CN102297541B - Third type absorbing-generating system and third type absorbed heat pump - Google Patents

Third type absorbing-generating system and third type absorbed heat pump Download PDF

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CN102297541B
CN102297541B CN2011102002169A CN201110200216A CN102297541B CN 102297541 B CN102297541 B CN 102297541B CN 2011102002169 A CN2011102002169 A CN 2011102002169A CN 201110200216 A CN201110200216 A CN 201110200216A CN 102297541 B CN102297541 B CN 102297541B
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generator
solution
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communicated
heat exchanger
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CN102297541A (en
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李华玉
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/008—Sorption machines, plants or systems, operating continuously, e.g. absorption type with multi-stage operation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems

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

Abstract

The invention provides a third type absorbing-generating system and a third type absorbed heat pump, which belong to the technical field of heat pumps. An absorber is provided with a dilute solution pipeline which is communicated with a first generator through a first solution pump and a first solution heat exchanger, wherein the first generator is also provided with a concentrated solution pipeline which is communicated with a second generator through a first solution heat exchanger and a second solution heat exchanger; the second generator is also provided with a concentrated solution pipeline which is communicated with the absorber through a second solution pump and the second solution heat exchanger; the first generator is also respectively provided with a refrigerant steam channel communicated with the outside as well as a driving heat medium pipeline communicated with the outside; the second generator is also respectively provided with a refrigerant steam channel communicated with the outside as well as a waste heat medium pipeline communicated with the outside; the absorber is also respectively provided with a refrigerant steam channel communicated with the outside as well as a heated medium pipeline communicated with the outside to form the third type absorbing-generating system; and other parts including a condenser, a second condenser and an evaporator are combined to form a series of third type absorbed heat pumps.

Description

The 3rd class absorption-generation systems and the 3rd class absorption heat pump
Technical field:
The invention belongs to low temperature exhaust heat and utilize technical field of heat pumps.
Background technology:
Use at the same time between high temperature driven thermal medium and the heated medium between the temperature difference and residual heat resources and environment in the 3rd class absorption heat pump of temperature difference as driving force, two kinds of driving forces have relative size; When temperature difference is relatively large between residual heat resources and the environment, the generating process that high temperature driven heat is used for the solution phase I, the generating process that low temperature exhaust heat is used for the solution second stage, this can give full play to the effect of residual heat resources and reduce temperature requirement to high temperature driven heat, thereby improves residual heat resources utilization ratio and the further effect of performance high temperature driven heat.
The high temperature driven heat of different temperatures, corresponding single-action, economic benefits and social benefits and the multiple-effect of solution high temperature generating process; Consider the diversity of the quality and quantity of residual heat resources, 1.5 grades of corresponding the single-action of solution low temperature generating process, economic benefits and social benefits, multiple-effect, 1.5 grades and back-heating type single-action, backheating type double-effect, back-heating type multiple-effect, back-heating types; Two aspects combine, corresponding series the 3rd class absorption heat pump that obtains.
Summary of the invention:
Main purpose of the present invention provides the 3rd class absorption-generation systems and the 3rd class absorption heat pump, and concrete summary of the invention subitem is described below:
1. the 3rd class absorption-generation systems mainly is made up of first generator, second generator, absorber, first solution pump, second solution pump, first solution heat exchanger and second solution heat exchanger; Absorber has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger, first generator also has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and second solution heat exchanger, second generator also has the concentrated solution pipeline to be communicated with absorber through second solution pump and second solution heat exchanger, first generator also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, second generator also has refrigerant vapour passage and external communications respectively and have surplus heat medium pipeline and external communications, absorber also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, and forms the 3rd class absorption-generation systems.
2. the 3rd class absorption heat pump, be in the 1st described the 3rd class absorption-generation systems, increase by first condenser, second condenser, evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator in first generator has the refrigerant vapour passage to be communicated with first condenser, first condenser also has the cryogen liquid pipeline to be communicated with evaporimeter through choke valve, having refrigerant vapour passage and external communications to be defined as second generator in second generator has the refrigerant vapour passage to be communicated with second condenser, second condenser also has the cryogen liquid pipeline to be communicated with evaporimeter through the cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as evaporimeter absorber has the refrigerant vapour passage to be communicated with absorber, first condenser also has heated medium pipeline and external communications, second condenser also has cooling medium pipeline and external communications, evaporimeter also have surplus heat medium pipeline and external communications form the 3rd class absorption heat pump.
3. the 3rd class absorption heat pump, be in the 2nd described the 3rd class absorption heat pump, increase by the 3rd generator, the 3rd solution heat exchanger, second absorber and the 3rd solution pump, having the concentrated solution pipeline to be communicated with second 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 second absorber through first solution heat exchanger and second solution heat exchanger, second absorber also has the weak solution pipeline to be communicated with second generator through the 3rd solution pump and the 3rd solution heat exchanger, having the concentrated solution pipeline to be communicated with absorber through second solution pump and second solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with absorber through second solution pump and second solution heat exchanger, the 3rd generator also has refrigerant vapour passage and the second absorber connected sum have surplus heat medium pipeline and external communications respectively, second absorber also has cooling medium pipeline and external communications, forms back-heating type the 3rd class absorption heat pump.
4. the 3rd class absorption heat pump, be in the 2nd described the 3rd class absorption heat pump, increase absorption-generator, divide steam chest, the 3rd condenser, second evaporimeter, the second cryogen liquid pump, the 3rd solution heat exchanger, the 3rd solution pump and the 4th solution pump, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger absorber is adjusted into absorber and has the weak solution pipeline to be communicated with absorption-generator through the 4th solution pump and the 3rd solution heat exchanger, absorption-generator also has the weak solution pipeline through first solution pump, the 3rd solution heat exchanger and first solution heat exchanger are communicated with first generator, having the concentrated solution pipeline to be communicated with absorber through second solution pump and second solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with dividing steam chest through the 3rd solution pump and absorption-generator, divide steam chest to also have the concentrated solution pipeline to be communicated with absorber through second solution pump and second solution heat exchanger, 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 second cryogen liquid pump, second evaporimeter also has the refrigerant vapour passage to be communicated with absorption-generator, the 3rd condenser also has cooling medium pipeline and external communications, second evaporimeter also have surplus heat medium pipeline and external communications, absorption-generator or also have heated medium pipeline and external communications forms back-heating type the 3rd class absorption heat pump; Wherein: when 1. not having second evaporimeter, the 3rd condenser has the cryogen liquid pipeline to be communicated with first evaporimeter through the second cryogen liquid pump, and first evaporimeter is set up the refrigerant vapour passage and is communicated with absorption-generator; When 2. not having second evaporimeter, second condenser, the 3rd solution pump and the second cryogen liquid pump, second generator has the concentrated solution pipeline to be communicated with dividing steam chest through absorption-generator, divide steam chest to have the refrigerant vapour passage to be communicated with first condenser, first evaporimeter is set up the refrigerant vapour passage and is communicated with absorption-generator.
5. the 3rd class absorption heat pump, be in the 2nd described the 3rd class absorption heat pump, increase by the 3rd generator, the 3rd solution heat exchanger and second choke valve, first solution pump is set up the weak solution pipeline and is communicated with the 3rd generator through the 3rd solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator after first solution heat exchanger after the 3rd solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with back the 3rd generator with the 3rd generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through second choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with first condenser, forms economic benefits and social benefits-single-action the 3rd class absorption heat pump.
6. the 3rd class absorption heat pump, be in the 2 three class absorption heat pump, increase by the 3rd generator, the 3rd solution heat exchanger and second choke valve, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger absorber is adjusted into absorber and the weak solution pipeline is arranged through first solution pump, first solution heat exchanger and the 3rd solution heat exchanger are communicated with first generator, having the concentrated solution pipeline to be communicated with second 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 3rd generator through the 3rd solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and second solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with back the 3rd generator with the 3rd generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through second choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with first condenser, forms economic benefits and social benefits-single-action the 3rd class absorption heat pump.
7. the 3rd class absorption heat pump, be in the 6th described the 3rd class absorption heat pump, increase the solution choke valve, having the weak solution pipeline to be communicated with first generator through first solution pump, first solution heat exchanger and the 3rd solution heat exchanger absorber is adjusted into absorber and has the weak solution pipeline to be communicated with first generator through the 3rd solution heat exchanger with the 3rd generator connected sum through the solution choke valve more respectively after first solution pump, first solution heat exchanger again, formation economic benefits and social benefits-single-action the 3rd class absorption heat pump.
8. the 3rd class absorption heat pump, be in the 2nd described the 3rd class absorption heat pump, increase by the 3rd generator, the 3rd solution heat exchanger, the 3rd solution pump and second choke valve, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger absorber is adjusted into absorber and has the weak solution pipeline to be communicated with the 3rd generator through first solution pump and first solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with first generator through the 3rd solution pump and the 3rd solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with second generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with back the 3rd generator with the 3rd generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through second choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with first condenser, forms economic benefits and social benefits-single-action the 3rd class absorption heat pump.
9. the 3rd class absorption heat pump, be in the 8th described the 3rd class absorption heat pump, increase the solution choke valve, having the weak solution pipeline to be communicated with the 3rd generator through first solution pump and first solution heat exchanger absorber is adjusted into absorber and has the weak solution pipeline directly to be communicated with the 3rd generator through the solution choke valve with the first generator connected sum respectively after first solution pump and first solution heat exchanger again, formation economic benefits and social benefits-single-action the 3rd class absorption heat pump.
10. the 3rd class absorption heat pump, be in the 5th described the 3rd class absorption heat pump, increase by the 4th generator, the 4th solution heat exchanger and the 3rd choke valve, first solution pump is set up the weak solution pipeline and is communicated with the 4th generator through the 4th solution heat exchanger, the 4th generator also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator after first solution heat exchanger after the 4th solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into the 3rd generator to have the refrigerant vapour passage to be communicated with back the 4th generator with the 4th generator in the 3rd generator has the cryogen liquid pipeline to be communicated with first condenser through the 3rd choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms triple effect-single-action the 3rd class absorption heat pump.
11. the 3rd class absorption heat pump, be in the 6th described the 3rd class absorption heat pump, increase by the 4th generator, the 4th solution heat exchanger and the 3rd choke valve, absorber there is the weak solution pipeline through first solution pump, first solution heat exchanger and the 3rd solution heat exchanger are communicated with first generator and are adjusted into absorber and the weak solution pipeline are arranged through first solution pump, first solution heat exchanger, the 4th solution heat exchanger and the 3rd solution heat exchanger are communicated with first generator, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and second solution heat exchanger in the 3rd generator is adjusted into the 3rd generator and has the concentrated solution pipeline to be communicated with the 4th generator through the 4th solution heat exchanger, the 4th generator also has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and second solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into the 3rd generator to have the refrigerant vapour passage to be communicated with back the 4th generator with the 4th generator in the 3rd generator has the cryogen liquid pipeline to be communicated with first condenser through the 3rd choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms triple effect-single-action the 3rd class absorption heat pump.
12. the 3rd class absorption heat pump, be in the 8th described the 3rd class absorption heat pump, increase by the 4th generator, the 4th solution heat exchanger, the 3rd choke valve and the 4th solution pump, having the weak solution pipeline to be communicated with the 3rd generator through first solution pump and first solution heat exchanger absorber is adjusted into absorber and has the weak solution pipeline to be communicated with the 4th generator through first solution pump and first solution heat exchanger, the 4th generator also has the concentrated solution pipeline to be communicated with the 3rd generator through the 4th solution pump and the 4th solution heat exchanger, first generator there is the concentrated solution pipeline through the 3rd solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with second generator and are adjusted into first generator and the concentrated solution pipeline are arranged through the 3rd solution heat exchanger, the 4th solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with second generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into the 3rd generator to have the refrigerant vapour passage to be communicated with back the 4th generator with the 4th generator in the 3rd generator has the cryogen liquid pipeline to be communicated with first condenser through the 3rd choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms triple effect-single-action the 3rd class absorption heat pump.
