CN102353170A - 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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CN102353170A
CN102353170A CN2011102324340A CN201110232434A CN102353170A CN 102353170 A CN102353170 A CN 102353170A CN 2011102324340 A CN2011102324340 A CN 2011102324340A CN 201110232434 A CN201110232434 A CN 201110232434A CN 102353170 A CN102353170 A CN 102353170A
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solution
generator
communicated
absorber
heat exchanger
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CN102353170B (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

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

The composite absorption heat pump that is the basis with economic benefits and social benefits or triple effect
Technical field:
The invention belongs to low temperature exhaust heat utilization 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 high advantage of performance index, but tangible deficiency is also arranged---can not have the interval and higher heating parameter of heat supply temperature of broad.The variable working condition heat supply that can not satisfy fully for single flow process; In order to obtain higher performance index and to satisfy the heat demand of using of heated medium; In the heat pump flowsheet arrangement, will carry out such consideration: adopt two ends heat supply economic benefits and social benefits or the three-effect absorption-type heat pump that adapts when heat supply temperature is low, when heat supply temperature, adopt the adjacent run of economic benefits and social benefits or triple effect; Simultaneously, in the arrangement of heat supply end, should be connected between the maximum heat supply temperature of each heat supply end rationally, the excessive phenomenon of heat supply temperature difference should not occur.
Reasonably technical scheme is; When being the basis with the double effect absorption flow process; Main second absorber, the 3rd generator and second condenser of increasing; The refrigerant vapour that the high pressure generator of double-effect process produces is respectively applied for double-effect process and the 3rd generator makes to drive thermal medium; The low pressure generator of double-effect process provides refrigerant vapour to second absorber, interval two the adjacent heat supply ends of formation temperature; When being the basis with the three-effect absorption-type flow process; Main second absorber, the 3rd generator and second condenser of increasing; The refrigerant vapour that the middle pressure generator of triple effect flow process produces is respectively applied for the 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 second absorber; Interval two the adjacent heat supply ends of formation temperature, thus corresponding high-performance index when variable parameter operation, obtained.
Summary of the invention:
Main purpose of the present invention is that the composite absorption heat pump (type I) that is the basis with economic benefits and social benefits or triple effect will be provided, and concrete summary of the invention subitem is set forth as follows:
1 based on double effect absorption heat pump compound, mainly by the first generator, the second generator, a third generator, a first absorber, the second absorber, the first condenser, second condenser, an evaporator, a first solution pump, a second solution pump, the first throttle valve, the second throttle valve, a third throttle valve, a fourth throttle valve, the first solution heat exchanger, a second solution heat exchanger and a third solution heat exchanger components; first absorber pipe by a dilute solution, respectively, after the first solution pump solution heat exchanger and then by first communicating with the first generator and then by a second solution heat exchanger and the first two generators connected, the first generator also concentrated solution through the first solution heat exchanger tube absorber connected with the first and second generators and piping concentrated solution through a second solution heat exchanger and the first absorption in communication, a dilute solution of the second absorber solution pump via the second conduit and the third heat exchanger and the third generator connected solution, third generator via a third conduit and a concentrated solution of the first solution heat exchanger two absorber communicating, the first generator and refrigerant vapor passage communicating with the second generator, the second generator, the refrigerant liquid line again through the first condenser communicating with the first throttle valve, a first generator There refrigerant vapor passage communicating with the third generator generator again after the third refrigerant liquid piping via a third throttle valve communicating with the second condenser, a second generator and refrigerant vapor channel and the first a condenser communicating a second refrigerant vapor generator and absorber passage communicates with the second, third generator and refrigerant vapor passage communicating with the second condenser, the second condenser and liquid refrigerant piping via The fourth throttle valve and communicating the first condenser or an evaporator, liquid refrigerant in the first condenser and piping through the second throttle valve communicates with the evaporator, the refrigerant evaporator and absorber of the first steam passage communication, the evaporator and heat medium pipe communicates with the outside, the first generator and driving the heat medium pipe communicates with the outside, a first absorber, a first condenser, a second absorber and the second condenser also separately there is a heating medium line communicates with the outside, to form a double-effect-based composite absorption heat pump.
2. with economic benefits and social benefits the composite absorption heat pump on basis; Be in the 1st described composite absorption heat pump; Having the weak solution pipeline to be communicated with the 3rd generator through second solution pump and the 3rd solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with first generator through second solution pump and first solution heat exchanger; Have the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger first absorber and be adjusted into first absorber and have the weak solution pipeline to be communicated with the 3rd generator through first solution pump and the 3rd solution heat exchanger, forming with economic benefits and social benefits is the composite absorption heat pump on basis.
3 based on the double effect absorption heat pump compound, mainly by the first generator, the second generator, a third generator, a first absorber, the second absorber, the first condenser, second condenser, an evaporator, a first solution pump, a second solution pump, the first throttle valve, the second throttle valve, a third throttle valve, a fourth throttle valve, the first solution heat exchanger, a second solution heat exchanger solution heat exchanger and a third component; first with dilute solution absorber via the first solution pump piping, heat exchanger and the first solution a second solution heat exchanger and the first generator communicating, the first generator and The first solution is a concentrated solution conduit and a second generator heat exchanger communicates, and concentrated solution of the second generator via a second conduit to the first absorber solution heat exchanger communicates with the second absorber dilute solution tube passing the second and third solution heat exchanger solution pump generator connected with the third, the third generator and a concentrated solution through a third solution heat exchanger tube absorber connected with the second, the first generator and refrigerant vapor passage communicating with the second generator, the second generator is then a liquid refrigerant pipe via the first throttle valve communicates with the first condenser, a first refrigerant vapor generator and generator and the third passage After the third generator connected again refrigerant liquid piping via a third throttle communicating with the second condenser, refrigerant vapor second generator and condenser passage communicating with the first and second generators and cold refrigerant vapor passage communicates with the second absorber, and the third refrigerant vapor generator and condenser communicating with the second passage, the second condenser and refrigerant liquid line throttle valve and the first through the fourth condenser or an evaporator connected, the first condenser and the refrigerant liquid line to the evaporator via the second throttle valve communicates the refrigerant evaporator and the steam passage communicating with the first absorber, the evaporator and the heat medium pipe communicates with the outside, the first generator and driving the heat medium pipe communicates with the outside, a first absorber, a first condenser, a second absorber and the second condenser is heated medium were also communicates with the outside line, to form based double effect absorption heat pump combined.
4. with economic benefits and social benefits the composite absorption heat pump on basis; Be in the 3rd described composite absorption heat pump; Increase the solution choke valve; With first absorber have the weak solution pipeline through first solution pump, second solution heat exchanger and first solution heat exchanger is communicated with first generator be adjusted into first absorber have the weak solution pipeline after first solution pump, second solution heat exchanger respectively again through solution choke valve and the second generator connected sum again warp first solution heat exchanger be communicated with first generator, formation is basic composite absorption heat pump with economic benefits and social benefits.
5. with economic benefits and social benefits the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 3-4 item; Having the weak solution pipeline to be communicated with the 3rd generator through second solution pump and the 3rd solution heat exchanger second absorber is adjusted into second absorber and has weak solution pipeline warp second solution pump and first solution heat exchanger to be communicated with first generator; First absorber there is the weak solution pipeline through first solution pump; Second solution heat exchanger and first solution heat exchanger are communicated with first generator and are adjusted into first absorber and the weak solution pipeline are arranged through first solution pump; Second solution heat exchanger and the 3rd solution heat exchanger are communicated with the 3rd generator, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
6 based on the double effect absorption heat pump compound, mainly by the first generator, the second generator, a third generator, a first absorber, the second absorber, the first condenser, second condenser, an evaporator, a first solution pump, a second solution pump, a third solution pump, the first throttle valve, the second throttle valve, a third throttle valve, a fourth throttle valve, the first solution heat exchanger, the first two solution heat exchanger and a third solution heat exchanger components; first absorber pipe with a dilute solution through the first solution and the second solution heat exchanger pump generator connected with the second, the second generator also concentrated solution The third solution is then pumped through the pipeline and the first heat exchanger and the first generator connectivity solution, concentrated solution of the first generator and solution heat exchanger tubing through the first heat exchanger and the first and second absorber solution communicating with the second absorber solution dilute solution pump via the second conduit and the third solution heat exchanger communicates with the third generator, a third generator and a concentrated solution through a third conduit and a second solution heat exchanger communicating absorber, generator, and the first refrigerant vapor passage communicating with the second generator, the second generator is then a liquid refrigerant pipe via the first condenser communicating with the first throttle valve, a first generator further There refrigerant vapor passage communicating with the third generator generator again after the third refrigerant liquid piping via a third throttle valve communicating with the second condenser, a second generator and refrigerant condensing steam passage and the first in communication, a second refrigerant vapor generator and absorber passage communicates with the second, third generator and refrigerant vapor passage communicating with the second condenser, the second condenser and liquid refrigerant through a first conduit four throttle valve and the first condenser or an evaporator connected, a first condenser and the refrigerant liquid line to the evaporator via the second throttle valve communicates the refrigerant evaporator and the steam passage communicating with the first absorber , the evaporator and heat medium pipe communicates with the outside, the first generator and driving the heat medium pipe communicates with the outside, a first absorber, a first condenser, a second absorber and the second condenser also were the heating medium line is connected with the outside, to form a double-effect-based composite absorption heat pump.
7. with economic benefits and social benefits the composite absorption heat pump on basis; Be in the 6th described composite absorption heat pump; Increase the solution choke valve; Have the weak solution pipeline to be communicated with second generator through first solution pump and second solution heat exchanger first absorber and be adjusted into first absorber and have the weak solution pipeline after first solution pump and second solution heat exchanger, directly to be communicated with second generator through the solution choke valve with the first generator connected sum respectively again, formation is basic composite absorption heat pump with economic benefits and social benefits.
8. with economic benefits and social benefits the composite absorption heat pump on basis; Be in the 6th described composite absorption heat pump; Having the weak solution pipeline to be communicated with the 3rd generator through second solution pump and the 3rd solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with second generator through second solution pump and second solution heat exchanger; Have the weak solution pipeline to be communicated with second generator through first solution pump and second solution heat exchanger first absorber and be adjusted into first absorber and have the weak solution pipeline to be communicated with the 3rd generator through first solution pump and the 3rd solution heat exchanger, forming with economic benefits and social benefits is the composite absorption heat pump on basis.
9. with the triple effect composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 1-2 item; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; First solution pump is set up the weak solution pipeline and is communicated with newly-increased generator through newly-increased solution heat exchanger; Newly-increased generator also has the concentrated solution pipeline to be communicated with first absorber through newly-increased solution heat exchanger; Having the refrigerant vapour passage to be communicated with first condenser to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again; Newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser; Have the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased generator to set up the refrigerant vapour passage in second generator and is communicated with second absorber, formation is basic composite absorption heat pump with the triple effect.
10. with the triple effect composite absorption heat pump on basis; Be in the 3rd described composite absorption heat pump; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; Having the weak solution pipeline to be communicated with second solution heat exchanger through first solution pump first absorber is adjusted into first absorber and has the weak solution pipeline to be communicated with second solution heat exchanger through first solution pump and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with first absorber through second solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with newly-increased generator through second solution heat exchanger; Newly-increased generator has the concentrated solution pipeline to be communicated with first absorber through newly-increased solution heat exchanger again; Having the refrigerant vapour passage to be communicated with first condenser to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again; Newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser; Have the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased generator to set up the refrigerant vapour passage in second generator and is communicated with second absorber, formation is basic composite absorption heat pump with the triple effect.
11. with the triple effect is the composite absorption heat pump on basis; Be in the 5th described composite absorption heat pump; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with first absorber through second solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger; Newly-increased generator also has the concentrated solution pipeline to be communicated with first absorber through second solution heat exchanger; Having the refrigerant vapour passage to be communicated with first condenser to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again; Newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser; Have the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased generator to set up the refrigerant vapour passage in second generator and is communicated with second absorber, formation is basic composite absorption heat pump with the triple effect.
12. with the triple effect is the composite absorption heat pump on basis; Be in the 6th described composite absorption heat pump; Increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump; Having the weak solution pipeline to be communicated with second generator through first solution pump and second solution heat exchanger first absorber is adjusted into first absorber and has the weak solution pipeline to be communicated with newly-increased generator through first solution pump and second solution heat exchanger; Newly-increased generator also has the concentrated solution pipeline to be communicated with second generator through newly-increased solution pump and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with first absorber through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with first absorber through first solution heat exchanger, newly-increased solution heat exchanger and second solution heat exchanger; Having the refrigerant vapour passage to be communicated with first condenser to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again; Newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser; Have the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased generator to set up the refrigerant vapour passage in second generator and is communicated with second absorber, formation is basic composite absorption heat pump with the triple effect.
13. with the triple effect is the composite absorption heat pump on basis; Be in the 8th described composite absorption heat pump; Increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump; Having the weak solution pipeline to be communicated with second generator through second solution pump and second solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased generator through second solution pump and second solution heat exchanger; Newly-increased generator also has the concentrated solution pipeline to be communicated with second generator through newly-increased solution pump and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with first absorber through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with first absorber through first solution heat exchanger, newly-increased solution heat exchanger and second solution heat exchanger; Having the refrigerant vapour passage to be communicated with first condenser to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again; Newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser; Have the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased generator to set up the refrigerant vapour passage in second generator and is communicated with second absorber, formation is basic composite absorption heat pump with the triple effect.
14. with the triple effect is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 9-13 item; With first generator have the refrigerant vapour passage be communicated with the 3rd generator back the 3rd generator have again the cryogen liquid pipeline through the 3rd choke valve is communicated with second condenser be adjusted into second generator and the refrigerant vapour passage arranged and the 3rd generator is communicated with after the 3rd generator have cryogen liquid pipeline warp the 3rd choke valve to be communicated with again with second condenser, formation is basic composite absorption heat pump with the triple effect.
15. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the 1st described composite absorption heat pump; Increase the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger; First absorber had the weak solution pipeline after first solution pump, to be communicated with first solution heat exchanger and second solution heat exchanger respectively to be adjusted into first absorber has the weak solution pipeline to be communicated with the 3rd absorber through first solution pump and the 4th solution heat exchanger; The 3rd absorber has the weak solution pipeline after the 3rd solution pump, to be communicated with first solution heat exchanger and second solution heat exchanger respectively again; Having the concentrated solution pipeline to be communicated with first absorber through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with the 4th generator through first solution heat exchanger; Having the concentrated solution pipeline to be communicated with first absorber through second solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with the 4th generator through second solution heat exchanger; The 4th generator has the concentrated solution pipeline to be communicated with first absorber through the 4th solution heat exchanger again; The 4th generator also has the refrigerant vapour passage to be communicated with the 3rd absorber; The 4th generator drives thermal medium pipeline and external communications in addition; The 3rd absorber also has heated medium pipeline and external communications, and forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
16. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the 15th described composite absorption heat pump; Having the weak solution pipeline to be communicated with the 3rd generator through second solution pump and the 3rd solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with first generator through second solution pump and first solution heat exchanger; Have the weak solution pipeline to be communicated with first generator through the 3rd solution pump and first solution heat exchanger the 3rd absorber and be adjusted into the 3rd absorber and have the weak solution pipeline to be communicated with the 3rd generator through the 3rd solution pump and the 3rd solution heat exchanger, forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
17. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the 3rd described composite absorption heat pump; Increase by the 4th generator; The 3rd absorber; The 3rd solution pump and the 4th solution heat exchanger; First absorber there is the weak solution pipeline through first solution pump; Second solution heat exchanger and first solution heat exchanger are communicated with first generator and are adjusted into first absorber and have the weak solution pipeline to be communicated with the 3rd absorber through first solution pump and the 4th solution heat exchanger; The 3rd absorber has the weak solution pipeline again through the 3rd solution pump; Second solution heat exchanger and first solution heat exchanger are communicated with first generator; Having the concentrated solution pipeline to be communicated with first absorber through second solution heat exchanger in second generator is adjusted into second generator and has concentrated solution pipeline warp second solution heat exchanger to be communicated with the 4th generator; The 4th generator has the concentrated solution pipeline to be communicated with first absorber through the 4th solution heat exchanger again; The 4th generator also has the refrigerant vapour passage to be communicated with the 3rd absorber; The 4th generator drives thermal medium pipeline and external communications in addition; The 3rd absorber also has heated medium pipeline and external communications, and forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
18. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the 17th described composite absorption heat pump; Having the weak solution pipeline to be communicated with the 3rd generator through second solution pump and the 3rd solution heat exchanger second absorber is adjusted into second absorber and has weak solution pipeline warp second solution pump and first solution heat exchanger to be communicated with first generator; The 3rd absorber there is the weak solution pipeline through the 3rd solution pump; Second solution heat exchanger and first solution heat exchanger are communicated with first generator and are adjusted into the 3rd absorber and the weak solution pipeline are arranged through the 3rd solution pump; Second solution heat exchanger and the 3rd solution heat exchanger are communicated with the 3rd generator, and forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
19. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the 6th described composite absorption heat pump; Increase the 4th generator, the 3rd absorber, the 4th solution pump and the 4th solution heat exchanger; Having the weak solution pipeline to be communicated with second generator through first solution pump and second solution heat exchanger first absorber is adjusted into first absorber and has the weak solution pipeline to be communicated with the 3rd absorber through first solution pump and the 4th solution heat exchanger; The 3rd absorber has the weak solution pipeline to be communicated with second generator through the 4th solution pump and second solution heat exchanger again; Having the concentrated solution pipeline to be communicated with first absorber through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with the 4th generator through first solution heat exchanger and second solution heat exchanger; The 4th generator has the concentrated solution pipeline to be communicated with first absorber through the 4th solution heat exchanger again; The 4th generator also has the refrigerant vapour passage to be communicated with the 3rd absorber; The 4th generator drives thermal medium pipeline and external communications in addition; The 3rd absorber also has heated medium pipeline and external communications, and forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
20. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the 19th described composite absorption heat pump; Having the weak solution pipeline to be communicated with the 3rd generator through second solution pump and the 3rd solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with second generator through second solution pump and second solution heat exchanger; Have the weak solution pipeline to be communicated with second generator through the 3rd solution pump and second solution heat exchanger the 3rd absorber and be adjusted into the 3rd absorber and have the weak solution pipeline to be communicated with the 3rd generator through the 3rd solution pump and the 3rd solution heat exchanger, forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
21. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 15-20 item; Increase by the 5th choke valve; Cancel the driving thermal medium pipeline of the 4th generator and external communications; First generator is set up the refrigerant vapour passage and is communicated with back the 4th generator with the 4th generator and has the cryogen liquid pipeline to be communicated with first condenser through the 5th choke valve again, and formation is basic with economic benefits and social benefits and has the composite absorption heat pump of backheat heat supply end.
