CN102353170B - Composite absorption type heat pump on basis of double-effect or triple-effect - Google Patents

Composite absorption type heat pump on basis of double-effect or triple-effect Download PDF

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CN102353170B
CN102353170B CN201110232434.0A CN201110232434A CN102353170B CN 102353170 B CN102353170 B CN 102353170B CN 201110232434 A CN201110232434 A CN 201110232434A CN 102353170 B CN102353170 B CN 102353170B
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communicated
generator
solution
absorber
pipeline
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CN102353170A (en
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李华玉
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    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems

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Abstract

The invention provides a composite absorption type heat pump on the basis of double-effect or triple-effect and belongs to the technical field of heat pumps/refrigeration. A double-effect absorption type heat pump consists of a first generator, a second generator, a first absorber, a first condenser, an evaporator, a first solution pump, a first throttling valve, a second throttling valve, a first solution heat exchanger and a second solution heat exchanger; a second absorber is communicated with a third generator by using a second solution pump and a third solution heat exchanger; a third generator is communicated with the second absorber by using the third solution heat exchanger; the first generator is communicated with the third generator through a refrigerant stream channel, and then the third generator is communicated with a second condenser through a refrigerant liquid pipeline by using a third throttling valve; the third generator is communicated with the second condenser through the refrigerant stream channel; the second generator is communicated with the second absorber through the refrigerant stream channel; and the second condenser is communicated with the first condenser by using a fourth throttling valve, so that the composite absorption type heat pump on the basis of double-effect is formed.

Description

Taking economic benefits and social benefits or triple effect as basic composite absorption heat pump
Technical field:
The invention belongs to low temperature heat and absorption type heat pump.
Background technology:
In each class absorption heat pump, economic benefits and social benefits or three-effect absorption-type heat pump have the advantage that performance index is high, but also have obvious deficiency---can not there is wider heat supply temperature interval and higher heating parameter.Variable working condition heat supply that can not be completely satisfied for single flow process, for obtain higher performance index and meet heated medium with heat demand, in heat pump flowsheet arrangement, will carry out such consideration: when heat supply temperature is low, adopt the two ends heat supply economic benefits and social benefits or the three-effect absorption-type heat pump that adapt, in the time of heat supply temperature, adopt the adjacent run of economic benefits and social benefits or triple effect; , in the arrangement of heat supply end, between the maximum heat supply temperature of each heat supply end, should be connected rationally meanwhile, should not occur the phenomenon that heat supply temperature difference is excessive.
Reasonably technical scheme is, during taking double effect absorption flow process as basis, main the second absorber, the 3rd generator and the second condenser of increasing, the refrigerant vapour that the high pressure generator of double-effect process produces is respectively used to double-effect process and the 3rd generator makes to drive thermal medium, the low pressure generator of double-effect process provides refrigerant vapour to the second absorber, interval two the adjacent heat supply ends of formation temperature; During taking three-effect absorption-type flow process as basis, main the second absorber, the 3rd generator and the second condenser of increasing, the refrigerant vapour that the middle pressure generator of triple effect flow process produces is respectively used to triple effect flow process and the 3rd generator makes to drive thermal medium, the low pressure generator of triple effect flow process provides refrigerant vapour to the second absorber, interval two the adjacent heat supply ends of formation temperature, thus corresponding high-performance index in the time of variable parameter operation, obtained.
Summary of the invention:
Main purpose of the present invention is will provide taking economic benefits and social benefits or triple effect as basic composite absorption heat pump (type I), and concrete summary of the invention subitem is described below:
1. taking economic benefits and social benefits as basic composite absorption heat pump, mainly formed by the first generator, the second generator, the 3rd generator, the first absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, first throttle valve, the second choke valve, the 3rd choke valve, the 4th choke valve, the first solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber has weak solution pipeline to be communicated with the second generator through the second solution heat exchanger with the first generator connected sum through the first solution heat exchanger more respectively after the first solution pump again, the first generator also has concentrated solution pipeline to be communicated with the first absorber through the first solution heat exchanger, the second generator also has concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger, the second absorber has weak solution pipeline to be communicated with the 3rd generator through the second solution pump and the 3rd solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger, after the first generator also has refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with the first condenser through first throttle valve again, after the first generator also has refrigerant vapour passage to be communicated with the 3rd generator, the 3rd generator has cryogen liquid pipeline to be communicated with the second condenser through the 3rd choke valve again, the second generator also has refrigerant vapour passage to be communicated with the first condenser, the second generator also has refrigerant vapour passage to be communicated with the second absorber, the 3rd generator also has refrigerant vapour passage to be communicated with the second condenser, the second condenser also has cryogen liquid pipeline to be communicated with the first condenser or evaporimeter through the 4th choke valve, the first condenser also has cryogen liquid pipeline to be communicated with evaporimeter through the second choke valve, evaporimeter also has refrigerant vapour passage to be communicated with the first absorber, the evaporimeter medium pipeline that also has surplus heat is communicated with outside, the first generator drives thermal medium pipeline to be communicated with outside in addition, the first absorber, the first condenser, the second absorber and the second condenser also have respectively heated medium pipeline to be communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump.
2. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in the 1st, there is weak solution pipeline to be communicated with the 3rd generator and to be adjusted into the second absorber and to have weak solution pipeline to be communicated with the first generator through the second solution pump and the first solution heat exchanger through the second solution pump and the 3rd solution heat exchanger the second absorber, there is weak solution pipeline to be communicated with the first generator and to be adjusted into the first absorber and to have weak solution pipeline to be communicated with the 3rd generator through the first solution pump and the 3rd solution heat exchanger through the first solution pump and the first solution heat exchanger the first absorber, form taking economic benefits and social benefits as basic composite absorption heat pump.
3. taking economic benefits and social benefits as basic composite absorption heat pump, mainly formed by the first generator, the second generator, the 3rd generator, the first absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, first throttle valve, the second choke valve, the 3rd choke valve, the 4th choke valve, the first solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber has weak solution pipeline through the first solution pump, the second solution heat exchanger and the first solution heat exchanger are communicated with the first generator, the first generator also has concentrated solution pipeline to be communicated with the second generator through the first solution heat exchanger, the second generator also has concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger, the second absorber has weak solution pipeline to be communicated with the 3rd generator through the second solution pump and the 3rd solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger, after the first generator also has refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with the first condenser through first throttle valve again, after the first generator also has refrigerant vapour passage to be communicated with the 3rd generator, the 3rd generator has cryogen liquid pipeline to be communicated with the second condenser through the 3rd choke valve again, the second generator also has refrigerant vapour passage to be communicated with the first condenser, the second generator also has refrigerant vapour passage to be communicated with the second absorber, the 3rd generator also has refrigerant vapour passage to be communicated with the second condenser, the second condenser also has cryogen liquid pipeline to be communicated with the first condenser or evaporimeter through the 4th choke valve, the first condenser also has cryogen liquid pipeline to be communicated with evaporimeter through the second choke valve, evaporimeter also has refrigerant vapour passage to be communicated with the first absorber, the evaporimeter medium pipeline that also has surplus heat is communicated with outside, the first generator drives thermal medium pipeline to be communicated with outside in addition, the first absorber, the first condenser, the second absorber and the second condenser also have respectively heated medium pipeline to be communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump.
4. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in the 3rd, increase solution choke valve, have weak solution pipeline to be communicated with the first generator through the first solution pump, the second solution heat exchanger and the first solution heat exchanger to be adjusted into the first absorber to have weak solution pipeline to be communicated with the first generator through the first solution heat exchanger with the second generator connected sum through solution choke valve more respectively after the first solution pump, the second solution heat exchanger the first absorber, formation is taking economic benefits and social benefits as basic composite absorption heat pump again.
5. taking economic benefits and social benefits as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 3-4 item, there is weak solution pipeline to be communicated with the 3rd generator and to be adjusted into the second absorber and to have weak solution pipeline to be communicated with the first generator through the second solution pump and the first solution heat exchanger through the second solution pump and the 3rd solution heat exchanger the second absorber, the first absorber is had to weak solution pipeline through the first solution pump, the second solution heat exchanger and the first solution heat exchanger are communicated with the first generator and are adjusted into the first absorber and have weak solution pipeline through the first solution pump, the second solution heat exchanger and the 3rd solution heat exchanger are communicated with the 3rd generator, form taking economic benefits and social benefits as basic composite absorption heat pump.
6. taking economic benefits and social benefits as basic composite absorption heat pump, mainly formed by the first generator, the second generator, the 3rd generator, the first absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, the 3rd solution pump, first throttle valve, the second choke valve, the 3rd choke valve, the 4th choke valve, the first solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber has weak solution pipeline to be communicated with the second generator through the first solution pump and the second solution heat exchanger, the second generator also has concentrated solution pipeline to be communicated with the first generator through the 3rd solution pump and the first solution heat exchanger, the first generator also has concentrated solution pipeline to be communicated with the first absorber through the first solution heat exchanger and the second solution heat exchanger, the second absorber has weak solution pipeline to be communicated with the 3rd generator through the second solution pump and the 3rd solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger, after the first generator also has refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with the first condenser through first throttle valve again, after the first generator also has refrigerant vapour passage to be communicated with the 3rd generator, the 3rd generator has cryogen liquid pipeline to be communicated with the second condenser through the 3rd choke valve again, the second generator also has refrigerant vapour passage to be communicated with the first condenser, the second generator also has refrigerant vapour passage to be communicated with the second absorber, the 3rd generator also has refrigerant vapour passage to be communicated with the second condenser, the second condenser also has cryogen liquid pipeline to be communicated with the first condenser or evaporimeter through the 4th choke valve, the first condenser also has cryogen liquid pipeline to be communicated with evaporimeter through the second choke valve, evaporimeter also has refrigerant vapour passage to be communicated with the first absorber, the evaporimeter medium pipeline that also has surplus heat is communicated with outside, the first generator drives thermal medium pipeline to be communicated with outside in addition, the first absorber, the first condenser, the second absorber and the second condenser also have respectively heated medium pipeline to be communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump.
7. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in the 6th, increase solution choke valve, have weak solution pipeline to be communicated with the second generator and to be adjusted into the first absorber and to have weak solution pipeline to be directly communicated with the second generator through solution choke valve with the first generator connected sum respectively after the first solution pump and the second solution heat exchanger again through the first solution pump and the second solution heat exchanger the first absorber, formation is taking economic benefits and social benefits as basic composite absorption heat pump.
8. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in the 6th, there is weak solution pipeline to be communicated with the 3rd generator and to be adjusted into the second absorber and to have weak solution pipeline to be communicated with the second generator through the second solution pump and the second solution heat exchanger through the second solution pump and the 3rd solution heat exchanger the second absorber, there is weak solution pipeline to be communicated with the second generator and to be adjusted into the first absorber and to have weak solution pipeline to be communicated with the 3rd generator through the first solution pump and the 3rd solution heat exchanger through the first solution pump and the second solution heat exchanger the first absorber, form taking economic benefits and social benefits as basic composite absorption heat pump.
9. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 1-2 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first 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 first absorber through newly-increased solution heat exchanger, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator to have refrigerant vapour passage to be communicated with newly-increased generator in the second generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into newly-increased generator to set up refrigerant vapour passage in the second generator is communicated with the second absorber, form taking triple effect as basic composite absorption heat pump.
10. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in the 3rd, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first absorber is had weak solution pipeline to be communicated with the second solution heat exchanger through the first solution pump to be adjusted into the first absorber has weak solution pipeline to be communicated with the second solution heat exchanger through the first solution pump and newly-increased solution heat exchanger, the second generator is had concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger to be adjusted into the second generator 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 first absorber through newly-increased solution heat exchanger again, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator to have refrigerant vapour passage to be communicated with newly-increased generator in the second generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into newly-increased generator to set up refrigerant vapour passage in the second generator is communicated with the second absorber, form taking triple effect as basic composite absorption heat pump.
11. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in the 5th, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first generator is had concentrated solution pipeline to be communicated with the second generator through the first solution heat exchanger to be adjusted into the first generator has concentrated solution pipeline to be communicated with the second generator through the first solution heat exchanger and newly-increased solution heat exchanger, there is concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger to be adjusted into the second generator to have concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger in the second generator, newly-increased generator also has concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator to have refrigerant vapour passage to be communicated with newly-increased generator in the second generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into newly-increased generator to set up refrigerant vapour passage in the second generator is communicated with the second absorber, form taking triple effect as basic composite absorption heat pump.
12. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in the 6th, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the second generator and to be adjusted into the first absorber and to have weak solution pipeline to be communicated with newly-increased generator through the first solution pump and the second solution heat exchanger through the first solution pump and the second solution heat exchanger the first absorber, newly-increased generator also has concentrated solution pipeline to be communicated with the second generator through newly-increased solution pump and newly-increased solution heat exchanger, there is concentrated solution pipeline to be communicated with the first absorber and to be adjusted into the first generator and to have concentrated solution pipeline through the first solution heat exchanger through the first solution heat exchanger and the second solution heat exchanger in the first generator, newly-increased solution heat exchanger and the second solution heat exchanger are communicated with the first absorber, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator to have refrigerant vapour passage to be communicated with newly-increased generator in the second generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into newly-increased generator to set up refrigerant vapour passage in the second generator is communicated with the second absorber, form taking triple effect as basic composite absorption heat pump.
13. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in the 8th, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the second generator and to be adjusted into the second absorber and to have weak solution pipeline to be communicated with newly-increased generator through the second solution pump and the second solution heat exchanger through the second solution pump and the second solution heat exchanger the second absorber, newly-increased generator also has concentrated solution pipeline to be communicated with the second generator through newly-increased solution pump and newly-increased solution heat exchanger, there is concentrated solution pipeline to be communicated with the first absorber and to be adjusted into the first generator and to have concentrated solution pipeline through the first solution heat exchanger through the first solution heat exchanger and the second solution heat exchanger in the first generator, newly-increased solution heat exchanger and the second solution heat exchanger are communicated with the first absorber, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator to have refrigerant vapour passage to be communicated with newly-increased generator in the second generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into newly-increased generator to set up refrigerant vapour passage in the second generator is communicated with the second absorber, form taking triple effect as basic composite absorption heat pump.
14. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 9-13 item, after having refrigerant vapour passage to be communicated with the 3rd generator in the first generator the 3rd generator have again cryogen liquid pipeline to be communicated with the second condenser through the 3rd choke valve to be adjusted into the second generator have refrigerant vapour passage to be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline to be communicated with the second condenser through the 3rd choke valve, formation is taking triple effect as basic composite absorption heat pump.
15. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in the 1st, increase by the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger, the first absorber is had weak solution pipeline to be communicated with the first solution heat exchanger and the second solution heat exchanger respectively after the first solution pump to be adjusted into the first absorber has weak solution pipeline to be communicated with the 3rd absorber through the first solution pump and the 4th solution heat exchanger, the 3rd absorber has weak solution pipeline to be communicated with the first solution heat exchanger and the second solution heat exchanger respectively after the 3rd solution pump again, the first generator is had concentrated solution pipeline to be communicated with the first absorber through the first solution heat exchanger to be adjusted into the first generator has concentrated solution pipeline to be communicated with the 4th generator through the first solution heat exchanger, the second generator is had concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger to be adjusted into the second generator has concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger, the 4th generator has concentrated solution pipeline to be communicated with the first absorber through the 4th solution heat exchanger again, the 4th generator also has refrigerant vapour passage to be communicated with the 3rd absorber, the 4th 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 taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
16. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in the 15th, there is weak solution pipeline to be communicated with the 3rd generator and to be adjusted into the second absorber and to have weak solution pipeline to be communicated with the first generator through the second solution pump and the first solution heat exchanger through the second solution pump and the 3rd solution heat exchanger the second absorber, there is weak solution pipeline to be communicated with the first generator and to be adjusted into the 3rd absorber and to have weak solution pipeline to be communicated with the 3rd generator through the 3rd solution pump and the 3rd solution heat exchanger through the 3rd solution pump and the first solution heat exchanger the 3rd absorber, form taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
17. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in the 3rd, increase by the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger, the first absorber is had to weak solution pipeline through the first solution pump, the second solution heat exchanger and the first solution heat exchanger are communicated with the first generator and are adjusted into the first absorber and have weak solution pipeline to be communicated with the 3rd absorber through the first solution pump and the 4th solution heat exchanger, the 3rd absorber has weak solution pipeline again through the 3rd solution pump, the second solution heat exchanger and the first solution heat exchanger are communicated with the first generator, the second generator is had concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger to be adjusted into the second generator has concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger, the 4th generator has concentrated solution pipeline to be communicated with the first absorber through the 4th solution heat exchanger again, the 4th generator also has refrigerant vapour passage to be communicated with the 3rd absorber, the 4th 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 taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
18. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in the 17th, there is weak solution pipeline to be communicated with the 3rd generator and to be adjusted into the second absorber and to have weak solution pipeline to be communicated with the first generator through the second solution pump and the first solution heat exchanger through the second solution pump and the 3rd solution heat exchanger the second absorber, the 3rd absorber is had to weak solution pipeline through the 3rd solution pump, the second solution heat exchanger and the first solution heat exchanger are communicated with the first generator and are adjusted into the 3rd absorber and have weak solution pipeline through the 3rd solution pump, the second solution heat exchanger and the 3rd solution heat exchanger are communicated with the 3rd generator, form taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
19. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in the 6th, increase by the 4th generator, the 3rd absorber, the 4th solution pump and the 4th solution heat exchanger, there is weak solution pipeline to be communicated with the second generator and to be adjusted into the first absorber and to have weak solution pipeline to be communicated with the 3rd absorber through the first solution pump and the 4th solution heat exchanger through the first solution pump and the second solution heat exchanger the first absorber, the 3rd absorber has weak solution pipeline to be communicated with the second generator through the 4th solution pump and the second solution heat exchanger again, there is concentrated solution pipeline to be communicated with the first absorber and to be adjusted into the first generator and to have concentrated solution pipeline to be communicated with the 4th generator through the first solution heat exchanger and the second solution heat exchanger through the first solution heat exchanger and the second solution heat exchanger in the first generator, the 4th generator has concentrated solution pipeline to be communicated with the first absorber through the 4th solution heat exchanger again, the 4th generator also has refrigerant vapour passage to be communicated with the 3rd absorber, the 4th 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 taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
20. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in the 19th, there is weak solution pipeline to be communicated with the 3rd generator and to be adjusted into the second absorber and to have weak solution pipeline to be communicated with the second generator through the second solution pump and the second solution heat exchanger through the second solution pump and the 3rd solution heat exchanger the second absorber, there is weak solution pipeline to be communicated with the second generator and to be adjusted into the 3rd absorber and to have weak solution pipeline to be communicated with the 3rd generator through the 3rd solution pump and the 3rd solution heat exchanger through the 3rd solution pump and the second solution heat exchanger the 3rd absorber, form taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
21. taking economic benefits and social benefits as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 15-20 item, increase by the 5th choke valve, cancel the 4th generator and the outside driving thermal medium pipeline being communicated with, the first generator set up refrigerant vapour passage and be communicated with the 4th generator after the 4th generator have again cryogen liquid pipeline to be communicated with the first condenser through the 5th choke valve, formation is taking economic benefits and social benefits as basic and have a composite absorption heat pump of backheat heat supply end.
22. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 15-16 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 3rd 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 4th generator through newly-increased solution heat exchanger, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator to have refrigerant vapour passage to be communicated with newly-increased generator in the second generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into newly-increased generator to set up refrigerant vapour passage in the second generator is communicated with the second absorber, form taking triple effect as basis and there is the composite absorption heat pump of backheat heat supply end.
23. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in the 17th, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 3rd absorber is had weak solution pipeline to be communicated with the second solution heat exchanger through the 3rd solution pump to be adjusted into the 3rd absorber has weak solution pipeline to be communicated with the second solution heat exchanger through the 3rd solution pump and newly-increased solution heat exchanger, the second generator is had concentrated solution pipeline to be communicated with the 3rd generator through the second solution heat exchanger to be adjusted into the second generator 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 the 3rd generator through newly-increased solution heat exchanger, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator to have refrigerant vapour passage to be communicated with newly-increased generator in the second generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into newly-increased generator to set up refrigerant vapour passage in the second generator is communicated with the second absorber, form taking triple effect as basis and there is the composite absorption heat pump of backheat heat supply end.
24. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in the 18th, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first generator is had concentrated solution pipeline to be communicated with the second generator through the first solution heat exchanger to be adjusted into the first generator has concentrated solution pipeline to be communicated with the second generator through the first solution heat exchanger and newly-increased solution heat exchanger, there is concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger to be adjusted into the second generator to have concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger in the second generator, newly-increased generator also has concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator to have refrigerant vapour passage to be communicated with newly-increased generator in the second generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into newly-increased generator to set up refrigerant vapour passage in the second generator is communicated with the second absorber, form taking triple effect as basis and there is the composite absorption heat pump of backheat heat supply end.
25. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in the 19th, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the second generator and to be adjusted into the 3rd absorber and to have weak solution pipeline to be communicated with newly-increased generator through the 4th solution pump and the second solution heat exchanger through the 4th solution pump and the second solution heat exchanger the 3rd absorber, newly-increased generator also has concentrated solution pipeline to be communicated with the second generator through newly-increased solution pump and newly-increased solution heat exchanger, there is concentrated solution pipeline to be communicated with the 4th generator and to be adjusted into the first generator and to have concentrated solution pipeline through the first solution heat exchanger through the first solution heat exchanger and the second solution heat exchanger in the first generator, newly-increased solution heat exchanger and the second solution heat exchanger are communicated with the 4th generator, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator to have refrigerant vapour passage to be communicated with newly-increased generator in the second generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into newly-increased generator to set up refrigerant vapour passage in the second generator is communicated with the second absorber, form taking triple effect as basis and there is the composite absorption heat pump of backheat heat supply end.
26. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in the 20th, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the second generator and to be adjusted into the second absorber and to have weak solution pipeline to be communicated with newly-increased generator through the second solution pump and the second solution heat exchanger through the second solution pump and the second solution heat exchanger the second absorber, newly-increased generator also has concentrated solution pipeline to be communicated with the second generator through newly-increased solution pump and newly-increased solution heat exchanger, there is concentrated solution pipeline to be communicated with the 4th generator and to be adjusted into the first generator and to have concentrated solution pipeline through the first solution heat exchanger through the first solution heat exchanger and the second solution heat exchanger in the first generator, newly-increased solution heat exchanger and the second solution heat exchanger are communicated with the 4th generator, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the second generator to have refrigerant vapour passage to be communicated with newly-increased generator in the second generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, having refrigerant vapour passage to be communicated with the second absorber to be adjusted into newly-increased generator to set up refrigerant vapour passage in the second generator is communicated with the second absorber, form taking triple effect as basis and there is the composite absorption heat pump of backheat heat supply end.
37. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 22-26 item, increase by the 5th choke valve, cancel the 4th generator and the outside driving thermal medium pipeline being communicated with, the first generator set up refrigerant vapour passage and be communicated with the 4th generator after the 4th generator have again cryogen liquid pipeline to be communicated with the first condenser through the 5th choke valve, formation is taking triple effect as basic and have a composite absorption heat pump of backheat heat supply end.
28. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 22-26 item, increase by the 5th choke valve, cancel the 4th generator and the outside driving thermal medium pipeline being communicated with, the second generator set up refrigerant vapour passage and be communicated with the 4th generator after the 4th generator have again cryogen liquid pipeline to be communicated with the first condenser through the 5th choke valve, formation is taking triple effect as basic and have a composite absorption heat pump of backheat heat supply end.
29. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 22-28 item, after having refrigerant vapour passage to be communicated with the 3rd generator in the first generator the 3rd generator have again cryogen liquid pipeline to be communicated with the second condenser through the 3rd choke valve to be adjusted into the second generator have refrigerant vapour passage to be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline to be communicated with the second condenser through the 3rd choke valve, formation is taking triple effect as basic composite absorption heat pump.
30. taking economic benefits and social benefits as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 1-5 item, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber and the outside heated medium pipeline being communicated with, the 3rd absorber has weak solution pipeline to be communicated with a point steam chest through newly-increased solution choke valve and the first absorber, divide steam chest to also have concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump, divide steam chest to also have refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, the second evaporimeter also has refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has heated medium pipeline to be communicated with outside, the 3rd condenser also has cooling medium pipeline to be communicated with outside, the second evaporimeter medium pipeline that also has surplus heat is communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 3rd condenser has cryogen liquid pipeline to be communicated with the first evaporimeter, and the first evaporimeter is set up refrigerant vapour passage and is communicated with the 3rd absorber.
31. taking economic benefits and social benefits as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 6-8 item, increase by the 4th solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber and the outside heated medium pipeline being communicated with, the 3rd absorber has weak solution pipeline to be communicated with a point steam chest through newly-increased solution choke valve and the first absorber, divide steam chest to also have concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution pump, divide steam chest to also have refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, the second evaporimeter also has refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has heated medium pipeline to be communicated with outside, the 3rd condenser also has cooling medium pipeline to be communicated with outside, the second evaporimeter medium pipeline that also has surplus heat is communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 3rd condenser has cryogen liquid pipeline to be communicated with the first evaporimeter, and the first evaporimeter is set up refrigerant vapour passage and is communicated with the 3rd absorber.
32. taking economic benefits and social benefits as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 1-2 item, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber through the first solution heat exchanger to be adjusted into the first generator to have concentrated solution pipeline to be communicated with a point steam chest through the first solution heat exchanger and the first absorber in the first generator, there is concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger to be adjusted into the second generator to have concentrated solution pipeline to be communicated with a point steam chest through the second solution heat exchanger and the first absorber in the second generator, divide steam chest to also have concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump, the 3rd absorber also has weak solution pipeline to be communicated with the first absorber through newly-increased solution choke valve, divide steam chest to also have refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with the first evaporimeter through cryogen liquid pump, the first evaporimeter has cryogen liquid pipeline to be communicated with the second evaporimeter through the 5th choke valve, the first evaporimeter is had refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has refrigerant vapour passage to be communicated with the 3rd absorber, the second evaporimeter also has refrigerant vapour passage to be communicated with the first absorber, the 3rd absorber also has heated medium pipeline to be communicated with outside, the 3rd condenser also has cooling medium pipeline to be communicated with outside, the second evaporimeter medium pipeline that also has surplus heat is communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has weak solution pipeline to be communicated with the first absorber, and the first evaporimeter is set up refrigerant vapour passage and is communicated with the first absorber.
33. taking economic benefits and social benefits as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 3-5 item, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger to be adjusted into the second generator to have concentrated solution pipeline to be communicated with a point steam chest through the second solution heat exchanger and the first absorber in the second generator, divide steam chest to also have concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump, the 3rd absorber also has weak solution pipeline to be communicated with the first absorber through newly-increased solution choke valve, divide steam chest to also have refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with the first evaporimeter through cryogen liquid pump, the first evaporimeter has cryogen liquid pipeline to be communicated with the second evaporimeter through the 5th choke valve, the first evaporimeter is had refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has refrigerant vapour passage to be communicated with the 3rd absorber, the second evaporimeter also has refrigerant vapour passage to be communicated with the first absorber, the 3rd absorber also has heated medium pipeline to be communicated with outside, the 3rd condenser also has cooling medium pipeline to be communicated with outside, the second evaporimeter medium pipeline that also has surplus heat is communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has weak solution pipeline to be communicated with the first absorber, and the first evaporimeter is set up refrigerant vapour passage and is communicated with the first absorber.
34. taking economic benefits and social benefits as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 6-8 item, increase by the 4th solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber and to be adjusted into the first generator and to have concentrated solution pipeline through the first solution heat exchanger through the first solution heat exchanger and the second solution heat exchanger in the first generator, the second solution heat exchanger and the first absorber are communicated with a point steam chest, divide steam chest to also have concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution pump, the 3rd absorber also has weak solution pipeline to be communicated with the first absorber through newly-increased solution choke valve, divide steam chest to also have refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with the first evaporimeter through cryogen liquid pump, the first evaporimeter has cryogen liquid pipeline to be communicated with the second evaporimeter through the 5th choke valve, the first evaporimeter is had refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has refrigerant vapour passage to be communicated with the 3rd absorber, the second evaporimeter also has refrigerant vapour passage to be communicated with the first absorber, the 3rd absorber also has heated medium pipeline to be communicated with outside, the 3rd condenser also has cooling medium pipeline to be communicated with outside, the second evaporimeter medium pipeline that also has surplus heat is communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has weak solution pipeline to be communicated with the first absorber, and the first evaporimeter is set up refrigerant vapour passage and is communicated with the first absorber.
35. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 9-11 item, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber and the outside heated medium pipeline being communicated with, the 3rd absorber has weak solution pipeline to be communicated with a point steam chest through newly-increased solution choke valve and the first absorber, divide steam chest to also have concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump, divide steam chest to also have refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, the second evaporimeter also has refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has heated medium pipeline to be communicated with outside, the 3rd condenser also has cooling medium pipeline to be communicated with outside, the second evaporimeter medium pipeline that also has surplus heat is communicated with outside, form taking triple effect as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 3rd condenser has cryogen liquid pipeline to be communicated with the first evaporimeter, and the first evaporimeter is set up refrigerant vapour passage and is communicated with the 3rd absorber.
36. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 12-13 item, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber and the outside heated medium pipeline being communicated with, the 3rd absorber has weak solution pipeline to be communicated with a point steam chest through newly-increased solution choke valve and the first absorber, divide steam chest to also have concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump, divide steam chest to also have refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, the second evaporimeter also has refrigerant vapour passage to be communicated with the 3rd absorber, the 3rd absorber also has heated medium pipeline to be communicated with outside, the 3rd condenser also has cooling medium pipeline to be communicated with outside, the second evaporimeter medium pipeline that also has surplus heat is communicated with outside, form taking triple effect as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 3rd condenser has cryogen liquid pipeline to be communicated with the first evaporimeter, and the first evaporimeter is set up refrigerant vapour passage and is communicated with the 3rd absorber.
37. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in the 9th, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber through the first solution heat exchanger to be adjusted into the first generator to have concentrated solution pipeline to be communicated with a point steam chest through the first solution heat exchanger and the first absorber in the first generator, there is concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger to be adjusted into the second generator to have concentrated solution pipeline to be communicated with a point steam chest through the second solution heat exchanger and the first absorber in the second generator, to increase generator newly has concentrated solution pipeline to be communicated with the first absorber and to be adjusted into newly-increased generator and to have concentrated solution pipeline to be communicated with dividing a steam chest through increasing solution heat exchanger and the first absorber newly through newly-increased solution heat exchanger, divide steam chest to also have concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump, the 3rd absorber also has weak solution pipeline to be communicated with the first absorber through newly-increased solution choke valve, divide steam chest to also have refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with the first evaporimeter through cryogen liquid pump, the first evaporimeter has cryogen liquid pipeline to be communicated with the second evaporimeter through the 5th choke valve, the first evaporimeter is had refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has refrigerant vapour passage to be communicated with the 3rd absorber, the second evaporimeter also has refrigerant vapour passage to be communicated with the first absorber, the 3rd absorber also has heated medium pipeline to be communicated with outside, the 3rd condenser also has cooling medium pipeline to be communicated with outside, the second evaporimeter medium pipeline that also has surplus heat is communicated with outside, form taking triple effect as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has weak solution pipeline to be communicated with the first absorber, and the first evaporimeter is set up refrigerant vapour passage and is communicated with the first absorber.
38. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 10-11 item, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber and the outside heated medium pipeline being communicated with, to increase generator newly has concentrated solution pipeline to be communicated with the first absorber through the second solution heat exchanger to be adjusted into newly-increased generator to have concentrated solution pipeline to be communicated with dividing a steam chest through the second solution heat exchanger and the first absorber, divide steam chest to also have concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump, the 3rd absorber also has weak solution pipeline to be communicated with the first absorber through newly-increased solution choke valve, divide steam chest to also have refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with the first evaporimeter through cryogen liquid pump, the first evaporimeter has cryogen liquid pipeline to be communicated with the second evaporimeter through the 5th choke valve, the first evaporimeter is had refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has refrigerant vapour passage to be communicated with the 3rd absorber, the second evaporimeter also has refrigerant vapour passage to be communicated with the first absorber, the 3rd absorber also has heated medium pipeline to be communicated with outside, the 3rd condenser also has cooling medium pipeline to be communicated with outside, the second evaporimeter medium pipeline that also has surplus heat is communicated with outside, form taking triple effect as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has weak solution pipeline to be communicated with the first absorber, and the first evaporimeter is set up refrigerant vapour passage and is communicated with the first absorber.
39. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 12-13 item, increase by the 4th solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber and the outside heated medium pipeline being communicated with, the first generator is had to concentrated solution pipeline through the first solution heat exchanger, newly-increased solution heat exchanger and the second solution heat exchanger are communicated with the first absorber and are adjusted into the first generator and have concentrated solution pipeline through the first solution heat exchanger, newly-increased solution heat exchanger, the second solution heat exchanger and the first absorber are communicated with a point steam chest, divide steam chest to also have concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution pump, the 3rd absorber also has weak solution pipeline to be communicated with the first absorber through newly-increased solution choke valve, divide steam chest to also have refrigerant vapour passage to be communicated with the 3rd condenser, the 3rd condenser also has cryogen liquid pipeline to be communicated with the first evaporimeter through cryogen liquid pump, the first evaporimeter has cryogen liquid pipeline to be communicated with the second evaporimeter through the 5th choke valve, the first evaporimeter is had refrigerant vapour passage to be communicated with the first absorber to be adjusted into the first evaporimeter has refrigerant vapour passage to be communicated with the 3rd absorber, the second evaporimeter also has refrigerant vapour passage to be communicated with the first absorber, the 3rd absorber also has heated medium pipeline to be communicated with outside, the 3rd condenser also has cooling medium pipeline to be communicated with outside, the second evaporimeter medium pipeline that also has surplus heat is communicated with outside, form taking triple effect as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has weak solution pipeline to be communicated with the first absorber, and the first evaporimeter is set up refrigerant vapour passage and is communicated with the first absorber.
40. taking triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 35-39 item, after having refrigerant vapour passage to be communicated with the 3rd generator in the first generator the 3rd generator have again cryogen liquid pipeline to be communicated with the second condenser through the 3rd choke valve to be adjusted into the second generator have refrigerant vapour passage to be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline to be communicated with the second condenser through the 3rd choke valve, formation is taking triple effect as basic composite absorption heat pump.
41. taking economic benefits and social benefits or triple effect as basic composite absorption heat pump, in the arbitrary composite absorption heat pump described in 1-40 item, increase first flow control valve and second adjustable valve, there are respectively heated medium pipeline and outside connection to be defined as outside and to have heated medium pipeline to be communicated with the first condenser afterwards with the first condenser to have again heated medium pipeline to be communicated with the second condenser through second adjustable valve with outside connected sum through first flow control valve respectively the first condenser and the second condenser, the second condenser has heated medium pipeline to be communicated with outside again, formation has adjust flux and distributes, taking economic benefits and social benefits or triple effect as basic composite absorption heat pump.
Brief description of the drawings:
Fig. 1 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 1st kind of structure and schematic flow sheet.
Fig. 2 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 2nd kind of structure and schematic flow sheet.
Fig. 3 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 3rd kind of structure and schematic flow sheet.
Fig. 4 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 4th kind of structure and schematic flow sheet.
Fig. 5 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 5th kind of structure and schematic flow sheet.
Fig. 6 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 6th kind of structure and schematic flow sheet.
Fig. 7 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 7th kind of structure and schematic flow sheet.
Fig. 8 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 8th kind of structure and schematic flow sheet.
Fig. 9 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 9th kind of structure and schematic flow sheet.
Figure 10 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 10th kind of structure and schematic flow sheet.
Figure 11 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 11st kind of structure and schematic flow sheet.
Figure 12 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 12nd kind of structure and schematic flow sheet.
Figure 13 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 13rd kind of structure and schematic flow sheet.
Figure 14 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 14th kind of structure and schematic flow sheet.
Figure 15 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 15th kind of structure and schematic flow sheet.
Figure 16 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 16th kind of structure and schematic flow sheet.
Figure 17 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 17th kind of structure and schematic flow sheet.
Figure 18 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 18th kind of structure and schematic flow sheet.
Figure 19 is according to provided by the present invention taking economic benefits and social benefits as basic composite absorption heat pump the 19th kind of structure and schematic flow sheet.
Figure 20 is according to provided by the present invention taking triple effect as basic composite absorption heat pump the 1st kind of structure and schematic flow sheet.
Figure 21 is according to provided by the present invention taking triple effect as basic composite absorption heat pump the 2nd kind of structure and schematic flow sheet.
Figure 22 is according to provided by the present invention taking triple effect as basic composite absorption heat pump the 3rd kind of structure and schematic flow sheet.
Figure 23 is according to provided by the present invention taking triple effect as basic composite absorption heat pump the 4th kind of structure and schematic flow sheet.
Figure 24 is according to provided by the present invention taking triple effect as basic composite absorption heat pump the 5th kind of structure and schematic flow sheet.
Figure 25 is according to provided by the present invention taking triple effect as basic composite absorption heat pump the 6th kind of structure and schematic flow sheet.
Figure 26 is according to provided by the present invention taking triple effect as basic composite absorption heat pump the 7th kind of structure and schematic flow sheet.
In figure, 1-the first generator, 2-the second generator, 3-the 3rd generator, 4-the first absorber, 5-the second absorber, 6-the first condenser, 7-the second condenser, 8-evaporimeter, 9-the first solution pump, 10-the second solution pump, 11-first throttle valve, 12-the second choke valve, 13-the 3rd choke valve, 14-the 4th choke valve, 15-the first solution heat exchanger, 16-the second solution heat exchanger, 17-the 3rd solution heat exchanger, 18-the 3rd solution pump, 19-the 4th generator, 20-the 3rd absorber, 21-the 4th solution heat exchanger, 22-the 5th choke valve, 23-divides steam chest, 24-the 3rd condenser, 25-the second evaporimeter, 26-cryogen liquid pump, 27-solution choke valve, 28-first flow control valve, 29-second adjustable valve, 30-the 4th solution pump, A-increases generator newly, and B-increases choke valve newly, and C-increases solution heat exchanger newly, and D-increases solution pump newly, and E-increases solution choke valve newly.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, in inessential situation, do not repeat statement.Describe the present invention in detail below in conjunction with accompanying drawing and example.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Fig. 1
1. in structure, it is mainly made up of the first generator, the second generator, the 3rd generator, the first absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, first throttle valve, the second choke valve, the 3rd choke valve, the 4th choke valve, the first solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger; the first absorber 4 has weak solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 16 with the first generator 1 connected sum through the first solution heat exchanger 15 more respectively after the first solution pump 9 again, the first generator 1 also has concentrated solution pipeline to be communicated with the first absorber 4 through the first solution heat exchanger 15, the second generator 2 also has concentrated solution pipeline to be communicated with the first absorber 4 through the second solution heat exchanger 16, the second absorber 5 has weak solution pipeline to be communicated with the 3rd generator 3 through the second solution pump 10 and the 3rd solution heat exchanger 17, the 3rd generator 3 also has concentrated solution pipeline to be communicated with the second absorber 5 through the 3rd solution heat exchanger 17, after the first generator 1 also has refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with the first condenser 6 through first throttle valve 11 again, after the first generator 1 also has refrigerant vapour passage to be communicated with the 3rd generator 3, the 3rd generator 3 has cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13 again, the second generator 2 also has refrigerant vapour passage to be communicated with the first condenser 6, the second generator 2 also has refrigerant vapour passage to be communicated with the second absorber 5, the 3rd generator 3 also has refrigerant vapour passage to be communicated with the second condenser 7, the second condenser 7 also has cryogen liquid pipeline to be communicated with the first condenser 6 through the 4th choke valve 14, the first condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 8 through the second choke valve 12, evaporimeter 8 also has refrigerant vapour passage to be communicated with the first absorber 4, evaporimeter 8 medium pipeline that also has surplus heat is communicated with outside, the first generator 1 drives thermal medium pipeline to be communicated with outside in addition, the first absorber 4, the first condenser 6, the second absorber 5 and the second condenser 7 also have respectively heated medium pipeline to be communicated with outside.
2. in flow process, the weak solution of the first absorber 4 enters the first generator 1 and enters the second generator 2 through the second solution heat exchanger 16 again through the first solution heat exchanger 15 more respectively after the first solution pump 9, the solution that drives heat medium flow to enter in it through the first generator 1, heating discharges and provides refrigerant vapour to the second generator 2 and the 3rd generator 3 respectively, and the concentrated solution of the first generator 1 enters the first absorber 4 through the first solution heat exchanger 15, the refrigerant vapour solution that the second generator 2, heating enter in it of flowing through discharges and provides refrigerant vapour to the first condenser 6 and the second absorber 5 respectively, the concentrated solution of the second generator 2 enters the first absorber 4 through the second solution heat exchanger 16, and the refrigerant vapour heat release of second generator 2 of flowing through enters the first condenser 6 through first throttle valve 11 after becoming cryogen liquid again, the weak solution of the second absorber 5 enters the 3rd generator 3 through the second solution pump 10 and the 3rd solution heat exchanger 17, the refrigerant vapour solution that the 3rd generator 3, heating enter in it of flowing through discharges and provides refrigerant vapour to the second condenser 7, the concentrated solution of the 3rd generator 3 enters the second absorber 5, absorbs from the refrigerant vapour of the second generator 2 heat release in heated medium through the 3rd solution heat exchanger 17, and the refrigerant vapour heat release of the 3rd generator 3 of flowing through enters the second condenser 7 through the 3rd choke valve 13 after becoming cryogen liquid again, the refrigerant vapour heat release of the second condenser 7 becomes cryogen liquid in heated medium, the cryogen liquid of the second condenser 7 enters the first condenser 6 through the 4th choke valve 14 throttlings, the refrigerant vapour heat release of the first condenser 6 becomes cryogen liquid in heated medium, the cryogen liquid of the first condenser 6 enters evaporimeter 8 through the second choke valve 12 throttlings, absorbing waste heat becomes refrigerant vapour and provides to the first absorber 4, the refrigerant vapour that enters the first absorber 4 is absorbed also heat release in heated medium by the concentrated solution from the first generator 1 and the second generator 2, form taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Fig. 2
1. in structure, in the composite absorption heat pump shown in Fig. 1, there is weak solution pipeline to be communicated with the 3rd generator 3 and to be adjusted into the second absorber 5 and to have weak solution pipeline to be communicated with the first generator 1 through the second solution pump 10 and the first solution heat exchanger 15 through the second solution pump 10 and the 3rd solution heat exchanger 17 the second absorber 5, there is weak solution pipeline to be communicated with the first generator 1 and to be adjusted into the first absorber 4 and to have weak solution pipeline to be communicated with the 3rd generator 3 through the first solution pump 9 and the 3rd solution heat exchanger 17 through the first solution pump 9 and the first solution heat exchanger 15 the first absorber 4.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively; The weak solution of the first absorber 4 enters the 3rd generator 3 through the first solution pump 9 and the 3rd solution heat exchanger 17, the concentrated solution of the 3rd generator 3 enters the second absorber 5 through the 3rd solution heat exchanger 17, the weak solution of the second absorber 5 enters the first generator 1 through the second solution pump 10 and the first solution heat exchanger 15, the concentrated solution of the first generator 1 enters the first absorber 4 through the first solution heat exchanger 15, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Fig. 3
1. in structure, it is mainly made up of the first generator, the second generator, the 3rd generator, the first absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, first throttle valve, the second choke valve, the 3rd choke valve, the 4th choke valve, the first solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger, the first absorber 4 has weak solution pipeline through the first solution pump 9, the second solution heat exchanger 16 and the first solution heat exchanger 15 are communicated with the first generator 1, the first generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through the first solution heat exchanger 15, the second generator 2 also has concentrated solution pipeline to be communicated with the first absorber 4 through the second solution heat exchanger 16, the second absorber 5 has weak solution pipeline to be communicated with the 3rd generator 3 through the second solution pump 10 and the 3rd solution heat exchanger 17, the 3rd generator 3 also has concentrated solution pipeline to be communicated with the second absorber 5 through the 3rd solution heat exchanger 17, after the first generator 1 also has refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with the first condenser 6 through first throttle valve 11 again, after the first generator 1 also has refrigerant vapour passage to be communicated with the 3rd generator 3, the 3rd generator 3 has cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13 again, the second generator 2 also has refrigerant vapour passage to be communicated with the first condenser 6, the second generator 2 also has refrigerant vapour passage to be communicated with the second absorber 5, the 3rd generator 3 also has refrigerant vapour passage to be communicated with the second condenser 7, the second condenser 7 also has cryogen liquid pipeline to be communicated with the first condenser 6 through the 4th choke valve 14, the first condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 8 through the second choke valve 12, evaporimeter 8 also has refrigerant vapour passage to be communicated with the first absorber 4, evaporimeter 8 medium pipeline that also has surplus heat is communicated with outside, the first generator 1 drives thermal medium pipeline to be communicated with outside in addition, the first absorber 4, the first condenser 6, the second absorber 5 and the second condenser 7 also have respectively heated medium pipeline to be communicated with outside.