13. the 3rd class absorption heat pump, be in the 3rd described the 3rd class absorption-generation systems, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, first solution pump is set up the weak solution pipeline and is communicated with the 4th generator through the 4th solution heat exchanger, the 4th generator also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator after first solution heat exchanger after the 4th solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with back the 4th generator with the 4th generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through second choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 4th generator, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
14. the 3rd class absorption heat pump, be in the 3 three class absorption heat pump, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger absorber is adjusted into absorber and the weak solution pipeline is arranged through first solution pump, first solution heat exchanger and the 4th solution heat exchanger are communicated with first generator, having the concentrated solution pipeline to be communicated with second 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 the 4th solution heat exchanger, the 4th generator also has the concentrated solution pipeline to be communicated with second absorber through first solution heat exchanger and second solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with back the 4th generator with the 4th generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through second choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 4th generator, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
15. the 3rd class absorption heat pump, be in the 14th described the 3rd class absorption heat pump, increase the solution choke valve, having the weak solution pipeline to be communicated with first generator through first solution pump, first solution heat exchanger and the 4th solution heat exchanger absorber is adjusted into absorber and has the weak solution pipeline to be communicated with first generator through the 4th solution heat exchanger with the 4th generator connected sum through the solution choke valve more respectively after first solution pump, first solution heat exchanger again, formation economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
16. the 3rd class absorption heat pump, be in the 3rd described the 3rd class absorption heat pump, increase by the 4th generator, the 4th solution heat exchanger, second choke valve and the 4th solution pump, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger absorber is adjusted into absorber and has the weak solution pipeline to be communicated with the 4th generator through first solution pump and first solution heat exchanger, the 4th generator also has the concentrated solution pipeline to be communicated with first generator through the 4th solution pump and the 4th solution heat exchanger, having the concentrated solution pipeline to be communicated with second absorber through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and the concentrated solution pipeline is arranged through the 4th solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with second absorber, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with back the 4th generator with the 4th generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through second choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 4th generator, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
17. the 3rd class absorption heat pump, be in the 16th described the 3rd class absorption heat pump, increase the solution choke valve, having the weak solution pipeline to be communicated with the 4th generator through first solution pump and first solution heat exchanger absorber is adjusted into absorber and has the weak solution pipeline directly to be communicated with the 4th generator through the solution choke valve with the first generator connected sum respectively after first solution pump and first solution heat exchanger again, formation economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
18. the 3rd class absorption heat pump, be in the 13rd described the 3rd class absorption heat pump, increase by the 5th generator, the 3rd choke valve and the 5th solution heat exchanger, first solution pump is set up the weak solution pipeline and is communicated with the 5th generator through the 5th solution heat exchanger, the 5th generator also has the concentrated solution pipeline, and the concentrated solution pipeline after first solution heat exchanger converges through the 5th solution heat exchanger and first generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into the 4th generator to have the refrigerant vapour passage to be communicated with back the 5th generator with the 5th generator in the 4th generator has the cryogen liquid pipeline to be communicated with first condenser through the 3rd choke valve again, the 5th generator also has the refrigerant vapour passage to be communicated with first condenser, forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
19. the 3rd class absorption heat pump, be in the 14th described the 3rd class absorption heat pump, increase by the 5th generator, the 3rd choke valve and the 5th solution heat exchanger, absorber there is the weak solution pipeline through first solution pump, first solution heat exchanger and the 4th solution heat exchanger are communicated with first generator and are adjusted into absorber and the weak solution pipeline are arranged through first solution pump, first solution heat exchanger, the 5th solution heat exchanger and the 4th solution heat exchanger are communicated with first generator, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and second solution heat exchanger in the 4th generator is adjusted into the 4th generator and has the concentrated solution pipeline to be communicated with the 5th generator through the 5th solution heat exchanger, the 5th generator also has the concentrated solution pipeline to be communicated with second absorber through first solution heat exchanger and second solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into the 4th generator to have the refrigerant vapour passage to be communicated with back the 5th generator with the 5th generator in the 4th generator has the cryogen liquid pipeline to be communicated with first condenser through the 3rd choke valve again, the 5th generator also has the refrigerant vapour passage to be communicated with first condenser, forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
20. the 3rd class absorption heat pump, be in the 16th described the 3rd class absorption heat pump, increase by the 5th generator, the 3rd choke valve, the 5th solution pump and the 5th solution heat exchanger, having the weak solution pipeline to be communicated with the 4th generator through first solution pump and first solution heat exchanger absorber is adjusted into absorber and has the weak solution pipeline to be communicated with the 5th generator through first solution pump and first solution heat exchanger, the 5th generator also has the concentrated solution pipeline to be communicated with the 4th generator through the 5th solution pump and the 5th solution heat exchanger, first generator there is the concentrated solution pipeline through the 4th solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with second absorber and are adjusted into first generator and the concentrated solution pipeline are arranged through the 4th solution heat exchanger, the 5th solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with second absorber, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into the 4th generator to have the refrigerant vapour passage to be communicated with back the 5th generator with the 5th generator in the 4th generator has the cryogen liquid pipeline to be communicated with first condenser through the 3rd choke valve again, the 5th generator also has the refrigerant vapour passage to be communicated with first condenser, forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
21. the 3rd class absorption heat pump, be in the 4th described the 3rd class absorption-generation systems, increase by the 3rd generator, the 4th solution heat exchanger and second choke valve, first solution pump is set up the weak solution pipeline through the 3rd solution heat exchanger and also is communicated with the 3rd generator through the 4th solution heat exchanger again, the 3rd generator also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator after first solution heat exchanger after the 4th solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with back the 3rd generator with the 3rd generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through second choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with first condenser, forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
22. the 3rd class absorption heat pump, be in the 4 three class absorption heat pump, increase by the 3rd generator, the 4th solution heat exchanger and second choke valve, having the weak solution pipeline to be communicated with first generator through the 3rd solution heat exchanger and first solution heat exchanger first solution pump is adjusted into first solution pump and the weak solution pipeline is arranged through the 3rd solution heat exchanger, first solution heat exchanger and the 4th solution heat exchanger are communicated with first generator, having the concentrated solution pipeline to be communicated with second 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 3rd generator through the 4th solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and second solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with back the 3rd generator with the 3rd generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through second choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with first condenser, forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
23. the 3rd class absorption heat pump, be in the 22nd described the 3rd class absorption heat pump, increase the solution choke valve, having the weak solution pipeline to be communicated with first generator through the 3rd solution heat exchanger, first solution heat exchanger and the 4th solution heat exchanger first solution pump is adjusted into first solution pump and has the weak solution pipeline to be communicated with first generator through the 4th solution heat exchanger with the 3rd generator connected sum through the solution choke valve more respectively after the 3rd solution heat exchanger, first solution heat exchanger again, formation economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
24. the 3rd class absorption heat pump, be in the 4th described the 3rd class absorption heat pump, increase by the 3rd generator, the 4th solution heat exchanger, the 4th solution pump and second choke valve, having the weak solution pipeline to be communicated with first generator through the 3rd solution heat exchanger and first solution heat exchanger first solution pump is adjusted into first solution pump and has the weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger and first solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with first generator through the 4th solution pump and the 4th solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and the concentrated solution pipeline is arranged through the 4th solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with second generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with back the 3rd generator with the 3rd generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through second choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator also has the refrigerant vapour passage to be communicated with first condenser, forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
25. the 3rd class absorption heat pump, be in the 24th described the 3rd class absorption heat pump, increase the solution choke valve, having the weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger and first solution heat exchanger first solution pump is adjusted into first solution pump and has the weak solution pipeline directly to be communicated with the 3rd generator through the solution choke valve with the first generator connected sum respectively after the 3rd solution heat exchanger and first solution heat exchanger again, formation economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
26. the 3rd class absorption heat pump, be in the 21st described the 3rd class absorption heat pump, increase by the 4th generator, the 5th solution heat exchanger and the 3rd choke valve, first solution pump is set up the weak solution pipeline through the 3rd solution heat exchanger and also is communicated with the 4th generator through the 5th solution heat exchanger again, the 4th generator also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator after first solution heat exchanger after the 5th solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into the 3rd generator to have the refrigerant vapour passage to be communicated with back the 4th generator with the 4th generator in the 3rd generator has the cryogen liquid pipeline to be communicated with first condenser through the 3rd choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
27. the 3rd class absorption heat pump, be in the 22nd described the 3rd class absorption heat pump, increase by the 4th generator, the 5th solution heat exchanger and the 3rd choke valve, first solution pump there is the weak solution pipeline through the 3rd solution heat exchanger, first solution heat exchanger and the 4th solution heat exchanger are communicated with first generator and are adjusted into first solution pump and the weak solution pipeline are arranged through the 3rd solution heat exchanger, first solution heat exchanger, the 5th solution heat exchanger and the 4th solution heat exchanger are communicated with first generator, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and second solution heat exchanger in the 3rd generator is adjusted into the 3rd generator and has the concentrated solution pipeline to be communicated with the 4th generator through the 5th solution heat exchanger, the 4th generator also has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and second solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into the 3rd generator to have the refrigerant vapour passage to be communicated with back the 4th generator with the 4th generator in the 3rd generator has the cryogen liquid pipeline to be communicated with first condenser through the 3rd choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
28. the 3rd class absorption heat pump, be in the 24th described the 3rd class absorption heat pump, increase by the 4th generator, the 5th solution heat exchanger, the 3rd choke valve and the 5th solution pump, having the weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger and first solution heat exchanger first solution pump is adjusted into first solution pump and has the weak solution pipeline to be communicated with the 4th generator through the 3rd solution heat exchanger and first solution heat exchanger, the 4th generator also has the concentrated solution pipeline to be communicated with the 3rd generator through the 5th solution pump and the 5th solution heat exchanger, first generator there is the concentrated solution pipeline through the 4th solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with second generator and are adjusted into first generator and the concentrated solution pipeline are arranged through the 4th solution heat exchanger, the 5th solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with second generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into the 3rd generator to have the refrigerant vapour passage to be communicated with back the 4th generator with the 4th generator in the 3rd generator has the cryogen liquid pipeline to be communicated with first condenser through the 3rd choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
29. the 3rd class absorption heat pump, be the 2nd, in interior any described the 3rd class absorption heat pump of 5-12 item, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, concentrated solution provides device to set up 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 absorber through newly-increased solution pump and newly-increased solution heat exchanger, having the refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with economic benefits and social benefits is the 3rd class absorption heat pump of low temperature generation flow process.
30. the 3rd class absorption heat pump, be the 2nd, in interior any described the 3rd class absorption heat pump of 5-12 item, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, providing device to have the concentrated solution pipeline to be communicated with second generator through second solution heat exchanger concentrated solution is adjusted into concentrated solution and provides device to have the concentrated solution pipeline to be communicated with second generator through newly-increased solution heat exchanger and second solution heat exchanger, having the concentrated solution pipeline to be communicated with absorber through second solution pump and 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 absorber through second solution pump and newly-increased solution heat exchanger, having the refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with economic benefits and social benefits is the 3rd class absorption heat pump of low temperature generation flow process.
31. the 3rd class absorption heat pump, be the 2nd, in interior any described the 3rd class absorption heat pump of 5-12 item, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, providing device to have the concentrated solution pipeline to be communicated with second generator through second solution heat exchanger concentrated solution is adjusted into concentrated solution and provides device to have the concentrated solution pipeline to be communicated with newly-increased generator through second solution heat exchanger and newly-increased 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 refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with economic benefits and social benefits is the 3rd class absorption heat pump of low temperature generation flow process.
32. the 3rd class absorption heat pump, be in the 29th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased second solution pump, concentrated solution provides device to set up the concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased second solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with absorber through newly-increased second solution pump and newly-increased second solution heat exchanger, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the triple effect is the 3rd class absorption heat pump of low temperature generation flow process.
33. the 3rd class absorption heat pump, be in the 30th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, providing device to have the concentrated solution pipeline to be communicated with second generator through newly-increased first solution heat exchanger and second solution heat exchanger concentrated solution is adjusted into concentrated solution and provides device to have concentrated solution pipeline warp to increase second solution heat exchanger newly, newly-increased first solution heat exchanger and second solution heat exchanger are communicated with second generator, to increase first generator newly has the concentrated solution pipeline to be communicated with absorber through second solution pump and newly-increased first solution heat exchanger to be adjusted into newly-increased first generator and to have concentrated solution pipeline warp to increase first solution heat exchanger newly to be communicated with newly-increased second generator, newly-increased second generator also has the concentrated solution pipeline to be communicated with absorber through second solution pump and newly-increased second solution heat exchanger, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the triple effect is the 3rd class absorption heat pump of low temperature generation flow process.
34. the 3rd class absorption heat pump, be in the 31st described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased second solution pump, providing device to have the concentrated solution pipeline to be communicated with newly-increased first generator through second solution heat exchanger and newly-increased first solution heat exchanger concentrated solution is adjusted into concentrated solution and provides device the concentrated solution pipeline to be arranged through second solution heat exchanger, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger are communicated with newly-increased second generator, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased second solution pump and newly-increased second solution heat exchanger, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the triple effect is the 3rd class absorption heat pump of low temperature generation flow process.
35. the 3rd class absorption heat pump, be the 3rd, in interior any described the 3rd class absorption heat pump of 13-20 item, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, 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 3rd generator through newly-increased solution heat exchanger, having the refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
36. the 3rd class absorption heat pump, be the 3rd, in interior any described the 3rd class absorption heat pump of 13-20 item, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, having the weak solution pipeline to be communicated with second generator through the 3rd solution heat exchanger the 3rd solution pump is adjusted into the 3rd solution pump and has the weak solution pipeline to be communicated with second generator through newly-increased solution heat exchanger and the 3rd solution heat exchanger, having the concentrated solution pipeline to be communicated with the 3rd generator through the 3rd 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 the 3rd 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 second 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 second condenser through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
37. the 3rd class absorption heat pump, be the 3rd, in interior any described the 3rd class absorption heat pump of 13-20 item, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, having the weak solution pipeline to be communicated with second generator through the 3rd solution heat exchanger the 3rd solution pump is adjusted into the 3rd solution pump and has the weak solution pipeline to be communicated with newly-increased generator through the 3rd 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 3rd generator through the 3rd solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with the 3rd generator through newly-increased solution heat exchanger and the 3rd solution heat exchanger, having the refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
38. the 3rd class absorption heat pump, be in the 35-37 item in any described the 3rd class absorption heat pump, cancel the waste heat medium pipeline of the 3rd generator and external communications, increase newly-increased second choke valve, second generator is set up the refrigerant vapour passage and is communicated with back the 3rd generator with the 3rd generator and has the cryogen liquid pipeline to be communicated with second condenser through newly-increased second choke valve again, and formation is the 3rd class absorption heat pump of low temperature generation flow process with the backheating type double-effect.