22. with the triple effect is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 15-16 item; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; The 3rd solution pump is set up the weak solution pipeline and is communicated with newly-increased generator through newly-increased solution heat exchanger; Newly-increased generator also has the concentrated solution pipeline to be communicated with the 4th generator through newly-increased solution heat exchanger; Having the refrigerant vapour passage to be communicated with first condenser to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again; Newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser; Have the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased generator to set up the refrigerant vapour passage in second generator and is communicated with second absorber, formation is basic with the triple effect and has the composite absorption heat pump of backheat heat supply end.
23. with the triple effect is the composite absorption heat pump on basis; Be in the 17th described composite absorption heat pump; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; Having the weak solution pipeline to be communicated with second solution heat exchanger through the 3rd solution pump the 3rd absorber is adjusted into the 3rd absorber and has the weak solution pipeline to be communicated with second solution heat exchanger through the 3rd solution pump and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with the 3rd generator through second solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with newly-increased generator through second solution heat exchanger; Newly-increased generator also has the concentrated solution pipeline to be communicated with the 3rd generator through newly-increased solution heat exchanger; Having the refrigerant vapour passage to be communicated with first condenser to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again; Newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser; Have the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased generator to set up the refrigerant vapour passage in second generator and is communicated with second absorber, formation is basic with the triple effect and has the composite absorption heat pump of backheat heat supply end.
24. with the triple effect is the composite absorption heat pump on basis; Be in the 18th described composite absorption heat pump; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with the 4th generator through second solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger; Newly-increased generator also has the concentrated solution pipeline to be communicated with the 4th generator through second solution heat exchanger; Having the refrigerant vapour passage to be communicated with first condenser to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again; Newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser; Have the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased generator to set up the refrigerant vapour passage in second generator and is communicated with second absorber, formation is basic with the triple effect and has the composite absorption heat pump of backheat heat supply end.
25. with the triple effect is the composite absorption heat pump on basis; Be in the 19th described composite absorption heat pump; Increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump; Having the weak solution pipeline to be communicated with second generator through the 4th solution pump and second solution heat exchanger the 3rd absorber is adjusted into the 3rd absorber and has the weak solution pipeline to be communicated with newly-increased generator through the 4th solution pump and second solution heat exchanger; Newly-increased generator also has the concentrated solution pipeline to be communicated with second generator through newly-increased solution pump and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with the 4th generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with the 4th generator through first solution heat exchanger, newly-increased solution heat exchanger and second solution heat exchanger; Having the refrigerant vapour passage to be communicated with first condenser to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again; Newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser; Have the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased generator to set up the refrigerant vapour passage in second generator and is communicated with second absorber, formation is basic with the triple effect and has the composite absorption heat pump of backheat heat supply end.
26. with the triple effect is the composite absorption heat pump on basis; Be in the 20th described composite absorption heat pump; Increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump; Having the weak solution pipeline to be communicated with second generator through second solution pump and second solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased generator through second solution pump and second solution heat exchanger; Newly-increased generator also has the concentrated solution pipeline to be communicated with second generator through newly-increased solution pump and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with the 4th generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with the 4th generator through first solution heat exchanger, newly-increased solution heat exchanger and second solution heat exchanger; Having the refrigerant vapour passage to be communicated with first condenser to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again; Newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser; Have the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased generator to set up the refrigerant vapour passage in second generator and is communicated with second absorber, formation is basic with the triple effect and has the composite absorption heat pump of backheat heat supply end.
37. with the triple effect is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 22-26 item; Increase by the 5th choke valve; Cancel the driving thermal medium pipeline of the 4th generator and external communications; First generator is set up the refrigerant vapour passage and is communicated with back the 4th generator with the 4th generator and has the cryogen liquid pipeline to be communicated with first condenser through the 5th choke valve again, and formation is basic with the triple effect and has the composite absorption heat pump of backheat heat supply end.
28. with the triple effect is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 22-26 item; Increase by the 5th choke valve; Cancel the driving thermal medium pipeline of the 4th generator and external communications; Second generator is set up the refrigerant vapour passage and is communicated with back the 4th generator with the 4th generator and has the cryogen liquid pipeline to be communicated with first condenser through the 5th choke valve again, and formation is basic with the triple effect and has the composite absorption heat pump of backheat heat supply end.
29. with the triple effect is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 22-28 item; With first generator have the refrigerant vapour passage be communicated with the 3rd generator back the 3rd generator have again the cryogen liquid pipeline through the 3rd choke valve is communicated with second condenser be adjusted into second generator and the refrigerant vapour passage arranged and the 3rd generator is communicated with after the 3rd generator have cryogen liquid pipeline warp the 3rd choke valve to be communicated with again with second condenser, formation is basic composite absorption heat pump with the triple effect.
30. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 1-5 item; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber and external communications; The 3rd absorber has the weak solution pipeline to be communicated with dividing steam chest through the newly-increased solution choke valve and first absorber; Divide steam chest to also have the concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump; Divide steam chest to also have the refrigerant vapour passage to be communicated with the 3rd condenser; The 3rd condenser also has the cryogen liquid pipeline to be communicated with second evaporimeter through the cryogen liquid pump; Second evaporimeter also has the refrigerant vapour passage to be communicated with the 3rd absorber; The 3rd absorber also has heated medium pipeline and external communications; The 3rd condenser also has cooling medium pipeline and external communications; Second evaporimeter also have surplus heat medium pipeline and external communications, forming with economic benefits and social benefits is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 3rd condenser has the cryogen liquid pipeline to be communicated with first evaporimeter, and first evaporimeter is set up the refrigerant vapour passage and is communicated with the 3rd absorber.
31. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 6-8 item; Increase by the 4th solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber and external communications; The 3rd absorber has the weak solution pipeline to be communicated with dividing steam chest through the newly-increased solution choke valve and first absorber; Divide steam chest to also have the concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution pump; Divide steam chest to also have the refrigerant vapour passage to be communicated with the 3rd condenser; The 3rd condenser also has the cryogen liquid pipeline to be communicated with second evaporimeter through the cryogen liquid pump; Second evaporimeter also has the refrigerant vapour passage to be communicated with the 3rd absorber; The 3rd absorber also has heated medium pipeline and external communications; The 3rd condenser also has cooling medium pipeline and external communications; Second evaporimeter also have surplus heat medium pipeline and external communications, forming with economic benefits and social benefits is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 3rd condenser has the cryogen liquid pipeline to be communicated with first evaporimeter, and first evaporimeter is set up the refrigerant vapour passage and is communicated with the 3rd absorber.
32. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 1-2 item; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber and external communications; Having the concentrated solution pipeline to be communicated with first absorber through first solution heat exchanger in first generator is adjusted into first generator and has concentrated solution pipeline warp first solution heat exchanger and first absorber to be communicated with the branch steam chest; Having the concentrated solution pipeline to be communicated with first absorber through second solution heat exchanger in second generator is adjusted into second generator and has concentrated solution pipeline warp second solution heat exchanger and first absorber to be communicated with the branch steam chest; Divide steam chest to also have the concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump; The 3rd absorber also has the weak solution pipeline to be communicated with first absorber through newly-increased solution choke valve; Divide steam chest to also have the refrigerant vapour passage to be communicated with the 3rd condenser; The 3rd condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump; First evaporimeter has the cryogen liquid pipeline to be communicated with second evaporimeter through the 5th choke valve; First evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with the 3rd absorber; Second evaporimeter also has the refrigerant vapour passage to be communicated with first absorber; The 3rd absorber also has heated medium pipeline and external communications; The 3rd condenser also has cooling medium pipeline and external communications; Second evaporimeter also have surplus heat medium pipeline and external communications, forming with economic benefits and social benefits is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has the weak solution pipeline to be communicated with first absorber, and first evaporimeter is set up the refrigerant vapour passage and is communicated with first absorber.
33. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 3-5 item; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber and external communications; Having the concentrated solution pipeline to be communicated with first absorber through second solution heat exchanger in second generator is adjusted into second generator and has concentrated solution pipeline warp second solution heat exchanger and first absorber to be communicated with the branch steam chest; Divide steam chest to also have the concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump; The 3rd absorber also has the weak solution pipeline to be communicated with first absorber through newly-increased solution choke valve; Divide steam chest to also have the refrigerant vapour passage to be communicated with the 3rd condenser; The 3rd condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump; First evaporimeter has the cryogen liquid pipeline to be communicated with second evaporimeter through the 5th choke valve; First evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with the 3rd absorber; Second evaporimeter also has the refrigerant vapour passage to be communicated with first absorber; The 3rd absorber also has heated medium pipeline and external communications; The 3rd condenser also has cooling medium pipeline and external communications; Second evaporimeter also have surplus heat medium pipeline and external communications, forming with economic benefits and social benefits is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has the weak solution pipeline to be communicated with first absorber, and first evaporimeter is set up the refrigerant vapour passage and is communicated with first absorber.
34. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 6-8 item; Increase by the 4th solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber and external communications; Having the concentrated solution pipeline to be communicated with first absorber through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator concentrated solution pipeline warp first solution heat exchanger is arranged; Second solution heat exchanger and first absorber are communicated with dividing steam chest; Divide steam chest to also have the concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution pump; The 3rd absorber also has the weak solution pipeline to be communicated with first absorber through newly-increased solution choke valve; Divide steam chest to also have the refrigerant vapour passage to be communicated with the 3rd condenser; The 3rd condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump; First evaporimeter has the cryogen liquid pipeline to be communicated with second evaporimeter through the 5th choke valve; First evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with the 3rd absorber; Second evaporimeter also has the refrigerant vapour passage to be communicated with first absorber; The 3rd absorber also has heated medium pipeline and external communications; The 3rd condenser also has cooling medium pipeline and external communications; Second evaporimeter also have surplus heat medium pipeline and external communications, forming with economic benefits and social benefits is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has the weak solution pipeline to be communicated with first absorber, and first evaporimeter is set up the refrigerant vapour passage and is communicated with first absorber.
35. with the triple effect is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 9-11 item; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber and external communications; The 3rd absorber has the weak solution pipeline to be communicated with dividing steam chest through the newly-increased solution choke valve and first absorber; Divide steam chest to also have the concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump; Divide steam chest to also have the refrigerant vapour passage to be communicated with the 3rd condenser; The 3rd condenser also has the cryogen liquid pipeline to be communicated with second evaporimeter through the cryogen liquid pump; Second evaporimeter also has the refrigerant vapour passage to be communicated with the 3rd absorber; The 3rd absorber also has heated medium pipeline and external communications; The 3rd condenser also has cooling medium pipeline and external communications; Second evaporimeter also have surplus heat medium pipeline and external communications, forming with the triple effect is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 3rd condenser has the cryogen liquid pipeline to be communicated with first evaporimeter, and first evaporimeter is set up the refrigerant vapour passage and is communicated with the 3rd absorber.
36. with the triple effect is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 12-13 item; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber and external communications; The 3rd absorber has the weak solution pipeline to be communicated with dividing steam chest through the newly-increased solution choke valve and first absorber; Divide steam chest to also have the concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump; Divide steam chest to also have the refrigerant vapour passage to be communicated with the 3rd condenser; The 3rd condenser also has the cryogen liquid pipeline to be communicated with second evaporimeter through the cryogen liquid pump; Second evaporimeter also has the refrigerant vapour passage to be communicated with the 3rd absorber; The 3rd absorber also has heated medium pipeline and external communications; The 3rd condenser also has cooling medium pipeline and external communications; Second evaporimeter also have surplus heat medium pipeline and external communications, forming with the triple effect is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 3rd condenser has the cryogen liquid pipeline to be communicated with first evaporimeter, and first evaporimeter is set up the refrigerant vapour passage and is communicated with the 3rd absorber.
37. with the triple effect is the composite absorption heat pump on basis; Be in the 9th described composite absorption heat pump; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber and external communications; Having the concentrated solution pipeline to be communicated with first absorber through first solution heat exchanger in first generator is adjusted into first generator and has concentrated solution pipeline warp first solution heat exchanger and first absorber to be communicated with the branch steam chest; Having the concentrated solution pipeline to be communicated with first absorber through second solution heat exchanger in second generator is adjusted into second generator and has concentrated solution pipeline warp second solution heat exchanger and first absorber to be communicated with the branch steam chest; To increase generator newly has the concentrated solution pipeline to be communicated with first absorber through newly-increased solution heat exchanger to be adjusted into newly-increased generator and to have the concentrated solution pipeline to be communicated with the branch steam chest through increasing the solution heat exchanger and first absorber newly; Divide steam chest to also have the concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump; The 3rd absorber also has the weak solution pipeline to be communicated with first absorber through newly-increased solution choke valve; Divide steam chest to also have the refrigerant vapour passage to be communicated with the 3rd condenser; The 3rd condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump; First evaporimeter has the cryogen liquid pipeline to be communicated with second evaporimeter through the 5th choke valve; First evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with the 3rd absorber; Second evaporimeter also has the refrigerant vapour passage to be communicated with first absorber; The 3rd absorber also has heated medium pipeline and external communications; The 3rd condenser also has cooling medium pipeline and external communications; Second evaporimeter also have surplus heat medium pipeline and external communications, forming with the triple effect is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has the weak solution pipeline to be communicated with first absorber, and first evaporimeter is set up the refrigerant vapour passage and is communicated with first absorber.
38. with the triple effect is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 10-11 item; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber and external communications; To increase generator newly has the concentrated solution pipeline to be communicated with first absorber through second solution heat exchanger to be adjusted into newly-increased generator and to have concentrated solution pipeline warp second solution heat exchanger and first absorber to be communicated with the branch steam chest; Divide steam chest to also have the concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution pump; The 3rd absorber also has the weak solution pipeline to be communicated with first absorber through newly-increased solution choke valve; Divide steam chest to also have the refrigerant vapour passage to be communicated with the 3rd condenser; The 3rd condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump; First evaporimeter has the cryogen liquid pipeline to be communicated with second evaporimeter through the 5th choke valve; First evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with the 3rd absorber; Second evaporimeter also has the refrigerant vapour passage to be communicated with first absorber; The 3rd absorber also has heated medium pipeline and external communications; The 3rd condenser also has cooling medium pipeline and external communications; Second evaporimeter also have surplus heat medium pipeline and external communications, forming with the triple effect is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has the weak solution pipeline to be communicated with first absorber, and first evaporimeter is set up the refrigerant vapour passage and is communicated with first absorber.
39. with the triple effect is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 12-13 item; Increase by the 4th solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber and external communications; First generator there is the concentrated solution pipeline through first solution heat exchanger; The newly-increased solution heat exchanger and second solution heat exchanger are communicated with first absorber and are adjusted into first generator concentrated solution pipeline warp first solution heat exchanger is arranged; Newly-increased solution heat exchanger; Second solution heat exchanger and first absorber are communicated with dividing steam chest; Divide steam chest to also have the concentrated solution pipeline to be communicated with the 3rd absorber through the 4th solution pump; The 3rd absorber also has the weak solution pipeline to be communicated with first absorber through newly-increased solution choke valve; Divide steam chest to also have the refrigerant vapour passage to be communicated with the 3rd condenser; The 3rd condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump; First evaporimeter has the cryogen liquid pipeline to be communicated with second evaporimeter through the 5th choke valve; First evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with the 3rd absorber; Second evaporimeter also has the refrigerant vapour passage to be communicated with first absorber; The 3rd absorber also has heated medium pipeline and external communications; The 3rd condenser also has cooling medium pipeline and external communications; Second evaporimeter also have surplus heat medium pipeline and external communications, forming with the triple effect is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber has the weak solution pipeline to be communicated with first absorber, and first evaporimeter is set up the refrigerant vapour passage and is communicated with first absorber.