2. in flow process, the weak solution of the first absorber 4 enters the first generator 1 through the first solution pump 9, the second solution heat exchanger 16 and the first solution heat exchanger 15, the solution that drives heat medium flow to enter in it through the first generator 1, heating discharges and provides refrigerant vapour to the second generator 2 and the 3rd generator 3 respectively, and the concentrated solution of the first generator 1 enters the second generator 2 through the first solution heat exchanger 15; The refrigerant vapour solution that the second generator 2, heating enter in it of flowing through discharges and provides refrigerant vapour to the first condenser 6 and the second absorber 5 respectively, the concentrated solution of the second generator 2 enters the first absorber 4 through the second solution heat exchanger 16, and the refrigerant vapour heat release of second generator 2 of flowing through enters the first condenser 6 through first throttle valve 11 after becoming cryogen liquid again; The weak solution of the second absorber 5 enters the 3rd generator 3 through the second solution pump 10 and the 3rd solution heat exchanger 17, the refrigerant vapour solution that the 3rd generator 3, heating enter in it of flowing through discharges and provides refrigerant vapour to the second condenser 7, the concentrated solution of the 3rd generator 3 enters the second absorber 5, absorbs from the refrigerant vapour of the second generator 2 heat release in heated medium through the 3rd solution heat exchanger 17, and the refrigerant vapour heat release of the 3rd generator 3 of flowing through enters the second condenser 7 through the 3rd choke valve 13 after becoming cryogen liquid again; The refrigerant vapour heat release of the second condenser 7 becomes cryogen liquid in heated medium, the cryogen liquid of the second condenser 7 enters the first condenser 6 through the 4th choke valve 14 throttlings, the refrigerant vapour heat release of the first condenser 6 becomes cryogen liquid in heated medium, the cryogen liquid of the first condenser 6 through the second choke valve 12 throttlings enter evaporimeter 8, absorb waste heat become refrigerant vapour and provide to the first absorber 4, the refrigerant vapour that enters the first absorber 4 is absorbed also heat release in heated medium by the concentrated solution from the second generator 2, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Fig. 4
1. in structure, in the composite absorption heat pump shown in Fig. 3, there is weak solution pipeline to be communicated with the 3rd generator 3 and to be adjusted into the second absorber 5 and to have weak solution pipeline to be communicated with the first generator 1 through the second solution pump 10 and the first solution heat exchanger 15 through the second solution pump 10 and the 3rd solution heat exchanger 17 the second absorber 5, the first absorber 4 is had to weak solution pipeline through the first solution pump 9, the second solution heat exchanger 16 and the first solution heat exchanger 15 are communicated with the first generator 1 and are adjusted into the first absorber 4 and have weak solution pipeline through the first solution pump 9, the second solution heat exchanger 16 and the 3rd solution heat exchanger 17 are communicated with the 3rd generator 3.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively, the weak solution of the first absorber 4 is through the first solution pump 9, the second solution heat exchanger 16 and the 3rd solution heat exchanger 17 enter the 3rd generator 3, the concentrated solution of the 3rd generator 3 enters the second absorber 5 through the 3rd solution heat exchanger 17, the weak solution of the second absorber 5 enters the first generator 1 through the second solution pump 10 and the first solution heat exchanger 15, the concentrated solution of the first generator 1 enters the second generator 2 through the first solution heat exchanger 15, the concentrated solution of the second generator 2 enters the first absorber 4 through the second solution heat exchanger 16, form taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Fig. 5
1. in structure, it is mainly made up of the first generator, the second generator, the 3rd generator, the first absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, the 3rd solution pump, first throttle valve, the second choke valve, the 3rd choke valve, the 4th choke valve, the first solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger; the first absorber 4 has weak solution pipeline to be communicated with the second generator 2 through the first solution pump 9 and the second solution heat exchanger 16, the second generator 2 also has concentrated solution pipeline to be communicated with the first generator 1 through the 3rd solution pump 18 and the first solution heat exchanger 15, the first generator 1 also has concentrated solution pipeline to be communicated with the first absorber 4 through the first solution heat exchanger 15 and the second solution heat exchanger 16, the second absorber 5 has weak solution pipeline to be communicated with the 3rd generator 3 through the second solution pump 10 and the 3rd solution heat exchanger 17, the 3rd generator 3 also has concentrated solution pipeline to be communicated with the second absorber 5 through the 3rd solution heat exchanger 17, after the first generator 1 also has refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with the first condenser 6 through first throttle valve 11 again, after the first generator 1 also has refrigerant vapour passage to be communicated with the 3rd generator 3, the 3rd generator 3 has cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13 again, the second generator 2 also has refrigerant vapour passage to be communicated with the first condenser 6, the second generator 2 also has refrigerant vapour passage to be communicated with the second absorber 5, the 3rd generator 3 also has refrigerant vapour passage to be communicated with the second condenser 7, the second condenser 7 also has cryogen liquid pipeline to be communicated with the first condenser 6 through the 4th choke valve 14, the first condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 8 through the second choke valve 12, evaporimeter 8 also has refrigerant vapour passage to be communicated with the first absorber 4, evaporimeter 8 medium pipeline that also has surplus heat is communicated with outside, the first generator 1 drives thermal medium pipeline to be communicated with outside in addition, the first absorber 4, the first condenser 6, the second absorber 5 and the second condenser 7 also have respectively heated medium pipeline to be communicated with outside.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 makes to drive thermal medium, the weak solution of the first absorber 4 enters the second generator 2 through the first solution pump 9 and the second solution heat exchanger 16, refrigerant vapour second generator 2 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to the first condenser 6 and the second absorber 5 respectively, the concentrated solution of the second generator 2 enters the first generator 1 through the 3rd solution pump 18 and the first solution heat exchanger 15, flow through after the refrigerant vapour heat release of the second generator 2 becomes cryogen liquid and enter the first condenser 6 through first throttle valve 11 again, the solution that drives heat medium flow to enter in it through the first generator 1, heating discharges and provides refrigerant vapour to the second generator 2 and the 3rd generator 3 respectively, and the concentrated solution of the first generator 1 enters the first absorber 4 through the first solution heat exchanger 15 and the second solution heat exchanger 16, the weak solution of the second absorber 5 enters the 3rd generator 3 through the second solution pump 10 and the 3rd solution heat exchanger 17, the refrigerant vapour solution that the 3rd generator 3, heating enter in it of flowing through discharges and provides refrigerant vapour to the second condenser 7, the concentrated solution of the 3rd generator 3 enters the second absorber 5, absorbs from the refrigerant vapour of the second generator 2 heat release in heated medium through the 3rd solution heat exchanger 17, and the refrigerant vapour heat release of the 3rd generator 3 of flowing through enters the second condenser 7 through the 3rd choke valve 13 after becoming cryogen liquid again, the refrigerant vapour heat release of the second condenser 7 becomes cryogen liquid in heated medium, the cryogen liquid of the second condenser 7 enters the first condenser 6 through the 4th choke valve 14 throttlings, the refrigerant vapour heat release of the first condenser 6 becomes cryogen liquid in heated medium, the cryogen liquid of the first condenser 6 through the second choke valve 12 throttlings enter evaporimeter 8, absorb waste heat become refrigerant vapour and provide to the first absorber 4, the refrigerant vapour that enters the first absorber 4 is absorbed also heat release in heated medium by the concentrated solution from the first generator 1, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Fig. 6
In the composite absorption heat pump shown in Fig. 5, increase solution choke valve, there is weak solution pipeline to be communicated with the second generator 2 and to be adjusted into the first absorber 4 and to have weak solution pipeline to be directly communicated with the second generator 2 through solution choke valve 27 again with the first generator 1 connected sum respectively after the first solution pump 9 and the second solution heat exchanger 16 through the first solution pump 9 and the second solution heat exchanger 16 the first absorber 4, form taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Fig. 7
1. in structure, in the composite absorption heat pump shown in Fig. 5, there is weak solution pipeline to be communicated with the 3rd generator 3 and to be adjusted into the second absorber 5 and to have weak solution pipeline to be communicated with the second generator 2 through the second solution pump 10 and the second solution heat exchanger 16 through the second solution pump 10 and the 3rd solution heat exchanger 17 the second absorber 5, there is weak solution pipeline to be communicated with the second generator 2 and to be adjusted into the first absorber 4 and to have weak solution pipeline to be communicated with the 3rd generator 3 through the first solution pump 9 and the 3rd solution heat exchanger 17 through the first solution pump 9 and the second solution heat exchanger 16 the first absorber 4.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively, the weak solution of the first absorber 4 enters the 3rd generator 3 through the first solution pump 9 and the 3rd solution heat exchanger 17, the concentrated solution of the 3rd generator 3 enters the second absorber 5 through the 3rd solution heat exchanger 17, the weak solution of the second absorber 5 enters the second generator 2 through the second solution pump 10 and the second solution heat exchanger 16, the concentrated solution of the second generator 2 enters the first generator 1 through the 3rd solution pump 18 and the first solution heat exchanger 15, the concentrated solution of the first generator 1 enters the first absorber 4 through the first solution heat exchanger 15 and the second solution heat exchanger 16, form taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Fig. 8
1. in structure, in the composite absorption heat pump shown in Fig. 1, increase by the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger, the first absorber 4 is had weak solution pipeline to be communicated with the first solution heat exchanger 15 and the second solution heat exchanger 16 respectively after the first solution pump 9 to be adjusted into the first absorber 4 has weak solution pipeline to be communicated with the 3rd absorber 20 through the first solution pump 9 and the 4th solution heat exchanger 21, the 3rd absorber 20 has weak solution pipeline to be communicated with the first solution heat exchanger 15 and the second solution heat exchanger 16 respectively after the 3rd solution pump 18 again, the first generator 1 is had concentrated solution pipeline to be communicated with the first absorber 4 through the first solution heat exchanger 15 to be adjusted into the first generator 1 has concentrated solution pipeline to be communicated with the 4th generator 19 through the first solution heat exchanger 15, the second generator 2 is had concentrated solution pipeline to be communicated with the first absorber 4 through the second solution heat exchanger 16 to be adjusted into the second generator 2 has concentrated solution pipeline to be communicated with the 4th generator 19 through the second solution heat exchanger 16, the 4th generator 19 has concentrated solution pipeline to be communicated with the first absorber 4 through the 4th solution heat exchanger 21 again, the 4th generator 19 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, the 4th generator 19 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 that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively; The weak solution of the first absorber 4 enters the 3rd absorber 20, absorbs from the refrigerant vapour of the 4th generator 19 heat release in heated medium through the first solution pump 9 and the 4th solution heat exchanger 21, and the weak solution of the 3rd absorber 20 enters the first generator 1 and enters the second generator 2 through the second solution heat exchanger 16 again through the first solution heat exchanger 15 more respectively after the 3rd solution pump 18; The concentrated solution of the first generator 1 enters the 4th generator 19 through the first solution heat exchanger 15, the concentrated solution of the second generator 2 enters the 4th generator 19 through the second solution heat exchanger 16, the solution that drives heat medium flow to enter in it through the 4th generator 19, heating discharges and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 4th generator 19 enters the first absorber 4 through the 4th solution heat exchanger 21, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Fig. 9
1. in structure, in the composite absorption heat pump shown in Fig. 3, increase by the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger, the first absorber 4 is had to weak solution pipeline through the first solution pump 9, the second solution heat exchanger 16 and the first solution heat exchanger 15 are communicated with the first generator 1 and are adjusted into the first absorber 4 and have weak solution pipeline to be communicated with the 3rd absorber 20 through the first solution pump 9 and the 4th solution heat exchanger 21, the 3rd absorber 20 has weak solution pipeline again through the 3rd solution pump 18, the second solution heat exchanger 16 and the first solution heat exchanger 15 are communicated with the first generator 1, the second generator 2 is had concentrated solution pipeline to be communicated with the first absorber 4 through the second solution heat exchanger 16 to be adjusted into the second generator 2 has concentrated solution pipeline to be communicated with the 4th generator 19 through the second solution heat exchanger 16, the 4th generator 19 has concentrated solution pipeline to be communicated with the first absorber 4 through the 4th solution heat exchanger 21 again, the 4th generator 19 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, the 4th generator 19 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 that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively; The weak solution of the first absorber 4 enters the 3rd absorber 20, absorbs from the refrigerant vapour of the 4th generator 19 heat release in heated medium through the first solution pump 9 and the 4th solution heat exchanger 21, and the weak solution of the 3rd absorber 20 enters the first generator 1 through the 3rd solution pump 18, the second solution heat exchanger 16 and the first solution heat exchanger 15; The concentrated solution of the first generator 1 enters the second generator 2 through the first solution heat exchanger 15, the concentrated solution of the second generator 2 enters the 4th generator 19 through the second solution heat exchanger 16, the solution that drives heat medium flow to enter in it through the 4th generator 19, heating discharges and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 4th generator 19 enters the first absorber 4 through the 4th solution heat exchanger 21, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Figure 10
1. in structure, in the composite absorption heat pump shown in Fig. 5, increase by the 4th generator, the 3rd absorber, the 4th solution pump and the 4th solution heat exchanger, there is weak solution pipeline to be communicated with the second generator 2 and to be adjusted into the first absorber 4 and to have weak solution pipeline to be communicated with the 3rd absorber 20 through the first solution pump 9 and the 4th solution heat exchanger 21 through the first solution pump 9 and the second solution heat exchanger 16 the first absorber 4, the 3rd absorber 20 has weak solution pipeline to be communicated with the second generator 2 through the 4th solution pump 30 and the second solution heat exchanger 16 again, there is concentrated solution pipeline to be communicated with the first absorber 4 and to be adjusted into the first generator 1 and to have concentrated solution pipeline to be communicated with the 4th generator 19 through the first solution heat exchanger 15 and the second solution heat exchanger 16 through the first solution heat exchanger 15 and the second solution heat exchanger 16 in the first generator 1, the 4th generator 19 has concentrated solution pipeline to be communicated with the first absorber 4 through the 4th solution heat exchanger 21 again, the 4th generator 19 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, the 4th generator 19 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 that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively; The weak solution of the first absorber 4 enters the 3rd absorber 20, absorbs from the refrigerant vapour of the 4th generator 19 heat release in heated medium through the first solution pump 9 and the 4th solution heat exchanger 21, and the weak solution of the 3rd absorber 20 enters the second generator 2 through the 4th solution pump 30 and the second solution heat exchanger 16; The concentrated solution of the second generator 2 enters the first generator 1 through the 3rd solution pump 18 and the first solution heat exchanger 15, the concentrated solution of the first generator 1 enters the 4th generator 19 through the first solution heat exchanger 15 and the second solution heat exchanger 16, the solution that drives heat medium flow to enter in it through the 4th generator 19, heating discharges and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 4th generator 19 enters the first absorber 4 through the 4th solution heat exchanger 21, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Figure 11
In the composite absorption heat pump shown in Fig. 9, increase by the 5th choke valve, cancel the 4th generator 19 and the outside driving thermal medium pipeline being communicated with, the first generator 1 is set up refrigerant vapour passage and is communicated with the 4th generator 19 afterwards with the 4th generator 19 and has cryogen liquid pipeline to be communicated with the first condenser 6 through the 5th choke valve 22 again; The refrigerant vapour that the first generator 1 produces provides refrigerant vapour to make to drive thermal medium to the second generator 2, the 3rd generator 3 and the 4th generator 19 respectively, forms taking economic benefits and social benefits as basis and has the composite absorption heat pump of backheat heat supply end.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Figure 12
In the composite absorption heat pump shown in Fig. 2, increase first flow control valve and second adjustable valve, have respectively heated medium pipeline and outside connection to be defined as outside and to have heated medium pipeline to be communicated with the first condenser 6 afterwards with the first condenser 6 to have heated medium pipeline to be communicated with the second condenser 7 through second adjustable valve 29 with outside connected sum through first flow control valve 28 respectively again the first condenser 6 and the second condenser 7, the second condenser 7 has heated medium pipeline to be communicated with outside again; Close first flow control valve 28 and while opening second adjustable valve 29, heated medium full flow flow through successively the first condenser 6 and the second condenser 7; Open first flow control valve 28 and while closing second adjustable valve 29, heated medium full flow first condenser 6 of only flowing through; When first flow control valve 28 and second adjustable valve 29 are all opened, heated medium full flow flow through the first condenser 6 and partial discharge is flowed through the second condenser 7, formation can carry out adjust flux distribution, taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Figure 13
1. in structure, in the composite absorption heat pump shown in Fig. 1, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, cryogen liquid pump and newly-increased solution choke valve, cancel the first absorber 4 and the outside heated medium pipeline being communicated with, the 3rd absorber 20 has weak solution pipeline to be communicated with a point steam chest 23 through newly-increased solution choke valve E and the first absorber 4, divide steam chest 23 to also have concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18, divide steam chest 23 to also have refrigerant vapour passage to be communicated with the 3rd condenser 24, the 3rd condenser 24 also has cryogen liquid pipeline to be communicated with the second evaporimeter 25 through cryogen liquid pump 26, the second evaporimeter 25 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, the 3rd absorber 20 also has heated medium pipeline to be communicated with outside, the 3rd condenser 24 also has cooling medium pipeline to be communicated with outside, the second evaporimeter 25 medium pipeline that also has surplus heat is communicated with outside.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively; Enter the first absorber 4, absorb from the refrigerant vapour of the first evaporimeter 8 heat release in the solution of first absorber 4 of flowing through from the concentrated solution of the first generator 1 and the second generator 2; The weak solution of the 3rd absorber 20 is through increasing solution choke valve E reducing pressure by regulating flow newly, flowing through after the first absorber 4 heat absorbing parts are vaporized and enter point steam chest 23 again, the refrigerant vapour of point steam chest 23 enters the 3rd condenser 24, and the concentrated solution of point steam chest 23 enters the 3rd absorber 20, absorbs from the refrigerant vapour of the second evaporimeter 25 heat release in heated medium through the 3rd solution pump 18; The refrigerant vapour heat release of the 3rd condenser 24 becomes cryogen liquid in cooling medium, the cryogen liquid of the 3rd condenser 24 pressurizes through cryogen liquid pump 26 and enters the second evaporimeter 25, absorption waste heat becomes refrigerant vapour and provides to the 3rd absorber 20, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Figure 14