39. the 3rd class absorption heat pump, be in the 35th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, the 3rd solution pump is set up the weak solution pipeline and is communicated with newly-increased second generator through newly-increased second solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with the 3rd generator through newly-increased second solution heat exchanger, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
40. the 3rd class absorption heat pump, be in the 36th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, having the weak solution pipeline to be communicated with second generator through newly-increased first solution heat exchanger and the 3rd solution heat exchanger the 3rd solution pump is adjusted into the 3rd solution pump and has weak solution pipeline warp to increase second solution heat exchanger newly, newly-increased first solution heat exchanger and the 3rd solution heat exchanger are communicated with second generator, to increase first generator newly has the concentrated solution pipeline to be communicated with the 3rd generator through newly-increased first solution heat exchanger to be adjusted into newly-increased first generator and to have concentrated solution pipeline warp to increase first solution heat exchanger newly to be communicated with newly-increased second generator, newly-increased second generator also has the concentrated solution pipeline to be communicated with the 3rd generator through newly-increased second solution heat exchanger, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
41. the 3rd class absorption heat pump, be in the 37th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased second solution pump, having the weak solution pipeline to be communicated with newly-increased first generator through the 3rd solution heat exchanger the 3rd solution pump is adjusted into the 3rd solution pump and has the weak solution pipeline to be communicated with through newly-increased second generator of the 3rd solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased second solution pump and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with the 3rd generator through newly-increased solution heat exchanger and the 3rd solution heat exchanger in second generator is adjusted into second generator and has concentrated solution pipeline warp to increase solution heat exchanger newly, newly-increased second solution heat exchanger and the 3rd solution heat exchanger are communicated with the 3rd generator, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
42. the 3rd class absorption heat pump, be in the 39-41 item in any described the 3rd class absorption heat pump, cancel the waste heat medium pipeline of the 3rd generator and external communications, increase newly-increased the 3rd choke valve, second generator is set up the refrigerant vapour passage and is communicated with back the 3rd generator with the 3rd generator and has the cryogen liquid pipeline to be communicated with second condenser through newly-increased the 3rd choke valve again, and formation is back-heating type the 3rd class absorption heat pump of low temperature generation flow process with the triple effect.
43. the 3rd class absorption heat pump, be in 39-41 in arbitrary described the 3rd class absorption heat pump, cancel the waste heat medium pipeline of the 3rd generator and external communications, increase newly-increased the 3rd choke valve, newly-increased first generator is set up the refrigerant vapour passage and is communicated with back the 3rd generator with the 3rd generator and has the cryogen liquid pipeline to be communicated with second condenser through increasing the 3rd choke valve newly again, and formation is the 3rd class absorption heat pump of low temperature generation flow process with the back-heating type triple-effect.
44. the 3rd class absorption heat pump, be the 4th, in interior any described the 3rd class absorption heat pump of 21-28 item, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution choke valve, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with the branch steam chest through newly-increased solution choke valve and absorption-generator through the 3rd solution pump and absorption-generator with dividing steam chest to be communicated with to be adjusted into second generator in second generator, having the concentrated solution pipeline directly to be communicated with second generator to be adjusted into second solution heat exchanger to have the concentrated solution pipeline directly to increase solution heat exchanger newly with second generator connected sum warp respectively second solution heat exchanger is communicated with newly-increased generator, newly-increased generator also has the concentrated solution pipeline through the 3rd solution pump, newly-increased solution heat exchanger and absorption-generator are communicated with dividing steam chest, having the refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
45. the 3rd class absorption heat pump, be the 4th, in interior any described the 3rd class absorption heat pump of 21-28 item, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution choke valve, having the concentrated solution pipeline directly to be communicated with second generator to be adjusted into second solution heat exchanger to have the concentrated solution pipeline to increase the solution choke valve through newly-increased solution heat exchanger newly with second generator connected sum warp respectively second solution heat exchanger is communicated with newly-increased generator, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with the branch steam chest through newly-increased solution heat exchanger and absorption-generator through the 3rd solution pump and absorption-generator with dividing steam chest to be communicated with to be adjusted into second generator in second generator, newly-increased generator also has the concentrated solution pipeline to be communicated with dividing steam chest through the 3rd solution pump and absorption-generator, having the refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, and newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser; Cancel the refrigerant vapour passage that first evaporimeter or second evaporimeter are communicated with absorption-generator, second generator is set up the refrigerant vapour passage and is communicated with absorption-generator, cancel the 4th solution pump, absorber has the weak solution pipeline to be communicated with absorption-generator through the 3rd solution heat exchanger, and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
46. the 3rd class absorption heat pump, be the 4th, in interior any described the 3rd class absorption heat pump of 21-28 item, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased generator through increasing solution heat exchanger newly through the 3rd solution pump and absorption-generator with dividing steam chest to be communicated with to be adjusted into second generator in second generator, newly-increased generator also has the concentrated solution pipeline through the 3rd solution pump, newly-increased solution heat exchanger and absorption-generator are communicated with dividing steam chest, having the refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
47. the 3rd class absorption heat pump, be the 4th, in interior any described the 3rd class absorption heat pump of 21-28 item, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, having the concentrated solution pipeline directly to be communicated with second generator to be adjusted into second solution heat exchanger to have concentrated solution pipeline warp to increase solution heat exchanger newly second solution heat exchanger is communicated with second generator, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased generator through increasing solution heat exchanger newly through the 3rd solution pump and absorption-generator with dividing steam chest to be communicated with to be adjusted into second generator in second generator, newly-increased generator also has the concentrated solution pipeline to be communicated with dividing steam chest through the 3rd solution pump and absorption-generator, having the refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, and newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser; Cancel the refrigerant vapour passage that first evaporimeter or second evaporimeter are communicated with absorption-generator, second generator is set up the refrigerant vapour passage and is communicated with absorption-generator, cancel the 4th solution pump, absorber has the weak solution pipeline to be communicated with absorption-generator through the 3rd solution heat exchanger, and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
48. the 3rd class absorption heat pump, be the 4th, in interior any described the 3rd class absorption heat pump of 21-28 item, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with the branch steam chest through newly-increased solution choke valve and absorption-generator through the 3rd solution pump and absorption-generator with dividing steam chest to be communicated with to be adjusted into second generator in second generator, there is the concentrated solution pipeline to be communicated with second generator to be adjusted into second solution heat exchanger to have the concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger second solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with second generator through the 3rd solution pump and newly-increased solution heat exchanger, having the refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
49. the 3rd class absorption heat pump, be the 4th, in interior any described the 3rd class absorption heat pump of 21-28 item, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, second solution heat exchanger had the concentrated solution pipeline to be communicated with second generator to be adjusted into second solution heat exchanger has the concentrated solution pipeline to be communicated with newly-increased generator, newly-increased generator also has the concentrated solution pipeline to be communicated with second generator through the 3rd solution pump and newly-increased solution heat exchanger, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with the branch steam chest through newly-increased solution heat exchanger and absorption-generator through the 3rd solution pump and absorption-generator with dividing steam chest to be communicated with to be adjusted into second generator in second generator, having the refrigerant vapour passage to be communicated with second 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 second condenser through newly-increased choke valve again, and newly-increased generator also has the refrigerant vapour passage to be communicated with second condenser; Cancel the refrigerant vapour passage that first evaporimeter or second evaporimeter are communicated with absorption-generator, second generator is set up the refrigerant vapour passage and is communicated with absorption-generator, cancel the 4th solution pump, absorber has the weak solution pipeline to be communicated with absorption-generator through the 3rd solution heat exchanger, and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
50. the 3rd class absorption heat pump, be in the 44th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second choke valve, the newly-increased second solution choke valve and newly-increased the 3rd solution choke valve, having the concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger second solution heat exchanger is adjusted into second solution heat exchanger and has concentrated solution pipeline warp to increase the second solution choke valve newly to be communicated with newly-increased generator, to increase generator newly and the concentrated solution pipeline be arranged through the 3rd solution pump, newly-increased solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with the branch steam chest through increasing the 3rd solution choke valve and absorption-generator newly with dividing steam chest to be communicated with to be adjusted into newly-increased generator, concentrated solution provides device to set up the concentrated solution pipeline through second solution heat exchanger to be communicated with newly-increased second generator through newly-increased solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline through the 3rd solution pump, newly-increased solution heat exchanger and absorption-generator are communicated with dividing steam chest, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
51. the 3rd class absorption heat pump, be in the 45th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second choke valve, the newly-increased second solution choke valve and newly-increased the 3rd solution choke valve, to increase first generator newly has the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with the branch steam chest through the newly-increased second solution choke valve and absorption-generator through the 3rd solution pump and absorption-generator with dividing steam chest to be communicated with to be adjusted into newly-increased first generator, concentrated solution provides device to set up the concentrated solution pipeline through second solution heat exchanger to be communicated with newly-increased second generator through newly-increased the 3rd solution choke valve, newly-increased second generator also has the concentrated solution pipeline to be communicated with dividing steam chest through the 3rd solution pump and absorption-generator, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
52. the 3rd class absorption heat pump, be in the 51st described the 3rd class absorption heat pump, the newly-increased first solution choke valve of cancellation and the newly-increased second solution choke valve, increase newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with newly-increased first generator through the newly-increased first solution choke valve second solution heat exchanger is adjusted into second solution heat exchanger and has concentrated solution pipeline warp to increase second solution heat exchanger newly to be communicated with newly-increased first generator, to increase first generator newly has the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with the branch steam chest through increasing second solution heat exchanger and absorption-generator newly through the newly-increased second solution choke valve and absorption-generator with dividing steam chest to be communicated with to be adjusted into newly-increased first generator, have the refrigerant vapour passage to be communicated with absorption-generator to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with absorption-generator in second generator, formation is the 3rd class absorption heat pump of low temperature generation flow process with the back-heating type triple-effect.
53. the 3rd class absorption heat pump, be in the 46th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, to increase first generator newly and the concentrated solution pipeline be arranged through the 3rd solution pump, newly-increased solution heat exchanger and absorption-generator with divide steam chest to be communicated with to be adjusted into newly-increased first generator to have concentrated solution pipeline warp to increase second solution heat exchanger newly to be communicated with newly-increased second generator, newly-increased second generator also has the concentrated solution pipeline through the 3rd solution pump, newly-increased second solution heat exchanger, newly-increased first solution heat exchanger and absorption-generator are communicated with dividing steam chest, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
54. the 3rd class absorption heat pump, be in the 47th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, to increase first generator newly has the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased second generator through increasing second solution heat exchanger newly through the 3rd solution pump and absorption-generator with dividing steam chest to be communicated with to be adjusted into newly-increased first generator, newly-increased second generator also has the concentrated solution pipeline through the 3rd solution pump, newly-increased second solution heat exchanger and absorption-generator are communicated with dividing steam chest, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
55. the 3rd class absorption heat pump, be in the 54th described the 3rd class absorption heat pump, with second solution heat exchanger have the concentrated solution pipeline through newly-increased first solution heat exchanger is communicated with second generator be adjusted into second solution heat exchanger have the concentrated solution pipeline through newly-increased second solution heat exchanger with increase first solution heat exchanger newly and be communicated with second generator, to increase second generator newly and the concentrated solution pipeline be arranged through the 3rd solution pump, newly-increased second solution heat exchanger and absorption-generator increase second generator newly and have the concentrated solution pipeline to be communicated with the branch steam chest through the 3rd solution pump and absorption-generator with dividing steam chest to be communicated with to be adjusted into, have the refrigerant vapour passage to be communicated with absorption-generator to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with absorption-generator in second generator, formation is the 3rd class absorption heat pump of low temperature generation flow process with the back-heating type triple-effect.
56. the 3rd class absorption heat pump, be in the 48th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased solution pump, having the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased first solution heat exchanger second solution heat exchanger is adjusted into second solution heat exchanger and has concentrated solution pipeline warp to increase second solution heat exchanger newly to be communicated with newly-increased second generator, newly-increased second generator also has the concentrated solution pipeline through newly-increased solution pump, newly-increased second solution heat exchanger and newly-increased first solution heat exchanger are communicated with newly-increased first generator, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
57. the 3rd class absorption heat pump, be in the 49th described the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased solution pump, there is the concentrated solution pipeline to be communicated with newly-increased first generator to be adjusted into second solution heat exchanger to have the concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased second solution heat exchanger second solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased solution pump and newly-increased second solution heat exchanger, to increase first generator newly has the refrigerant vapour passage to be communicated with second condenser to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator to increase second generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with second condenser, newly-increased second generator also has the refrigerant vapour passage to be communicated with second condenser, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
58. the 3rd class absorption heat pump, be in the 57th described the 3rd class absorption heat pump, having the concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased second solution heat exchanger second solution heat exchanger is adjusted into second solution heat exchanger and has the concentrated solution pipeline directly to be communicated with newly-increased second generator, there is the concentrated solution pipeline to have concentrated solution pipeline warp to increase first solution heat exchanger newly through newly-increased first solution heat exchanger and absorption-generator with dividing steam chest to be communicated with to be adjusted into second generator in second generator, newly-increased second solution heat exchanger and absorption-generator are communicated with dividing steam chest, have the refrigerant vapour passage to be communicated with absorption-generator to be adjusted into newly-increased first generator to have the refrigerant vapour passage to be communicated with absorption-generator in second generator, formation is the 3rd class absorption heat pump of low temperature generation flow process with the back-heating type triple-effect.