40. with the triple effect is the composite absorption heat pump on basis; Be in the described arbitrary composite absorption heat pump of 35-39 item; With first generator have the refrigerant vapour passage be communicated with the 3rd generator back the 3rd generator have again the cryogen liquid pipeline through the 3rd choke valve is communicated with second condenser be adjusted into second generator and the refrigerant vapour passage arranged and the 3rd generator is communicated with after the 3rd generator have cryogen liquid pipeline warp the 3rd choke valve to be communicated with again with second condenser, formation is basic composite absorption heat pump with the triple effect.
41. the composite absorption heat pump that is the basis with economic benefits and social benefits or triple effect; Be in the described arbitrary composite absorption heat pump of 1-40 item; Increase the first flow control valve and second flow control valve; Having heated medium pipeline and external communications to confirm as the outside respectively first condenser and second condenser has the heated medium pipeline to be communicated with back first condenser with first condenser to have the heated medium pipeline to be communicated with second condenser with external communications with through second flow control valve through the first flow control valve respectively again; Second condenser has heated medium pipeline and external communications again, forms to have the composite absorption heat pump of regulating flow distribution, being the basis with economic benefits and social benefits or triple effect.
Description of drawings:
Fig. 1 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 1st kind of structure and schematic flow sheet.
Fig. 2 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 2nd kind of structure and schematic flow sheet.
Fig. 3 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 3rd kind of structure and schematic flow sheet.
Fig. 4 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 4th kind of structure and schematic flow sheet.
Fig. 5 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 5th kind of structure and schematic flow sheet.
Fig. 6 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 6th kind of structure and schematic flow sheet.
Fig. 7 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 7th kind of structure and schematic flow sheet.
Fig. 8 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 8th kind of structure and schematic flow sheet.
Fig. 9 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 9th kind of structure and schematic flow sheet.
Figure 10 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 10th kind of structure and schematic flow sheet.
Figure 11 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 11st kind of structure and schematic flow sheet.
Figure 12 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 12nd kind of structure and schematic flow sheet.
Figure 13 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 13rd kind of structure and schematic flow sheet.
Figure 14 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 14th kind of structure and schematic flow sheet.
Figure 15 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 15th kind of structure and schematic flow sheet.
Figure 16 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 16th kind of structure and schematic flow sheet.
Figure 17 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 17th kind of structure and schematic flow sheet.
Figure 18 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 18th kind of structure and schematic flow sheet.
Figure 19 be according to provided by the present invention with economic benefits and social benefits be the basis composite absorption heat pump the 19th kind of structure and schematic flow sheet.
Figure 20 be according to provided by the present invention with the triple effect be the basis composite absorption heat pump the 1st kind of structure and schematic flow sheet.
Figure 21 be according to provided by the present invention with the triple effect be the basis composite absorption heat pump the 2nd kind of structure and schematic flow sheet.
Figure 22 be according to provided by the present invention with the triple effect be the basis composite absorption heat pump the 3rd kind of structure and schematic flow sheet.
Figure 23 be according to provided by the present invention with the triple effect be the basis composite absorption heat pump the 4th kind of structure and schematic flow sheet.
Figure 24 be according to provided by the present invention with the triple effect be the basis composite absorption heat pump the 5th kind of structure and schematic flow sheet.
Figure 25 be according to provided by the present invention with the triple effect be the basis composite absorption heat pump the 6th kind of structure and schematic flow sheet.
Figure 26 be according to provided by the present invention with the triple effect be the basis composite absorption heat pump the 7th kind of structure and schematic flow sheet.
Among the figure, 1-first generator, 2-second generator; 3-the 3rd generator, 4-first absorber, 5-second absorber; 6-first condenser, 7-second condenser, 8-evaporimeter; 9-first solution pump, 10-second solution pump, 11-first throttle valve; 12-second choke valve, 13-the 3rd choke valve, 14-the 4th choke valve; 15-first solution heat exchanger, 16-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-second evaporimeter; 26-cryogen liquid pump, 27-solution choke valve, 28-first flow control valve; 29-second flow control 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 the solution choke valve newly.
The specific embodiment:
At first be noted that in the statement of structure and flow process, do not repeat statement under the inessential situation.Describe the present invention in detail below in conjunction with accompanying drawing and instance.
Shown in Figure 1 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
① the structure, it is mainly from the first generator, the second generator, a third generator, a first absorber, the second absorber, the first condenser, second condenser, evaporator, a first solution pump, The second solution pump, the first throttle valve, the second throttle valve, a third throttle valve, a fourth throttle valve, the first solution heat exchanger, the second solution heat exchanger and a third solution composed of ; the first absorber through line 4 a dilute solution pump 9, respectively, after the first solution and then the first solution heat exchanger 15 communicating with the first generator 1 and then by the second solution heat exchanger 16 and the second generator 2 communicates the first generator 1 and the first solution through the concentrated solution conduit 15 and the first absorber heat exchanger 4 communicates, the second generator 2 has a concentrated solution via the second solution heat exchanger tube 16 and the 4 communicates a first absorber, the second absorber via line 5 with a dilute solution pump 10, the second solution and the third solution heat exchanger 17 communicates with the third generator 3, the third line generator 3 and a concentrated solution The third solution heat exchanger 17 communicates with the second absorber 5, the first steam generator 1 and refrigerant passage communicating with the second generator 2 again after the second generator 2 through the first refrigerant fluid piping throttle valve 11 communicates with the first condenser 6, the first steam generator 1 and refrigerant passage communicating with the third generator 3 generator 3 again after the third refrigerant liquid line throttle valve 13 via a third 7 communicates with the second condenser, the second generator 2 and the refrigerant vapor passage communicates with the first condenser 6, the second generator 2 and the refrigerant vapor passage 5 communicates with the second absorber, third generator 3 there is refrigerant vapor passage 7 communicates with the second condenser, a second condenser 7 and the refrigerant liquid line through the fourth throttle valve 14 communicates with the first condenser 6, a first condenser 6 and the cold agent solution line via the second throttle valve 12 communicates with the evaporator 8, evaporator 8 and the refrigerant vapor passage 4 communicates with the first absorber, an evaporator 8 and heat medium pipe communicates with the outside, the first place 1 is also driving the heat medium pipe communicates with the outside, a first absorber 4, the first condenser 6, the second absorber 5 and the second condenser 7 also were heated medium line communicates with the outside.
2. on the flow process; The weak solution of first absorber 4 gets into first generator 1 and gets into second generator 2 through second solution heat exchanger 16 again through first solution heat exchanger 15 more respectively after first solution pump 9; Drive heat medium flow and get into solution in it through first generator 1, heating and discharge and to second generator 2 and the 3rd generator 3 refrigerant vapour is provided respectively, the concentrated solution of first generator 1 gets into first absorber 4 through first solution heat exchanger 15; Flow through second generator 2, heating of refrigerant vapour gets into solution in it and discharges and to first condenser 6 and second absorber 5 refrigerant vapour is provided respectively; The concentrated solution of second generator 2 gets into first absorber 4 through second solution heat exchanger 16, and the refrigerant vapour heat release of second generator 2 of flowing through gets into first condenser 6 through first throttle valve 11 after becoming cryogen liquid again; The weak solution of second absorber 5 gets into the 3rd generator 3 through second solution pump 10 and the 3rd solution heat exchanger 17; Flow through the 3rd generator 3, heating of refrigerant vapour gets into solution in it and discharges and to second condenser 7 refrigerant vapour is provided; The concentrated solution of the 3rd generator 3 gets into second absorber 5, absorbs from the refrigerant vapour of second generator 2 and 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 gets into second condenser 7 through the 3rd choke valve 13 after becoming cryogen liquid again; The refrigerant vapour heat release of second condenser 7 becomes cryogen liquid in heated medium; The cryogen liquid of second condenser 7 gets into first condenser 6 through 14 throttlings of the 4th choke valve; The refrigerant vapour heat release of first condenser 6 becomes cryogen liquid in heated medium; The cryogen liquid of first condenser 6 gets into evaporimeter 8 through 12 throttlings of second choke valve; The absorption waste heat becomes refrigerant vapour and provides to first absorber 4; The refrigerant vapour that gets into first absorber 4 is absorbed also heat release in heated medium by the concentrated solution from first generator 1 and second generator 2, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 2 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 1; There is the weak solution pipeline to be communicated with the 3rd generator 3 second absorber 5 and is adjusted into second absorber 5 and has the weak solution pipeline to be communicated with first generator 1, have the weak solution pipeline to be communicated with first generator 1 first absorber 4 and be adjusted into first absorber 4 and have the weak solution pipeline to be communicated with the 3rd generator 3 through first solution pump 9 and the 3rd solution heat exchanger 17 through first solution pump 9 and first solution heat exchanger 15 through second solution pump 10 and first solution heat exchanger 15 through second solution pump 10 and the 3rd solution heat exchanger 17.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; The weak solution of first absorber 4 gets into the 3rd generator 3 through first solution pump 9 and the 3rd solution heat exchanger 17; The concentrated solution of the 3rd generator 3 gets into second absorber 5 through the 3rd solution heat exchanger 17; The weak solution of second absorber 5 gets into first generator 1 through second solution pump 10 and first solution heat exchanger 15; The concentrated solution of first generator 1 gets into first absorber 4 through first solution heat exchanger 15, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 3 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
① the structure, it is mainly from the first generator, the second generator, a third generator, a first absorber, the second absorber, the first condenser, second condenser, evaporator, a first solution pump, The second solution pump, the first throttle valve, the second throttle valve, a third throttle valve, a fourth throttle valve, the first solution heat exchanger, the second solution heat exchanger and a third solution composed of ; first absorber tube 4 with dilute solution pump 9 via the first solution, the second solution heat exchanger 16 and the first solution heat exchanger 15 communicates with the first generator 1, a first generator 1 and the concentrated solution solution heat exchanger 15 via the first conduit and the second generator 2 connected, the second generator 2 has a concentrated solution conduit 16 via the second solution heat exchanger 4 is connected with the first absorber, the second absorber 5 There dilute solution piping solution pump 10 via a second and third solution heat exchanger 17 communicates with the third generator 3, the third generator 3 and the concentrated solution through a third solution heat exchanger tube 17 and the second absorption 5 is connected, the first steam generator 1 and refrigerant passage communicating with the second generator 2 again after the second generator 2 refrigerant liquid line through the first throttle valve 11 communicates with the first condenser 6, The first generator is a well refrigerant vapor passage communicating with the third generator 3 generator 3 again after the third refrigerant liquid piping via a third throttle valve 13 communicates with the second condenser 7, the second generator 2 there is refrigerant vapor passage communicates with the first condenser 6, the second generator 2 and the refrigerant vapor passage 5 communicates with the second absorber, generator 3 and the third passage and a second refrigerant vapor condenser 7 connectivity, the second condenser 7 and liquid refrigerant pipes through the fourth throttle valve 14 communicates with the first condenser 6, the first condenser 6 and liquid refrigerant pipes through the second throttle valve 12 and communicating evaporator 8, evaporator 8 and the refrigerant vapor passage 4 communicates with the first absorber, an evaporator 8 and heat medium pipe communicates with the outside, the first generator 1 and the heat medium pipe driver communicates with the outside , a first absorber 4, the first condenser 6, the second absorber 5 and the second condenser 7 also were heated medium line communicates with the outside.
2. on the flow process; The weak solution of first absorber 4 gets into first generator 1 through first solution pump 9, second solution heat exchanger 16 and first solution heat exchanger 15; Drive heat medium flow and get into solution in it through first generator 1, heating and discharge and to second generator 2 and the 3rd generator 3 refrigerant vapour is provided respectively, the concentrated solution of first generator 1 gets into second generator 2 through first solution heat exchanger 15; Flow through second generator 2, heating of refrigerant vapour gets into solution in it and discharges and to first condenser 6 and second absorber 5 refrigerant vapour is provided respectively; The concentrated solution of second generator 2 gets into first absorber 4 through second solution heat exchanger 16, and the refrigerant vapour heat release of second generator 2 of flowing through gets into first condenser 6 through first throttle valve 11 after becoming cryogen liquid again; The weak solution of second absorber 5 gets into the 3rd generator 3 through second solution pump 10 and the 3rd solution heat exchanger 17; Flow through the 3rd generator 3, heating of refrigerant vapour gets into solution in it and discharges and to second condenser 7 refrigerant vapour is provided; The concentrated solution of the 3rd generator 3 gets into second absorber 5, absorbs from the refrigerant vapour of second generator 2 and 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 gets into second condenser 7 through the 3rd choke valve 13 after becoming cryogen liquid again; The refrigerant vapour heat release of second condenser 7 becomes cryogen liquid in heated medium; The cryogen liquid of second condenser 7 gets into first condenser 6 through 14 throttlings of the 4th choke valve; The refrigerant vapour heat release of first condenser 6 becomes cryogen liquid in heated medium; The cryogen liquid warp second choke valve 12 throttlings entering evaporimeter 8 of first condenser 6, absorption waste heat become refrigerant vapour and provide to first absorber 4; The refrigerant vapour that gets into first absorber 4 is absorbed also heat release in heated medium by the concentrated solution from second generator 2, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 4 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 3; Having the weak solution pipeline to be communicated with the 3rd generator 3 through second solution pump 10 and the 3rd solution heat exchanger 17 second absorber 5 is adjusted into second absorber 5 and has weak solution pipeline warp second solution pump 10 and first solution heat exchanger 15 to be communicated with first generator 1, first absorber 4 is had weak solution pipeline warp first solution pump 9; Second solution heat exchanger 16 and first solution heat exchanger 15 are communicated with first generator 1 and are adjusted into first absorber 4 and the weak solution pipeline are arranged through first solution pump 9; Second solution heat exchanger 16 and the 3rd solution heat exchanger 17 are communicated with the 3rd generator 3.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; The weak solution of first absorber 4 is through first solution pump 9; Second solution heat exchanger 16 and the 3rd solution heat exchanger 17 get into the 3rd generator 3; The concentrated solution of the 3rd generator 3 gets into second absorber 5 through the 3rd solution heat exchanger 17; The weak solution of second absorber 5 gets into first generator 1 through second solution pump 10 and first solution heat exchanger 15; The concentrated solution of first generator 1 gets into second generator 2 through first solution heat exchanger 15; The concentrated solution of second generator 2 gets into first absorber 4 through second solution heat exchanger 16, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 5 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
① the structure, it is mainly from the first generator, the second generator, a third generator, a first absorber, the second absorber, the first condenser, second condenser, evaporator, a first solution pump, The second solution pump, a third solution pump, the first throttle valve, the second throttle valve, a third throttle valve, a fourth throttle valve, the first solution heat exchanger, a third heat exchanger and the second solution solution heat exchanger component; first absorber 4 is a dilute solution via the first solution pump conduit 9 and the second solution heat exchanger 16 communicates with the second generator 2, the second generator 2 has a concentrated solution via line The third solution is the solution pump 18 and the first heat exchanger 15 communicates with the first generator 1, a first generator 1 and the concentrated solution conduit 15 via the first solution and the second solution heat exchanger 16 and the first an absorber 4 is connected, the second absorber via line 5 with a dilute solution pump 10, the second solution and the third solution heat exchanger 17 communicates with the third generator 3, third generator via line 3 and a concentrated solution The third solution heat exchanger 17 communicates with the second absorber 5, the first steam generator 1 and refrigerant passage communicating with the second generator 2 2 again after the second generator liquid refrigerant piping by Section flow valve 11 communicates with the first condenser 6, the first steam generator 1 and refrigerant passage communicating with the third generator 3 generator 3 again after the third refrigerant liquid line throttle valve 13 via a third communicating the second condenser 7, the second generator 2 and the refrigerant vapor passage communicates with the first condenser 6, the second generator 2 and the refrigerant vapor passage 5 communicates with the second absorber, and the third generator 3 There refrigerant vapor passage 7 communicates with the second condenser, a second condenser 7 and the refrigerant liquid line through the fourth throttle valve 14 communicates with the first condenser 6, a first condenser 6 and the refrigerant liquid conduit 12 via the second throttle valve 8 communicates with the evaporator, the evaporator 8 and the refrigerant vapor passage 4 communicates with the first absorber, an evaporator 8 and communicates with the outside heat medium line, first generator 1 and drive the heat medium pipe communicates with the outside, a first absorber 4, the first condenser 6, the second absorber 5 and the second condenser 7 also were heated medium line communicates with the outside.
