (13), after dividing steam chest (14) to have refrigerant vapour passage to be communicated with the second condenser (5) to be adjusted into a point steam chest (14) to have refrigerant vapour passage to be communicated with newly-increased generator (A), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the second condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the second condenser (5), 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 1-15, increase newly-increased point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second evaporimeter (7) is had refrigerant vapour passage to be communicated with the second absorber (3) to be adjusted into the second evaporimeter (7) has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased absorber (E) also has weak solution pipeline through newly-increased solution pump (D), newly-increased solution heat exchanger (C) and absorber (2) are communicated with a newly-increased point steam chest (F), newly-increased point steam chest (F) also has concentrated solution pipeline to be communicated with newly-increased absorber (E) through newly-increased solution heat exchanger (C), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with the second absorber (3), newly-increased absorber (E) also has heated medium pipeline to be communicated with outside, 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, at claim 1-6, 8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, increase newly-increased point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased absorber (E) has weak solution pipeline again through newly-increased solution pump (D), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) to have concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through the second solution heat exchanger (13) and absorber (2), newly-increased point steam chest (F) also has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased absorber (E) also has heated medium pipeline to be communicated with outside, 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 claim 7, in arbitrary shunt circulation first-class absorption type heat pump described in 15, increase newly-increased point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased absorber (E) has weak solution pipeline again through newly-increased solution pump (D), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline through the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a newly-increased point steam chest (F), newly-increased point steam chest (F) also has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased absorber (E) also has heated medium pipeline to be communicated with outside, 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 12, increase newly-increased point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), and absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or have weak solution pipeline to be communicated with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C) through the 3rd absorber (20) with dividing a steam chest (14) to be communicated with to be adjusted into the second absorber (3) again, newly-increased absorber (E) has weak solution pipeline again through newly-increased solution pump (D), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or are communicated with a point steam chest (14) through the 3rd absorber (20), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline through the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a newly-increased point steam chest (F) or are communicated with a newly-increased point steam chest (F) through the 3rd absorber (20), newly-increased point steam chest (F) also has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased absorber (E) also has heated medium pipeline to be communicated with outside, 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 14, increase newly-increased point steam chest, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased absorber (E) has weak solution pipeline again through newly-increased solution pump (D), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) to have concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through the second solution heat exchanger (13) and the 3rd absorber (20), newly-increased point steam chest (F) also has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased absorber (E) also has heated medium pipeline to be communicated with outside, 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, at claim 1-6, 8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, increase 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 solution choke valve, newly-increased point steam chest and newly-increased second point of steam chest, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased the second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased the second absorber (K) also has weak solution pipeline to be communicated with newly-increased absorber (E) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (H), newly-increased absorber (E) has weak solution pipeline again through newly-increased the second solution pump (G), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) to have concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through the second solution heat exchanger (13) and absorber (2), newly-increased point steam chest (F) also has concentrated solution pipeline to be communicated with newly-increased second point of steam chest (I) through newly-increased solution choke valve (J) and newly-increased absorber (E), newly-increased second point of steam chest (I) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased the second solution heat exchanger (H) and newly-increased solution heat exchanger (C) again, newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased second point of steam chest (I) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (K), newly-increased absorber (E) or in addition heated medium pipeline are communicated with outside, newly-increased the second absorber (K) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.

31. first-class absorption type heat pumps that circulate along separate routes, in claim 7, in arbitrary shunt circulation first-class absorption type heat pump described in 15, increase 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 solution choke valve, newly-increased point steam chest and newly-increased second point of steam chest, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased the second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased the second absorber (K) also has weak solution pipeline to be communicated with newly-increased absorber (E) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (H), newly-increased absorber (E) has weak solution pipeline again through newly-increased the second solution pump (G), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline through the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a newly-increased point steam chest (F), newly-increased point steam chest (F) also has concentrated solution pipeline to be communicated with newly-increased second point of steam chest (I) through newly-increased solution choke valve (J) and newly-increased absorber (E), newly-increased second point of steam chest (I) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased the second solution heat exchanger (H) and newly-increased solution heat exchanger (C) again, newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased second point of steam chest (I) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (K), newly-increased absorber (E) or in addition heated medium pipeline are communicated with outside, newly-increased the second absorber (K) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.