1. in structure, in the composite absorption heat pump shown in Fig. 2, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel the first absorber 4 and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber 4 through the first solution heat exchanger 15 to be adjusted into the first generator 1 to have concentrated solution pipeline to be communicated with a point steam chest 23 through the first solution heat exchanger 15 and the first absorber 4 in the first generator 1, there is concentrated solution pipeline to be communicated with the first absorber 4 through the second solution heat exchanger 16 to be adjusted into the second generator 2 to have concentrated solution pipeline to be communicated with a point steam chest 23 through the second solution heat exchanger 16 and the first absorber 4 in the second generator 2, divide steam chest 23 to also have concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18, the 3rd absorber 20 also has weak solution pipeline to be communicated with the first absorber 4 through newly-increased solution choke valve E, divide steam chest 23 to also have refrigerant vapour passage to be communicated with the 3rd condenser 24, the 3rd condenser 24 also has cryogen liquid pipeline to be communicated with the first evaporimeter 8 through cryogen liquid pump 26, the first evaporimeter 8 also has cryogen liquid pipeline to be communicated with the second evaporimeter 25 through the 5th choke valve 22, the first evaporimeter 8 is had refrigerant vapour passage to be communicated with the first absorber 4 to be adjusted into the first evaporimeter 8 has refrigerant vapour passage to be communicated with the 3rd absorber 20, the second evaporimeter 25 also has refrigerant vapour passage to be communicated with the first absorber 4, the 3rd absorber 20 also has heated medium pipeline to be communicated with outside, the 3rd condenser 24 also has cooling medium pipeline to be communicated with outside, the second evaporimeter 25 medium pipeline that also has surplus heat is communicated with outside.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively; The concentrated solution of the first generator 1 enters point steam chest 23 with the first absorber 4 heat absorbing parts vaporizations that converge, flow through of the concentrated solution of the second generator 2 after the second solution heat exchanger 16 after the first solution heat exchanger 15, the refrigerant vapour of point steam chest 23 enters the 3rd condenser 24, and the concentrated solution of point steam chest 23 enters the 3rd absorber 20, absorbs from the refrigerant vapour of the first evaporimeter 8 heat release in heated medium through the 3rd solution pump 18; The weak solution of the 3rd absorber 20 enters the first absorber 4, absorbs from the refrigerant vapour of the second evaporimeter 25 heat release in the solution of first absorber 4 of flowing through through newly-increased solution choke valve E reducing pressure by regulating flow; The refrigerant vapour heat release of the 3rd condenser 24 becomes cryogen liquid in cooling medium, the cryogen liquid of the 3rd condenser 24 enters the first evaporimeter 8 through cryogen liquid pump 26, the cryogen liquid of evaporimeter 8 is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to the 3rd absorber 20, the second tunnel the 5th choke valve enters the second evaporimeter 25, absorption waste heat becomes refrigerant vapour and provides to the first absorber 4, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Figure 15
1. in structure, in the composite absorption heat pump shown in Fig. 1, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser and cryogen liquid pump, cancel the first absorber 4 and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber 4 through the first solution heat exchanger 15 to be adjusted into the first generator 1 to have concentrated solution pipeline to be communicated with a point steam chest 23 through the first solution heat exchanger 15 and the first absorber 4 in the first generator 1, there is concentrated solution pipeline to be communicated with the first absorber 4 through the second solution heat exchanger 16 to be adjusted into the second generator 2 to have concentrated solution pipeline to be communicated with a point steam chest 23 through the second solution heat exchanger 16 and the first absorber 4 in the second generator 2, divide steam chest 23 to also have concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18, the 3rd absorber 20 also has weak solution pipeline to be communicated with the first absorber 4, divide steam chest 23 to also have refrigerant vapour passage to be communicated with the 3rd condenser 24, the 3rd condenser 24 also has cryogen liquid pipeline to be communicated with evaporimeter 8 through cryogen liquid pump 26, evaporimeter 8 is set up refrigerant vapour passage and is communicated with the 3rd absorber 20, the 3rd absorber 20 also has heated medium pipeline to be communicated with outside, the 3rd condenser 24 also has cooling medium pipeline to be communicated with outside.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively; The concentrated solution of the first generator 1 enters point steam chest 23 with the first absorber 4 heat absorbing parts vaporizations that converge, flow through of the concentrated solution of the second generator 2 after the second solution heat exchanger 16 after the first solution heat exchanger 15, divide the refrigerant vapour of steam chest 23 to enter the 3rd condenser 24, the concentrated solution of point steam chest 23 enters the 3rd absorber 20, the refrigerant vapour that absorbs flash-pot 8 heat release in heated medium through the 3rd solution pump 18; The weak solution of the 3rd absorber 20 enters the first absorber 4, the refrigerant vapour that absorbs flash-pot 8 heat release in the solution of first absorber 4 of flowing through; The refrigerant vapour heat release of the 3rd condenser 24 becomes cryogen liquid in cooling medium, the cryogen liquid of the 3rd condenser 24 enters evaporimeter 8 through cryogen liquid pump 26, the cryogen liquid of evaporimeter 8 is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to the 3rd absorber 20, the second tunnel absorbs waste heat and becomes refrigerant vapour and provide to the first absorber 4, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Figure 16
1. in structure, in the composite absorption heat pump shown in Fig. 3, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, cryogen liquid pump and newly-increased solution choke valve, the 3rd absorber 20 has weak solution pipeline to be communicated with a point steam chest 23 through newly-increased solution choke valve E and the first absorber 4, divide steam chest 23 to also have concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18, divide steam chest 23 to also have refrigerant vapour passage to be communicated with the 3rd condenser 24, the 3rd condenser 24 also has cryogen liquid pipeline to be communicated with the second evaporimeter 25 through cryogen liquid pump 26, the second evaporimeter 25 also has refrigerant vapour passage to be communicated with the 3rd absorber 20, the 3rd absorber 20 also has heated medium pipeline to be communicated with outside, the 3rd condenser 24 also has cooling medium pipeline to be communicated with outside, the second evaporimeter 25 medium pipeline that also has surplus heat is communicated with outside.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively; The concentrated solution of the second generator 2 through the second solution heat exchanger 16 enter the first absorber 4, absorb from the refrigerant vapour of the first evaporimeter 8 and respectively heat release in the solution of heated medium and first absorber 4 of flowing through; The weak solution of the 3rd absorber 20 is through increasing solution choke valve E reducing pressure by regulating flow newly, flowing through after the first absorber 4 heat absorbing parts are vaporized and enter point steam chest 23 again, the refrigerant vapour of point steam chest 23 enters the 3rd condenser 24, and the concentrated solution of point steam chest 23 enters the 3rd absorber 20, absorbs from the refrigerant vapour of the second evaporimeter 25 heat release in heated medium through the 3rd solution pump 18; The refrigerant vapour heat release of the 3rd condenser 24 becomes cryogen liquid in cooling medium, the cryogen liquid of the 3rd condenser 24 pressurizes through cryogen liquid pump 26 and enters the second evaporimeter 25, absorption waste heat becomes refrigerant vapour and provides to the 3rd absorber 20, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Figure 17
1. in structure, in the composite absorption heat pump shown in Fig. 3, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser and cryogen liquid pump, cancel the first absorber 4 and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber 4 through the second solution heat exchanger 16 to be adjusted into the second generator 2 to have concentrated solution pipeline to be communicated with a point steam chest 23 through the second solution heat exchanger 16 and the first absorber 4 in the second generator 2, divide steam chest 23 to also have concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18, the 3rd absorber 20 also has weak solution pipeline to be communicated with the first absorber 4, divide steam chest 23 to also have refrigerant vapour passage to be communicated with the 3rd condenser 24, the 3rd condenser 24 also has cryogen liquid pipeline to be communicated with evaporimeter 8 through cryogen liquid pump 26, evaporimeter 8 is set up refrigerant vapour passage and is communicated with the 3rd absorber 20, the 3rd absorber 20 also has heated medium pipeline to be communicated with outside, the 3rd condenser 24 also has cooling medium pipeline to be communicated with outside.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively; The first absorber 4, the heat absorbing part vaporization of flowing through again after the second solution heat exchanger 16 of the concentrated solution of the second generator 2 enters point steam chest 23, divide the refrigerant vapour of steam chest 23 to enter the 3rd condenser 24, the concentrated solution of point steam chest 23 enters the 3rd absorber 20, the refrigerant vapour that absorbs flash-pot 8 heat release in heated medium through the 3rd solution pump 18; The weak solution of the 3rd absorber 20 enters the first absorber 4, the refrigerant vapour that absorbs flash-pot 8 heat release in the solution of first absorber 4 of flowing through; The refrigerant vapour heat release of the 3rd condenser 24 becomes cryogen liquid in cooling medium, the cryogen liquid of the 3rd condenser 24 enters evaporimeter 8 through cryogen liquid pump 26, the cryogen liquid of evaporimeter 8 is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to the 3rd absorber 20, the second tunnel absorbs waste heat and becomes refrigerant vapour and provide to the first absorber 4, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Figure 18
1. in structure, in the composite absorption heat pump shown in Fig. 5, increase by the 4th solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, cryogen liquid pump and newly-increased solution choke valve, cancel the first absorber 4 and the outside heated medium pipeline being communicated with, the 3rd absorber 20 has weak solution pipeline to be communicated with a point steam chest 23 through newly-increased solution choke valve E and the first absorber 4, divide steam chest 23 to also have concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 4th solution pump 30, divide steam chest 23 to also have refrigerant vapour passage to be communicated with the 3rd condenser 24, the 3rd condenser 24 also has cryogen liquid pipeline to be communicated with evaporimeter 8 through cryogen liquid pump 26, evaporimeter 25 is set up refrigerant vapour passage and is communicated with the 3rd absorber 20, the 3rd absorber 20 also has heated medium pipeline to be communicated with outside, the 3rd condenser 24 also has cooling medium pipeline to be communicated with outside.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 makes to drive thermal medium, the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively, and the concentrated solution of the first generator 1 enters the first absorber 4, the refrigerant vapour that absorbs flash-pot 8 heat release in the solution of first absorber 4 of flowing through through the first solution heat exchanger 15 and the second solution heat exchanger 16; The weak solution of the 3rd absorber 20 is through increasing solution choke valve E reducing pressure by regulating flow newly, flowing through after the first absorber 4 heat absorbing parts are vaporized and enter point steam chest 23 again, divide steam chest 23 refrigerant vapours to enter the 3rd condenser 24, the concentrated solution of point steam chest 23 enters the 3rd absorber 20, the refrigerant vapour that absorbs flash-pot 8 heat release in heated medium through the 4th solution pump 30; The refrigerant vapour heat release of the 3rd condenser 24 becomes cryogen liquid in cooling medium, the cryogen liquid of the 3rd condenser 24 enters evaporimeter 8 through cryogen liquid pump 26, the cryogen liquid of evaporimeter 8 is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to the 3rd absorber 20, the second tunnel absorbs waste heat and becomes refrigerant vapour and provide to the first absorber 4, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking economic benefits and social benefits as basic composite absorption heat pump shown in Figure 19
1. in structure, in the composite absorption heat pump shown in Fig. 5, increase by the 4th solution pump, the 3rd absorber, divide steam chest, the 3rd condenser and cryogen liquid pump, cancel the first absorber 4 and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber 4 and to be adjusted into the first generator 1 and to have concentrated solution pipeline through the first solution heat exchanger 15 through the first solution heat exchanger 15 and the second solution heat exchanger 16 in the first generator 1, the second solution heat exchanger 16 and the first absorber 4 are communicated with a point steam chest 23, divide steam chest 23 to also have concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 4th solution pump 30, the 3rd absorber 20 also has weak solution pipeline to be communicated with the first absorber 4, divide steam chest 23 to also have refrigerant vapour passage to be communicated with the 3rd condenser 24, the 3rd condenser 24 also has cryogen liquid pipeline to be communicated with evaporimeter 8 through cryogen liquid pump 26, evaporimeter 8 is set up refrigerant vapour passage and is communicated with the 3rd absorber 20, the 3rd absorber 20 also has heated medium pipeline to be communicated with outside, the 3rd condenser 24 also has cooling medium pipeline to be communicated with outside.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 is done to drive thermal medium, and the refrigerant vapour that the second generator 2 produces provides to the first condenser 6 and the second absorber 5 respectively; The first absorber 4, the heat absorbing part vaporization of flowing through again after the first solution heat exchanger 15 and the second solution heat exchanger 16 of the concentrated solution of the first generator 1 enters point steam chest 23, divide the refrigerant vapour of steam chest 23 to enter the 3rd condenser 24, divide the concentrated solution of steam chest 23 to enter the 3rd absorber 20, the refrigerant vapour that absorbs flash-pot 8 heat release in heated medium through the 4th solution pump 30, the weak solution of the 3rd absorber 20 enters the first absorber 4, the refrigerant vapour that absorbs flash-pot 8 heat release in the solution of first absorber 4 of flowing through; The refrigerant vapour heat release of the 3rd condenser 24 becomes cryogen liquid in cooling medium, the cryogen liquid of the 3rd condenser 24 enters evaporimeter 8 through cryogen liquid pump 26, the cryogen liquid of evaporimeter 8 is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to the 3rd absorber 20, the second tunnel absorbs waste heat and becomes refrigerant vapour and provide to the first absorber 4, forms taking economic benefits and social benefits as basic composite absorption heat pump.
Being achieved in that taking triple effect as basic composite absorption heat pump shown in Figure 20
1. in structure, in the composite absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first 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 first absorber 4 through newly-increased solution heat exchanger C, after having refrigerant vapour passage to be communicated with the first condenser 6 to be adjusted into the second generator 2 to have refrigerant vapour passage to be communicated with newly-increased generator A in the second generator 2, newly-increased generator A has cryogen liquid pipeline to be communicated with the first condenser 6 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the first condenser 6, having refrigerant vapour passage to be communicated with the second absorber 5 to be adjusted into newly-increased generator A to set up refrigerant vapour passage in the second generator 2 is communicated with the second absorber 5, after having refrigerant vapour passage to be communicated with the 3rd generator 3 in the first generator 1 the 3rd generator 3 have again cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13 to be adjusted into the second generator 2 have refrigerant vapour passage to be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers the second generator 2 and makes to drive thermal medium, and the refrigerant vapour that the second generator 2 produces offers respectively newly-increased generator A and the 3rd generator 3 makes to drive thermal medium; A part of weak solution of the first absorber 4 enters newly-increased generator A through the first solution pump 9 and newly-increased solution heat exchanger C, refrigerant vapour is flowed through and is increased generator A newly, heating enters solution release in it and provides refrigerant vapour to the first condenser 6 and the second absorber 5 respectively, the concentrated solution of newly-increased generator A enters the first absorber 4 through newly-increased solution heat exchanger C, the refrigerant vapour heat release of newly-increased generator A of flowing through becomes cryogen liquid, enters the first condenser 6 through newly-increased choke valve B throttling again, forms taking triple effect as basic composite absorption heat pump.
Being achieved in that taking triple effect as basic composite absorption heat pump shown in Figure 21
1. in structure, in the composite absorption heat pump shown in Fig. 2, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first 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 first absorber 4 through newly-increased solution heat exchanger C, after having refrigerant vapour passage to be communicated with the first condenser 6 to be adjusted into the second generator 2 to have refrigerant vapour passage to be communicated with newly-increased generator A in the second generator 2, newly-increased generator A has cryogen liquid pipeline to be communicated with the first condenser 6 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the first condenser 6, having refrigerant vapour passage to be communicated with the second absorber 5 to be adjusted into newly-increased generator A to set up refrigerant vapour passage in the second generator 2 is communicated with the second absorber 5, form taking triple effect as basic composite absorption heat pump.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that the second generator 2 produces offers newly-increased generator A and makes to drive thermal medium; A part of weak solution of the first absorber 4 enters newly-increased generator A through the first solution pump 9 and newly-increased solution heat exchanger C, refrigerant vapour is flowed through and is increased generator A newly, heating enters solution release in it and provides refrigerant vapour to the first condenser 6 and the second absorber 5 respectively, the concentrated solution of newly-increased generator A enters the first absorber 4 through newly-increased solution heat exchanger C, the refrigerant vapour heat release of newly-increased generator A of flowing through becomes cryogen liquid, enters the first condenser 6 through newly-increased choke valve B throttling again, forms taking triple effect as basic composite absorption heat pump.
Being achieved in that taking triple effect as basic composite absorption heat pump shown in Figure 22
1. in structure, in the composite absorption heat pump shown in Fig. 3, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first absorber 4 is had weak solution pipeline to be communicated with the second solution heat exchanger 16 through the first solution pump 9 to be adjusted into the first absorber 4 has weak solution pipeline to be communicated with the second solution heat exchanger 16 through the first solution pump 9 and newly-increased solution heat exchanger C, the second generator 2 is had concentrated solution pipeline to be communicated with the first absorber 4 through the second solution heat exchanger 16 to be adjusted into the second generator 2 has concentrated solution pipeline to be communicated with newly-increased generator A through the second solution heat exchanger 16, newly-increased generator A has concentrated solution pipeline to be communicated with the first absorber 4 through newly-increased solution heat exchanger C again, after having refrigerant vapour passage to be communicated with the first condenser 6 to be adjusted into the second generator 2 to have refrigerant vapour passage to be communicated with newly-increased generator A in the second generator 2, newly-increased generator A has cryogen liquid pipeline to be communicated with the first condenser 6 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the first condenser 6, having refrigerant vapour passage to be communicated with the second absorber 5 to be adjusted into newly-increased generator A to set up refrigerant vapour passage in the second generator 2 is communicated with the second absorber 5, after having refrigerant vapour passage to be communicated with the 3rd generator 3 in the first generator 1 the 3rd generator 3 have again cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13 to be adjusted into the second generator 2 have refrigerant vapour passage to be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers the second generator 2 and makes to drive thermal medium, and the refrigerant vapour that the second generator 2 produces offers respectively newly-increased generator A and the 3rd generator 3 makes to drive thermal medium, the weak solution of the first absorber 4 is through newly-increased solution heat exchanger C, the second solution heat exchanger 16 and the first solution heat exchanger 15 enter the first generator 1, the concentrated solution of the first generator 1 enters the second generator 2 through the first solution heat exchanger 15, the concentrated solution of the second generator 2 enters newly-increased generator A through the second solution heat exchanger 16, 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 first condenser 6 and the second absorber 5 respectively, the concentrated solution of newly-increased generator A enters the first absorber 4 through newly-increased solution heat exchanger C, the refrigerant vapour heat release of newly-increased generator A of flowing through becomes cryogen liquid, enter the first condenser 6 through newly-increased choke valve B throttling again, form taking triple effect as basic composite absorption heat pump.
Being achieved in that taking triple effect as basic composite absorption heat pump shown in Figure 23
1. in structure, in the composite absorption heat pump shown in Fig. 4, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first generator 1 is had concentrated solution pipeline to be communicated with the second generator 2 through the first solution heat exchanger 15 to be adjusted into the first generator 1 has concentrated solution pipeline to be communicated with the second generator 2 through the first solution heat exchanger 15 and newly-increased solution heat exchanger C, there is concentrated solution pipeline to be communicated with the first absorber 4 through the second solution heat exchanger 16 to be adjusted into the second generator 2 to have concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased solution heat exchanger C in the second generator 2, newly-increased generator A also has concentrated solution pipeline to be communicated with the first absorber 4 through the second solution heat exchanger 16, after having refrigerant vapour passage to be communicated with the first condenser 6 to be adjusted into the second generator 2 to have refrigerant vapour passage to be communicated with newly-increased generator A in the second generator 2, newly-increased generator A has cryogen liquid pipeline to be communicated with the first condenser 6 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the first condenser 6, having refrigerant vapour passage to be communicated with the second absorber 5 to be adjusted into newly-increased generator A to set up refrigerant vapour passage in the second generator 2 is communicated with the second absorber 5.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers respectively the second generator 2 and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that the second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, the weak solution of the first absorber 4 is through the first solution pump 9, the second solution heat exchanger 16 and the 3rd solution heat exchanger 17 enter the 3rd generator 3, the concentrated solution of the 3rd generator 3 enters the second absorber 5 through the 3rd solution heat exchanger 17, the weak solution of the second absorber 5 enters the first generator 1 through the second solution pump 10 and the first solution heat exchanger 15, the concentrated solution of the first generator 1 enters the second generator 2 through the first solution heat exchanger 15 and newly-increased solution heat exchanger C, the concentrated solution of the second generator 2 enters newly-increased generator A through 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 first condenser 6 and the second absorber 5 respectively, the concentrated solution of newly-increased generator A enters the first absorber 4 through the second solution heat exchanger 16, the refrigerant vapour heat release of newly-increased generator A of flowing through becomes cryogen liquid, enter the first condenser 6 through newly-increased choke valve B throttling again, form taking triple effect as basic composite absorption heat pump.