② the process, the first generator 1 generates a refrigerant vapor generator 2 are supplied to the second and third heat medium is used to drive generator 3, a first dilute solution absorber 4 via the first solution pump 9 and the second solution heat exchanger 16 to the second generator 2, the refrigerant vapor flowing through the second generator 2, heating the solution into its release and, respectively, to the first condenser 6 and the second absorber to provide refrigerant vapor 5, the first two generator 2 via the third solution, a concentrated solution pump 18 and the first solution heat exchanger 15 into the first generator 1, the generator 2 through the second refrigerant vapor after the exothermic liquid refrigerant through the first throttle 11 into the first condenser 6; drive the heat medium flowing through the first generator 1, the solution is heated into its release and, respectively, to the second generator 2 and the third refrigerant vapor generator 3 to provide the first concentrated solution of the generator 1 via the first solution and the second solution heat exchanger 15 into the first heat exchanger 16 and the absorber 4; second dilute solution absorber 5 is the solution pump 10 via the second and third solution heat exchanger 3 into the third generator 17, the refrigerant flows through the third steam generator 3, the solution is heated into its release to the second refrigerant vapor condenser 7 provides, third generator 3 via the third solution is a concentrated solution 17 into the second absorber heat exchanger 5, the absorption from the second refrigerant vapor generator 2 and the heat in the heating medium flowing through the third refrigerant vapor generator 3 exothermic liquid refrigerant then by The third throttle valve 13 into the second condenser 7; second refrigerant vapor condenser 7, the heating medium into the heat in the refrigerant liquid, the second liquid refrigerant in the condenser 7, the throttle valve 14 through the fourth 6 flow into the first condenser, the first condenser 6, the refrigerant vapor is heated heat medium in a liquid refrigerant, the first condenser 6, the refrigerant liquid through the second throttle valve 12 into the evaporator throttle 8 , absorbing heat into the refrigerant vapor to provide the first absorber 4, enters the first absorber 4 from the first refrigerant vapor is absorbed by the solution concentration of the generator 1 and the heat in the heating medium to form a double effect as based composite absorption heat pump.
Shown in Figure 6 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
In composite absorption heat pump shown in Figure 5; Increase the solution choke valve; With first absorber 4 have the weak solution pipeline through first solution pump 9 and second solution heat exchanger 16 is communicated with second generator 2 be adjusted into first absorber 4 have the weak solution pipeline through first solution pump 9 and second solution heat exchanger 16 afterwards difference directly be communicated with second generator 2 through solution choke valve 27 again with first generator, 1 connected sum, formation is basic composite absorption heat pump with economic benefits and social benefits.
Shown in Figure 7 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 5; There is the weak solution pipeline to be communicated with the 3rd generator 3 second absorber 5 and is adjusted into second absorber 5 and has the weak solution pipeline to be communicated with second generator 2, have the weak solution pipeline to be communicated with second generator 2 first absorber 4 and be adjusted into first absorber 4 and have the weak solution pipeline to be communicated with the 3rd generator 3 through first solution pump 9 and the 3rd solution heat exchanger 17 through first solution pump 9 and second solution heat exchanger 16 through second solution pump 10 and second solution heat exchanger 16 through second solution pump 10 and the 3rd solution heat exchanger 17.
② the process, the first generator 1 refrigerant vapor generated are supplied to the second generator 2 and the generator 3 is used to drive the third heat medium, the second generator 2 generates a vapor refrigerant to the first condenser 6, respectively, 5 provides the second absorber; first absorber 4 is a dilute solution of the solution pump 9 via the first and third solution heat exchanger 17 into the third generator 3, the third generator 3 via the third solution is a concentrated solution of heat exchanger 17 into the second absorber 5, a second dilute solution absorber 5 via the second solution pump 10 and the second solution heat exchanger 16 to the second generator 2, a concentrated solution of the second generator 2 via the third solution pump 18 and the first solution heat exchanger 15 into the first generator 1, a concentrated solution of the first generator 1 via the first solution and the second solution heat exchanger 15 into the first heat exchanger 16 and the absorber 4, to form based double effect absorption heat pump combined.
Shown in Figure 8 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 1; Increase the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger; First absorber 4 had the weak solution pipeline after first solution pump 9, to be communicated with first solution heat exchanger 15 and second solution heat exchanger 16 respectively to be adjusted into first absorber 4 has the weak solution pipeline to be communicated with the 3rd absorber 20 through first solution pump 9 and the 4th solution heat exchanger 21; The 3rd absorber 20 has the weak solution pipeline after the 3rd solution pump 18, to be communicated with first solution heat exchanger 15 and second solution heat exchanger 16 respectively again; Having the concentrated solution pipeline to be communicated with first absorber 4 through first solution heat exchanger 15 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with the 4th generator 19 through first solution heat exchanger 15; Having the concentrated solution pipeline to be communicated with first absorber 4 through second solution heat exchanger 16 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with the 4th generator 19 through second solution heat exchanger 16; The 4th generator 19 has the concentrated solution pipeline to be communicated with first absorber 4 through the 4th solution heat exchanger 21 again; The 4th generator 19 also has the refrigerant vapour passage to be communicated with the 3rd absorber 20; The 4th generator 19 drives thermal medium pipeline and external communications in addition, and the 3rd absorber 20 also has heated medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; The weak solution of first absorber 4 gets into the 3rd absorber 20, absorbs from the refrigerant vapour of the 4th generator 19 and heat release in heated medium through first solution pump 9 and the 4th solution heat exchanger 21, and the weak solution of the 3rd absorber 20 gets into first generators 1 and warp second solution heat exchanger 16 entering second generator 2 again through first solution heat exchanger 15 respectively again after the 3rd solution pump 18; The concentrated solution of first generator 1 gets into the 4th generator 19 through first solution heat exchanger 15; The concentrated solution of second generator 2 gets into the 4th generator 19 through second solution heat exchanger 16; Driving heat medium flow gets into solution in it through the 4th generator 19, heating and discharges and to the 3rd absorber 20 refrigerant vapour is provided; The concentrated solution of the 4th generator 19 gets into first absorber 4 through the 4th solution heat exchanger 21, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 9 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 3; Increase by the 4th generator; The 3rd absorber; The 3rd solution pump and the 4th solution heat exchanger; First absorber 4 there is the weak solution pipeline through first solution pump 9; Second solution heat exchanger 16 and first solution heat exchanger 15 are communicated with first generator 1 and are adjusted into first absorber 4 and have the weak solution pipeline to be communicated with the 3rd absorber 20 through first solution pump 9 and the 4th solution heat exchanger 21; The 3rd absorber 20 has the weak solution pipeline again through the 3rd solution pump 18; Second solution heat exchanger 16 and first solution heat exchanger 15 are communicated with first generator 1; Having the concentrated solution pipeline to be communicated with first absorber 4 through second solution heat exchanger 16 in second generator 2 is adjusted into second generator 2 and has concentrated solution pipeline warp second solution heat exchanger 16 to be communicated with the 4th generator 19; The 4th generator 19 has the concentrated solution pipeline to be communicated with first absorber 4 through the 4th solution heat exchanger 21 again; The 4th generator 19 also has the refrigerant vapour passage to be communicated with the 3rd absorber 20; The 4th generator 19 drives thermal medium pipeline and external communications in addition, and the 3rd absorber 20 also has heated medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; The weak solution of first absorber 4 gets into the 3rd absorber 20, absorbs from the refrigerant vapour of the 4th generator 19 and heat release in heated medium through first solution pump 9 and the 4th solution heat exchanger 21, and the weak solution of the 3rd absorber 20 is through the 3rd solution pump 18, second solution heat exchanger 16 and first solution heat exchanger, 15 entering, first generator 1; The concentrated solution of first generator 1 gets into second generator 2 through first solution heat exchanger 15; The concentrated solution of second generator 2 gets into the 4th generator 19 through second solution heat exchanger 16; Driving heat medium flow gets into solution in it through the 4th generator 19, heating and discharges and to the 3rd absorber 20 refrigerant vapour is provided; The concentrated solution of the 4th generator 19 gets into first absorber 4 through the 4th solution heat exchanger 21, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 10 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 5; Increase the 4th generator, the 3rd absorber, the 4th solution pump and the 4th solution heat exchanger; Having the weak solution pipeline to be communicated with second generator 2 through first solution pump 9 and second solution heat exchanger 16 first absorber 4 is adjusted into first absorber 4 and has the weak solution pipeline to be communicated with the 3rd absorber 20 through first solution pump 9 and the 4th solution heat exchanger 21; The 3rd absorber 20 has the weak solution pipeline to be communicated with second generator 2 through the 4th solution pump 30 and second solution heat exchanger 16 again; Having the concentrated solution pipeline to be communicated with first absorber 4 through first solution heat exchanger 15 and second solution heat exchanger 16 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with the 4th generator 19 through first solution heat exchanger 15 and second solution heat exchanger 16; The 4th generator 19 has the concentrated solution pipeline to be communicated with first absorber 4 through the 4th solution heat exchanger 21 again; The 4th generator 19 also has the refrigerant vapour passage to be communicated with the 3rd absorber 20; The 4th generator 19 drives thermal medium pipeline and external communications in addition, and the 3rd absorber 20 also has heated medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; The weak solution of first absorber 4 gets into the 3rd absorber 20, absorbs from the refrigerant vapour of the 4th generator 19 and heat release in heated medium through first solution pump 9 and the 4th solution heat exchanger 21, and the weak solution of the 3rd absorber 20 is through the 4th solution pump 30 and second solution heat exchanger, 16 entering, second generator 2; The concentrated solution of second generator 2 gets into first generator 1 through the 3rd solution pump 18 and first solution heat exchanger 15; The concentrated solution of first generator 1 gets into the 4th generator 19 through first solution heat exchanger 15 and second solution heat exchanger 16; Driving heat medium flow gets into solution in it through the 4th generator 19, heating and discharges and to the 3rd absorber 20 refrigerant vapour is provided; The concentrated solution of the 4th generator 19 gets into first absorber 4 through the 4th solution heat exchanger 21, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 11 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
In composite absorption heat pump shown in Figure 9; Increase by the 5th choke valve; Cancel the driving thermal medium pipeline of the 4th generator 19 and external communications, first generator 1 is set up the refrigerant vapour passage and is communicated with the 4th generator 19 afterwards that the 4th generator 19 has cryogen liquid pipeline warp the 5th choke valve 22 to be communicated with first condenser 6 again; The refrigerant vapour that first generator 1 produces provides refrigerant vapour to make to drive thermal medium to second generator 2, the 3rd generator 3 and the 4th generator 19 respectively, and forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
Shown in Figure 12 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
In composite absorption heat pump shown in Figure 2; Increase the first flow control valve and second flow control valve; Having heated medium pipeline and external communications to confirm as the outside respectively first condenser 6 and second condenser 7 has the heated medium pipeline to be communicated with back first condenser 6 with first condenser 6 to have the heated medium pipeline to be communicated with second condenser 7 with external communications and warp second flow control valve 29 through first flow control valve 28 respectively again, and second condenser 7 has heated medium pipeline and external communications again; Close first flow control valve 28 and when opening second flow control valve 29, heated medium full flow flow through successively first condenser 6 and second condenser 7; Open first flow control valve 28 and when closing second flow control valve 29, heated medium full flow first condenser 6 of only flowing through; When the first flow control valve 28 and second flow control valve 29 are all opened, heated medium full flow first condenser 6 and partial discharge second condenser 7 of flowing through of flowing through, formation can be regulated flow distribution, be the composite absorption heat pump on basis with economic benefits and social benefits.
Shown in Figure 13 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 1; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; Cryogen liquid pump and newly-increased solution choke valve; Cancel the heated medium pipeline of first absorber 4 and external communications; The 3rd absorber 20 has the weak solution pipeline to be communicated with dividing steam chest 23 through the newly-increased solution choke valve E and first absorber 4; Divide steam chest 23 to also have the concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18; Divide steam chest 23 to also have the refrigerant vapour passage to be communicated with the 3rd condenser 24; The 3rd condenser 24 also has the cryogen liquid pipeline to be communicated with second evaporimeter 25 through cryogen liquid pump 26; Second evaporimeter 25 also has the refrigerant vapour passage to be communicated with the 3rd absorber 20; The 3rd absorber 20 also has heated medium pipeline and external communications; The 3rd condenser 24 also has cooling medium pipeline and external communications, second evaporimeter 25 also have surplus heat medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; Get into first absorber 4, absorb from the refrigerant vapour of first evaporimeter 8 and heat release from the concentrated solution of first generator 1 and second generator 2 in the solution of first absorber 4 of flowing through; The weak solution of the 3rd absorber 20 is through newly-increased solution choke valve E throttling step-down, first absorber, the 4 heat absorbing parts vaporization back of flowing through gets into a minute steam chest 23 again; Divide the refrigerant vapour of steam chest 23 to get into the 3rd condenser 24, the concentrated solution of dividing steam chest 23 gets into the 3rd absorber 20, absorbs from the refrigerant vapour of second evaporimeter 25 and 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 gets into second evaporimeter 25, absorbs waste heat and become refrigerant vapour and provide to the 3rd absorber 20 through cryogen liquid pump 26 pressurization, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 14 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 2; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel the heated medium pipeline of first absorber 4 and external communications; Having the concentrated solution pipeline to be communicated with first absorber 4 through first solution heat exchanger 15 in first generator 1 is adjusted into first generator 1 and has concentrated solution pipeline warp first solution heat exchanger 15 and first absorber 4 to be communicated with branch steam chest 23; Having the concentrated solution pipeline to be communicated with first absorber 4 through second solution heat exchanger 16 in second generator 2 is adjusted into second generator 2 and has concentrated solution pipeline warp second solution heat exchanger 16 and first absorber 4 to be communicated with branch steam chest 23; Divide steam chest 23 to also have the concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18; The 3rd absorber 20 also has the weak solution pipeline to be communicated with first absorber 4 through newly-increased solution choke valve E; Divide steam chest 23 to also have the refrigerant vapour passage to be communicated with the 3rd condenser 24; The 3rd condenser 24 also has the cryogen liquid pipeline to be communicated with first evaporimeter 8 through cryogen liquid pump 26; First evaporimeter 8 also has the cryogen liquid pipeline to be communicated with second evaporimeter 25 through the 5th choke valve 22; First evaporimeter 8 had the refrigerant vapour passage to be communicated with first absorber 4 to be adjusted into first evaporimeter 8 has the refrigerant vapour passage to be communicated with the 3rd absorber 20; Second evaporimeter 25 also has the refrigerant vapour passage to be communicated with first absorber 4; The 3rd absorber 20 also has heated medium pipeline and external communications; The 3rd condenser 24 also has cooling medium pipeline and external communications, second evaporimeter 25 also have surplus heat medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; The concentrated solution of first generator 1 is through getting into and divide steam chest 23 with first absorber, the 4 heat absorbing parts vaporization that converges, flows through of the concentrated solution of second generator 2 after second solution heat exchanger 16 after first solution heat exchanger 15; Divide the refrigerant vapour of steam chest 23 to get into the 3rd condenser 24, the concentrated solution of dividing steam chest 23 gets into the 3rd absorber 20, absorbs from the refrigerant vapour of first evaporimeter 8 and heat release in heated medium through the 3rd solution pump 18; The weak solution of the 3rd absorber 20 gets into first absorber 4, absorbs from the refrigerant vapour of second evaporimeter 25 and heat release in the solution of first absorber 4 of flowing through through newly-increased solution choke valve E throttling step-down; The refrigerant vapour heat release of the 3rd condenser 24 becomes cryogen liquid in cooling medium; The cryogen liquid of the 3rd condenser 24 gets into first evaporimeter 8 through cryogen liquid pump 26; The cryogen liquid of evaporimeter 8 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to the 3rd absorber 20; The second the tunnel gets into second evaporimeter 25, absorbs waste heat and become refrigerant vapour and provide to first absorber 4 through the 5th choke valve, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 15 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 1; Increase the 3rd solution pump, the 3rd absorber, divide steam chest, the 3rd condenser and cryogen liquid pump; Cancel the heated medium pipeline of first absorber 4 and external communications; Having the concentrated solution pipeline to be communicated with first absorber 4 through first solution heat exchanger 15 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with dividing steam chest 23 through first solution heat exchanger 15 and first absorber 4; Having the concentrated solution pipeline to be communicated with first absorber 4 through second solution heat exchanger 16 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with dividing steam chest 23 through second solution heat exchanger 16 and first absorber 4; Divide steam chest 23 to also have the concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18; The 3rd absorber 20 also has the weak solution pipeline to be communicated with first absorber 4; Divide steam chest 23 to also have the refrigerant vapour passage to be communicated with the 3rd condenser 24; The 3rd condenser 24 also has the cryogen liquid pipeline to be communicated with evaporimeter 8 through cryogen liquid pump 26; Evaporimeter 8 is set up the refrigerant vapour passage and is communicated with the 3rd absorber 20; The 3rd absorber 20 also has heated medium pipeline and external communications, and the 3rd condenser 24 also has cooling medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; The concentrated solution of first generator 1 is through getting into and divide steam chest 23 with first absorber, the 4 heat absorbing parts vaporization that converges, flows through of the concentrated solution of second generator 2 after second solution heat exchanger 16 after first solution heat exchanger 15; Divide the refrigerant vapour of steam chest 23 to get into the 3rd condenser 24, the concentrated solution of dividing steam chest 23 through the 3rd solution pump 18 get into the 3rd absorber 20, the refrigerant vapour and the heat release that absorb flash-pot 8 be in heated medium; The weak solution of the 3rd absorber 20 gets into first absorber 4, the refrigerant vapour that absorbs flash-pot 8 and 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 gets into evaporimeter 8 through cryogen liquid pump 26; The cryogen liquid of evaporimeter 8 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to the 3rd absorber 20; The second tunnel absorption waste heat becomes refrigerant vapour and provides to first absorber 4, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 16 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 3; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; Cryogen liquid pump and newly-increased solution choke valve; The 3rd absorber 20 has the weak solution pipeline to be communicated with dividing steam chest 23 through the newly-increased solution choke valve E and first absorber 4; Divide steam chest 23 to also have the concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18; Divide steam chest 23 to also have the refrigerant vapour passage to be communicated with the 3rd condenser 24; The 3rd condenser 24 also has the cryogen liquid pipeline to be communicated with second evaporimeter 25 through cryogen liquid pump 26; Second evaporimeter 25 also has the refrigerant vapour passage to be communicated with the 3rd absorber 20; The 3rd absorber 20 also has heated medium pipeline and external communications; The 3rd condenser 24 also has cooling medium pipeline and external communications, second evaporimeter 25 also have surplus heat medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; The concentrated solution of second generator 2 through second solution heat exchanger 16 get into first absorber 4, absorb from the refrigerant vapour of first evaporimeter 8 and respectively heat release in the solution of the heated medium and first absorber 4 of flowing through; The weak solution of the 3rd absorber 20 is through newly-increased solution choke valve E throttling step-down, first absorber, the 4 heat absorbing parts vaporization back of flowing through gets into a minute steam chest 23 again; Divide the refrigerant vapour of steam chest 23 to get into the 3rd condenser 24, the concentrated solution of dividing steam chest 23 gets into the 3rd absorber 20, absorbs from the refrigerant vapour of second evaporimeter 25 and 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 gets into second evaporimeter 25, absorbs waste heat and become refrigerant vapour and provide to the 3rd absorber 20 through cryogen liquid pump 26 pressurization, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 17 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 3; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser and cryogen liquid pump; Cancel the heated medium pipeline of first absorber 4 and external communications; Having the concentrated solution pipeline to be communicated with first absorber 4 through second solution heat exchanger 16 in second generator 2 is adjusted into second generator 2 and has concentrated solution pipeline warp second solution heat exchanger 16 and first absorber 4 to be communicated with branch steam chest 23; Divide steam chest 23 to also have the concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 3rd solution pump 18; The 3rd absorber 20 also has the weak solution pipeline to be communicated with first absorber 4; Divide steam chest 23 to also have the refrigerant vapour passage to be communicated with the 3rd condenser 24; The 3rd condenser 24 also has the cryogen liquid pipeline to be communicated with evaporimeter 8 through cryogen liquid pump 26; Evaporimeter 8 is set up the refrigerant vapour passage and is communicated with the 3rd absorber 20; The 3rd absorber 20 also has heated medium pipeline and external communications, and the 3rd condenser 24 also has cooling medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; After second solution heat exchanger 16, flow through again first absorber 4, heat absorbing part vaporization of the concentrated solution of second generator 2 gets into and divides steam chest 23; Divide the refrigerant vapour of steam chest 23 to get into the 3rd condenser 24, the concentrated solution of dividing steam chest 23 through the 3rd solution pump 18 get into the 3rd absorber 20, the refrigerant vapour and the heat release that absorb flash-pot 8 be in heated medium; The weak solution of the 3rd absorber 20 gets into first absorber 4, the refrigerant vapour that absorbs flash-pot 8 and 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 gets into evaporimeter 8 through cryogen liquid pump 26; The cryogen liquid of evaporimeter 8 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to the 3rd absorber 20; The second tunnel absorption waste heat becomes refrigerant vapour and provides to first absorber 4, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 180 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 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 heated medium pipeline of first absorber 4 and external communications; The 3rd absorber 20 has the weak solution pipeline to be communicated with dividing steam chest 23 through the newly-increased solution choke valve E and first absorber 4; Divide steam chest 23 to also have the concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 4th solution pump 30; Divide steam chest 23 to also have the refrigerant vapour passage to be communicated with the 3rd condenser 24; The 3rd condenser 24 also has the cryogen liquid pipeline to be communicated with evaporimeter 8 through cryogen liquid pump 26; Evaporimeter 25 is set up the refrigerant vapour passage and is communicated with the 3rd absorber 20; The 3rd absorber 20 also has heated medium pipeline and external communications, and the 3rd condenser 24 also has cooling medium pipeline and external communications.