59. the 3rd class absorption heat pump, be the 2nd, in interior any described the 3rd class absorption heat pump of 5-12 item, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, having the weak solution pipeline to be communicated with first solution heat exchanger through first solution pump absorber is adjusted into absorber and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with first solution heat exchanger through first solution pump and newly-increased solution heat exchanger, evaporimeter had the refrigerant vapour passage to be communicated with absorber to be adjusted into evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, evaporimeter is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with absorber again, and forming with 1.5 grades is the 3rd class absorption heat pump of low temperature generation flow process.
60. the 3rd class absorption heat pump, be the 3rd, in interior any described the 3rd class absorption heat pump of 13-20 item, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, having the weak solution pipeline to be communicated with first solution heat exchanger through first solution pump absorber is adjusted into absorber and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with first solution heat exchanger through first solution pump and newly-increased solution heat exchanger, evaporimeter had the refrigerant vapour passage to be communicated with absorber to be adjusted into evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, evaporimeter is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with absorber again, and forming with 1.5 grades of back-heating types is the 3rd class absorption heat pump of low temperature generation flow process.
61. the 3rd class absorption heat pump, be the 4th, in interior any described the 3rd class absorption heat pump of 21-28 item, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, having the weak solution pipeline to be communicated with absorption-generator through the 4th solution pump and the 3rd solution heat exchanger absorber is adjusted into absorber and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline through the 4th solution pump, newly-increased solution heat exchanger and the 3rd solution heat exchanger are communicated with absorption-generator, evaporimeter had the refrigerant vapour passage to be communicated with absorber to be adjusted into evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, evaporimeter is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with absorber again, and forming with 1.5 grades of back-heating types is the 3rd class absorption heat pump of low temperature generation flow process.
62. the 3rd class absorption heat pump, be in the 59th described the 3rd class absorption heat pump, there is the concentrated solution pipeline to be communicated with absorber to be adjusted into second solution heat exchanger to have the concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger second solution heat exchanger, to increase absorption-evaporimeter newly has the weak solution pipeline to be communicated with first solution heat exchanger through first solution pump and newly-increased solution heat exchanger to be adjusted into newly-increased absorptions-evaporimeter and to have the weak solution pipeline to be communicated with first solution heat exchanger through first solution pump, and formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades.
63. the 3rd class absorption heat pump, be in the 60th described the 3rd class absorption heat pump, there is the concentrated solution pipeline to be communicated with absorber to be adjusted into second solution heat exchanger to have the concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger second solution heat exchanger, to increase absorption-evaporimeter newly has the weak solution pipeline to be communicated with first solution heat exchanger through first solution pump and newly-increased solution heat exchanger to be adjusted into newly-increased absorptions-evaporimeter and to have the weak solution pipeline to be communicated with first solution heat exchanger through first solution pump, and formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
64. the 3rd class absorption heat pump, be in the 61st described the 3rd class absorption heat pump, there is the concentrated solution pipeline to be communicated with absorber to be adjusted into second solution heat exchanger to have the concentrated solution pipeline to be communicated with absorber through newly-increased solution heat exchanger second solution heat exchanger, to increase absorption-evaporimeter newly has the weak solution pipeline to be communicated with the 3rd solution heat exchanger through the 4th solution pump and newly-increased solution heat exchanger to be adjusted into newly-increased absorptions-evaporimeter and to have the weak solution pipeline to be communicated with the 3rd solution heat exchanger through the 4th solution pump, and formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
65. the 3rd class absorption heat pump, be in the 59th described the 3rd class absorption heat pump, increase newly-increased solution pump, second solution heat exchanger had the concentrated solution pipeline to be communicated with absorber to be adjusted into second solution heat exchanger has the concentrated solution pipeline to be communicated with absorption-evaporimeter, to increase absorption-evaporimeter newly has the weak solution pipeline to be communicated with first solution heat exchanger through first solution pump and newly-increased solution heat exchanger to be adjusted into newly-increased absorption-evaporimeter and to have the weak solution pipeline to be communicated with absorber through first solution pump and newly-increased solution heat exchanger, have the weak solution pipeline to be communicated with absorption-evaporimeter through newly-increased solution heat exchanger absorber and be adjusted into absorber and have the weak solution pipeline to be communicated with first solution heat exchanger through increasing solution heat exchanger and newly-increased solution pump newly, formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades.
66. the 3rd class absorption heat pump, be in the 60th described the 3rd class absorption heat pump, increase newly-increased solution pump, second solution heat exchanger had the concentrated solution pipeline to be communicated with absorber to be adjusted into second solution heat exchanger has the concentrated solution pipeline to be communicated with absorption-evaporimeter, to increase absorption-evaporimeter newly has the weak solution pipeline to be communicated with first solution heat exchanger through first solution pump and newly-increased solution heat exchanger to be adjusted into newly-increased absorption-evaporimeter and to have the weak solution pipeline to be communicated with absorber through first solution pump and newly-increased solution heat exchanger, have the weak solution pipeline to be communicated with absorption-evaporimeter through newly-increased solution heat exchanger absorber and be adjusted into absorber and have the weak solution pipeline to be communicated with first solution heat exchanger through increasing solution heat exchanger and newly-increased solution pump newly, formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
67. the 3rd class absorption heat pump, be in the 61st described the 3rd class absorption heat pump, second solution heat exchanger had the concentrated solution pipeline to be communicated with absorber to be adjusted into second solution heat exchanger has the concentrated solution pipeline to be communicated with absorption-evaporimeter, to increase absorption-evaporimeter newly has the weak solution pipeline to be communicated with the 3rd solution heat exchanger through first solution pump and newly-increased solution heat exchanger to be adjusted into newly-increased absorption-evaporimeter and to have the weak solution pipeline to be communicated with absorber through first solution pump and newly-increased solution heat exchanger, have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter through newly-increased solution heat exchanger absorber and be adjusted into absorber and have weak solution pipeline warp to increase solution heat exchanger newly to be communicated with first solution heat exchanger, formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
68. the 3rd class absorption heat pump, be in the 65th described the 3rd class absorption heat pump, there is the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter to be adjusted into second solution heat exchanger to have the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger second solution heat exchanger, have the weak solution pipeline to be communicated with first solution heat exchanger through newly-increased solution heat exchanger and newly-increased solution pump absorber and be adjusted into absorber and have the weak solution pipeline to be communicated with first solution heat exchanger through increasing solution pump newly, formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades.
69. the 3rd class absorption heat pump, be in the 66th described the 3rd class absorption heat pump, there is the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter to be adjusted into second solution heat exchanger to have the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger second solution heat exchanger, have the weak solution pipeline to be communicated with first solution heat exchanger through newly-increased solution heat exchanger and newly-increased solution pump absorber and be adjusted into absorber and have the weak solution pipeline to be communicated with first solution heat exchanger through increasing solution pump newly, formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
70. the 3rd class absorption heat pump, be in the 67th described the 3rd class absorption heat pump, there is the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter to be adjusted into second solution heat exchanger to have the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger second solution heat exchanger, have the weak solution pipeline to be communicated with the 3rd solution heat exchanger through newly-increased solution heat exchanger absorber and be adjusted into absorber and have the weak solution pipeline to be communicated with the 3rd solution heat exchanger, formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
Description of drawings:
Fig. 1 is according to the 3rd class absorption-generation systems structure and flow chart provided by the present invention.
Fig. 2 is according to the 3rd class absorption heat pump structure and flow chart provided by the present invention.
Fig. 3 is according to back-heating type the 3rd class absorption heat pump provided by the present invention the 1st kind of structure and flow chart.
Fig. 4 is according to back-heating type the 3rd class absorption heat pump provided by the present invention the 2nd kind of structure and flow chart.
Fig. 5 is according to back-heating type the 3rd class absorption heat pump provided by the present invention the 3rd kind of structure and flow chart.
Fig. 6 is according to economic benefits and social benefits-single-action the 3rd class absorption heat pump provided by the present invention the 1st kind of structure and flow chart.
Fig. 7 is according to economic benefits and social benefits-single-action the 3rd class absorption heat pump provided by the present invention the 2nd kind of structure and flow chart.
Fig. 8 is according to economic benefits and social benefits-single-action the 3rd class absorption heat pump provided by the present invention the 3rd kind of structure and flow chart.
Fig. 9 is according to triple effect-single-action the 3rd class absorption heat pump provided by the present invention the 1st kind of structure and flow chart.
Figure 10 is according to triple effect-single-action the 3rd class absorption heat pump provided by the present invention the 2nd kind of structure and flow chart.
Figure 11 is according to triple effect-single-action the 3rd class absorption heat pump provided by the present invention the 3rd kind of structure and flow chart.
Figure 12 is according to economic benefits and social benefits provided by the present invention-back-heating type single-action the 3rd class absorption heat pump the 1st kind of structure and flow chart.
Figure 13 is according to economic benefits and social benefits provided by the present invention-back-heating type single-action the 3rd class absorption heat pump the 2nd kind of structure and flow chart.
Figure 14 is according to economic benefits and social benefits provided by the present invention-back-heating type single-action the 3rd class absorption heat pump the 3rd kind of structure and flow chart.
Figure 15 is according to single-action-economic benefits and social benefits the 3rd class absorption heat pump provided by the present invention the 1st kind of structure and flow chart.
Figure 16 is according to single-action-economic benefits and social benefits the 3rd class absorption heat pump provided by the present invention the 2nd kind of structure and flow chart.
Figure 17 is according to single-action-economic benefits and social benefits the 3rd class absorption heat pump provided by the present invention the 3rd kind of structure and flow chart.
Figure 18 is according to single-action-triple effect the 3rd class absorption heat pump provided by the present invention the 1st kind of structure and flow chart.
Figure 19 is according to single-action-triple effect the 3rd class absorption heat pump provided by the present invention the 2nd kind of structure and flow chart.
Figure 20 is according to single-action-triple effect the 3rd class absorption heat pump provided by the present invention the 3rd kind of structure and flow chart.
Figure 21 is according to single-action-backheating type double-effect the 3rd class absorption heat pump provided by the present invention the 1st kind of structure and flow chart.
Figure 22 is according to single-action-backheating type double-effect the 3rd class absorption heat pump provided by the present invention the 2nd kind of structure and flow chart.
Figure 23 is according to single-action-backheating type double-effect the 3rd class absorption heat pump provided by the present invention the 3rd kind of structure and flow chart.
Figure 24 is according to single-action-backheating type double-effect the 3rd class absorption heat pump provided by the present invention the 4th kind of structure and flow chart.
Figure 25 is according to single-action-backheating type double-effect the 3rd class absorption heat pump provided by the present invention the 5th kind of structure and flow chart.
Figure 26 is according to single-action-backheating type double-effect the 3rd class absorption heat pump provided by the present invention the 6th kind of structure and flow chart.
Figure 27 is according to single-action-backheating type double-effect the 3rd class absorption heat pump provided by the present invention the 7th kind of structure and flow chart.
Figure 28 is according to single-action-backheating type double-effect the 3rd class absorption heat pump provided by the present invention the 8th kind of structure and flow chart.
Figure 29 is according to single-action-backheating type double-effect the 3rd class absorption heat pump provided by the present invention the 9th kind of structure and flow chart.
Figure 30 is according to single-action-back-heating type triple-effect the 3rd class absorption heat pump provided by the present invention the 1st kind of structure and flow chart.
Figure 31 is according to single-action-back-heating type triple-effect the 3rd class absorption heat pump provided by the present invention the 2nd kind of structure and flow chart.
Figure 32 is according to single-action-back-heating type triple-effect the 3rd class absorption heat pump provided by the present invention the 3rd kind of structure and flow chart.
Figure 33 is according to single-action-back-heating type triple-effect the 3rd class absorption heat pump provided by the present invention the 4th kind of structure and flow chart.
Figure 34 is according to single-action-back-heating type triple-effect the 3rd class absorption heat pump provided by the present invention the 5th kind of structure and flow chart.
Figure 35 is according to single-action-back-heating type triple-effect the 3rd class absorption heat pump provided by the present invention the 6th kind of structure and flow chart.
Figure 36 is according to single-action-back-heating type triple-effect the 3rd class absorption heat pump provided by the present invention the 7th kind of structure and flow chart.
Figure 37 is according to single-action-back-heating type triple-effect the 3rd class absorption heat pump provided by the present invention the 8th kind of structure and flow chart.
Figure 38 is according to single-action-back-heating type triple-effect the 3rd class absorption heat pump provided by the present invention the 9th kind of structure and flow chart.