Being achieved in that taking triple effect as basic composite absorption heat pump shown in Figure 24
In the composite absorption heat pump shown in Figure 23, after having refrigerant vapour passage to be communicated with the 3rd generator 3 in the first generator 1 the 3rd generator 3 have again cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13 to be adjusted into the second generator 2 have refrigerant vapour passage to be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13, formation is taking triple effect as basic composite absorption heat pump.
Being achieved in that taking triple effect as basic composite absorption heat pump shown in Figure 25
1. in structure, in the composite absorption heat pump shown in Fig. 5, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the second generator 2 and to be adjusted into the first absorber 4 and to have weak solution pipeline to be communicated with newly-increased generator A through the first solution pump 9 and the second solution heat exchanger 16 through the first solution pump 9 and the second solution heat exchanger 16 the first absorber 4, newly-increased generator A also has concentrated solution pipeline to be communicated with the second generator 2 through newly-increased solution pump D and newly-increased solution heat exchanger C, there is concentrated solution pipeline to be communicated with the first absorber 4 and to be adjusted into the first generator 1 and to have concentrated solution pipeline through the first solution heat exchanger 15 through the first solution heat exchanger 15 and the second solution heat exchanger 16 in the first generator 1, newly-increased solution heat exchanger C and the second solution heat exchanger 16 are communicated with the first absorber 4, after having refrigerant vapour passage to be communicated with the first condenser 6 to be adjusted into the second generator 2 to have refrigerant vapour passage to be communicated with newly-increased generator A in the second generator 2, newly-increased generator A has cryogen liquid pipeline to be communicated with the first condenser 6 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the first condenser 6, having refrigerant vapour passage to be communicated with the second absorber 5 to be adjusted into newly-increased generator A to set up refrigerant vapour passage in the second generator 2 is communicated with the second absorber 5, after having refrigerant vapour passage to be communicated with the 3rd generator 3 in the first generator 1 the 3rd generator 3 have again cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13 to be adjusted into the second generator 2 have refrigerant vapour passage to be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers the second generator 2 and makes to drive thermal medium, and the refrigerant vapour that the second generator 2 produces offers respectively newly-increased generator A and the 3rd generator 3 makes to drive thermal medium, the weak solution of the first absorber 4 enters newly-increased generator A through the first solution pump 9 and the second solution heat exchanger 16, 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 first condenser 6 and the second absorber 5 respectively, the concentrated solution of newly-increased generator A enters the second generator 2 through newly-increased solution pump D and newly-increased solution heat exchanger C, the concentrated solution of the second generator 2 enters the first generator 1 through the 3rd solution pump 18 and the first solution heat exchanger 15, the concentrated solution of the first generator 1 is through the first solution heat exchanger 15, newly-increased solution heat exchanger C and the second solution heat exchanger 16 enter the first absorber 4, form taking triple effect as basic composite absorption heat pump.
Being achieved in that taking triple effect as basic composite absorption heat pump shown in Figure 26
1. in structure, in the composite absorption heat pump shown in Fig. 7, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the second generator 2 and to be adjusted into the second absorber 5 and to have weak solution pipeline to be communicated with newly-increased generator A through the second solution pump 10 and the second solution heat exchanger 16 through the second solution pump 10 and the second solution heat exchanger 16 the second absorber 5, newly-increased generator A also has concentrated solution pipeline to be communicated with the second generator 2 through newly-increased solution pump D and newly-increased solution heat exchanger C, there is concentrated solution pipeline to be communicated with the first absorber 4 and to be adjusted into the first generator 1 and to have concentrated solution pipeline through the first solution heat exchanger 15 through the first solution heat exchanger 15 and the second solution heat exchanger 16 in the first generator 1, newly-increased solution heat exchanger C and the second solution heat exchanger 16 are communicated with the first absorber 4, after having refrigerant vapour passage to be communicated with the first condenser 6 to be adjusted into the second generator 2 to have refrigerant vapour passage to be communicated with newly-increased generator A in the second generator 2, newly-increased generator A has cryogen liquid pipeline to be communicated with the first condenser 6 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the first condenser 6, having refrigerant vapour passage to be communicated with the second absorber 5 to be adjusted into newly-increased generator A to set up refrigerant vapour passage in the second generator 2 is communicated with the second absorber 5, after having refrigerant vapour passage to be communicated with the 3rd generator 3 in the first generator 1 the 3rd generator 3 have again cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13 to be adjusted into the second generator 2 have refrigerant vapour passage to be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline to be communicated with the second condenser 7 through the 3rd choke valve 13.
2. in flow process, the refrigerant vapour that the first generator 1 produces offers the second generator 2 and makes to drive thermal medium, and the refrigerant vapour that the second generator 2 produces offers respectively newly-increased generator A and the 3rd generator 3 makes to drive thermal medium, the weak solution of the first absorber 4 enters the 3rd generator 3 through the first solution pump 9 and the 3rd solution heat exchanger 17, the concentrated solution of the 3rd generator 3 enters the second absorber 5 through the 3rd solution heat exchanger 17, the weak solution of the second absorber 5 enters newly-increased generator A through the second solution pump 10 and the second solution heat exchanger 16, 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 first condenser 6 and the second absorber 5 respectively, the concentrated solution of newly-increased generator A enters the second generator 2 through newly-increased solution pump D and newly-increased solution heat exchanger C, the concentrated solution of the second generator 2 enters the first generator 1 through the 3rd solution pump 18 and the first solution heat exchanger 15, the concentrated solution of the first generator 1 is through the first solution heat exchanger 15, newly-increased solution heat exchanger C and the second solution heat exchanger 16 enter the first absorber 4, form taking triple effect as basic composite absorption heat pump.
The effect that the technology of the present invention can realize---proposed by the invention have following effect and advantage taking economic benefits and social benefits or triple effect as basic composite absorption heat pump:
(1) taking economic benefits and social benefits as basic composite absorption heat pump, when low-temperature heat supply, can realize economic benefits and social benefits or approach the thermodynamic effect of economic benefits and social benefits, when high-temperature heat supply, between thermodynamic effect and economic benefits and social benefits, realize and being connected continuously, can obtain rational performance index.
(2) taking triple effect as basic composite absorption heat pump, when low-temperature heat supply, can realize triple effect or approach the thermodynamic effect of triple effect, when high-temperature heat supply, between thermodynamic effect and triple effect, realize and being connected continuously, can obtain rational performance index.
(3), taking economic benefits and social benefits as basic composite absorption heat pump, obtained the absorption heat pump of thermodynamic parameter on double-effect process; Taking triple effect as basic composite absorption heat pump, obtain the absorption heat pump of thermodynamic parameter on triple effect flow process, enrich the type of absorption type heat pump assembly.
(4) be applied to load, variable parameter operation occasion that heat supply temperature excursion is larger, can realize between heating parameter, heat supply interval and performance index rationally corresponding, and can give full play to economic benefits and social benefits or the high advantage of triple effect performance of MRC process index, thereby improve largely energy-saving benefit.

Claims (41)

1. taking economic benefits and social benefits as basic composite absorption heat pump, mainly formed by the first generator, the second generator, the 3rd generator, the first absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, first throttle valve, the second choke valve, the 3rd choke valve, the 4th choke valve, the first solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger; the first absorber (4) has weak solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (16) with the first generator (1) connected sum through the first solution heat exchanger (15) more respectively after the first solution pump (9) again, the first generator (1) also has concentrated solution pipeline to be communicated with the first absorber (4) through the first solution heat exchanger (15), the second generator (2) also has concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16), the second absorber (5) has weak solution pipeline to be communicated with the 3rd generator (3) through the second solution pump (10) and the 3rd solution heat exchanger (17), the 3rd generator (3) also has concentrated solution pipeline to be communicated with the second absorber (5) through the 3rd solution heat exchanger (17), after the first generator (1) also has refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline to be communicated with the first condenser (6) through first throttle valve (11) again, after the first generator (1) also has refrigerant vapour passage to be communicated with the 3rd generator (3), the 3rd generator (3) has cryogen liquid pipeline to be communicated with the second condenser (7) through the 3rd choke valve (13) again, the second generator (2) also has refrigerant vapour passage to be communicated with the first condenser (6), the second generator (2) also has refrigerant vapour passage to be communicated with the second absorber (5), the 3rd generator (3) also has refrigerant vapour passage to be communicated with the second condenser (7), the second condenser (7) also has cryogen liquid pipeline to be communicated with the first condenser (6) or evaporimeter (8) through the 4th choke valve (14), the first condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (8) through the second choke valve (12), evaporimeter (8) also has refrigerant vapour passage to be communicated with the first absorber (4), evaporimeter (8) medium pipeline that also has surplus heat is communicated with outside, the first generator (1) drives thermal medium pipeline to be communicated with outside in addition, the first absorber (4), the first condenser (6), the second absorber (5) and the second condenser (7) also have respectively heated medium pipeline to be communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump.
2. taking economic benefits and social benefits as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 1, there is weak solution pipeline to be communicated with the 3rd generator (3) and to be adjusted into the second absorber (5) and to have weak solution pipeline to be communicated with the first generator (1) through the second solution pump (10) and the first solution heat exchanger (15) through the second solution pump (10) and the 3rd solution heat exchanger (17) the second absorber (5), there is weak solution pipeline to be communicated with the first generator (1) and to be adjusted into the first absorber (4) and to have weak solution pipeline to be communicated with the 3rd generator (3) through the first solution pump (9) and the 3rd solution heat exchanger (17) through the first solution pump (9) and the first solution heat exchanger (15) the first absorber (4), form taking economic benefits and social benefits as basic composite absorption heat pump.
3. taking economic benefits and social benefits as basic composite absorption heat pump, mainly formed by the first generator, the second generator, the 3rd generator, the first absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, first throttle valve, the second choke valve, the 3rd choke valve, the 4th choke valve, the first solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger; the first absorber (4) has weak solution pipeline through the first solution pump (9), the second solution heat exchanger (16) and the first solution heat exchanger (15) are communicated with the first generator (1), the first generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through the first solution heat exchanger (15), the second generator (2) also has concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16), the second absorber (5) has weak solution pipeline to be communicated with the 3rd generator (3) through the second solution pump (10) and the 3rd solution heat exchanger (17), the 3rd generator (3) also has concentrated solution pipeline to be communicated with the second absorber (5) through the 3rd solution heat exchanger (17), after the first generator (1) also has refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline to be communicated with the first condenser (6) through first throttle valve (11) again, after the first generator (1) also has refrigerant vapour passage to be communicated with the 3rd generator (3), the 3rd generator (3) has cryogen liquid pipeline to be communicated with the second condenser (7) through the 3rd choke valve (13) again, the second generator (2) also has refrigerant vapour passage to be communicated with the first condenser (6), the second generator (2) also has refrigerant vapour passage to be communicated with the second absorber (5), the 3rd generator (3) also has refrigerant vapour passage to be communicated with the second condenser (7), the second condenser (7) also has cryogen liquid pipeline to be communicated with the first condenser (6) or evaporimeter (8) through the 4th choke valve (14), the first condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (8) through the second choke valve (12), evaporimeter (8) also has refrigerant vapour passage to be communicated with the first absorber (4), evaporimeter (8) medium pipeline that also has surplus heat is communicated with outside, the first generator (1) drives thermal medium pipeline to be communicated with outside in addition, the first absorber (4), the first condenser (6), the second absorber (5) and the second condenser (7) also have respectively heated medium pipeline to be communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump.
4. taking economic benefits and social benefits as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 3, increase solution choke valve, the first absorber (4) is had to weak solution pipeline through the first solution pump (9), the second solution heat exchanger (16) and the first solution heat exchanger (15) are communicated with the first generator (1) and are adjusted into the first absorber (4) and have weak solution pipeline through the first solution pump (9), the second solution heat exchanger (16) is communicated with the first generator (1) through the first solution heat exchanger (15) with the second generator (2) connected sum through solution choke valve (27) respectively afterwards more again, form taking economic benefits and social benefits as basic composite absorption heat pump.
5. taking economic benefits and social benefits as basic composite absorption heat pump, in claim 3-4 in the composite absorption heat pump described in arbitrary claim, there is weak solution pipeline to be communicated with the 3rd generator (3) and to be adjusted into the second absorber (5) and to have weak solution pipeline to be communicated with the first generator (1) through the second solution pump (10) and the first solution heat exchanger (15) through the second solution pump (10) and the 3rd solution heat exchanger (17) the second absorber (5), the first absorber (4) is had to weak solution pipeline through the first solution pump (9), the second solution heat exchanger (16) and the first solution heat exchanger (15) are communicated with the first generator (1) and are adjusted into the first absorber (4) and have weak solution pipeline through the first solution pump (9), the second solution heat exchanger (16) and the 3rd solution heat exchanger (17) are communicated with the 3rd generator (3), form taking economic benefits and social benefits as basic composite absorption heat pump.
6. taking economic benefits and social benefits as basic composite absorption heat pump, mainly formed by the first generator, the second generator, the 3rd generator, the first absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, the 3rd solution pump, first throttle valve, the second choke valve, the 3rd choke valve, the 4th choke valve, the first solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger; the first absorber (4) has weak solution pipeline to be communicated with the second generator (2) through the first solution pump (9) and the second solution heat exchanger (16), the second generator (2) also has concentrated solution pipeline to be communicated with the first generator (1) through the 3rd solution pump (18) and the first solution heat exchanger (15), the first generator (1) also has concentrated solution pipeline to be communicated with the first absorber (4) through the first solution heat exchanger (15) and the second solution heat exchanger (16), the second absorber (5) has weak solution pipeline to be communicated with the 3rd generator (3) through the second solution pump (10) and the 3rd solution heat exchanger (17), the 3rd generator (3) also has concentrated solution pipeline to be communicated with the second absorber (5) through the 3rd solution heat exchanger (17), after the first generator (1) also has refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline to be communicated with the first condenser (6) through first throttle valve (11) again, after the first generator (1) also has refrigerant vapour passage to be communicated with the 3rd generator (3), the 3rd generator (3) has cryogen liquid pipeline to be communicated with the second condenser (7) through the 3rd choke valve (13) again, the second generator (2) also has refrigerant vapour passage to be communicated with the first condenser (6), the second generator (2) also has refrigerant vapour passage to be communicated with the second absorber (5), the 3rd generator (3) also has refrigerant vapour passage to be communicated with the second condenser (7), the second condenser (7) also has cryogen liquid pipeline to be communicated with the first condenser (6) or evaporimeter (8) through the 4th choke valve (14), the first condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (8) through the second choke valve (12), evaporimeter (8) also has refrigerant vapour passage to be communicated with the first absorber (4), evaporimeter (8) medium pipeline that also has surplus heat is communicated with outside, the first generator (1) drives thermal medium pipeline to be communicated with outside in addition, the first absorber (4), the first condenser (6), the second absorber (5) and the second condenser (7) also have respectively heated medium pipeline to be communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump.
7. taking economic benefits and social benefits as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 6, increase solution choke valve, there is weak solution pipeline to be communicated with the second generator (2) and to be adjusted into the first absorber (4) and to have weak solution pipeline to be directly communicated with the second generator (2) through solution choke valve (27) again with the first generator (1) connected sum respectively afterwards through the first solution pump (9) and the second solution heat exchanger (16) through the first solution pump (9) and the second solution heat exchanger (16) the first absorber (4), form taking economic benefits and social benefits as basic composite absorption heat pump.
8. taking economic benefits and social benefits as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 6, there is weak solution pipeline to be communicated with the 3rd generator (3) and to be adjusted into the second absorber (5) and to have weak solution pipeline to be communicated with the second generator (2) through the second solution pump (10) and the second solution heat exchanger (16) through the second solution pump (10) and the 3rd solution heat exchanger (17) the second absorber (5), there is weak solution pipeline to be communicated with the second generator (2) and to be adjusted into the first absorber (4) and to have weak solution pipeline to be communicated with the 3rd generator (3) through the first solution pump (9) and the 3rd solution heat exchanger (17) through the first solution pump (9) and the second solution heat exchanger (16) the first absorber (4), form taking economic benefits and social benefits as basic composite absorption heat pump.