2. on the flow process; The refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium; The refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively, and refrigerant vapour and heat release that the concentrated solution of first generator 1 is come flash-pot 8 through first solution heat exchanger 15 and second solution heat exchanger, 16 entering, first absorber 4, absorption are in the solution of first absorber 4 of flowing through; The weak solution of the 3rd absorber 20 is through newly-increased solution choke valve E throttling step-down, first absorber, the 4 heat absorbing parts vaporization back of flowing through gets into a minute steam chest 23 again; Divide steam chest 23 refrigerant vapours to get into the 3rd condenser 24, the concentrated solution of dividing steam chest 23 through the 4th solution pump 30 get into the 3rd absorber 20, the refrigerant vapour and the heat release that absorb flash-pot 8 be in heated medium; The refrigerant vapour heat release of the 3rd condenser 24 becomes cryogen liquid in cooling medium; The cryogen liquid of the 3rd condenser 24 gets into evaporimeter 8 through cryogen liquid pump 26; The cryogen liquid of evaporimeter 8 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to the 3rd absorber 20; The second tunnel absorption waste heat becomes refrigerant vapour and provides to first absorber 4, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 19 is that basic composite absorption heat pump is achieved in that with economic benefits and social benefits
1. on the structure; In composite absorption heat pump shown in Figure 5; Increase by the 4th solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser and cryogen liquid pump; Cancel the heated medium pipeline of first absorber 4 and external communications; Having the concentrated solution pipeline to be communicated with first absorber 4 through first solution heat exchanger 15 and second solution heat exchanger 16 in first generator 1 is adjusted into first generator 1 concentrated solution pipeline warp first solution heat exchanger 15 is arranged; Second solution heat exchanger 16 and first absorber 4 are communicated with dividing steam chest 23; Divide steam chest 23 to also have the concentrated solution pipeline to be communicated with the 3rd absorber 20 through the 4th solution pump 30; The 3rd absorber 20 also has the weak solution pipeline to be communicated with first absorber 4; Divide steam chest 23 to also have the refrigerant vapour passage to be communicated with the 3rd condenser 24; The 3rd condenser 24 also has the cryogen liquid pipeline to be communicated with evaporimeter 8 through cryogen liquid pump 26; Evaporimeter 8 is set up the refrigerant vapour passage and is communicated with the 3rd absorber 20; The 3rd absorber 20 also has heated medium pipeline and external communications, and the 3rd condenser 24 also has cooling medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces provides to first condenser 6 and second absorber 5 respectively; After first solution heat exchanger 15 and second solution heat exchanger 16, flow through again first absorber 4, heat absorbing part vaporization of the concentrated solution of first generator 1 gets into branch steam chest 23; Divide the refrigerant vapour of steam chest 23 to get into the 3rd condenser 24; The concentrated solution of dividing steam chest 23 through the 4th solution pump 30 get into the 3rd absorber 20, the refrigerant vapour and the heat release that absorb flash-pot 8 be in heated medium, refrigerant vapour and heat release that the weak solution of the 3rd absorber 20 gets into first absorber 4, absorb flash-pot 8 are 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 gets into evaporimeter 8 through cryogen liquid pump 26; The cryogen liquid of evaporimeter 8 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to the 3rd absorber 20; The second tunnel absorption waste heat becomes refrigerant vapour and provides to first absorber 4, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
Shown in Figure 20 is that basic composite absorption heat pump is achieved in that with the triple effect
1. on the structure; In composite absorption heat pump shown in Figure 1; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; First solution pump 9 is set up the weak solution pipeline and is communicated with newly-increased generator A through newly-increased solution heat exchanger C; Newly-increased generator A also has the concentrated solution pipeline to be communicated with first absorber 4 through newly-increased solution heat exchanger C; Having the refrigerant vapour passage to be communicated with first condenser 6 to be adjusted into second generator 2 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first condenser 6 through newly-increased choke valve B again; Newly-increased generator A also has the refrigerant vapour passage to be communicated with first condenser 6; Have the refrigerant vapour passage to be communicated with to be adjusted into newly-increased generator A to set up the refrigerant vapour passage in second generator 2 and be communicated with second absorber 5 with second absorber 5, with first generator 1 have the refrigerant vapour passage be communicated with the 3rd generator 3 afterwards the 3rd generator 3 have again the cryogen liquid pipeline through the 3rd choke valve 13 be communicated with second condenser 7 be adjusted into second generator 2 and the refrigerant vapour passage arranged and the 3rd generator 3 is communicated with after the 3rd generator 3 have the cryogen liquid pipeline to be communicated with second condenser 7 again through the 3rd choke valve 13.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 and makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces offers newly-increased generator A respectively and the 3rd generator 3 makes to drive thermal medium; A part of weak solution of first absorber 4 gets into newly-increased generator A through first solution pump 9 with newly-increased solution heat exchanger C; Refrigerant vapour is flowed through and is increased generator A newly, heating gets into solution release in it and to first condenser 6 and second absorber 5 refrigerant vapour is provided respectively; The concentrated solution of newly-increased generator A gets into first absorber 4 through newly-increased solution heat exchanger C; The refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, gets into first condenser 6 through newly-increased choke valve B throttling again, and forming with the triple effect is the composite absorption heat pump on basis.
Shown in Figure 21 is that basic composite absorption heat pump is achieved in that with the triple effect
1. on the structure; In composite absorption heat pump shown in Figure 2; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; First solution pump 9 is set up the weak solution pipeline and is communicated with newly-increased generator A through newly-increased solution heat exchanger C; Newly-increased generator A also has the concentrated solution pipeline to be communicated with first absorber 4 through newly-increased solution heat exchanger C; Having the refrigerant vapour passage to be communicated with first condenser 6 to be adjusted into second generator 2 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first condenser 6 through newly-increased choke valve B again; Newly-increased generator A also has the refrigerant vapour passage to be communicated with first condenser 6; Have the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into newly-increased generator A to set up the refrigerant vapour passage in second generator 2 and is communicated with second absorber 5, formation is basic composite absorption heat pump with the triple effect.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium; A part of weak solution of first absorber 4 gets into newly-increased generator A through first solution pump 9 with newly-increased solution heat exchanger C; Refrigerant vapour is flowed through and is increased generator A newly, heating gets into solution release in it and to first condenser 6 and second absorber 5 refrigerant vapour is provided respectively; The concentrated solution of newly-increased generator A gets into first absorber 4 through newly-increased solution heat exchanger C; The refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, gets into first condenser 6 through newly-increased choke valve B throttling again, and forming with the triple effect is the composite absorption heat pump on basis.
Shown in Figure 22 is that basic composite absorption heat pump is achieved in that with the triple effect
1. on the structure; In composite absorption heat pump shown in Figure 3; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; Having the weak solution pipeline to be communicated with second solution heat exchanger 16 through first solution pump 9 first absorber 4 is adjusted into first absorber 4 and has the weak solution pipeline to be communicated with second solution heat exchanger 16 with newly-increased solution heat exchanger C through first solution pump 9; Having the concentrated solution pipeline to be communicated with first absorber 4 through second solution heat exchanger 16 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with newly-increased generator A through second solution heat exchanger 16; Newly-increased generator A has the concentrated solution pipeline to be communicated with first absorber 4 through newly-increased solution heat exchanger C again; Having the refrigerant vapour passage to be communicated with first condenser 6 to be adjusted into second generator 2 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first condenser 6 through newly-increased choke valve B again; Newly-increased generator A also has the refrigerant vapour passage to be communicated with first condenser 6; Have the refrigerant vapour passage to be communicated with to be adjusted into newly-increased generator A to set up the refrigerant vapour passage in second generator 2 and be communicated with second absorber 5 with second absorber 5, with first generator 1 have the refrigerant vapour passage be communicated with the 3rd generator 3 afterwards the 3rd generator 3 have again the cryogen liquid pipeline through the 3rd choke valve 13 be communicated with second condenser 7 be adjusted into second generator 2 and the refrigerant vapour passage arranged and the 3rd generator 3 is communicated with after the 3rd generator 3 have the cryogen liquid pipeline to be communicated with second condenser 7 again through the 3rd choke valve 13.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 and makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces offers newly-increased generator A respectively and the 3rd generator 3 makes to drive thermal medium; The weak solution of first absorber 4 is through newly-increased solution heat exchanger C; Second solution heat exchanger 16 and first solution heat exchanger 15 get into first generator 1; The concentrated solution of first generator 1 gets into second generator 2 through first solution heat exchanger 15; The concentrated solution of second generator 2 gets into newly-increased generator A through second solution heat exchanger 16; Refrigerant vapour is flowed through and is increased generator A newly; Heating gets into the solution release in it and to first condenser 6 and second absorber 5 refrigerant vapour is provided respectively; The concentrated solution of newly-increased generator A gets into first absorber 4 through newly-increased solution heat exchanger C; The refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid; Get into first condenser 6 through newly-increased choke valve B throttling again, forming with the triple effect is the composite absorption heat pump on basis.
Shown in Figure 23 is that basic composite absorption heat pump is achieved in that with the triple effect
1. on the structure; In composite absorption heat pump shown in Figure 4; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with second generator 2 through first solution heat exchanger 15 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with second generator 2 with newly-increased solution heat exchanger C through first solution heat exchanger 15; Having the concentrated solution pipeline to be communicated with first absorber 4 through second solution heat exchanger 16 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased solution heat exchanger C; Newly-increased generator A also has the concentrated solution pipeline to be communicated with first absorber 4 through second solution heat exchanger 16; Having the refrigerant vapour passage to be communicated with first condenser 6 to be adjusted into second generator 2 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first condenser 6 through newly-increased choke valve B again; Newly-increased generator A also has the refrigerant vapour passage to be communicated with first condenser 6, second generator 2 is had the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into increase generator A newly and set up the refrigerant vapour passage and be communicated with second absorber 5.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers second generator 2 respectively and the 3rd generator 3 makes to drive thermal medium, and the refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium; The weak solution of first absorber 4 is through first solution pump 9; Second solution heat exchanger 16 and the 3rd solution heat exchanger 17 get into the 3rd generator 3; The concentrated solution of the 3rd generator 3 gets into second absorber 5 through the 3rd solution heat exchanger 17; The weak solution of second absorber 5 gets into first generator 1 through second solution pump 10 and first solution heat exchanger 15; The concentrated solution of first generator 1 gets into second generator 2 through first solution heat exchanger 15 with newly-increased solution heat exchanger C; The concentrated solution of second generator 2 gets into newly-increased generator A through newly-increased solution heat exchanger C; Refrigerant vapour is flowed through and is increased generator A newly; Heating gets into the solution release in it and to first condenser 6 and second absorber 5 refrigerant vapour is provided respectively; The concentrated solution of newly-increased generator A gets into first absorber 4 through second solution heat exchanger 16; The refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid; Get into first condenser 6 through newly-increased choke valve B throttling again, forming with the triple effect is the composite absorption heat pump on basis.
Shown in Figure 24 is that basic composite absorption heat pump is achieved in that with the triple effect
In composite absorption heat pump shown in Figure 23; With first generator 1 have the refrigerant vapour passage be communicated with the 3rd generator 3 back the 3rd generator 3 have again the cryogen liquid pipeline through the 3rd choke valve 13 is communicated with second condenser 7 be adjusted into second generator 2 and the refrigerant vapour passage arranged and the 3rd generator 3 is communicated with after the 3rd generator 3 have cryogen liquid pipeline warp the 3rd choke valve 13 to be communicated with again with second condenser 7, formation is basic composite absorption heat pump with the triple effect.
Shown in Figure 25 is that basic composite absorption heat pump is achieved in that with the triple effect
1. on the structure; In composite absorption heat pump shown in Figure 5; Increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump; Having the weak solution pipeline to be communicated with second generator 2 through first solution pump 9 and second solution heat exchanger 16 first absorber 4 is adjusted into first absorber 4 and has the weak solution pipeline to be communicated with newly-increased generator A through first solution pump 9 and second solution heat exchanger 16; Newly-increased generator A also has the concentrated solution pipeline to be communicated with second generator 2 through newly-increased solution pump D and newly-increased solution heat exchanger C; Having the concentrated solution pipeline to be communicated with first absorber 4 through first solution heat exchanger 15 and second solution heat exchanger 16 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with first absorber 4 through first solution heat exchanger 15, newly-increased solution heat exchanger C and second solution heat exchanger 16; Having the refrigerant vapour passage to be communicated with first condenser 6 to be adjusted into second generator 2 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first condenser 6 through newly-increased choke valve B again; Newly-increased generator A also has the refrigerant vapour passage to be communicated with first condenser 6; Have the refrigerant vapour passage to be communicated with to be adjusted into newly-increased generator A to set up the refrigerant vapour passage in second generator 2 and be communicated with second absorber 5 with second absorber 5, with first generator 1 have the refrigerant vapour passage be communicated with the 3rd generator 3 afterwards the 3rd generator 3 have again the cryogen liquid pipeline through the 3rd choke valve 13 be communicated with second condenser 7 be adjusted into second generator 2 and the refrigerant vapour passage arranged and the 3rd generator 3 is communicated with after the 3rd generator 3 have the cryogen liquid pipeline to be communicated with second condenser 7 again through the 3rd choke valve 13.