Figure 39 is according to single-action provided by the present invention-1.5 grade the 3rd class absorption heat pump the 1st kind of structure and flow chart.
Figure 40 is according to single-action provided by the present invention-1.5 grade the 3rd class absorption heat pump the 2nd kind of structure and flow chart.
Figure 41 is according to single-action provided by the present invention-1.5 grade the 3rd class absorption heat pump the 3rd kind of structure and flow chart.
Figure 42 is according to single-action provided by the present invention-1.5 grade the 3rd class absorption heat pump the 4th kind of structure and flow chart.
Figure 43 is according to 1.5 grade of the 3rd class absorption heat pump of single-action-back-heating type provided by the present invention the 1st kind of structure and flow chart.
Figure 44 is according to 1.5 grade of the 3rd class absorption heat pump of single-action-back-heating type provided by the present invention the 2nd kind of structure and flow chart.
Among the figure, 1-first generator, 2-second generator, 3-absorber/first absorber, 4-first solution pump, 5-second solution pump, 6-first solution heat exchanger, 7-second solution heat exchanger, 8-first condenser, 9-second condenser, 10-evaporimeter/first evaporimeter, 11-choke valve/first throttle valve, the 12-cryogen liquid pump/first cryogen liquid pump, 13-the 3rd generator, 14-the 3rd solution heat exchanger, 15-second absorber, 16-the 3rd solution pump, 17-absorption-generator, 18-divides steam chest, 19-the 3rd condenser, 20-second evaporimeter, the 21-second cryogen liquid pump, 22-solution choke valve, 23-second choke valve, 24-the 4th generator, 25-the 4th solution heat exchanger, 26-the 3rd choke valve, 27-the 4th solution pump; A-increases generator/newly-increased first generator newly, B-increases solution heat exchanger/newly-increased first solution heat exchanger newly, C-increases choke valve/newly-increased first throttle valve newly, D-increases solution pump/newly-increased first solution pump newly, E-increases second generator newly, F-increases second solution heat exchanger newly, G-increases second choke valve newly, H-increases second solution pump newly, I-increases solution choke valve/newly-increased first solution choke valve newly, and J-increases the second solution choke valve newly, and K-increases the 3rd solution choke valve newly, L-increases absorption-evaporimeter newly, and M-increases the cryogen liquid pump newly.
What need definition and explanation is:
(1) concentrated solution provides device---refer to provide to second generator 2 through second solution heat exchanger 7 parts of concentrated solution, as first solution heat exchanger 6 among Fig. 2---source is first generator 1, and for example first solution heat exchanger 6 among Fig. 6 and the 3rd solution heat exchanger 14---source is first generator 1 and the 3rd generator 14.
(2) among Fig. 4, the main effect of first solution pump 4 is to overcome flow of solution through resistance and the pipe resistance of the 3rd solution heat exchanger 14; When pressure reduction or gravitational difference can be utilized, first solution pump 4 can save.
(3) among Fig. 4, the pressure when the 3rd solution pump 16 is flowed through the 13 heat absorption vaporizations of absorption-generator for regulator solution, the refrigerant vapour pressure of this time-division steam chest 18 (i.e. refrigerant vapour pressure in second condenser 19) is higher than the refrigerant vapour pressure of first condenser 9; When selecting the refrigerant vapour pressure of second condenser 19 to be lower than the refrigerant vapour pressure of first condenser 9, then adopt the solution choke valve to substitute the 3rd solution pump 16.
(4) among Fig. 4, when absorber 3 outlet weak solution temperature and absorption-generator 17 outlet weak solution temperature near the time, the 3rd solution heat exchanger 14 can not arrange; At this moment, when the pressure of absorption-generator 17 is lower than the pressure of absorber 3, can saves the 4th solution pump 27 or adopt the solution choke valve to substitute the 4th solution pump 27.
(5) among Fig. 5, the 4th solution pump 27 is mainly used in overcoming flow of solution through resistance and the pipe resistance of the 3rd solution heat exchanger 14; Among Fig. 4, during pressure in the pressure in second evaporimeter 20 is lower than first evaporimeter 10, the 4th solution pump 27 can save.
(6) when employing was working media such as ammonia spirit, Figure 2 shows that example, generator was rectifying column, and first rectifying column 1 also has heated medium pipeline and external communications, and second rectifying column 2 also has cooling medium pipeline and external communications.
(7) when employing is working media such as ammonia spirit, Figure 4 shows that example, divide the branch vapour of steam chest to need distillation process, increase cooling medium pipeline and external communications this moment.
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 example.
The 3rd class absorption-generation systems shown in Figure 1 is achieved in that
1. on the structure, it mainly is made up of first generator, second generator, absorber, first solution pump, second solution pump, first solution heat exchanger and second solution heat exchanger; Absorber 3 has the weak solution pipeline to be communicated with first generator 1 through first solution pump 4 and first solution heat exchanger 6, first generator 1 also has the concentrated solution pipeline to be communicated with second generator 2 through first solution heat exchanger 6 and second solution heat exchanger 7, second generator 2 also has the concentrated solution pipeline to be communicated with absorber 3 through second solution pump 5 and second solution heat exchanger 7, first generator 1 also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, second generator 2 also has refrigerant vapour passage and external communications respectively and have surplus heat medium pipeline and external communications, and absorber 3 also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications are arranged.
2. on the flow process, the concentrated solution of second generator 2 enters absorber 3, absorbs from the refrigerant vapour of outside and heat release in heated medium through second solution pump 5 and second solution heat exchanger 7, and the weak solution of absorber 3 enters first generator 1 through first solution pump 4 and first solution heat exchanger 6; Drive heat medium flow and enter the solution release in it and refrigerant vapour externally is provided through first generator 1, heating, the concentrated solution of first generator 1 enters second generator 2 after first solution heat exchanger 6 and second solution heat exchanger 7; The waste heat MEDIA FLOW enters the solution release in it and refrigerant vapour externally is provided through second generator 2, heating, and the concentrated solution of second generator 2 enters absorber 3 through second solution pump 5 and second solution heat exchanger 7, forms the 3rd class absorption-generation systems.
The 3rd class absorption heat pump shown in Figure 2 is achieved in that
1. on the structure, in the 3rd class absorption-generation systems shown in Figure 1, increase by first condenser, second condenser, evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator 1 in first generator 1 has the refrigerant vapour passage to be communicated with first condenser 8, first condenser 8 also has the cryogen liquid pipeline to be communicated with evaporimeter 10 through choke valve 11, having refrigerant vapour passage and external communications to be defined as second generator 2 in second generator 2 has the refrigerant vapour passage to be communicated with second condenser 9, second condenser 9 also has the cryogen liquid pipeline to be communicated with evaporimeter 10 through cryogen liquid pump 12, having refrigerant vapour passage and external communications to be defined as evaporimeter 10 absorber 3 has the refrigerant vapour passage to be communicated with absorber 3, first condenser 8 also has heated medium pipeline and external communications, second condenser 9 also has cooling medium pipeline and external communications, evaporimeter 10 also have surplus heat medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces enters first condenser 8, heat release becomes cryogen liquid in heated medium, and the cryogen liquid of first condenser 8 enters evaporimeter 10 through choke valve 11 throttling step-downs; The refrigerant vapour that second generator 2 produces enters second condenser 10, heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of second condenser 10 boosts through cryogen liquid pump 12 and enters evaporimeter 10; The cryogen liquid absorption waste heat of evaporimeter 10 becomes refrigerant vapour and provides to absorber 3, forms the 3rd class absorption heat pump.
Back-heating type the 3rd class absorption heat pump shown in Figure 3 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 2, increase by the 3rd generator, the 3rd solution heat exchanger, second absorber and the 3rd solution pump, having the concentrated solution pipeline to be communicated with second generator 2 through first solution heat exchanger 6 and second solution heat exchanger 7 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with second absorber 15 through first solution heat exchanger 6 and second solution heat exchanger 7, second absorber 15 also has the weak solution pipeline to be communicated with second generator 2 through the 3rd solution pump 16 and the 3rd solution heat exchanger 14, having the concentrated solution pipeline to be communicated with absorber 3 through second solution pump 5 and second solution heat exchanger 7 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with the 3rd generator 13 through the 3rd solution heat exchanger 14, the 3rd generator 13 also has the concentrated solution pipeline to be communicated with absorber 3 through second solution pump 5 and second solution heat exchanger 7, the 3rd generator 13 also has refrigerant vapour passage and second absorber, 15 connected sums have surplus heat medium pipeline and external communications respectively, and second absorber 15 also has cooling medium pipeline and external communications.
2. on the flow process, the concentrated solution of first generator 1 enters second absorber 15, absorbs from the refrigerant vapour of the 3rd generator 13 and heat release in cooling medium through first solution heat exchanger 6 and second solution heat exchanger 7, and the weak solution of second absorber 15 enters second generator 2 through the 3rd solution pump 16 and the 3rd solution heat exchanger 14; The concentrated solution of second generator 2 enters the 3rd generator 13 through the 3rd solution heat exchanger 14, the waste heat MEDIA FLOW enters solution in it through the 3rd generator 13, heating and discharges and provide refrigerant vapour to second absorber 15, the concentrated solution of the 3rd generator 13 enters absorber 3 through second solution pump 5 and second solution heat exchanger 7, forms back-heating type the 3rd class absorption heat pump.
Back-heating type the 3rd class absorption heat pump shown in Figure 4 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 2, increase absorption-generator, divide steam chest, the 3rd condenser, second evaporimeter, the second cryogen liquid pump, the 3rd solution heat exchanger, the 3rd solution pump and the 4th solution pump, having the weak solution pipeline to be communicated with first generator 1 through first solution pump 4 and first solution heat exchanger 6 absorber 3 is adjusted into absorber 3 and has the weak solution pipeline to be communicated with absorption-generator 17 through the 4th solution pump 27 and the 3rd solution heat exchanger 14, absorption-generator 17 also has the weak solution pipeline through first solution pump 4, the 3rd solution heat exchanger 14 and first solution heat exchanger 6 are communicated with first generator 1, having the concentrated solution pipeline to be communicated with absorber 3 through second solution pump 5 and second solution heat exchanger 7 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with dividing steam chest 18 through the 3rd solution pump 16 and absorption-generator 17, divide steam chest 18 to also have the concentrated solution pipeline to be communicated with absorber 3 through second solution pump 5 and second solution heat exchanger 7, divide steam chest 18 to also have the refrigerant vapour passage to be communicated with the 3rd condenser 19, the 3rd condenser 19 also has the cryogen liquid pipeline to be communicated with second evaporimeter 20 through the second cryogen liquid pump 21, second evaporimeter 20 also has the refrigerant vapour passage to be communicated with absorption-generator 17, the 3rd condenser 19 also has cooling medium pipeline and external communications, second evaporimeter 20 also have surplus heat medium pipeline and external communications.
2. on the flow process, the weak solution of absorber 3 enters absorption-generator 17, absorbs from the refrigerant vapour of second evaporimeter 10 and heat release in the solution of the absorption-generator 17 of flowing through through the 4th solution pump 27 and the 3rd solution heat exchanger 14, and the weak solution of absorption-generator 17 enters first generator 1 through first solution pump 4, the 3rd solution heat exchanger 14 and first solution heat exchanger 6; Absorption-generator 17, the heat absorbing part vaporization of flowing through again after the 3rd solution pump 16 appropriateness are boosted of the concentrated solution of second generator 2 enters branch steam chest 18, the refrigerant vapour that divides steam chest 18 to discharge enters the 3rd condenser 19, heat release becomes cryogen liquid in cooling medium, the cryogen liquid of the 3rd condenser 19 enters second evaporimeter 20, absorbs waste heat and become refrigerant vapour and provide to absorption-generator 17 through the pressurization of the second cryogen liquid pump 21, divide the concentrated solution of steam chest 18 to enter absorber 3 through second solution pump 5 and second solution heat exchanger 7, form back-heating type the 3rd class absorption heat pump.
Back-heating type the 3rd class absorption heat pump shown in Figure 5 is achieved in that
In the 3rd class absorption heat pump shown in Figure 4, cancel second evaporimeter, the 3rd condenser 19 has the cryogen liquid pipeline to be communicated with first evaporimeter 10 through the second cryogen liquid pump 21, first evaporimeter 10 is set up the refrigerant vapour passage and is communicated with absorption-generator 17, forms back-heating type the 3rd class absorption heat pump.
Economic benefits and social benefits-single-action the 3rd class absorption heat pump shown in Figure 6 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 2, increase by the 3rd generator, the 3rd solution heat exchanger and second choke valve, first solution pump 4 is set up the weak solution pipeline and is communicated with the 3rd generator 13 through the 3rd solution heat exchanger 14, the 3rd generator 13 also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator 1 after first solution heat exchanger 6 after the 3rd solution heat exchanger 14, having the refrigerant vapour passage to be communicated with first condenser 8 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 13 with the 3rd generator 13 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 8 through second choke valve 23 again, and the 3rd generator 13 refrigerant vapour passage in addition is communicated with first condenser 8.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers the 3rd generator 13 and makes to drive thermal medium, the weak solution of absorber 3 enters first generator 1 and enters the 3rd generator 13 through the 3rd solution heat exchanger 14 again through first solution heat exchanger 6 more respectively after first solution pump 4, refrigerant vapour the 3rd generator 13 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 8, the concentrated solution of the 3rd generator 13 is converged with the concentrated solution of first generator 1 after first solution heat exchanger 6 after the 3rd solution heat exchanger 14, enter second generator 2 through second solution heat exchanger 7 again, the refrigerant vapour heat release of the 3rd generator 13 of flowing through becomes cryogen liquid, enter first condenser 8 through 23 throttlings of second choke valve again, form economic benefits and social benefits-single-action the 3rd class absorption heat pump.