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 12, increase 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 solution choke valve, newly-increased point steam chest and newly-increased second point of steam chest, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or have weak solution pipeline to be communicated with newly-increased the second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C) through the 3rd absorber (20) with dividing a steam chest (14) to be communicated with to be adjusted into the second absorber (3) again, newly-increased the second absorber (K) also has weak solution pipeline to be communicated with newly-increased absorber (E) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (H), newly-increased absorber (E) has weak solution pipeline again through newly-increased the second solution pump (G), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or are communicated with a point steam chest (14) through the 3rd absorber (20), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline through the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a newly-increased point steam chest (F) or are communicated with a newly-increased point steam chest (F) through the 3rd absorber (20), newly-increased point steam chest (F) also has concentrated solution pipeline to be communicated with newly-increased second point of steam chest (I) through newly-increased solution choke valve (J) and newly-increased absorber (E), newly-increased second point of steam chest (I) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased the second solution heat exchanger (H) and newly-increased solution heat exchanger (C) again, newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased second point of steam chest (I) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (K), newly-increased absorber (E) or in addition heated medium pipeline are communicated with outside, newly-increased the second absorber (K) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.

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 14, increase 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 solution choke valve, newly-increased point steam chest and newly-increased second point of steam chest, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased the second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased the second absorber (K) also has weak solution pipeline to be communicated with newly-increased absorber (E) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (H), newly-increased absorber (E) has weak solution pipeline again through newly-increased the second solution pump (G), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) to have concentrated solution pipeline to be communicated with a newly-increased point steam chest (F) through the second solution heat exchanger (13) and the 3rd absorber (20), newly-increased point steam chest (F) also has concentrated solution pipeline to be communicated with newly-increased second point of steam chest (I) through newly-increased solution choke valve (J) and newly-increased absorber (E), newly-increased second point of steam chest (I) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased the second solution heat exchanger (H) and newly-increased solution heat exchanger (C) again, newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased second point of steam chest (I) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (K), newly-increased absorber (E) or in addition heated medium pipeline are communicated with outside, newly-increased the second absorber (K) also has heated medium pipeline to be communicated with outside, 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, at claim 1-6, 8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased absorber (E) has weak solution pipeline again through newly-increased solution pump (D), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber (E) also has heated medium pipeline to be communicated with outside, 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 claim 7, in arbitrary shunt circulation first-class absorption type heat pump described in 15, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased absorber (E) has weak solution pipeline again through newly-increased solution pump (D), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber (E) also has heated medium pipeline to be communicated with outside, 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 12, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or have weak solution pipeline to be communicated with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C) through the 3rd absorber (20) with dividing a steam chest (14) to be communicated with to be adjusted into the second absorber (3) again, newly-increased absorber (E) has weak solution pipeline again through newly-increased solution pump (D), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or are communicated with a point steam chest (14) through the 3rd absorber (20), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber (E) also has heated medium pipeline to be communicated with outside, 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 14, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased absorber (E) has weak solution pipeline again through newly-increased solution pump (D), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber (E) also has heated medium pipeline to be communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.

38. first-class absorption type heat pumps that circulate along separate routes, at claim 1-6, 8-11, in arbitrary shunt circulation first-class absorption type heat pump described in 13, 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 solution choke valve and newly-increased point steam chest, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased the second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased the second absorber (K) also has weak solution pipeline to be communicated with newly-increased absorber (E) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (H), newly-increased absorber (E) has weak solution pipeline again through newly-increased the second solution pump (G), the second solution heat exchanger (13) and absorber (2) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), 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 (J) and newly-increased absorber (E), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased the second solution heat exchanger (H) and newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (K), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber (E) or in addition heated medium pipeline are communicated with outside, newly-increased the second absorber (K) also has heated medium pipeline to be communicated with outside, 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 claim 7, in arbitrary shunt circulation first-class absorption type heat pump described in 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 solution choke valve and newly-increased point steam chest, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased the second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased the second absorber (K) also has weak solution pipeline to be communicated with newly-increased absorber (E) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (H), newly-increased absorber (E) has weak solution pipeline again through newly-increased the second solution pump (G), the second solution heat exchanger (13), absorber (2) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), 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 (J) and newly-increased absorber (E), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased the second solution heat exchanger (H) and newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (K), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber (E) or in addition heated medium pipeline are communicated with outside, newly-increased the second absorber (K) also has heated medium pipeline to be communicated with outside, 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 12, 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 solution choke valve and newly-increased point steam chest, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or have weak solution pipeline to be communicated with newly-increased the second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C) through the 3rd absorber (20) with dividing a steam chest (14) to be communicated with to be adjusted into the second absorber (3) again, newly-increased the second absorber (K) also has weak solution pipeline to be communicated with newly-increased absorber (E) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (H), newly-increased absorber (E) has weak solution pipeline again through newly-increased the second solution pump (G), the second solution heat exchanger (13), absorber (2) and the 4th absorber (24) are communicated with a point steam chest (14) or are communicated with a point steam chest (14) through the 3rd absorber (20), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), 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 (J) and newly-increased absorber (E), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased the second solution heat exchanger (H) and newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (K), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber (E) or in addition heated medium pipeline are communicated with outside, newly-increased the second absorber (K) also has heated medium pipeline to be communicated with outside, 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 14, 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 solution choke valve and newly-increased point steam chest, the second absorber (3) is had to weak solution pipeline through the second solution pump (9), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14) and are adjusted into the second absorber (3) and have weak solution pipeline to be communicated with newly-increased the second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C), newly-increased the second absorber (K) also has weak solution pipeline to be communicated with newly-increased absorber (E) through newly-increased solution pump (D) and newly-increased the second solution heat exchanger (H), newly-increased absorber (E) has weak solution pipeline again through newly-increased the second solution pump (G), the second solution heat exchanger (13) and the 3rd absorber (20) are communicated with a point steam chest (14), to divide steam chest (14) to have concentrated solution pipeline to be communicated with the second absorber (3) through the second solution heat exchanger (13) to be adjusted into a point steam chest (14) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (13), 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 (J) and newly-increased absorber (E), a newly-increased point steam chest (F) has concentrated solution pipeline to be communicated with the second absorber (3) through newly-increased the second solution heat exchanger (H) and newly-increased solution heat exchanger (C) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased the second absorber (K), newly-increased generator (A) drives thermal medium pipeline to be communicated with outside in addition, newly-increased absorber (E) or in addition heated medium pipeline are communicated with outside, newly-increased the second absorber (K) also has heated medium pipeline to be communicated with outside, 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 (6) and the second evaporimeter (7) are united two into one, form the first-class absorption type heat pump that circulates along separate routes.