9. taking triple effect as basic composite absorption heat pump, in claim 1-2 in the composite absorption heat pump described in arbitrary claim, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first 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 first absorber (4) through newly-increased solution heat exchanger (C), after having refrigerant vapour passage to be communicated with the first condenser (6) to be adjusted into the second generator (2) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the second generator (2), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (6) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (6), having refrigerant vapour passage to be communicated with the second absorber (5) to be adjusted into newly-increased generator (A) to set up refrigerant vapour passage in the second generator (2) is communicated with the second absorber (5), form taking triple effect as basic composite absorption heat pump.
10. taking triple effect as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 3, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first absorber (4) is had weak solution pipeline to be communicated with the second solution heat exchanger (16) through the first solution pump (9) to be adjusted into the first absorber (4) has weak solution pipeline to be communicated with the second solution heat exchanger (16) through the first solution pump (9) and newly-increased solution heat exchanger (C), the second generator (2) is had concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16) to be adjusted into the second generator (2) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (16), newly-increased generator (A) has concentrated solution pipeline to be communicated with the first absorber (4) through newly-increased solution heat exchanger (C) again, after having refrigerant vapour passage to be communicated with the first condenser (6) to be adjusted into the second generator (2) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the second generator (2), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (6) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (6), having refrigerant vapour passage to be communicated with the second absorber (5) to be adjusted into newly-increased generator (A) to set up refrigerant vapour passage in the second generator (2) is communicated with the second absorber (5), form taking triple effect as basic composite absorption heat pump.
11. taking triple effect as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 5, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first generator (1) is had concentrated solution pipeline to be communicated with the second generator (2) through the first solution heat exchanger (15) to be adjusted into the first generator (1) has concentrated solution pipeline to be communicated with the second generator (2) through the first solution heat exchanger (15) and newly-increased solution heat exchanger (C), there is concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16) to be adjusted into the second generator (2) to have concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C) in the second generator (2), newly-increased generator (A) also has concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16), after having refrigerant vapour passage to be communicated with the first condenser (6) to be adjusted into the second generator (2) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the second generator (2), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (6) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (6), having refrigerant vapour passage to be communicated with the second absorber (5) to be adjusted into newly-increased generator (A) to set up refrigerant vapour passage in the second generator (2) is communicated with the second absorber (5), form taking triple effect as basic composite absorption heat pump.
12. taking triple effect as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 6, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the second generator (2) and to be adjusted into the first absorber (4) and to have weak solution pipeline to be communicated with newly-increased generator (A) through the first solution pump (9) and the second solution heat exchanger (16) through the first solution pump (9) and the second solution heat exchanger (16) the first absorber (4), newly-increased generator (A) also has concentrated solution pipeline to be communicated with the second generator (2) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), there is concentrated solution pipeline to be communicated with the first absorber (4) and to be adjusted into the first generator (1) and to have concentrated solution pipeline through the first solution heat exchanger (15) through the first solution heat exchanger (15) and the second solution heat exchanger (16) in the first generator (1), newly-increased solution heat exchanger (C) and the second solution heat exchanger (16) are communicated with the first absorber (4), after having refrigerant vapour passage to be communicated with the first condenser (6) to be adjusted into the second generator (2) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the second generator (2), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (6) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (6), having refrigerant vapour passage to be communicated with the second absorber (5) to be adjusted into newly-increased generator (A) to set up refrigerant vapour passage in the second generator (2) is communicated with the second absorber (5), form taking triple effect as basic composite absorption heat pump.
13. taking triple effect as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 8, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the second generator (2) and to be adjusted into the second absorber (5) and to have weak solution pipeline to be communicated with newly-increased generator (A) through the second solution pump (10) and the second solution heat exchanger (16) through the second solution pump (10) and the second solution heat exchanger (16) the second absorber (5), newly-increased generator (A) also has concentrated solution pipeline to be communicated with the second generator (2) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), there is concentrated solution pipeline to be communicated with the first absorber (4) and to be adjusted into the first generator (1) and to have concentrated solution pipeline through the first solution heat exchanger (15) through the first solution heat exchanger (15) and the second solution heat exchanger (16) in the first generator (1), newly-increased solution heat exchanger (C) and the second solution heat exchanger (16) are communicated with the first absorber (4), after having refrigerant vapour passage to be communicated with the first condenser (6) to be adjusted into the second generator (2) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the second generator (2), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (6) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (6), having refrigerant vapour passage to be communicated with the second absorber (5) to be adjusted into newly-increased generator (A) to set up refrigerant vapour passage in the second generator (2) is communicated with the second absorber (5), form taking triple effect as basic composite absorption heat pump.
14. taking triple effect as basic composite absorption heat pump, in claim 9-13 in the composite absorption heat pump described in arbitrary claim, after having refrigerant vapour passage to be communicated with the 3rd generator (3) in the first generator (1) the 3rd generator (3) have again cryogen liquid pipeline to be communicated with the second condenser (7) through the 3rd choke valve (13) to be adjusted into the second generator (2) have refrigerant vapour passage to be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline to be communicated with the second condenser (7) through the 3rd choke valve (13), form taking triple effect as basic composite absorption heat pump.
15. taking economic benefits and social benefits as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 1, increase by the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger, there is weak solution pipeline to be communicated with the first solution heat exchanger (15) and the second solution heat exchanger (16) respectively afterwards and to be adjusted into the first absorber (4) and to have weak solution pipeline to be communicated with the 3rd absorber (20) through the first solution pump (9) and the 4th solution heat exchanger (21) through the first solution pump (9) the first absorber (4), the 3rd absorber (20) has weak solution pipeline to be communicated with the first solution heat exchanger (15) and the second solution heat exchanger (16) respectively afterwards through the 3rd solution pump (18) again, the first generator (1) is had concentrated solution pipeline to be communicated with the first absorber (4) through the first solution heat exchanger (15) to be adjusted into the first generator (1) has concentrated solution pipeline to be communicated with the 4th generator (19) through the first solution heat exchanger (15), the second generator (2) is had concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16) to be adjusted into the second generator (2) has concentrated solution pipeline to be communicated with the 4th generator (19) through the second solution heat exchanger (16), the 4th generator (19) has concentrated solution pipeline to be communicated with the first absorber (4) through the 4th solution heat exchanger (21) again, the 4th generator (19) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 4th generator (19) 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 taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
16. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in claim 15, there is weak solution pipeline to be communicated with the 3rd generator (3) and to be adjusted into the second absorber (5) and to have weak solution pipeline to be communicated with the first generator (1) through the second solution pump (10) and the first solution heat exchanger (15) through the second solution pump (10) and the 3rd solution heat exchanger (17) the second absorber (5), there is weak solution pipeline to be communicated with the first generator (1) and to be adjusted into the 3rd absorber (20) and to have weak solution pipeline to be communicated with the 3rd generator (3) through the 3rd solution pump (18) and the 3rd solution heat exchanger (17) through the 3rd solution pump (18) and the first solution heat exchanger (15) the 3rd absorber (20), form taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
17. taking economic benefits and social benefits as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 3, increase by the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger, the first absorber (4) is had to weak solution pipeline through the first solution pump (9), the second solution heat exchanger (16) and the first solution heat exchanger (15) are communicated with the first generator (1) and are adjusted into the first absorber (4) and have weak solution pipeline to be communicated with the 3rd absorber (20) through the first solution pump (9) and the 4th solution heat exchanger (21), the 3rd absorber (20) has weak solution pipeline again through the 3rd solution pump (18), the second solution heat exchanger (16) and the first solution heat exchanger (15) are communicated with the first generator (1), the second generator (2) is had concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16) to be adjusted into the second generator (2) has concentrated solution pipeline to be communicated with the 4th generator (19) through the second solution heat exchanger (16), the 4th generator (19) has concentrated solution pipeline to be communicated with the first absorber (4) through the 4th solution heat exchanger (21) again, the 4th generator (19) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 4th generator (19) 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 taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
18. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in claim 17, there is weak solution pipeline to be communicated with the 3rd generator (3) and to be adjusted into the second absorber (5) and to have weak solution pipeline to be communicated with the first generator (1) through the second solution pump (10) and the first solution heat exchanger (15) through the second solution pump (10) and the 3rd solution heat exchanger (17) the second absorber (5), the 3rd absorber (20) is had to weak solution pipeline through the 3rd solution pump (18), the second solution heat exchanger (16) and the first solution heat exchanger (15) are communicated with the first generator (1) and are adjusted into the 3rd absorber (20) and have weak solution pipeline through the 3rd solution pump (18), the second solution heat exchanger (16) and the 3rd solution heat exchanger (17) are communicated with the 3rd generator (3), form taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
19. taking economic benefits and social benefits as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 6, increase by the 4th generator, the 3rd absorber, the 4th solution pump and the 4th solution heat exchanger, there is weak solution pipeline to be communicated with the second generator (2) and to be adjusted into the first absorber (4) and to have weak solution pipeline to be communicated with the 3rd absorber (20) through the first solution pump (9) and the 4th solution heat exchanger (21) through the first solution pump (9) and the second solution heat exchanger (16) the first absorber (4), the 3rd absorber (20) has weak solution pipeline to be communicated with the second generator (2) through the 4th solution pump (20) and the second solution heat exchanger (16) again, there is concentrated solution pipeline to be communicated with the first absorber (4) and to be adjusted into the first generator (1) and to have concentrated solution pipeline to be communicated with the 4th generator (19) through the first solution heat exchanger (15) and the second solution heat exchanger (16) through the first solution heat exchanger (15) and the second solution heat exchanger (16) in the first generator (1), the 4th generator (19) has concentrated solution pipeline to be communicated with the first absorber (4) through the 4th solution heat exchanger (21) again, the 4th generator (19) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 4th generator (19) 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 taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
20. taking economic benefits and social benefits as basic composite absorption heat pump, in the composite absorption heat pump described in claim 19, there is weak solution pipeline to be communicated with the 3rd generator (3) and to be adjusted into the second absorber (5) and to have weak solution pipeline to be communicated with the second generator (2) through the second solution pump (10) and the second solution heat exchanger (16) through the second solution pump (10) and the 3rd solution heat exchanger (17) the second absorber (5), there is weak solution pipeline to be communicated with the second generator (2) and to be adjusted into the 3rd absorber (20) and to have weak solution pipeline to be communicated with the 3rd generator (3) through the 3rd solution pump (18) and the 3rd solution heat exchanger (17) through the 3rd solution pump (18) and the second solution heat exchanger (16) the 3rd absorber (20), form taking economic benefits and social benefits as basis and there is the composite absorption heat pump of backheat heat supply end.
21. taking economic benefits and social benefits as basic composite absorption heat pump, in claim 15-20 in the composite absorption heat pump described in arbitrary claim, increase by the 5th choke valve, cancel the 4th generator (19) and the outside driving thermal medium pipeline being communicated with, the first generator (1) set up refrigerant vapour passage and be communicated with the 4th generator (19) after the 4th generator (19) have again cryogen liquid pipeline to be communicated with the first condenser (6) through the 5th choke valve (22), formation is taking economic benefits and social benefits as basic and have a composite absorption heat pump of backheat heat supply end.
22. taking triple effect as basic composite absorption heat pump, in claim 15-16 in the composite absorption heat pump described in arbitrary claim, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 3rd solution pump (18) 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 4th generator (19) through newly-increased solution heat exchanger (C), after having refrigerant vapour passage to be communicated with the first condenser (6) to be adjusted into the second generator (2) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the second generator (2), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (6) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (6), having refrigerant vapour passage to be communicated with the second absorber (5) to be adjusted into newly-increased generator (A) to set up refrigerant vapour passage in the second generator (2) is communicated with the second absorber (5), form taking triple effect as basis and there is the composite absorption heat pump of backheat heat supply end.
23. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in claim 17, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 3rd absorber (20) is had weak solution pipeline to be communicated with the second solution heat exchanger (16) through the 3rd solution pump (18) to be adjusted into the 3rd absorber (20) has weak solution pipeline to be communicated with the second solution heat exchanger (16) through the 3rd solution pump (18) and newly-increased solution heat exchanger (C), the second generator (2) is had concentrated solution pipeline to be communicated with the 3rd generator (19) through the second solution heat exchanger (16) to be adjusted into the second generator (2) has concentrated solution pipeline to be communicated with newly-increased generator (A) through the second solution heat exchanger (16), newly-increased generator (A) also has concentrated solution pipeline to be communicated with the 3rd generator (19) through newly-increased solution heat exchanger (C), after having refrigerant vapour passage to be communicated with the first condenser (6) to be adjusted into the second generator (2) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the second generator (2), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (6) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (6), having refrigerant vapour passage to be communicated with the second absorber (5) to be adjusted into newly-increased generator (A) to set up refrigerant vapour passage in the second generator (2) is communicated with the second absorber (5), form taking triple effect as basis and there is the composite absorption heat pump of backheat heat supply end.
24. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in claim 18, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first generator (1) is had concentrated solution pipeline to be communicated with the second generator (2) through the first solution heat exchanger (15) to be adjusted into the first generator (1) has concentrated solution pipeline to be communicated with the second generator (2) through the first solution heat exchanger (15) and newly-increased solution heat exchanger (C), there is concentrated solution pipeline to be communicated with the 4th generator (19) through the second solution heat exchanger (16) to be adjusted into the second generator (2) to have concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C) in the second generator (2), newly-increased generator (A) also has concentrated solution pipeline to be communicated with the 4th generator (19) through the second solution heat exchanger (16), after having refrigerant vapour passage to be communicated with the first condenser (6) to be adjusted into the second generator (2) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the second generator (2), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (6) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (6), having refrigerant vapour passage to be communicated with the second absorber (5) to be adjusted into newly-increased generator (A) to set up refrigerant vapour passage in the second generator (2) is communicated with the second absorber (5), form taking triple effect as basis and there is the composite absorption heat pump of backheat heat supply end.
25. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in claim 19, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the second generator (2) and to be adjusted into the 3rd absorber (20) and to have weak solution pipeline to be communicated with newly-increased generator (A) through the 4th solution pump (30) and the second solution heat exchanger (16) through the 4th solution pump (30) and the second solution heat exchanger (16) the 3rd absorber (20), newly-increased generator (A) also has concentrated solution pipeline to be communicated with the second generator (2) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), there is concentrated solution pipeline to be communicated with the 4th generator (19) and to be adjusted into the first generator (1) and to have concentrated solution pipeline through the first solution heat exchanger (15) through the first solution heat exchanger (15) and the second solution heat exchanger (16) in the first generator (1), newly-increased solution heat exchanger (C) and the second solution heat exchanger (16) are communicated with the 4th generator (19), after having refrigerant vapour passage to be communicated with the first condenser (6) to be adjusted into the second generator (2) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the second generator (2), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (6) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (6), having refrigerant vapour passage to be communicated with the second absorber (5) to be adjusted into newly-increased generator (A) to set up refrigerant vapour passage in the second generator (2) is communicated with the second absorber (5), form taking triple effect as basis and there is the composite absorption heat pump of backheat heat supply end.
26. taking triple effect as basic composite absorption heat pump, in the composite absorption heat pump described in claim 20, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the second generator (2) and to be adjusted into the second absorber (5) and to have weak solution pipeline to be communicated with newly-increased generator (A) through the second solution pump (10) and the second solution heat exchanger (16) through the second solution pump (10) and the second solution heat exchanger (16) the second absorber (5), newly-increased generator (A) also has concentrated solution pipeline to be communicated with the second generator (2) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), there is concentrated solution pipeline to be communicated with the 4th generator (19) and to be adjusted into the first generator (1) and to have concentrated solution pipeline through the first solution heat exchanger (15) through the first solution heat exchanger (15) and the second solution heat exchanger (16) in the first generator (1), newly-increased solution heat exchanger (C) and the second solution heat exchanger (16) are communicated with the 4th generator (4), after having refrigerant vapour passage to be communicated with the first condenser (6) to be adjusted into the second generator (2) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the second generator (2), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (6) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (6), having refrigerant vapour passage to be communicated with the second absorber (5) to be adjusted into newly-increased generator (A) to set up refrigerant vapour passage in the second generator (2) is communicated with the second absorber (5), form taking triple effect as basis and there is the composite absorption heat pump of backheat heat supply end.
27. taking triple effect as basic composite absorption heat pump, in claim 22-26 in the composite absorption heat pump described in arbitrary claim, increase by the 5th choke valve, cancel the 4th generator (19) and the outside driving thermal medium pipeline being communicated with, the first generator (1) set up refrigerant vapour passage and be communicated with the 4th generator (19) after the 4th generator (19) have again cryogen liquid pipeline to be communicated with the first condenser (6) through the 5th choke valve (22), formation is taking triple effect as basic and have a composite absorption heat pump of backheat heat supply end.