Economic benefits and social benefits-single-action the 3rd class absorption heat pump shown in Figure 7 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 2, increase by the 3rd generator, the 3rd solution heat exchanger, second choke valve and solution choke valve, having the weak solution pipeline to be communicated with first generator 1 through first solution pump 4 and first solution heat exchanger 6 absorber 3 is adjusted into absorber 3 and the weak solution pipeline is arranged through first solution pump 4, be communicated with first generator 1 through the 3rd solution heat exchanger 14 again with the 3rd generator 13 connected sums through solution choke valve 22 more respectively after first solution heat exchanger 6, having the concentrated solution pipeline to be communicated with second generator 2 through first solution heat exchanger 6 and second solution heat exchanger 7 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with the 3rd generator 13 through the 3rd solution heat exchanger 14, the 3rd generator 13 also has the concentrated solution pipeline to be communicated with second generator 2 through first solution heat exchanger 6 and second solution heat exchanger 7, having the refrigerant vapour passage to be communicated with first condenser 8 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 13 with the 3rd generator 13 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 8 through second choke valve 23 again, and the 3rd generator 13 refrigerant vapour passage in addition is communicated with first condenser 8.
2. on the flow process, the weak solution of absorber 3 enters the 3rd generator 13 and enters first generator 1 through the 3rd solution heat exchanger 14 again through solution choke valve 22 more respectively after first solution pump 4 and first solution heat exchanger 6, the refrigerant vapour that first generator 1 produces offers the 3rd generator 13 and does to drive thermal medium, and the concentrated solution of first generator 1 enters the 3rd generator 13 through the 3rd solution heat exchanger 14; Flow through the 3rd generator 13, heating of refrigerant vapour enters solution in it and discharges and provide refrigerant vapour to first condenser 8, the concentrated solution of the 3rd generator 13 enters second generator 2 through first solution heat exchanger 6 and second solution heat exchanger 7, the refrigerant vapour heat release of the 3rd generator 13 of flowing through becomes cryogen liquid, enters first condenser 8 through 23 throttlings of second choke valve again, forms economic benefits and social benefits-single-action the 3rd class absorption heat pump.
Economic benefits and social benefits-single-action the 3rd class absorption heat pump shown in Figure 8 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 2, increase by the 3rd generator, the 3rd solution heat exchanger, the 3rd solution pump and second choke valve, having the weak solution pipeline to be communicated with first generator 1 through first solution pump 4 and first solution heat exchanger 6 absorber 3 is adjusted into absorber 3 and has the weak solution pipeline to be communicated with the 3rd generator 13 through first solution pump 4 and first solution heat exchanger 6, the 3rd generator 13 also has the concentrated solution pipeline to be communicated with first generator 1 through the 3rd solution pump 16 and the 3rd solution heat exchanger 14, having the concentrated solution pipeline to be communicated with second generator 2 through first solution heat exchanger 6 and second solution heat exchanger 7 in first generator 1 is adjusted into first generator 1 and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger 14, first solution heat exchanger 6 and second solution heat exchanger 7 are communicated with second generator 2, having the refrigerant vapour passage to be communicated with first condenser 8 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 13 with the 3rd generator 13 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 8 through second choke valve 23 again, and the 3rd generator 13 refrigerant vapour passage in addition is communicated with first condenser 8.
2. on the flow process, the weak solution of absorber 3 enters the 3rd generator 13 through first solution pump 4 and first solution heat exchanger 6, the refrigerant vapour that first generator 1 produces offers the 3rd generator 13 and makes to drive thermal medium, refrigerant vapour the 3rd generator 13 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 8, the concentrated solution of the 3rd generator 13 enters first generator 1 through the 3rd solution pump 16 and the 3rd solution heat exchanger 14, the refrigerant vapour heat release of the 3rd generator 13 of flowing through becomes cryogen liquid, enter first condenser 8 through 23 throttlings of second choke valve again, the concentrated solution of first generator 1 is through the 3rd solution heat exchanger 14, first solution heat exchanger 6 and second solution heat exchanger 7 enter second generator 2, form economic benefits and social benefits-single-action the 3rd class absorption heat pump.
Triple effect-single-action the 3rd class absorption heat pump shown in Figure 9 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 6, increase by the 4th generator, the 4th solution heat exchanger and the 3rd choke valve, first solution pump 4 is set up the weak solution pipeline and is communicated with the 4th generator 24 through the 4th solution heat exchanger 25, the 4th generator 24 also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator 1 after first solution heat exchanger 6 after the 4th solution heat exchanger 25, having the refrigerant vapour passage to be communicated with first condenser 8 to be adjusted into the 3rd generator 13 to have the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 in the 3rd generator 13 has the cryogen liquid pipeline to be communicated with first condenser 8 through the 3rd choke valve 26 again, and the 4th generator 24 refrigerant vapour passage in addition is communicated with first condenser 8.
2. on the flow process, the refrigerant vapour that the 3rd generator 13 produces offers the 4th generator 24 and makes to drive thermal medium, the part weak solution of absorber 3 enters the 4th generator 24 through first solution pump 4 and the 4th solution heat exchanger 25, refrigerant vapour the 4th generator 24 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 8, the concentrated solution of the 4th generator 24 is converged with the concentrated solution of first generator 1 after first solution heat exchanger 6 after the 4th solution heat exchanger 25, enter second generator 2 through second solution heat exchanger 7 again, the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enter first condenser 8 through 26 throttlings of the 3rd choke valve again, form triple effect-single-action the 3rd class absorption heat pump.
Triple effect-single-action the 3rd class absorption heat pump shown in Figure 10 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 7, the solution pipeline that cancellation is communicated with the 3rd generator 13 through solution choke valve 22, increase by the 4th generator, the 4th solution heat exchanger and the 3rd choke valve, absorber 3 there is the weak solution pipeline through first solution pump 4, first solution heat exchanger 6 and the 3rd solution heat exchanger 14 are communicated with first generator 1 and are adjusted into absorber 3 and the weak solution pipeline are arranged through first solution pump 4, first solution heat exchanger 6, the 4th solution heat exchanger 25 and the 3rd solution heat exchanger 14 are communicated with first generator 1, having the concentrated solution pipeline to be communicated with second generator 2 through first solution heat exchanger 6 and second solution heat exchanger 7 in the 3rd generator 13 is adjusted into the 3rd generator 13 and has the concentrated solution pipeline to be communicated with the 4th generator 24 through the 4th solution heat exchanger 25, the 4th generator 24 also has the concentrated solution pipeline to be communicated with second generator 2 through first solution heat exchanger 6 and second solution heat exchanger 7, having the refrigerant vapour passage to be communicated with first condenser 8 to be adjusted into the 3rd generator 13 to have the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 in the 3rd generator 13 has the cryogen liquid pipeline to be communicated with first condenser 8 through the 3rd choke valve 26 again, and the 4th generator 24 refrigerant vapour passage in addition is communicated with first condenser 8.
2. on the flow process, the weak solution of absorber 3 enters first generator 1 through first solution pump 4, first solution heat exchanger 6, the 4th solution heat exchanger 25 and the 3rd solution heat exchanger 14, the concentrated solution of first generator 1 enters the 4th generator 24 through the concentrated solution that the 3rd solution heat exchanger 14 enters the 3rd generator 13, the three generators 13 through the 4th solution heat exchanger 25; The refrigerant vapour that the 3rd generator 13 produces offers the 4th generator 24 and makes to drive thermal medium, flow through the 4th generator 24, heating of refrigerant vapour enters solution in it and discharges and provide refrigerant vapour to first condenser 8, the concentrated solution of the 4th generator 24 enters second generator 2 through first solution heat exchanger 6 and second solution heat exchanger 7, the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enters first condenser 8 through the 3rd choke valve 26 again, forms triple effect-single-action the 3rd class absorption heat pump.
Triple effect-single-action the 3rd class absorption heat pump shown in Figure 11 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 8, increase by the 4th generator, the 4th solution heat exchanger, the 3rd choke valve and the 4th solution pump, having the weak solution pipeline to be communicated with the 3rd generator 13 through first solution pump 4 and first solution heat exchanger 6 absorber 3 is adjusted into absorber 3 and has the weak solution pipeline to be communicated with the 4th generator 24 through first solution pump 4 and first solution heat exchanger 6, the 4th generator 24 also has the concentrated solution pipeline to be communicated with the 3rd generator 13 through the 4th solution pump 27 and the 4th solution heat exchanger 25, first generator 1 there is the concentrated solution pipeline through the 3rd solution heat exchanger 14, first solution heat exchanger 6 and second solution heat exchanger 7 are communicated with second generator 2 and are adjusted into first generator 1 and the concentrated solution pipeline are arranged through the 3rd solution heat exchanger 14, the 4th solution heat exchanger 25, first solution heat exchanger 6 and second solution heat exchanger 7 are communicated with second generator 2, having the refrigerant vapour passage to be communicated with first condenser 8 to be adjusted into the 3rd generator 13 to have the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 in the 3rd generator 13 has the cryogen liquid pipeline to be communicated with first condenser 8 through the 3rd choke valve 26 again, and the 4th generator 24 refrigerant vapour passage in addition is communicated with first condenser 8.
2. on the flow process, the weak solution of absorber 3 enters the 4th generator 24 through first solution pump 4 and first solution heat exchanger 6, the refrigerant vapour that the 3rd generator 13 produces offers the 4th generator 24 and makes to drive thermal medium, refrigerant vapour the 4th generator 24 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 8, the concentrated solution of the 4th generator 24 enters the 3rd generator 13 through the 4th solution pump 27 and the 4th solution heat exchanger 25, the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enter first condenser 8 through the 3rd choke valve 26 again, the concentrated solution of first generator 1 is through the 3rd solution heat exchanger 14, the 4th solution heat exchanger 25, first solution heat exchanger 6 and second solution heat exchanger 7 enter second generator 2, form triple effect-single-action the 3rd class absorption heat pump.
Triple effect shown in Figure 12-back-heating type single-action the 3rd class absorption heat pump is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, first solution pump 4 is set up the weak solution pipeline and is communicated with the 4th generator 24 through the 4th solution heat exchanger 25, the 4th generator 24 also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator 1 after first solution heat exchanger 6 after the 4th solution heat exchanger 25, having the refrigerant vapour passage to be communicated with first condenser 8 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 8 through second choke valve 23 again, and the 4th generator 24 refrigerant vapour passage in addition is communicated with first condenser 8.
2. on the flow process, the refrigerant vapour that first generator 1 produces offers the 4th generator 24 and makes to drive thermal medium, the weak solution of absorber 3 enters first generator 1 and enters the 4th generator 24 through the 4th solution heat exchanger 25 again through first solution heat exchanger 6 more respectively after first solution pump 4, refrigerant vapour the 4th generator 24 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 8, the concentrated solution of the 4th generator 24 is converged with the concentrated solution of first generator 1 after first solution heat exchanger 6 after the 4th solution heat exchanger 25, enter second absorber 15 through second solution heat exchanger 7 again, the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enter first condenser 8 through 23 throttlings of second choke valve again, form economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
Triple effect shown in Figure 13-back-heating type single-action the 3rd class absorption heat pump is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, having the weak solution pipeline to be communicated with first generator 1 through first solution pump 4 and first solution heat exchanger 6 absorber 3 is adjusted into absorber 3 and the weak solution pipeline is arranged through first solution pump 4, first solution heat exchanger 6 and the 4th solution heat exchanger 25 are communicated with first generator 1, having the concentrated solution pipeline to be communicated with second absorber 15 through first solution heat exchanger 6 and second solution heat exchanger 7 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with the 4th generator 24 through the 4th solution heat exchanger 25, the 4th generator 24 also has the concentrated solution pipeline to be communicated with second absorber 15 through first solution heat exchanger 6 and second solution heat exchanger 7, having the refrigerant vapour passage to be communicated with first condenser 8 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 8 through second choke valve 23 again, and the 4th generator 24 refrigerant vapour passage in addition is communicated with first condenser 8.