43. 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 1-42, condenser (5) and the second condenser (6) are united two into one, form the first-class absorption type heat pump that circulates along separate routes.

44. 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 choke valve, newly-increased solution heat exchanger and newly-increased solution pump, the second evaporimeter (7) is had refrigerant vapour passage to be communicated with the second absorber (3) to be adjusted into the second evaporimeter (7) has refrigerant vapour passage to be communicated with newly-increased absorber (E), after dividing steam chest (14) to have refrigerant vapour passage to be communicated with the second condenser (5) to be adjusted into a point steam chest (14) to have refrigerant vapour passage to be communicated with newly-increased generator (A), newly-increased generator (A) has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (M) through newly-increased choke valve (B) again, newly-increased evaporimeter (M) also has refrigerant vapour passage to be communicated with the second absorber (3), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (E) through newly-increased solution heat exchanger (C), newly-increased absorber (E) also has weak solution pipeline to be 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 refrigerant vapour passage to be communicated with the second condenser (5), newly-increased absorber (E) also has heated medium pipeline to be communicated with outside, newly-increased evaporimeter (M) medium pipeline that also has surplus heat is communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.

45. 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 choke valve, newly-increased solution heat exchanger, newly-increased solution pump, newly-increased absorber, newly-increased point steam chest, newly-increased condenser and newly-increased evaporimeter, cancel the second absorber (3) and the outside heated medium pipeline being communicated with, newly-increased absorber (E) has weak solution pipeline through newly-increased solution pump (D), newly-increased solution heat exchanger (C) and the second absorber (3) are communicated with a newly-increased point steam chest (F), newly-increased point steam chest (F) also has concentrated solution to be communicated with newly-increased absorber (E) through newly-increased solution heat exchanger (C), newly-increased point steam chest (F) also has refrigerant vapour passage to be communicated with newly-increased condenser (L), newly-increased condenser (L) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (M) through newly-increased choke valve (B), newly-increased evaporimeter (M) also has refrigerant vapour passage to be communicated with newly-increased absorber (E), newly-increased absorber (E) and newly-increased condenser (L) also have respectively heated medium pipeline to be communicated with outside, newly-increased evaporimeter (M) medium pipeline that also has surplus heat is communicated with outside, form the first-class absorption type heat pump that circulates along separate routes.

46. 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 44-45, it is one that evaporimeter (6), the second evaporimeter (7) and newly-increased evaporimeter (M) are closed to three, forms the first-class absorption type heat pump that circulates along separate routes.

47. 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 44, condenser (4) and the second condenser (5) are united two into one, form the first-class absorption type heat pump that circulates along separate routes.

48. 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 45, it is one that condenser (4), the second condenser (5) and newly-increased condenser (L) are closed to three, forms the first-class absorption type heat pump that circulates along separate routes.