② the process, the first generator 1 refrigerant vapor generated to drive the second generator 2 as the heat medium, the second generator 2 generates a refrigerant vapor generator are supplied to the new and third generators 3 A used to drive the heat medium; first dilute solution absorber 4 via the first solution pump 9 and the second solution heat exchanger 16 into the new generator A, the refrigerant vapor flowing through the new generator A, into which the heating was released and, respectively, to the first condenser 6 and the second refrigerant absorber 5 provides steam generator A new solution was added a concentrated solution pump D and C added to the second solution heat exchanger generator 2, a concentrated solution of the second generator 2 via the third solution is the solution pump 18 and the first heat exchanger 15 into the first generator 1, a concentrated solution of the first generator 1 via the first solution heat exchanger 15, the new solution heat Switch C and the second solution heat exchanger 16 into the first absorber 4, forming
Figure BSA00000556596800231
Three-based composite absorption heat pump.
Shown in Figure 26 is that basic composite absorption heat pump is achieved in that with the triple effect
① structure, shown in Figure 7 a composite absorption heat pump, increasing the new generator, new throttle, add solution heat exchanger and the new solution pump, and the second absorber solution tube 5 with dilute passing the second solution pump 10 and the second solution heat exchanger 16 communicates with the second generator 2 is adjusted to the second absorber via line 5 with a dilute solution pump 10, the second solution and the second solution heat exchanger
Figure BSA00000556596800232
and adding A generator is connected, there is a concentrated solution A new generator tubing solution by adding new solution heat exchanger pump D and C and the second generator 2 connected, there will be a concentrated solution of the first generator tubing through The first solution and the second solution heat exchanger 15 and the first absorber heat exchanger 16 is adjusted to the first generator 4 communicates with a concentrated solution 1 solution heat exchanger 15 via the first pipe, the new solution heat exchanger C and a second solution heat exchanger 16 communicates with the first absorber 4, the second refrigerant vapor generator 2 a passage communicating with the first condenser 6 is adjusted to the second generator 2 refrigerant vapor passage has occurred and to add A is connected again after the new generator A liquid refrigerant piping by adding throttle B communicates with the first condenser 6, the new steam generator A well refrigerant passage communicating with the first condenser 6, the second refrigerant vapor generator 2 a passage communicating with the second absorber 5 is adjusted to add the steam generators A and additional refrigerant passage communicates with a second absorber 5, the first generator 1 with the refrigerant vapor passage and The third generator generator 3 3-connected again after the third refrigerant liquid piping via a third throttle valve 13 communicates with the second condenser 7 is adjusted to have a second refrigerant vapor generator 2 channels and third generator 3 connectivity again after the third generator 3 liquid refrigerant piping via a third throttle valve 13 communicates with the second condenser 7.
② the process, the first generator 1 refrigerant vapor generated to drive the second generator 2 as the heat medium, the second generator 2 generates a refrigerant vapor generator are supplied to the new and third generators 3 A used to drive the heat medium; first dilute solution absorber 4 via the first solution pump 9 and the third solution heat exchanger 17 into the third generator 3, a concentrated solution of the third generator 3 solution heat exchanger 17 via the third 5 into the second absorber, the absorber 5 of the second dilute solution pump 10 via the second solution and the second solution heat exchanger 16 into the new generator A, the refrigerant vapor flowing through the new generator A, heated into its release and the solution, respectively, to the first condenser 6 and the second refrigerant absorber 5 provides steam generator A new solution was added a concentrated solution pump D and the new generator, the second solution heat exchanger C 2, the second generator 2 via the third solution, a concentrated solution pump 18 and the first solution heat exchanger 15 into the first generator 1, a concentrated solution of the first generator 1 via the first solution heat exchanger 15, the new Solution C and the second solution heat exchanger 16 enters the first absorber 4, to form a composite three-based absorption heat pump.
The effect that technology of the present invention can realize---the composite absorption heat pump that is the basis with economic benefits and social benefits or triple effect proposed by the invention has following effect and advantage:
(1) is the composite absorption heat pump on basis with economic benefits and social benefits, can realizes economic benefits and social benefits during low-temperature heat supply or, realize being connected continuously between thermodynamic effect and the economic benefits and social benefits during high-temperature heat supply, can access rational performance index near the thermodynamic effect of economic benefits and social benefits.
(2) be the composite absorption heat pump on basis with the triple effect, can realize triple effect during low-temperature heat supply or, realize being connected continuously between thermodynamic effect and the triple effect during high-temperature heat supply, can access rational performance index near the thermodynamic effect of triple effect.
(3) be the composite absorption heat pump on basis with economic benefits and social benefits, obtained the absorption heat pump of thermodynamic parameter on double-effect process; With the triple effect is the composite absorption heat pump on basis, has obtained the absorption heat pump of thermodynamic parameter on the triple effect flow process, has enriched the type of absorption type heat pump assembly.
(4) in the variable parameter operation occasion that is applied to load, the heat supply temperature excursion is bigger; Can realize between heating parameter, heat supply interval and the performance index rationally corresponding; And can give full play to economic benefits and social benefits or the high advantage of triple effect flow process performance index, thereby improve energy-saving benefit largely.

Claims (41)

1 based on double effect absorption heat pump compound, mainly by the first generator, the second generator, a third generator, a first absorber, the second absorber, the first condenser, second condenser, an evaporator, a first solution pump, a second solution pump, the first throttle valve, the second throttle valve, a third throttle valve, a fourth throttle valve, the first solution heat exchanger, a second solution heat exchanger solution heat exchanger and a third component; first absorber (4) with a dilute solution via a first solution pump line (9), respectively, after the first solution and then the heat exchanger (15) and the first generator (1) Connecting and then by the second solution heat exchanger (16) and the second generator (2) communicates a first generator (1) and the concentrated solution was heat exchanger via a first conduit (15) and the first absorption (4) is connected, the second generator (2) and the concentrated solution conduit via a second solution heat exchanger (16) and the first absorber (4) connected, a second absorber (5) a dilute solution tube passing the second solution pump (10) and a third solution heat exchanger (17) and the third generator (3) communicating, third generator (3) and the concentrated solution through a third solution heat exchanger tubing ( 17) and a second absorber (5) communicates a first generator (1) and the refrigerant vapor passage and the second generator (2) connecting the second generator (2) again through the refrigerant liquid line first throttle valve (11) and the first condenser (6) communicating, the first generator (1) and the refrigerant vapor passage and the third generator (3) communicating the third generator (3) again Liquid refrigerant piping via the third throttle valve (13) and a second condenser (7) communicating, the second generator (2) and the refrigerant vapor passage of the first condenser (6) communicates, and the second occurrence device (2) and a second refrigerant vapor passage and the absorber (5) communicates, third generator (3) and the refrigerant vapor passage and the second condenser (7) communicating, the second condenser (7) There refrigerant liquid line through the fourth throttle valve (14) and the first condenser (6) or an evaporator (8) communicating, the first condenser (6) and the refrigerant fluid through the second conduit valve (12) and the evaporator (8) communicates, an evaporator (8) and the refrigerant vapor passage of the first absorber (4) connected, an evaporator (8) and communicates with the outside heat medium line, the first a generator (1) and drive the heat medium pipe communicates with the outside, a first absorber (4), a first condenser (6), a second absorber (5) and a second condenser (7) also separately there is a heating medium line communicates with the outside, to form a double-effect-based composite absorption heat pump.
2. with economic benefits and social benefits the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 1; Having the weak solution pipeline to be communicated with the 3rd generator (3) through second solution pump (10) and the 3rd solution heat exchanger (17) second absorber (5) is adjusted into second absorber (5) and has the weak solution pipeline to be communicated with first generator (1) through second solution pump (10) and first solution heat exchanger (15); Have the weak solution pipeline to be communicated with first generator (1) through first solution pump (9) and first solution heat exchanger (15) first absorber (4) and be adjusted into first absorber (4) and have the weak solution pipeline to be communicated with the 3rd generator (3) through first solution pump (9) and the 3rd solution heat exchanger (17), forming with economic benefits and social benefits is the composite absorption heat pump on basis.
3 based on the double effect absorption heat pump compound, mainly by the first generator, the second generator, a third generator, a first absorber, the second absorber, the first condenser, second condenser, an evaporator, a first solution pump, a second solution pump, the first throttle valve, the second throttle valve, a third throttle valve, a fourth throttle valve, the first solution heat exchanger, a second solution heat exchanger solution heat exchanger and a third component; first absorber (4) with a dilute solution via a first solution pump line (9), the second solution heat exchanger (16) and a first solution heat exchanger (15) and first generator (1) communicates a first generator (1) and the concentrated solution was heat exchanger via a first conduit (15) and the second generator (2) connected, the second generator (2) further solution of concentrated solution through the second heat exchanger tube (16) and the first absorber (4) connected, a second absorber (5) with a dilute solution via a second solution pump tube (10) and a third solution heat exchanger (17) and the third generator (3) communicating, third generator (3) and the concentrated solution was heat exchanger via a third conduit (17) and a second absorber (5) communicates, the first Generator (1) and the refrigerant vapor passage and the second generator (2) communicating the second generator (2) again through the first refrigerant liquid line throttle valve (11) and the first condenser ( 6) communicating, the first generator (1) and the refrigerant vapor passage and the third generator (3) communicating the third generator (3) again the refrigerant liquid line via a third throttle valve (13) and the second condenser (7) communicating, the second generator (2) and the refrigerant vapor passage and the first condenser (6) communicating, the second generator (2) and the refrigerant vapor passage and the second absorbent (5) is connected, a third generator (3) and the refrigerant vapor passage and the second condenser (7) communicating, the second condenser (7) and the refrigerant liquid line through the fourth throttle valve ( 14) and the first condenser (6) or an evaporator (8) communicating, the first condenser (6) and the refrigerant liquid line via a second throttle valve (12) and the evaporator (8) communicates, evaporated (8) and the refrigerant vapor passage of the first absorber (4) connected, an evaporator (8) and communicates with the outside heat medium pipe, a first generator (1) and drive the heat medium pipe and communicates with the outside, a first absorber (4), a first condenser (6), a second absorber (5) and a second condenser (7) there is a heating medium, respectively, also communicates with the outside line, to form a double-effect based composite absorption heat pump.
4. with economic benefits and social benefits the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 3; Increase the solution choke valve; First absorber (4) there is the weak solution pipeline through first solution pump (9); Second solution heat exchanger (16) and first solution heat exchanger (15) are communicated with first generator (1) and are adjusted into first absorber (4) and the weak solution pipeline are arranged through first solution pump (9); Second solution heat exchanger (16) is communicated with first generator (1) through first solution heat exchanger (15) with second generator (2) connected sum through solution choke valve (27) respectively afterwards more again, and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
5. with economic benefits and social benefits the composite absorption heat pump on basis; Be in claim 3-4 in the described composite absorption heat pump of arbitrary claim; Having the weak solution pipeline to be communicated with the 3rd generator (3) through second solution pump (10) and the 3rd solution heat exchanger (17) second absorber (5) is adjusted into second absorber (5) and has weak solution pipeline warp second solution pump (10) and first solution heat exchanger (15) to be communicated with first generator (1); First absorber (4) there is the weak solution pipeline through first solution pump (9); Second solution heat exchanger (16) and first solution heat exchanger (15) are communicated with first generator (1) and are adjusted into first absorber (4) and the weak solution pipeline are arranged through first solution pump (9); Second solution heat exchanger (16) and the 3rd solution heat exchanger (17) are communicated with the 3rd generator (3), and forming with economic benefits and social benefits is the composite absorption heat pump on basis.
6 based on the double effect absorption heat pump compound, mainly by the first generator, the second generator, a third generator, a first absorber, the second absorber, the first condenser, second condenser, an evaporator, a first solution pump, a second solution pump, a third solution pump, the first throttle valve, the second throttle valve, a third throttle valve, a fourth throttle valve, the first solution heat exchanger, the first These two solutions and a third solution heat exchanger composed of a heat exchanger; first absorber (4) via a first solution of dilute solution pump line (9) and a second solution heat exchanger (16) and the second generator ( 2) communicates the second generator (2) and the concentrated solution through a third solution pump tubing (18) and a first solution heat exchanger (15) and the first generator (1) communicates a first generator ( 1) and the concentrated solution was heat exchanger via a first conduit (15) and a second solution heat exchanger (16) and the first absorber (4) connected, a second absorber (5) a dilute solution of tubing The second solution pump (10) and a third solution heat exchanger (17) and the third generator (3) communicating, third generator (3) and the concentrated solution through a third solution heat exchanger tubing (17 ) and the second absorber (5) communicates a first generator (1) and the refrigerant vapor passage and the second generator (2) communicating the second generator (2) again through the first refrigerant liquid line a throttle valve (11) and the first condenser (6) communicating, the first generator (1) and the refrigerant vapor passage and the third generator (3) connecting the third generator (3) again with cold agent solution piping via the third throttle valve (13) and a second condenser (7) communicating, the second generator (2) and the refrigerant vapor passage of the first condenser (6) communicates the second generator (2) and a second refrigerant vapor passage and the absorber (5) communicates, third generator (3) and the refrigerant vapor passage and the second condenser (7) communicating, the second condenser (7) is also a refrigerant liquid line through the fourth throttle valve (14) and the first condenser (6) or an evaporator (8) communicating, the first condenser (6) and the refrigerant fluid through the second flow line valve (12) and the evaporator (8) communicates, an evaporator (8) and the refrigerant vapor passage of the first absorber (4) connected, an evaporator (8) and communicates with the outside heat medium line, the first Generator (1) and drive the heat medium pipe communicates with the outside, a first absorber (4), a first condenser (6), a second absorber (5) and a second condenser (7) were also the heating medium line is connected with the outside, to form a double-effect-based composite absorption heat pump.
7. with economic benefits and social benefits the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 6; Increase the solution choke valve; Have the weak solution pipeline to be communicated with second generator (2) through first solution pump (9) and second solution heat exchanger (16) first absorber (4) and be adjusted into first absorber (4) and have weak solution pipeline warp first solution pump (9) and second solution heat exchanger (16) directly to be communicated with second generator (2) through solution choke valve (27) with first generator (1) connected sum respectively afterwards again, formation is basic composite absorption heat pump with economic benefits and social benefits.
8. with economic benefits and social benefits the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 6; Having the weak solution pipeline to be communicated with the 3rd generator (3) through second solution pump (10) and the 3rd solution heat exchanger (17) second absorber (5) is adjusted into second absorber (5) and has the weak solution pipeline to be communicated with second generator (2) through second solution pump (10) and second solution heat exchanger (16); Have the weak solution pipeline to be communicated with second generator (2) through first solution pump (9) and second solution heat exchanger (16) first absorber (4) and be adjusted into first absorber (4) and have the weak solution pipeline to be communicated with the 3rd generator (3) through first solution pump (9) and the 3rd solution heat exchanger (17), forming with economic benefits and social benefits is the composite absorption heat pump on basis.
9. with the triple effect composite absorption heat pump on basis; Be in claim 1-2 in the described composite absorption heat pump of arbitrary claim; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; First solution pump (9) is set up the weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C); Newly-increased generator (A) also has the concentrated solution pipeline to be communicated with first absorber (4) through newly-increased solution heat exchanger (C); Having the refrigerant vapour passage to be communicated with first condenser (6) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first condenser (6) through newly-increased choke valve (B) again; Newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (6); Have the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased generator (A) to set up the refrigerant vapour passage in second generator (2) and be communicated with second absorber (5), forming with the triple effect is the composite absorption heat pump on basis.
10. with the triple effect composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 3; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; Having the weak solution pipeline to be communicated with second solution heat exchanger (16) through first solution pump (9) first absorber (4) is adjusted into first absorber (4) and has the weak solution pipeline to be communicated with second solution heat exchanger (16) through first solution pump (9) and newly-increased solution heat exchanger (C); Having the concentrated solution pipeline to be communicated with first absorber (4) through second solution heat exchanger (16) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through second solution heat exchanger (16); Newly-increased generator (A) has the concentrated solution pipeline to be communicated with first absorber (4) through newly-increased solution heat exchanger (C) again; Having the refrigerant vapour passage to be communicated with first condenser (6) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first condenser (6) through newly-increased choke valve (B) again; Newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (6); Have the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased generator (A) to set up the refrigerant vapour passage in second generator (2) and be communicated with second absorber (5), forming with the triple effect is the composite absorption heat pump on basis.