2. on the flow process, the weak solution of absorber 3 enters first generator 1 through first solution pump 4, first solution heat exchanger 6 and the 4th solution heat exchanger 25, the concentrated solution of first generator 1 offers the 4th generator 24 do driving thermal mediums through the refrigerant vapour that the 4th solution heat exchanger 25 enters 1 generation of the 4th generator 24, the first generators; Flow through the 4th generator 24, heating of refrigerant vapour enters solution in it and discharges and provide refrigerant vapour to first condenser 8, the concentrated solution of the 4th generator 24 enters second absorber 15 through first solution heat exchanger 6 and second solution heat exchanger 7, the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enters first condenser 8 through 23 throttlings of second choke valve again, forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
Triple effect shown in Figure 14-back-heating type single-action the 3rd class absorption heat pump is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, increase by the 4th generator, the 4th solution heat exchanger, second choke valve and the 4th solution pump, having the weak solution pipeline to be communicated with first generator 1 through first solution pump 4 and first solution heat exchanger 6 absorber 3 is adjusted into absorber 3 and has the weak solution pipeline to be communicated with the 4th generator 24 through first solution pump 4 and first solution heat exchanger 6, the 4th generator 24 also has the concentrated solution pipeline to be communicated with first generator 1 through the 4th solution pump 27 and the 4th solution heat exchanger 25, having the concentrated solution pipeline to be communicated with second absorber 15 through first solution heat exchanger 6 and second solution heat exchanger 7 in first generator 1 is adjusted into first generator 1 and the concentrated solution pipeline is arranged through the 4th solution heat exchanger 25, first solution heat exchanger 6 and second solution heat exchanger 7 are communicated with second absorber 15, having the refrigerant vapour passage to be communicated with first condenser 8 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 8 through second choke valve 23 again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 4th generator, and the 4th generator 24 refrigerant vapour passage in addition is communicated with first condenser 8.
2. on the flow process, the weak solution of absorber 3 enters the 4th generator 24 through first solution pump 4 and first solution heat exchanger 6, the refrigerant vapour that first generator 1 produces offers the 4th generator 24 and makes to drive thermal medium, refrigerant vapour the 4th generator 24 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 8, the concentrated solution of the 4th generator 24 enters first generator 1 through the 4th solution pump 27 and the 4th solution heat exchanger 25, the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enter first condenser 8 through 23 throttlings of second choke valve again, the concentrated solution of first generator 1 is through the 4th solution heat exchanger 25, first solution heat exchanger 6 and second solution heat exchanger 7 enter second absorber 15, form economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
Single-action-economic benefits and social benefits the 3rd class absorption heat pump shown in Figure 15 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 2, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, first solution heat exchanger 6 is set up the concentrated solution pipeline and is communicated with newly-increased generator A through newly-increased solution heat exchanger B, newly-increased generator A also has the concentrated solution pipeline to be communicated with absorber 3 through newly-increased solution pump D and newly-increased solution heat exchanger B, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the concentrated solution of first generator 1 is divided into two-way after first solution heat exchanger 6---and the first via enters second generator 2, the second tunnel through second solution heat exchanger 7 and enters newly-increased generator A through newly-increased solution heat exchanger B; The refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of newly-increased generator A enters absorber 3 through newly-increased solution pump D and newly-increased solution heat exchanger B, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enters second condenser 9 through newly-increased choke valve C throttling again, forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
Single-action-economic benefits and social benefits the 3rd class absorption heat pump shown in Figure 16 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 2, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, having the concentrated solution pipeline to be communicated with second generator 2 through second solution heat exchanger 7 first solution heat exchanger 6 is adjusted into first solution heat exchanger 6 and has the concentrated solution pipeline to be communicated with second generator 2 through newly-increased solution heat exchanger B and second solution heat exchanger 7, having the concentrated solution pipeline to be communicated with absorber 3 through second solution pump 5 and second solution heat exchanger 7 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 7, newly-increased generator A also has the concentrated solution pipeline to be communicated with absorber 3 through second solution pump 5 and newly-increased solution heat exchanger B, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the concentrated solution of first generator 1 is through first solution heat exchanger 6, newly-increased solution heat exchanger B and second solution heat exchanger 7 enter second generator 2, the concentrated solution of second generator 2 enters newly-increased generator A through second solution heat exchanger 7, the refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of newly-increased generator A enters absorber 3 through second solution pump 5 and newly-increased solution heat exchanger B, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enter second condenser 9 through newly-increased choke valve C again, form single-action-economic benefits and social benefits the 3rd class absorption heat pump.
Single-action-economic benefits and social benefits the 3rd class absorption heat pump shown in Figure 17 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 2, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, having the concentrated solution pipeline to be communicated with second generator 2 through second solution heat exchanger 7 first solution heat exchanger 6 is adjusted into first solution heat exchanger 6 and has the concentrated solution pipeline to be communicated with newly-increased generator A through second solution heat exchanger 7 and newly-increased solution heat exchanger B, 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 B, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the concentrated solution of first generator 1 is through first solution heat exchanger 6, second solution heat exchanger 7 and newly-increased solution heat exchanger B enter newly-increased generator A, the refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of newly-increased generator A enters second generator 2 through newly-increased solution pump D and newly-increased solution heat exchanger B, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enter second condenser 9 through newly-increased choke valve C again, form single-action-economic benefits and social benefits the 3rd class absorption heat pump.
Single-action-triple effect the 3rd class absorption heat pump shown in Figure 180 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 15, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased second solution pump, first solution heat exchanger 6 is set up the concentrated solution pipeline and is communicated with the newly-increased second generator E through the newly-increased second solution heat exchanger F, the newly-increased second generator E also has the concentrated solution pipeline to be communicated with absorber 3 through the newly-increased second solution pump H and the newly-increased second solution heat exchanger F, to increase the first generator A newly has the refrigerant vapour passage to be communicated with second condenser 9 to be adjusted into the newly-increased first generator A to have the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with second condenser 9, to increase the second generator E newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the part concentrated solution of first generator 1 enters the newly-increased second generator E through first solution heat exchanger 6 and the newly-increased second solution heat exchanger F, the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and makes to drive thermal medium, refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of the newly-increased second generator E enters absorber 3 through the newly-increased second solution pump H and the newly-increased second solution heat exchanger F, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enter second condenser 9 through the newly-increased second choke valve G again, form single-action-triple effect the 3rd class absorption heat pump.
Single-action-triple effect the 3rd class absorption heat pump shown in Figure 19 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 16, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, having the concentrated solution pipeline to be communicated with second generator 2 through the newly-increased first solution heat exchanger B and second solution heat exchanger 7 first solution heat exchanger 6 is adjusted into first solution heat exchanger 6 and has concentrated solution pipeline warp to increase the second solution heat exchanger F newly, the newly-increased first solution heat exchanger B and second solution heat exchanger 7 are communicated with second generator 2, to increase the first generator A newly has the concentrated solution pipeline to be communicated with absorber 3 through second solution pump 5 and the newly-increased first solution heat exchanger B to be adjusted into the newly-increased first generator A and to have concentrated solution pipeline warp to increase the first solution heat exchanger B newly to be communicated with the newly-increased second generator E, the newly-increased second generator E also has the concentrated solution pipeline to be communicated with absorber 3 through second solution pump 5 and the newly-increased second solution heat exchanger F, to increase the first generator A newly has the refrigerant vapour passage to be communicated with second condenser 9 to be adjusted into the newly-increased first generator A to have the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with second condenser 9, to increase the second generator E newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the concentrated solution of first generator 1 is through first solution heat exchanger 6, the newly-increased second solution heat exchanger F, the newly-increased first solution heat exchanger B and second solution heat exchanger 7 enter second generator 2, the concentrated solution of the newly-increased first generator A enters the newly-increased second generator E through the newly-increased first solution heat exchanger B, the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and makes to drive thermal medium, refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of the newly-increased second generator E enters absorber 3 through second solution pump 5 and the newly-increased second solution heat exchanger F, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enter second condenser 9 through the newly-increased second choke valve G again, form single-action-triple effect the 3rd class absorption heat pump.
Single-action-triple effect the 3rd class absorption heat pump shown in Figure 20 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 17, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased second solution pump, having the concentrated solution pipeline to be communicated with the newly-increased first generator A through second solution heat exchanger 7 and the newly-increased first solution heat exchanger B first solution heat exchanger 6 is adjusted into first solution heat exchanger 6 and the concentrated solution pipeline is arranged through second solution heat exchanger 7, the newly-increased first solution heat exchanger B and the newly-increased second solution heat exchanger F are communicated with the newly-increased second generator E, the newly-increased second generator E also has the concentrated solution pipeline to be communicated with the newly-increased first generator A through the newly-increased second solution pump H and the newly-increased second solution heat exchanger F, to increase the first generator A newly has the refrigerant vapour passage to be communicated with second condenser 9 to be adjusted into the newly-increased first generator A to have the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with second condenser 9, to increase the second generator E newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the concentrated solution of first generator 1 is through first solution heat exchanger 6, second solution heat exchanger 7, the newly-increased first solution heat exchanger B and the newly-increased second solution heat exchanger F enter the newly-increased second generator E, the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and makes to drive thermal medium, refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of the newly-increased second generator E enters the newly-increased first generator A through the newly-increased second solution pump H and the newly-increased second solution heat exchanger F, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enter second condenser 9 through the newly-increased second choke valve G again, form single-action-triple effect the 3rd class absorption heat pump.
Single-action-backheating type double-effect the 3rd class absorption heat pump shown in Figure 21 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, the 3rd solution pump 16 is set up the weak solution pipeline and is communicated with newly-increased generator A through newly-increased solution heat exchanger B, newly-increased generator A also has the concentrated solution pipeline to be communicated with the 3rd generator 13 through newly-increased solution heat exchanger B, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the part weak solution of second absorber 15 enters newly-increased generator A through the 3rd solution pump 16 and newly-increased solution heat exchanger B, the refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of newly-increased generator A enters the 3rd generator 13 through newly-increased solution heat exchanger B, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enter second condenser 9 through newly-increased choke valve C throttling again, form single-action-backheating type double-effect the 3rd class absorption heat pump.
Single-action-backheating type double-effect the 3rd class absorption heat pump shown in Figure 22 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased first throttle valve, having the weak solution pipeline to be communicated with second generator 2 through the 3rd solution heat exchanger 14 the 3rd solution pump 16 is adjusted into the 3rd solution pump 16 and has the weak solution pipeline to be communicated with second generator 2 through newly-increased solution heat exchanger B and the 3rd solution heat exchanger 14, having the concentrated solution pipeline to be communicated with the 3rd generator 13 through the 3rd solution heat exchanger 14 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 the 3rd solution heat exchanger 14, newly-increased generator A also has the concentrated solution pipeline to be communicated with the 3rd generator 13 through newly-increased solution heat exchanger B, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased first throttle valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9; Cancel the waste heat medium pipeline of the 3rd generator 13 and external communications, increase newly-increased second choke valve, second generator 2 is set up the refrigerant vapour passage and is communicated with back the 3rd generator 13 with the 3rd generator 13 and has cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with second condenser 9.
2. on the flow process, the weak solution of second absorber 15 enters second generator 2 through the 3rd solution pump 16, newly-increased solution heat exchanger B and the 3rd solution heat exchanger 14, the concentrated solution of second generator 2 enters newly-increased generator A through the 3rd solution heat exchanger 14, and the concentrated solution of newly-increased generator A enters the 3rd generator 13 through newly-increased solution heat exchanger B; The refrigerant vapour that second generator 2 produces offers newly-increased generator A respectively and the 3rd generator 13 makes to drive thermal medium, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, refrigerant vapour the 3rd generator 13 of flowing through, heating enters its interior solution release and provides refrigerant vapour to second absorber 15, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enter second condenser 9 through newly-increased first throttle valve C throttling again, the refrigerant vapour heat release of the 3rd generator 13 of flowing through becomes cryogen liquid, enter second condenser 9 through the newly-increased second choke valve G throttling again, form single-action-backheating type double-effect the 3rd class absorption heat pump.
Single-action-backheating type double-effect the 3rd class absorption heat pump shown in Figure 23 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, having the weak solution pipeline to be communicated with second generator 2 through the 3rd solution heat exchanger 14 the 3rd solution pump 16 is adjusted into the 3rd solution pump 16 and has the weak solution pipeline to be communicated with newly-increased generator A through the 3rd solution heat exchanger 14, 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 B, having the concentrated solution pipeline to be communicated with the 3rd generator 13 through the 3rd solution heat exchanger 14 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with the 3rd generator 13 through newly-increased solution heat exchanger B and the 3rd solution heat exchanger 14, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, and the concentrated solution of second generator 2 enters the 3rd generator 13 through newly-increased solution heat exchanger B and the 3rd solution heat exchanger 14; The weak solution of second absorber 15 enters newly-increased generator A through the 3rd solution pump 16 and the 3rd solution heat exchanger 14, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of newly-increased generator A enters second generator 2 through newly-increased solution pump D and newly-increased solution heat exchanger B, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enters second condenser 9 through newly-increased choke valve C throttling again, forms single-action-backheating type double-effect the 3rd class absorption heat pump.
Single-action-backheating type double-effect the 3rd class absorption heat pump shown in Figure 24 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 4, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution choke valve, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest 18 through newly-increased solution choke valve I and absorption-generator 17 through the 3rd solution pump 16 and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into second generator 2 in second generator 2, having the concentrated solution pipeline directly to be communicated with second generator 2 to be adjusted into second solution heat exchanger 7 to have the concentrated solution pipeline directly to increase solution heat exchanger B newly with second generator, 2 connected sums warp respectively second solution heat exchanger 7 is communicated with newly-increased generator A, newly-increased generator A also has the concentrated solution pipeline through the 3rd solution pump 16, newly-increased solution heat exchanger B and absorption-generator 17 are communicated with dividing steam chest 18, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the concentrated solution of first generator 1 is divided into two-way after first solution heat exchanger 6 and second solution heat exchanger 7---and the first via directly enters second generator 2, the second tunnel and enters newly-increased generator A through newly-increased solution heat exchanger B again; The refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, and the absorption-generator 17 of flowing through again after the newly-increased solution choke valve I of concentrated solution warp of second generator 2, heat absorbing part vaporization enter branch steam chest 18; Refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, flow through again through the 3rd solution pump 16 and newly-increased solution heat exchanger B after absorption-generator 17, heat absorbing part of the concentrated solution of newly-increased generator A vaporized and entered branch steam chest 18, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enters second condenser 9 through newly-increased choke valve C throttling again, forms single-action-backheating type double-effect the 3rd class absorption heat pump.