28. taking triple effect as basic composite absorption heat pump, in claim 22-26 in the composite absorption heat pump described in arbitrary claim, increase by the 5th choke valve, cancel the 4th generator (19) and the outside driving thermal medium pipeline being communicated with, the second generator (2) set up refrigerant vapour passage and be communicated with the 4th generator (19) after the 4th generator (19) have again cryogen liquid pipeline to be communicated with the first condenser (6) through the 5th choke valve (22), formation is taking triple effect as basic and have a composite absorption heat pump of backheat heat supply end.
29. taking triple effect as basic composite absorption heat pump, in claim 22-28 in the composite absorption heat pump described in arbitrary claim, after having refrigerant vapour passage to be communicated with the 3rd generator (3) in the first generator (1) the 3rd generator (3) have again cryogen liquid pipeline to be communicated with the second condenser (7) through the 3rd choke valve (13) to be adjusted into the second generator (2) have refrigerant vapour passage to be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline to be communicated with the second condenser (7) through the 3rd choke valve (13), form taking triple effect as basic composite absorption heat pump.
30. taking economic benefits and social benefits as basic composite absorption heat pump, in claim 1-5 in the composite absorption heat pump described in arbitrary claim, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber (4) and the outside heated medium pipeline being communicated with, the 3rd absorber (20) has weak solution pipeline to be communicated with a point steam chest (23) through newly-increased solution choke valve (E) and the first absorber (4), divide steam chest (23) to also have concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18), divide steam chest (23) to also have refrigerant vapour passage to be communicated with the 3rd condenser (24), the 3rd condenser (24) also has cryogen liquid pipeline to be communicated with the second evaporimeter (25) through cryogen liquid pump (26), the second evaporimeter (25) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, the 3rd condenser (24) also has cooling medium pipeline to be communicated with outside, the second evaporimeter (25) medium pipeline that also has surplus heat is communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 3rd condenser (24) has cryogen liquid pipeline to be communicated with the first evaporimeter (8), and the first evaporimeter (8) is set up refrigerant vapour passage and is communicated with the 3rd absorber (20).
31. taking economic benefits and social benefits as basic composite absorption heat pump, in claim 6-8 in the composite absorption heat pump described in arbitrary claim, increase by the 4th solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber (4) and the outside heated medium pipeline being communicated with, the 3rd absorber (20) has weak solution pipeline to be communicated with a point steam chest (23) through newly-increased solution choke valve (E) and the first absorber (4), divide steam chest (23) to also have concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 4th solution pump (30), divide steam chest (23) to also have refrigerant vapour passage to be communicated with the 3rd condenser (24), the 3rd condenser (24) also has cryogen liquid pipeline to be communicated with the second evaporimeter (25) through cryogen liquid pump (26), the second evaporimeter (25) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, the 3rd condenser (24) also has cooling medium pipeline to be communicated with outside, the second evaporimeter (25) medium pipeline that also has surplus heat is communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 3rd condenser (24) has cryogen liquid pipeline to be communicated with the first evaporimeter (8), and the first evaporimeter (8) is set up refrigerant vapour passage and is communicated with the 3rd absorber (20).
32. taking economic benefits and social benefits as basic composite absorption heat pump, in claim 1-2 in the composite absorption heat pump described in arbitrary claim, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber (4) and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber (4) through the first solution heat exchanger (15) to be adjusted into the first generator (1) to have concentrated solution pipeline to be communicated with a point steam chest (23) through the first solution heat exchanger (15) and the first absorber (4) in the first generator (1), there is concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16) to be adjusted into the second generator (2) to have concentrated solution pipeline to be communicated with a point steam chest (23) through the second solution heat exchanger (16) and the first absorber (4) in the second generator (2), divide steam chest (23) to also have concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18), the 3rd absorber (20) also has weak solution pipeline to be communicated with the first absorber (4) through newly-increased solution choke valve (E), divide steam chest (23) to also have refrigerant vapour passage to be communicated with the 3rd condenser (24), the 3rd condenser (24) also has cryogen liquid pipeline to be communicated with the first evaporimeter (8) through cryogen liquid pump (26), the first evaporimeter (8) has cryogen liquid pipeline to be communicated with the second evaporimeter (25) through the 5th choke valve (22), the first evaporimeter (8) is had refrigerant vapour passage to be communicated with the first absorber (4) to be adjusted into the first evaporimeter (8) has refrigerant vapour passage to be communicated with the 3rd absorber (20), the second evaporimeter (25) also has refrigerant vapour passage to be communicated with the first absorber (4), the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, the 3rd condenser (24) also has cooling medium pipeline to be communicated with outside, the second evaporimeter (25) medium pipeline that also has surplus heat is communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has weak solution pipeline to be communicated with the first absorber (4), and the first evaporimeter (8) is set up refrigerant vapour passage and is communicated with the first absorber (4).
33. taking economic benefits and social benefits as basic composite absorption heat pump, in claim 3-5 in the composite absorption heat pump described in arbitrary claim, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber (4) and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16) to be adjusted into the second generator (2) to have concentrated solution pipeline to be communicated with a point steam chest (23) through the second solution heat exchanger (16) and the first absorber (4) in the second generator (2), divide steam chest (23) to also have concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18), the 3rd absorber (20) also has weak solution pipeline to be communicated with the first absorber (4) through newly-increased solution choke valve (E), divide steam chest (23) to also have refrigerant vapour passage to be communicated with the 3rd condenser (24), the 3rd condenser (24) also has cryogen liquid pipeline to be communicated with the first evaporimeter (8) through cryogen liquid pump (26), the first evaporimeter (8) has cryogen liquid pipeline to be communicated with the second evaporimeter (25) through the 5th choke valve (22), the first evaporimeter (8) is had refrigerant vapour passage to be communicated with the first absorber (4) to be adjusted into the first evaporimeter (8) has refrigerant vapour passage to be communicated with the 3rd absorber (20), the second evaporimeter (25) also has refrigerant vapour passage to be communicated with the first absorber (4), the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, the 3rd condenser (24) also has cooling medium pipeline to be communicated with outside, the second evaporimeter (25) medium pipeline that also has surplus heat is communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has weak solution pipeline to be communicated with the first absorber (4), and the first evaporimeter (8) is set up refrigerant vapour passage and is communicated with the first absorber (4).
34. taking economic benefits and social benefits as basic composite absorption heat pump, in claim 6-8 in the composite absorption heat pump described in arbitrary claim, increase by the 4th solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber (4) and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber (4) and to be adjusted into the first generator (1) and to have concentrated solution pipeline through the first solution heat exchanger (15) through the first solution heat exchanger (15) and the second solution heat exchanger (16) in the first generator (1), the second solution heat exchanger (16) and the first absorber (4) are communicated with a point steam chest (23), divide steam chest (23) to also have concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 4th solution pump (30), the 3rd absorber (20) also has weak solution pipeline to be communicated with the first absorber (4) through newly-increased solution choke valve (E), divide steam chest (23) to also have refrigerant vapour passage to be communicated with the 3rd condenser (24), the 3rd condenser (24) also has cryogen liquid pipeline to be communicated with the first evaporimeter (8) through cryogen liquid pump (26), the first evaporimeter (8) has cryogen liquid pipeline to be communicated with the second evaporimeter (25) through the 5th choke valve (22), the first evaporimeter (8) is had refrigerant vapour passage to be communicated with the first absorber (4) to be adjusted into the first evaporimeter (8) has refrigerant vapour passage to be communicated with the 3rd absorber (20), the second evaporimeter (25) also has refrigerant vapour passage to be communicated with the first absorber (4), the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, the 3rd condenser (24) also has cooling medium pipeline to be communicated with outside, the second evaporimeter (25) medium pipeline that also has surplus heat is communicated with outside, form taking economic benefits and social benefits as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has weak solution pipeline to be communicated with the first absorber (4), and the first evaporimeter (8) is set up refrigerant vapour passage and is communicated with the first absorber (4).
35. taking triple effect as basic composite absorption heat pump, in claim 9-11 in the composite absorption heat pump described in arbitrary claim, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber (4) and the outside heated medium pipeline being communicated with, the 3rd absorber (20) has weak solution pipeline to be communicated with a point steam chest (23) through newly-increased solution choke valve (E) and the first absorber (4), divide steam chest (23) to also have concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18), divide steam chest (23) to also have refrigerant vapour passage to be communicated with the 3rd condenser (24), the 3rd condenser (24) also has cryogen liquid pipeline to be communicated with the second evaporimeter (25) through cryogen liquid pump (26), the second evaporimeter (25) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, the 3rd condenser (24) also has cooling medium pipeline to be communicated with outside, the second evaporimeter (25) medium pipeline that also has surplus heat is communicated with outside, form taking triple effect as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 3rd condenser (24) has cryogen liquid pipeline to be communicated with the first evaporimeter (8), and the first evaporimeter (8) is set up refrigerant vapour passage and is communicated with the 3rd absorber (20).
36. taking triple effect as basic composite absorption heat pump, in claim 12-13 in the composite absorption heat pump described in arbitrary claim, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber (4) and the outside heated medium pipeline being communicated with, the 3rd absorber (20) has weak solution pipeline to be communicated with a point steam chest (23) through newly-increased solution choke valve (E) and the first absorber (4), divide steam chest (23) to also have concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18), divide steam chest (23) to also have refrigerant vapour passage to be communicated with the 3rd condenser (24), the 3rd condenser (24) also has cryogen liquid pipeline to be communicated with the second evaporimeter (25) through cryogen liquid pump (26), the second evaporimeter (25) also has refrigerant vapour passage to be communicated with the 3rd absorber (20), the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, the 3rd condenser (24) also has cooling medium pipeline to be communicated with outside, the second evaporimeter (25) medium pipeline that also has surplus heat is communicated with outside, form taking triple effect as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 3rd condenser (24) has cryogen liquid pipeline to be communicated with the first evaporimeter (8), and the first evaporimeter (8) is set up refrigerant vapour passage and is communicated with the 3rd absorber (20).
37. taking triple effect as basic composite absorption heat pump, in composite absorption heat pump claimed in claim 9, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber (4) and the outside heated medium pipeline being communicated with, there is concentrated solution pipeline to be communicated with the first absorber (4) through the first solution heat exchanger (15) to be adjusted into the first generator (1) to have concentrated solution pipeline to be communicated with a point steam chest (23) through the first solution heat exchanger (15) and the first absorber (4) in the first generator (1), there is concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16) to be adjusted into the second generator (2) to have concentrated solution pipeline to be communicated with a point steam chest (23) through the second solution heat exchanger (16) and the first absorber (4) in the second generator (2), to increase generator (A) newly has concentrated solution pipeline to be communicated with the first absorber (4) and to be adjusted into newly-increased generator (A) and to have concentrated solution pipeline to be communicated with dividing a steam chest (23) through increasing solution heat exchanger (C) and the first absorber (4) newly through newly-increased solution heat exchanger (C), divide steam chest (23) to also have concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18), the 3rd absorber (20) also has weak solution pipeline to be communicated with the first absorber (4) through newly-increased solution choke valve (E), divide steam chest (23) to also have refrigerant vapour passage to be communicated with the 3rd condenser (24), the 3rd condenser (24) also has cryogen liquid pipeline to be communicated with the first evaporimeter (8) through cryogen liquid pump (26), the first evaporimeter (8) has cryogen liquid pipeline to be communicated with the second evaporimeter (25) through the 5th choke valve (22), the first evaporimeter (8) is had refrigerant vapour passage to be communicated with the first absorber (4) to be adjusted into the first evaporimeter (8) has refrigerant vapour passage to be communicated with the 3rd absorber (20), the second evaporimeter (25) also has refrigerant vapour passage to be communicated with the first absorber (4), the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, the 3rd condenser (24) also has cooling medium pipeline to be communicated with outside, the second evaporimeter (25) medium pipeline that also has surplus heat is communicated with outside, form taking triple effect as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has weak solution pipeline to be communicated with the first absorber (4), and the first evaporimeter (8) is set up refrigerant vapour passage and is communicated with the first absorber (4).
38. taking triple effect as basic composite absorption heat pump, in claim 10-11 in the composite absorption heat pump described in arbitrary claim, increase by the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber (4) and the outside heated medium pipeline being communicated with, to increase generator (A) newly has concentrated solution pipeline to be communicated with the first absorber (4) through the second solution heat exchanger (16) to be adjusted into newly-increased generator (A) to have concentrated solution pipeline to be communicated with a point steam chest (23) through the second solution heat exchanger (16) and the first absorber (4), divide steam chest (23) to also have concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18), the 3rd absorber (20) also has weak solution pipeline to be communicated with the first absorber (4) through newly-increased solution choke valve (E), divide steam chest (23) to also have refrigerant vapour passage to be communicated with the 3rd condenser (24), the 3rd condenser (24) also has cryogen liquid pipeline to be communicated with the first evaporimeter (8) through cryogen liquid pump (26), the first evaporimeter (8) has cryogen liquid pipeline to be communicated with the second evaporimeter (25) through the 5th choke valve (22), the first evaporimeter (8) is had refrigerant vapour passage to be communicated with the first absorber (4) to be adjusted into the first evaporimeter (8) has refrigerant vapour passage to be communicated with the 3rd absorber (20), the second evaporimeter (25) also has refrigerant vapour passage to be communicated with the first absorber (4), the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, the 3rd condenser (24) also has cooling medium pipeline to be communicated with outside, the second evaporimeter (25) medium pipeline that also has surplus heat is communicated with outside, form taking triple effect as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has weak solution pipeline to be communicated with the first absorber (4), and the first evaporimeter (8) is set up refrigerant vapour passage and is communicated with the first absorber (4).
39. taking triple effect as basic composite absorption heat pump, in claim 12-13 in the composite absorption heat pump described in arbitrary claim, increase by the 4th solution pump, the 3rd absorber, divide steam chest, the 3rd condenser, the second evaporimeter, the 5th choke valve, cryogen liquid pump and newly-increased solution choke valve, cancel or reservation the first absorber (4) and the outside heated medium pipeline being communicated with, the first generator (1) is had to concentrated solution pipeline through the first solution heat exchanger (15), newly-increased solution heat exchanger (C) and the second solution heat exchanger (16) are communicated with the first absorber (4) and are adjusted into the first generator (1) and have concentrated solution pipeline through the first solution heat exchanger (15), newly-increased solution heat exchanger (C), the second solution heat exchanger (16) and the first absorber (4) are communicated with a point steam chest (23), divide steam chest (23) to also have concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 4th solution pump (30), the 3rd absorber (20) also has weak solution pipeline to be communicated with the first absorber (4) through newly-increased solution choke valve (E), divide steam chest (23) to also have refrigerant vapour passage to be communicated with the 3rd condenser (24), the 3rd condenser (24) also has cryogen liquid pipeline to be communicated with the first evaporimeter (8) through cryogen liquid pump (26), the first evaporimeter (8) has cryogen liquid pipeline to be communicated with the second evaporimeter (25) through the 5th choke valve (22), the first evaporimeter (8) is had refrigerant vapour passage to be communicated with the first absorber (4) to be adjusted into the first evaporimeter (8) has refrigerant vapour passage to be communicated with the 3rd absorber (20), the second evaporimeter (25) also has refrigerant vapour passage to be communicated with the first absorber (4), the 3rd absorber (20) also has heated medium pipeline to be communicated with outside, the 3rd condenser (24) also has cooling medium pipeline to be communicated with outside, the second evaporimeter (25) medium pipeline that also has surplus heat is communicated with outside, form taking triple effect as basic composite absorption heat pump, wherein, during without the second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has weak solution pipeline to be communicated with the first absorber (4), and the first evaporimeter (8) is set up refrigerant vapour passage and is communicated with the first absorber (4).
40. taking triple effect as basic composite absorption heat pump, in claim 35-39 in the composite absorption heat pump described in arbitrary claim, after having refrigerant vapour passage to be communicated with the 3rd generator (3) in the first generator (1) the 3rd generator (3) have again cryogen liquid pipeline to be communicated with the second condenser (7) through the 3rd choke valve (13) to be adjusted into the second generator (2) have refrigerant vapour passage to be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline to be communicated with the second condenser (7) through the 3rd choke valve (13), form taking triple effect as basic composite absorption heat pump.
41. taking economic benefits and social benefits or triple effect as basic composite absorption heat pump, in claim 1-40 in the composite absorption heat pump described in arbitrary claim, increase first flow control valve and second adjustable valve, there are respectively heated medium pipeline and outside connection to be defined as outside and to have heated medium pipeline to be communicated with the first condenser (6) afterwards with the first condenser (6) to have again heated medium pipeline to be communicated with the second condenser (7) through second adjustable valve (29) with outside connected sum through first flow control valve (28) respectively the first condenser (6) and the second condenser (7), the second condenser (7) has heated medium pipeline to be communicated with outside again, formation has adjust flux and distributes, taking economic benefits and social benefits or triple effect as basic composite absorption heat pump.
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