11. with the triple effect is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 5; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (15) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (15) and newly-increased solution heat exchanger (C); Having the concentrated solution pipeline to be communicated with first absorber (4) through second solution heat exchanger (16) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C); Newly-increased generator (A) also has the concentrated solution pipeline to be communicated with first absorber (4) through second solution heat exchanger (16); Having the refrigerant vapour passage to be communicated with first condenser (6) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first condenser (6) through newly-increased choke valve (B) again; Newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (6); Have the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased generator (A) to set up the refrigerant vapour passage in second generator (2) and be communicated with second absorber (5), forming with the triple effect is the composite absorption heat pump on basis.
12. with the triple effect is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 6; Increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump; Having the weak solution pipeline to be communicated with second generator (2) through first solution pump (9) and second solution heat exchanger (16) first absorber (4) is adjusted into first absorber (4) and has the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (9) and second solution heat exchanger (16); Newly-increased generator (A) also has the concentrated solution pipeline to be communicated with second generator (2) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C); Having the concentrated solution pipeline to be communicated with first absorber (4) through first solution heat exchanger (15) and second solution heat exchanger (16) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with first absorber (4) through first solution heat exchanger (15), newly-increased solution heat exchanger (C) and second solution heat exchanger (16); Having the refrigerant vapour passage to be communicated with first condenser (6) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first condenser (6) through newly-increased choke valve (B) again; Newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (6); Have the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased generator (A) to set up the refrigerant vapour passage in second generator (2) and be communicated with second absorber (5), forming with the triple effect is the composite absorption heat pump on basis.
13. with the triple effect is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 8; Increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump; Having the weak solution pipeline to be communicated with second generator (2) through second solution pump (10) and second solution heat exchanger (16) second absorber (5) is adjusted into second absorber (5) and has the weak solution pipeline to be communicated with newly-increased generator (A) through second solution pump (10) and second solution heat exchanger (16); Newly-increased generator (A) also has the concentrated solution pipeline to be communicated with second generator (2) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C); Having the concentrated solution pipeline to be communicated with first absorber (4) through first solution heat exchanger (15) and second solution heat exchanger (16) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with first absorber (4) through first solution heat exchanger (15), newly-increased solution heat exchanger (C) and second solution heat exchanger (16); Having the refrigerant vapour passage to be communicated with first condenser (6) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first condenser (6) through newly-increased choke valve (B) again; Newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (6); Have the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased generator (A) to set up the refrigerant vapour passage in second generator (2) and be communicated with second absorber (5), forming with the triple effect is the composite absorption heat pump on basis.
14. with the triple effect is the composite absorption heat pump on basis; Be in claim 9-13 in the described composite absorption heat pump of arbitrary claim; With first generator (1) have the refrigerant vapour passage be communicated with the 3rd generator (3) back the 3rd generator (3) have again the cryogen liquid pipeline through the 3rd choke valve (13) is communicated with second condenser (7) be adjusted into second generator (2) and the refrigerant vapour passage arranged and the 3rd generator (3) is communicated with after the 3rd generator (3) have the cryogen liquid pipeline to be communicated with second condenser (7) again through the 3rd choke valve (13), formation is basic composite absorption heat pump with the triple effect.
15. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 1; Increase the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger; Having the weak solution pipeline to be communicated with first solution heat exchanger (15) and second solution heat exchanger (16) respectively afterwards through first solution pump (9) first absorber (4) is adjusted into first absorber (4) and has the weak solution pipeline to be communicated with the 3rd absorber (20) through first solution pump (9) and the 4th solution heat exchanger (21); The 3rd absorber (20) has the weak solution pipeline to be communicated with first solution heat exchanger (15) and second solution heat exchanger (16) respectively afterwards through the 3rd solution pump (18) again; Having the concentrated solution pipeline to be communicated with first absorber (4) through first solution heat exchanger (15) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with the 4th generator (19) through first solution heat exchanger (15); Having the concentrated solution pipeline to be communicated with first absorber (4) through second solution heat exchanger (16) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with the 4th generator (19) through second solution heat exchanger (16); The 4th generator (19) has the concentrated solution pipeline to be communicated with first absorber (4) through the 4th solution heat exchanger (21) again; The 4th generator (19) also has the refrigerant vapour passage to be communicated with the 3rd absorber (20); The 4th generator (19) drives thermal medium pipeline and external communications in addition; The 3rd absorber (20) also has heated medium pipeline and external communications, and forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
16. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 15; Having the weak solution pipeline to be communicated with the 3rd generator (3) through second solution pump (10) and the 3rd solution heat exchanger (17) second absorber (5) is adjusted into second absorber (5) and has the weak solution pipeline to be communicated with first generator (1) through second solution pump (10) and first solution heat exchanger (15); Have the weak solution pipeline to be communicated with first generator (1) through the 3rd solution pump (18) and first solution heat exchanger (15) the 3rd absorber (20) and be adjusted into the 3rd absorber (20) and have the weak solution pipeline to be communicated with the 3rd generator (3) through the 3rd solution pump (18) and the 3rd solution heat exchanger (17), forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
17. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 3; Increase by the 4th generator; The 3rd absorber; The 3rd solution pump and the 4th solution heat exchanger; First absorber (4) there is the weak solution pipeline through first solution pump (9); Second solution heat exchanger (16) and first solution heat exchanger (15) are communicated with first generator (1) and are adjusted into first absorber (4) and have the weak solution pipeline to be communicated with the 3rd absorber (20) through first solution pump (9) and the 4th solution heat exchanger (21); The 3rd absorber (20) has the weak solution pipeline again through the 3rd solution pump (18); Second solution heat exchanger (16) and first solution heat exchanger (15) are communicated with first generator (1); Having the concentrated solution pipeline to be communicated with first absorber (4) through second solution heat exchanger (16) in second generator (2) is adjusted into second generator (2) and has concentrated solution pipeline warp second solution heat exchanger (16) to be communicated with the 4th generator (19); The 4th generator (19) has the concentrated solution pipeline to be communicated with first absorber (4) through the 4th solution heat exchanger (21) again; The 4th generator (19) also has the refrigerant vapour passage to be communicated with the 3rd absorber (20); The 4th generator (19) drives thermal medium pipeline and external communications in addition; The 3rd absorber (20) also has heated medium pipeline and external communications, and forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
18. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 17; Having the weak solution pipeline to be communicated with the 3rd generator (3) through second solution pump (10) and the 3rd solution heat exchanger (17) second absorber (5) is adjusted into second absorber (5) and has weak solution pipeline warp second solution pump (10) and first solution heat exchanger (15) to be communicated with first generator (1); The 3rd absorber (20) there is the weak solution pipeline through the 3rd solution pump (18); Second solution heat exchanger (16) and first solution heat exchanger (15) are communicated with first generator (1) and are adjusted into the 3rd absorber (20) and the weak solution pipeline are arranged through the 3rd solution pump (18); Second solution heat exchanger (16) and the 3rd solution heat exchanger (17) are communicated with the 3rd generator (3), and forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
19. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 6; Increase the 4th generator, the 3rd absorber, the 4th solution pump and the 4th solution heat exchanger; Having the weak solution pipeline to be communicated with second generator (2) through first solution pump (9) and second solution heat exchanger (16) first absorber (4) is adjusted into first absorber (4) and has the weak solution pipeline to be communicated with the 3rd absorber (20) through first solution pump (9) and the 4th solution heat exchanger (21); The 3rd absorber (20) has the weak solution pipeline to be communicated with second generator (2) through the 4th solution pump (20) and second solution heat exchanger (16) again; Having the concentrated solution pipeline to be communicated with first absorber (4) through first solution heat exchanger (15) and second solution heat exchanger (16) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with the 4th generator (19) through first solution heat exchanger (15) and second solution heat exchanger (16); The 4th generator (19) has the concentrated solution pipeline to be communicated with first absorber (4) through the 4th solution heat exchanger (21) again; The 4th generator (19) also has the refrigerant vapour passage to be communicated with the 3rd absorber (20); The 4th generator (19) drives thermal medium pipeline and external communications in addition; The 3rd absorber (20) also has heated medium pipeline and external communications, and forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
20. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 19; Having the weak solution pipeline to be communicated with the 3rd generator (3) through second solution pump (10) and the 3rd solution heat exchanger (17) second absorber (5) is adjusted into second absorber (5) and has the weak solution pipeline to be communicated with second generator (2) through second solution pump (10) and second solution heat exchanger (16); Have the weak solution pipeline to be communicated with second generator (2) through the 3rd solution pump (18) and second solution heat exchanger (16) the 3rd absorber (20) and be adjusted into the 3rd absorber (20) and have the weak solution pipeline to be communicated with the 3rd generator (3) through the 3rd solution pump (18) and the 3rd solution heat exchanger (17), forming with economic benefits and social benefits is basis and the composite absorption heat pump with backheat heat supply end.
21. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in claim 15-20 in the described composite absorption heat pump of arbitrary claim; Increase by the 5th choke valve; Cancel the driving thermal medium pipeline of the 4th generator (19) and external communications; First generator (1) is set up the refrigerant vapour passage and is communicated with back the 4th generator (19) with the 4th generator (19) and has the cryogen liquid pipeline to be communicated with first condenser (6) through the 5th choke valve (22) again, and formation is basic with economic benefits and social benefits and has the composite absorption heat pump of backheat heat supply end.
22. with the triple effect is the composite absorption heat pump on basis; Be in claim 15-16 in the described composite absorption heat pump of arbitrary claim; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; The 3rd solution pump (18) is set up the weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C); Newly-increased generator (A) also has the concentrated solution pipeline to be communicated with the 4th generator (19) through newly-increased solution heat exchanger (C); Having the refrigerant vapour passage to be communicated with first condenser (6) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first condenser (6) through newly-increased choke valve (B) again; Newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (6); Have the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased generator (A) to set up the refrigerant vapour passage in second generator (2) and be communicated with second absorber (5), forming with the triple effect is basis and the composite absorption heat pump with backheat heat supply end.
23. with the triple effect is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 17; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; Having the weak solution pipeline to be communicated with second solution heat exchanger (16) through the 3rd solution pump (18) the 3rd absorber (20) is adjusted into the 3rd absorber (20) and has the weak solution pipeline to be communicated with second solution heat exchanger (16) through the 3rd solution pump (18) and newly-increased solution heat exchanger (C); Having the concentrated solution pipeline to be communicated with the 3rd generator (19) through second solution heat exchanger (16) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through second solution heat exchanger (16); Newly-increased generator (A) also has the concentrated solution pipeline to be communicated with the 3rd generator (19) through newly-increased solution heat exchanger (C); Having the refrigerant vapour passage to be communicated with first condenser (6) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first condenser (6) through newly-increased choke valve (B) again; Newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (6); Have the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased generator (A) to set up the refrigerant vapour passage in second generator (2) and be communicated with second absorber (5), forming with the triple effect is basis and the composite absorption heat pump with backheat heat supply end.
24. with the triple effect is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 18; Increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger; Having the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (15) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (15) and newly-increased solution heat exchanger (C); Having the concentrated solution pipeline to be communicated with the 4th generator (19) through second solution heat exchanger (16) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C); Newly-increased generator (A) also has the concentrated solution pipeline to be communicated with the 4th generator (19) through second solution heat exchanger (16); Having the refrigerant vapour passage to be communicated with first condenser (6) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first condenser (6) through newly-increased choke valve (B) again; Newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (6); Have the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased generator (A) to set up the refrigerant vapour passage in second generator (2) and be communicated with second absorber (5), forming with the triple effect is basis and the composite absorption heat pump with backheat heat supply end.
25. with the triple effect is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 19; Increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump; Having the weak solution pipeline to be communicated with second generator (2) through the 4th solution pump (30) and second solution heat exchanger (16) the 3rd absorber (20) is adjusted into the 3rd absorber (20) and has the weak solution pipeline to be communicated with newly-increased generator (A) through the 4th solution pump (30) and second solution heat exchanger (16); Newly-increased generator (A) also has the concentrated solution pipeline to be communicated with second generator (2) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C); Having the concentrated solution pipeline to be communicated with the 4th generator (19) through first solution heat exchanger (15) and second solution heat exchanger (16) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with the 4th generator (19) through first solution heat exchanger (15), newly-increased solution heat exchanger (C) and second solution heat exchanger (16); Having the refrigerant vapour passage to be communicated with first condenser (6) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first condenser (6) through newly-increased choke valve (B) again; Newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (6); Have the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased generator (A) to set up the refrigerant vapour passage in second generator (2) and be communicated with second absorber (5), forming with the triple effect is basis and the composite absorption heat pump with backheat heat supply end.
26. with the triple effect is the composite absorption heat pump on basis; Be in the described composite absorption heat pump of claim 20; Increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump; Having the weak solution pipeline to be communicated with second generator (2) through second solution pump (10) and second solution heat exchanger (16) second absorber (5) is adjusted into second absorber (5) and has the weak solution pipeline to be communicated with newly-increased generator (A) through second solution pump (10) and second solution heat exchanger (16); Newly-increased generator (A) also has the concentrated solution pipeline to be communicated with second generator (2) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C); Having the concentrated solution pipeline to be communicated with the 4th generator (19) through first solution heat exchanger (15) and second solution heat exchanger (16) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with the 4th generator (4) through first solution heat exchanger (15), newly-increased solution heat exchanger (C) and second solution heat exchanger (16); Having the refrigerant vapour passage to be communicated with first condenser (6) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first condenser (6) through newly-increased choke valve (B) again; Newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (6); Have the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased generator (A) to set up the refrigerant vapour passage in second generator (2) and be communicated with second absorber (5), forming with the triple effect is basis and the composite absorption heat pump with backheat heat supply end.
27. with the triple effect is the composite absorption heat pump on basis; Be in claim 22-26 in the described composite absorption heat pump of arbitrary claim; Increase by the 5th choke valve; Cancel the driving thermal medium pipeline of the 4th generator (19) and external communications; First generator (1) is set up the refrigerant vapour passage and is communicated with back the 4th generator (19) with the 4th generator (19) and has the cryogen liquid pipeline to be communicated with first condenser (6) through the 5th choke valve (22) again, and formation is basic with the triple effect and has the composite absorption heat pump of backheat heat supply end.
28. with the triple effect is the composite absorption heat pump on basis; Be in claim 22-26 in the described composite absorption heat pump of arbitrary claim; Increase by the 5th choke valve; Cancel the driving thermal medium pipeline of the 4th generator (19) and external communications; Second generator (2) is set up the refrigerant vapour passage and is communicated with back the 4th generator (19) with the 4th generator (19) and has the cryogen liquid pipeline to be communicated with first condenser (6) through the 5th choke valve (22) again, and formation is basic with the triple effect and has the composite absorption heat pump of backheat heat supply end.
29. with the triple effect is the composite absorption heat pump on basis; Be in claim 22-28 in the described composite absorption heat pump of arbitrary claim; With first generator (1) have the refrigerant vapour passage be communicated with the 3rd generator (3) back the 3rd generator (3) have again the cryogen liquid pipeline through the 3rd choke valve (13) is communicated with second condenser (7) be adjusted into second generator (2) and the refrigerant vapour passage arranged and the 3rd generator (3) is communicated with after the 3rd generator (3) have the cryogen liquid pipeline to be communicated with second condenser (7) again through the 3rd choke valve (13), formation is basic composite absorption heat pump with the triple effect.
30. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in claim 1-5 in the described composite absorption heat pump of arbitrary claim; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber (4) and external communications; The 3rd absorber (20) has the weak solution pipeline to be communicated with dividing steam chest (23) through newly-increased solution choke valve (E) and first absorber (4); Divide steam chest (23) to also have the concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18); Divide steam chest (23) to also have the refrigerant vapour passage to be communicated with the 3rd condenser (24); The 3rd condenser (24) also has the cryogen liquid pipeline to be communicated with second evaporimeter (25) through cryogen liquid pump (26); Second evaporimeter (25) also has the refrigerant vapour passage to be communicated with the 3rd absorber (20); The 3rd absorber (20) also has heated medium pipeline and external communications; The 3rd condenser (24) also has cooling medium pipeline and external communications; Second evaporimeter (25) also have surplus heat medium pipeline and external communications, forming with economic benefits and social benefits is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 3rd condenser (24) has the cryogen liquid pipeline to be communicated with first evaporimeter (8), and first evaporimeter (8) is set up the refrigerant vapour passage and is communicated with the 3rd absorber (20).
31. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in claim 6-8 in the described composite absorption heat pump of arbitrary claim; Increase by the 4th solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber (4) and external communications; The 3rd absorber (20) has the weak solution pipeline to be communicated with dividing steam chest (23) through newly-increased solution choke valve (E) and first absorber (4); Divide steam chest (23) to also have the concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 4th solution pump (30); Divide steam chest (23) to also have the refrigerant vapour passage to be communicated with the 3rd condenser (24); The 3rd condenser (24) also has the cryogen liquid pipeline to be communicated with second evaporimeter (25) through cryogen liquid pump (26); Second evaporimeter (25) also has the refrigerant vapour passage to be communicated with the 3rd absorber (20); The 3rd absorber (20) also has heated medium pipeline and external communications; The 3rd condenser (24) also has cooling medium pipeline and external communications; Second evaporimeter (25) also have surplus heat medium pipeline and external communications, forming with economic benefits and social benefits is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 3rd condenser (24) has the cryogen liquid pipeline to be communicated with first evaporimeter (8), and first evaporimeter (8) is set up the refrigerant vapour passage and is communicated with the 3rd absorber (20).
32. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in claim 1-2 in the described composite absorption heat pump of arbitrary claim; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber (4) and external communications; Having the concentrated solution pipeline to be communicated with first absorber (4) through first solution heat exchanger (15) in first generator (1) is adjusted into first generator (1) and has concentrated solution pipeline warp first solution heat exchanger (15) and first absorber (4) to be communicated with branch steam chest (23); Having the concentrated solution pipeline to be communicated with first absorber (4) through second solution heat exchanger (16) in second generator (2) is adjusted into second generator (2) and has concentrated solution pipeline warp second solution heat exchanger (16) and first absorber (4) to be communicated with branch steam chest (23); Divide steam chest (23) to also have the concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18); The 3rd absorber (20) also has the weak solution pipeline to be communicated with first absorber (4) through newly-increased solution choke valve (E); Divide steam chest (23) to also have the refrigerant vapour passage to be communicated with the 3rd condenser (24); The 3rd condenser (24) also has the cryogen liquid pipeline to be communicated with first evaporimeter (8) through cryogen liquid pump (26); First evaporimeter (8) has the cryogen liquid pipeline to be communicated with second evaporimeter (25) through the 5th choke valve (22); First evaporimeter (8) had the refrigerant vapour passage to be communicated with first absorber (4) to be adjusted into first evaporimeter (8) has the refrigerant vapour passage to be communicated with the 3rd absorber (20); Second evaporimeter (25) also has the refrigerant vapour passage to be communicated with first absorber (4); The 3rd absorber (20) also has heated medium pipeline and external communications; The 3rd condenser (24) also has cooling medium pipeline and external communications; Second evaporimeter (25) also have surplus heat medium pipeline and external communications, forming with economic benefits and social benefits is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has the weak solution pipeline to be communicated with first absorber (4), and first evaporimeter (8) is set up the refrigerant vapour passage and is communicated with first absorber (4).
33. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in claim 3-5 in the described composite absorption heat pump of arbitrary claim; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber (4) and external communications; Having the concentrated solution pipeline to be communicated with first absorber (4) through second solution heat exchanger (16) in second generator (2) is adjusted into second generator (2) and has concentrated solution pipeline warp second solution heat exchanger (16) and first absorber (4) to be communicated with branch steam chest (23); Divide steam chest (23) to also have the concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18); The 3rd absorber (20) also has the weak solution pipeline to be communicated with first absorber (4) through newly-increased solution choke valve (E); Divide steam chest (23) to also have the refrigerant vapour passage to be communicated with the 3rd condenser (24); The 3rd condenser (24) also has the cryogen liquid pipeline to be communicated with first evaporimeter (8) through cryogen liquid pump (26); First evaporimeter (8) has the cryogen liquid pipeline to be communicated with second evaporimeter (25) through the 5th choke valve (22); First evaporimeter (8) had the refrigerant vapour passage to be communicated with first absorber (4) to be adjusted into first evaporimeter (8) has the refrigerant vapour passage to be communicated with the 3rd absorber (20); Second evaporimeter (25) also has the refrigerant vapour passage to be communicated with first absorber (4); The 3rd absorber (20) also has heated medium pipeline and external communications; The 3rd condenser (24) also has cooling medium pipeline and external communications; Second evaporimeter (25) also have surplus heat medium pipeline and external communications, forming with economic benefits and social benefits is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has the weak solution pipeline to be communicated with first absorber (4), and first evaporimeter (8) is set up the refrigerant vapour passage and is communicated with first absorber (4).
34. with economic benefits and social benefits is the composite absorption heat pump on basis; Be in claim 6-8 in the described composite absorption heat pump of arbitrary claim; Increase by the 4th solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber (4) and external communications; Having the concentrated solution pipeline to be communicated with first absorber (4) through first solution heat exchanger (15) and second solution heat exchanger (16) in first generator (1) is adjusted into first generator (1) concentrated solution pipeline warp first solution heat exchanger (15) is arranged; Second solution heat exchanger (16) and first absorber (4) are communicated with dividing steam chest (23); Divide steam chest (23) to also have the concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 4th solution pump (30); The 3rd absorber (20) also has the weak solution pipeline to be communicated with first absorber (4) through newly-increased solution choke valve (E); Divide steam chest (23) to also have the refrigerant vapour passage to be communicated with the 3rd condenser (24); The 3rd condenser (24) also has the cryogen liquid pipeline to be communicated with first evaporimeter (8) through cryogen liquid pump (26); First evaporimeter (8) has the cryogen liquid pipeline to be communicated with second evaporimeter (25) through the 5th choke valve (22); First evaporimeter (8) had the refrigerant vapour passage to be communicated with first absorber (4) to be adjusted into first evaporimeter (8) has the refrigerant vapour passage to be communicated with the 3rd absorber (20); Second evaporimeter (25) also has the refrigerant vapour passage to be communicated with first absorber (4); The 3rd absorber (20) also has heated medium pipeline and external communications; The 3rd condenser (24) also has cooling medium pipeline and external communications; Second evaporimeter (25) also have surplus heat medium pipeline and external communications, forming with economic benefits and social benefits is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has the weak solution pipeline to be communicated with first absorber (4), and first evaporimeter (8) is set up the refrigerant vapour passage and is communicated with first absorber (4).
35. with the triple effect is the composite absorption heat pump on basis; Be in claim 9-11 in the described composite absorption heat pump of arbitrary claim; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber (4) and external communications; The 3rd absorber (20) has the weak solution pipeline to be communicated with dividing steam chest (23) through newly-increased solution choke valve (E) and first absorber (4); Divide steam chest (23) to also have the concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18); Divide steam chest (23) to also have the refrigerant vapour passage to be communicated with the 3rd condenser (24); The 3rd condenser (24) also has the cryogen liquid pipeline to be communicated with second evaporimeter (25) through cryogen liquid pump (26); Second evaporimeter (25) also has the refrigerant vapour passage to be communicated with the 3rd absorber (20); The 3rd absorber (20) also has heated medium pipeline and external communications; The 3rd condenser (24) also has cooling medium pipeline and external communications; Second evaporimeter (25) also have surplus heat medium pipeline and external communications, forming with the triple effect is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 3rd condenser (24) has the cryogen liquid pipeline to be communicated with first evaporimeter (8), and first evaporimeter (8) is set up the refrigerant vapour passage and is communicated with the 3rd absorber (20).
36. with the triple effect is the composite absorption heat pump on basis; Be in claim 12-13 in the described composite absorption heat pump of arbitrary claim; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber (4) and external communications; The 3rd absorber (20) has the weak solution pipeline to be communicated with dividing steam chest (23) through newly-increased solution choke valve (E) and first absorber (4); Divide steam chest (23) to also have the concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18); Divide steam chest (23) to also have the refrigerant vapour passage to be communicated with the 3rd condenser (24); The 3rd condenser (24) also has the cryogen liquid pipeline to be communicated with second evaporimeter (25) through cryogen liquid pump (26); Second evaporimeter (25) also has the refrigerant vapour passage to be communicated with the 3rd absorber (20); The 3rd absorber (20) also has heated medium pipeline and external communications; The 3rd condenser (24) also has cooling medium pipeline and external communications; Second evaporimeter (25) also have surplus heat medium pipeline and external communications, forming with the triple effect is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 3rd condenser (24) has the cryogen liquid pipeline to be communicated with first evaporimeter (8), and first evaporimeter (8) is set up the refrigerant vapour passage and is communicated with the 3rd absorber (20).
37 with three-based composite absorption heat pump, is claimed in claim 9, wherein the composite absorption heat pump, the addition of a third solution pump, a third absorber, of steam chamber, a third condenser, a second evaporator device, the fifth throttle valve, and the new solution, the refrigerant pump throttle, to cancel or keep the first absorber (4) communicates with the external medium to be heated piping, the first generator (1) of concentrated The first solution was piping heat exchanger (15) and the first absorber (4) connected to adjust the first generator (1) via a first solution of the concentrated solution heat exchanger tube (15) and a first absorption device (4) and of steam chamber (23) communicates the second generator (2) with a concentrated solution via the second solution heat exchanger tube (16) and the first absorber (4) is adjusted to a second occurrence of communicating device (2) with a concentrated solution via the second solution heat exchanger tube (16) and a first absorber (4) and of steam chamber (23) communicates the new generator (A) a concentrated solution conduit via Add the solution heat exchanger (C) of the first absorber (4) connected to adjust the new generator (A) by adding a concentrated solution of the solution heat exchanger conduit (C) and a first absorber (4) and of steam chamber (23) communicating, of steam chamber (23) and the solution concentrated solution pump via a third line (18) and the third absorber (20) communicates, a third absorber (20) and a dilute solution The new solution of the throttle pipe (E) of the first absorber (4) communication of steam chamber (23) and the refrigerant vapor passage and the third condenser (24) communicates, a third condenser (24 ) and the refrigerant piping by the refrigerant fluid pump (26) and the first evaporator (8) communicates, a first evaporator (8) via a fifth refrigerant liquid line throttle valve (22) and the second two evaporator (25) communicating the first evaporator (8) of the first refrigerant vapor passage absorber (4) connected to adjust the first evaporator (8) and the third refrigerant vapor passage absorber ( 20) connected, the second evaporator (25) and the refrigerant vapor passage of the first absorber (4) connected, a third absorber (20) and the heating medium pipe communicates with the outside, a third condenser ( 24) and the cooling medium line communicates with the outside, the second evaporator (25) and communicates with the outside heat medium line, to form a composite three-based absorption heat pump; wherein no second evaporator section five throttle throttle and the new solution, the third absorber (20) with a dilute solution of the first absorber tube (4) communicates, a first evaporator (8) Creation of the first refrigerant vapor passage absorber (4) connected.
38. with the triple effect is the composite absorption heat pump on basis; Be in claim 10-11 in the described composite absorption heat pump of arbitrary claim; Increase by the 3rd solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber (4) and external communications; To increase generator (A) newly has the concentrated solution pipeline to be communicated with first absorber (4) through second solution heat exchanger (16) to be adjusted into newly-increased generator (A) and to have concentrated solution pipeline warp second solution heat exchanger (16) and first absorber (4) to be communicated with branch steam chest (23); Divide steam chest (23) to also have the concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 3rd solution pump (18); The 3rd absorber (20) also has the weak solution pipeline to be communicated with first absorber (4) through newly-increased solution choke valve (E); Divide steam chest (23) to also have the refrigerant vapour passage to be communicated with the 3rd condenser (24); The 3rd condenser (24) also has the cryogen liquid pipeline to be communicated with first evaporimeter (8) through cryogen liquid pump (26); First evaporimeter (8) has the cryogen liquid pipeline to be communicated with second evaporimeter (25) through the 5th choke valve (22); First evaporimeter (8) had the refrigerant vapour passage to be communicated with first absorber (4) to be adjusted into first evaporimeter (8) has the refrigerant vapour passage to be communicated with the 3rd absorber (20); Second evaporimeter (25) also has the refrigerant vapour passage to be communicated with first absorber (4); The 3rd absorber (20) also has heated medium pipeline and external communications; The 3rd condenser (24) also has cooling medium pipeline and external communications; Second evaporimeter (25) also have surplus heat medium pipeline and external communications, forming with the triple effect is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has the weak solution pipeline to be communicated with first absorber (4), and first evaporimeter (8) is set up the refrigerant vapour passage and is communicated with first absorber (4).
39. with the triple effect is the composite absorption heat pump on basis; Be in claim 12-13 in the described composite absorption heat pump of arbitrary claim; Increase by the 4th solution pump; The 3rd absorber; Divide steam chest; The 3rd condenser; Second evaporimeter; The 5th choke valve; Cryogen liquid pump and newly-increased solution choke valve; Cancel or keep the heated medium pipeline of first absorber (4) and external communications; First generator (1) there is the concentrated solution pipeline through first solution heat exchanger (15); Newly-increased solution heat exchanger (C) and second solution heat exchanger (16) are communicated with first absorber (4) and are adjusted into first generator (1) concentrated solution pipeline warp first solution heat exchanger (15) is arranged; Newly-increased solution heat exchanger (C); Second solution heat exchanger (16) and first absorber (4) are communicated with dividing steam chest (23); Divide steam chest (23) to also have the concentrated solution pipeline to be communicated with the 3rd absorber (20) through the 4th solution pump (30); The 3rd absorber (20) also has the weak solution pipeline to be communicated with first absorber (4) through newly-increased solution choke valve (E); Divide steam chest (23) to also have the refrigerant vapour passage to be communicated with the 3rd condenser (24); The 3rd condenser (24) also has the cryogen liquid pipeline to be communicated with first evaporimeter (8) through cryogen liquid pump (26); First evaporimeter (8) has the cryogen liquid pipeline to be communicated with second evaporimeter (25) through the 5th choke valve (22); First evaporimeter (8) had the refrigerant vapour passage to be communicated with first absorber (4) to be adjusted into first evaporimeter (8) has the refrigerant vapour passage to be communicated with the 3rd absorber (20); Second evaporimeter (25) also has the refrigerant vapour passage to be communicated with first absorber (4); The 3rd absorber (20) also has heated medium pipeline and external communications; The 3rd condenser (24) also has cooling medium pipeline and external communications; Second evaporimeter (25) also have surplus heat medium pipeline and external communications, forming with the triple effect is the composite absorption heat pump on basis; Wherein, when not having second evaporimeter, the 5th choke valve and newly-increased solution choke valve, the 3rd absorber (20) has the weak solution pipeline to be communicated with first absorber (4), and first evaporimeter (8) is set up the refrigerant vapour passage and is communicated with first absorber (4).
40. with the triple effect is the composite absorption heat pump on basis; Be in claim 35-39 in the described composite absorption heat pump of arbitrary claim; With first generator (1) have the refrigerant vapour passage be communicated with the 3rd generator (3) back the 3rd generator (3) have again the cryogen liquid pipeline through the 3rd choke valve (13) is communicated with second condenser (7) be adjusted into second generator (2) and the refrigerant vapour passage arranged and the 3rd generator (3) is communicated with after the 3rd generator (3) have the cryogen liquid pipeline to be communicated with second condenser (7) again through the 3rd choke valve (13), formation is basic composite absorption heat pump with the triple effect.
41. the composite absorption heat pump that is the basis with economic benefits and social benefits or triple effect; Be in claim 1-40 in the described composite absorption heat pump of arbitrary claim; Increase the first flow control valve and second flow control valve; Having heated medium pipeline and external communications to confirm as the outside respectively first condenser (6) and second condenser (7) has the heated medium pipeline to be communicated with back first condenser (6) with first condenser (6) to have the heated medium pipeline to be communicated with second condenser (7) with external communications with through second flow control valve (29) through first flow control valve (28) respectively again; Second condenser (7) has heated medium pipeline and external communications again, forms to have the composite absorption heat pump of regulating flow distribution, being the basis with economic benefits and social benefits or triple effect.
CN201110232434.0A 2011-08-03 2011-08-03 Composite absorption type heat pump on basis of double-effect or triple-effect Active CN102353170B (en)

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CN102353170A true CN102353170A (en) 2012-02-15
CN102353170B CN102353170B (en) 2014-09-03

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CN104807235A (en) * 2014-03-24 2015-07-29 李华玉 Fifth type absorption heat pump
WO2015149565A1 (en) * 2014-03-30 2015-10-08 李华玉 Type five absorption heat pump

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CN101458006A (en) * 2009-01-01 2009-06-17 李华玉 Method for enhancing first kind absorption heat pump heat supply temperature and high temperature heat pump
CN101706174A (en) * 2009-11-11 2010-05-12 李华玉 Two-stage first class absorption heat pump taking double effect as first stage
CN101706173A (en) * 2009-11-11 2010-05-12 李华玉 Two-stage first class absorption heat pump taking triple effect as first stage
CN102116538A (en) * 2011-03-06 2011-07-06 李华玉 Double-effect and triple-effect first-type absorption heat pump with heat return end and heat supply end

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CN101458006A (en) * 2009-01-01 2009-06-17 李华玉 Method for enhancing first kind absorption heat pump heat supply temperature and high temperature heat pump
CN101706174A (en) * 2009-11-11 2010-05-12 李华玉 Two-stage first class absorption heat pump taking double effect as first stage
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CN104807235A (en) * 2014-03-24 2015-07-29 李华玉 Fifth type absorption heat pump
CN104807235B (en) * 2014-03-24 2017-06-20 李华玉 5th class absorption heat pump
WO2015149565A1 (en) * 2014-03-30 2015-10-08 李华玉 Type five absorption heat pump

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