Single-action-backheating type double-effect the 3rd class absorption heat pump shown in Figure 25 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 5, cancel the 4th solution pump, absorber 3 has the weak solution pipeline to be communicated with absorption-generator 17 through the 3rd solution heat exchanger 14; Increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution choke valve, having the concentrated solution pipeline directly to be communicated with second generator 2 to be adjusted into second solution heat exchanger 7 to have the concentrated solution pipeline to increase solution choke valve I through newly-increased solution heat exchanger B newly with second generator, 2 connected sums warp respectively second solution heat exchanger 7 is communicated with newly-increased generator A, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest 18 through newly-increased solution heat exchanger B and absorption-generator 17 through the 3rd solution pump 16 and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into second generator 2 in second generator 2, newly-increased generator A also has the concentrated solution pipeline to be communicated with dividing steam chest 18 through the 3rd solution pump 16 and absorption-generator 17, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9; The refrigerant vapour passage that cancellation evaporimeter 10 is communicated with absorption-generator 17, second generator 2 is set up the refrigerant vapour passage and is communicated with absorption-generator 17.
2. on the flow process, the concentrated solution of first generator 1 is divided into two-way after first solution heat exchanger 6 and second solution heat exchanger 7---and the first via enters second generator 2, the second tunnel through newly-increased solution heat exchanger B again and enters newly-increased generator A through newly-increased solution choke valve I again; Flow through again after newly-increased solution heat exchanger B absorptions-generator 17, heat absorbing part of the concentrated solution that the refrigerant vapour that second generator 2 produces offers newly-increased generator A and absorption-generator 17, the second generators 2 respectively vaporized and entered branch steam chest 18; Refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, flow through again through the 3rd solution pump 16 after absorption-generator 17, heat absorbing part of the concentrated solution of newly-increased generator A vaporized and entered branch steam chest 18, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enters second condenser 9 through newly-increased choke valve C throttling again, forms single-action-backheating type double-effect the 3rd class absorption heat pump.
Single-action-backheating type double-effect the 3rd class absorption heat pump shown in Figure 26 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 4, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased generator A through increasing solution heat exchanger B newly through the 3rd solution pump 16 and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into second generator 2 in second generator 2, newly-increased generator A also has the concentrated solution pipeline through the 3rd solution pump 16, newly-increased solution heat exchanger B and absorption-generator 17 are communicated with dividing steam chest 18, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the concentrated solution of second generator 2 enters newly-increased generator A through newly-increased solution heat exchanger B, the refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of the newly-increased generator A absorption-generator 17 of after the 3rd solution pump 16 and newly-increased solution heat exchanger B, flowing through again, the heat absorbing part vaporization enters branch steam chest 18, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enter second condenser 9 through newly-increased choke valve C throttling again, form single-action-backheating type double-effect the 3rd class absorption heat pump.
Single-action-backheating type double-effect the 3rd class absorption heat pump shown in Figure 27 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 5, cancel the 4th solution pump, absorber 3 has the weak solution pipeline to be communicated with absorption-generator 17 through the 3rd solution heat exchanger 14; Increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, having the concentrated solution pipeline directly to be communicated with second generator 2 to be adjusted into second solution heat exchanger 7 to have concentrated solution pipeline warp to increase solution heat exchanger B newly second solution heat exchanger 7 is communicated with second generator 2, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased generator A through increasing solution heat exchanger B newly through the 3rd solution pump 16 and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into second generator 2 in second generator 2, newly-increased generator A also has the concentrated solution pipeline to be communicated with dividing steam chest 18 through the 3rd solution pump 16 and absorption-generator 17, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9; The refrigerant vapour passage that cancellation evaporimeter 10 is communicated with absorption-generator 17, second generator 2 is set up the refrigerant vapour passage and is communicated with absorption-generator 17.
2. on the flow process, the concentrated solution of first generator 1 enters second generator 2 through first solution heat exchanger 6, second solution heat exchanger 7 and newly-increased solution heat exchanger B, the concentrated solution that the refrigerant vapour that second generator 2 produces offers newly-increased generator A and absorption-generator 17, the second generators 2 respectively enters newly-increased generator A through newly-increased solution heat exchanger B; Refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, flow through again through the 3rd solution pump 16 after absorption-generator 17, heat absorbing part of the concentrated solution of newly-increased generator A vaporized and entered branch steam chest 18, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enters second condenser 9 through newly-increased choke valve C throttling again, forms single-action-backheating type double-effect the 3rd class absorption heat pump.
Single-action-backheating type double-effect the 3rd class absorption heat pump shown in Figure 28 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 5, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest 18 through newly-increased solution choke valve I and absorption-generator 17 through the 3rd solution pump 16 and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into second generator 2 in second generator 2, there is the concentrated solution pipeline to be communicated with second generator 2 to be adjusted into second solution heat exchanger 7 to have the concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased solution heat exchanger B second solution heat exchanger 7, newly-increased generator A also has the concentrated solution pipeline to be communicated with second generator 2 through the 3rd solution pump 16 and newly-increased solution heat exchanger B, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the concentrated solution of first generator 1 is through first solution heat exchanger 6, second solution heat exchanger 7 and newly-increased solution heat exchanger B enter newly-increased generator A, the refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of newly-increased generator A enters second generator 2 through the 3rd solution pump 16 and newly-increased solution heat exchanger B, the concentrated solution of the second generator 2 absorption-generator 17 of after newly-increased solution choke valve I, flowing through again, the heat absorbing part vaporization enters branch steam chest 18, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enter second condenser 9 through newly-increased choke valve C throttling again, form single-action-backheating type double-effect the 3rd class absorption heat pump.
Single-action-backheating type double-effect the 3rd class absorption heat pump shown in Figure 29 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 5, cancel the 4th solution pump, absorber 3 has the weak solution pipeline to be communicated with absorption-generator 17 through the 3rd solution heat exchanger 14; Increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, second solution heat exchanger 7 had the concentrated solution pipeline to be communicated with second generator 2 to be adjusted into second solution heat exchanger 7 has the concentrated solution pipeline to be communicated with newly-increased generator A, newly-increased generator A also has the concentrated solution pipeline to be communicated with second generator 2 through the 3rd solution pump 16 and newly-increased solution heat exchanger B, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest 18 through newly-increased solution heat exchanger B and absorption-generator 17 through the 3rd solution pump 16 and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into second generator 2 in second generator 2, having the refrigerant vapour passage to be communicated with second condenser 9 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 second condenser 9 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second condenser 9; The refrigerant vapour passage that cancellation evaporimeter 10 is communicated with absorption-generator 17, second generator 2 is set up the refrigerant vapour passage and is communicated with absorption-generator 17.
2. on the flow process, the concentrated solution of first generator 1 enters newly-increased generator A through first solution heat exchanger 6 and second solution heat exchanger 7, the refrigerant vapour that second generator 2 produces offers newly-increased generator A and absorption-generator 17 respectively, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of newly-increased generator A enters second generator 2 through the 3rd solution pump 16 and newly-increased solution heat exchanger B, the concentrated solution of the second generator 2 absorption-generator 17 of after newly-increased solution heat exchanger B, flowing through again, the heat absorbing part vaporization enters branch steam chest 18, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enter second condenser 9 through newly-increased choke valve C throttling again, form single-action-backheating type double-effect the 3rd class absorption heat pump.
Single-action-back-heating type triple-effect the 3rd class absorption heat pump shown in Figure 30 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 24, increase newly-increased second generator, newly-increased second choke valve, the newly-increased second solution choke valve and newly-increased the 3rd solution choke valve, having the concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased solution heat exchanger B second solution heat exchanger 7 is adjusted into second solution heat exchanger 7 and has concentrated solution pipeline warp to increase the second solution choke valve J newly to be communicated with newly-increased generator A, to increase generator A newly and the concentrated solution pipeline be arranged through the 3rd solution pump 16, newly-increased solution heat exchanger B and absorption-generator 17 have the concentrated solution pipeline to be communicated with branch steam chest 18 through increasing the 3rd solution choke valve K and absorption-generator 17 newly with dividing steam chest 18 to be communicated with to be adjusted into newly-increased generator A, second solution heat exchanger 7 is set up the concentrated solution pipeline and is communicated with the newly-increased second generator E through newly-increased solution heat exchanger B, and the newly-increased second generator E also has the concentrated solution pipeline through the 3rd solution pump
16, newly-increased solution heat exchanger B and absorption-generator 17 are communicated with dividing steam chest 18, to increase the first generator A newly has the refrigerant vapour passage to be communicated with second condenser 9 to be adjusted into the newly-increased first generator A to have the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with second condenser 9, to increase the second generator E newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the concentrated solution of first generator 1 is divided into three the tunnel after first solution heat exchanger 6 and second solution heat exchanger 7---and the first via directly enters second generator 2, the newly-increased second solution choke valve J of the second road warp enters the newly-increased first generator A, and Third Road enters through newly-increased solution heat exchanger B and increases the second generator E newly; The refrigerant vapour of newly-increased first generator A generation offers the newly-increased second generator E and makes to drive thermal medium, and the absorption-generator 17 of flowing through again after newly-increased the 3rd solution choke valve K of concentrated solution warp of the newly-increased first generator A, heat absorbing part vaporization enter branch steam chest 18; Refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, flow through again through the 3rd solution pump 16 and newly-increased solution heat exchanger B after absorption-generator 17, heat absorbing part of the concentrated solution of the newly-increased second generator E vaporized and entered branch steam chest 18, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enters second condenser 9 through the newly-increased second choke valve G throttling again, forms single-action-back-heating type triple-effect the 3rd class absorption heat pump.
Single-action-back-heating type triple-effect the 3rd class absorption heat pump shown in Figure 31 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 25, increase newly-increased second generator, newly-increased second choke valve, the newly-increased second solution choke valve and newly-increased the 3rd solution choke valve, to increase the first generator A newly has the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest 18 through the newly-increased second solution choke valve J and absorption-generator 17 through the 3rd solution pump 16 and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into the newly-increased first generator A, second solution heat exchanger 7 is set up the concentrated solution pipeline and is communicated with the newly-increased second generator E through newly-increased the 3rd solution choke valve K, the newly-increased second generator E also has the concentrated solution pipeline to be communicated with dividing steam chest 18 through the 3rd solution pump 16 and absorption-generator 17, to increase the first generator A newly has the refrigerant vapour passage to be communicated with second condenser 9 to be adjusted into the newly-increased first generator A to have the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with second condenser 9, to increase the second generator E newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the refrigerant vapour of newly-increased first generator A generation offers the newly-increased second generator E and makes to drive thermal medium, and the absorption-generator 17 of flowing through again after the newly-increased second solution choke valve J of concentrated solution warp of the newly-increased first generator A, heat absorbing part vaporization enter branch steam chest 18; The part concentrated solution of first generator 1 is through first solution heat exchanger 6, second solution heat exchanger 7 and newly-increased the 3rd solution choke valve K enter the newly-increased second generator E, refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of the newly-increased second generator E absorption-generator 17 of after the 3rd solution pump 16, flowing through again, the heat absorbing part vaporization enters branch steam chest 18, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enter second condenser 9 through the newly-increased second choke valve G again, form single-action-back-heating type triple-effect the 3rd class absorption heat pump.
Single-action-back-heating type triple-effect the 3rd class absorption heat pump shown in Figure 32 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 31, the newly-increased first solution choke valve of cancellation and the newly-increased second solution choke valve, increase newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with the newly-increased first generator A through the newly-increased first solution choke valve I second solution heat exchanger 7 is adjusted into second solution heat exchanger 7 and has concentrated solution pipeline warp to increase the second solution heat exchanger F newly to be communicated with the newly-increased first generator A, to increase the first generator A newly has the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest 18 through the newly-increased second solution heat exchanger F and absorption-generator 17 through the newly-increased second solution choke valve J and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into the newly-increased first generator A, second generator 2 is had the refrigerant vapour passage to be communicated with absorption-generator 17 to be adjusted into increase the first generator A newly and have the refrigerant vapour passage to be communicated with absorption-generator 17.
2. on the flow process, the part concentrated solution of first generator 1 enters the newly-increased first generator A through first solution heat exchanger 6, second solution heat exchanger 7 and the newly-increased first solution heat exchanger B, the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and absorption-generator 17 respectively, flow through again after the newly-increased second solution heat exchanger F absorptions-generator 17, heat absorbing part vaporization of the concentrated solution of the newly-increased first generator A enters branch steam chest 18, formation single-action-back-heating type triple-effect the 3rd class absorption heat pump.
Single-action-back-heating type triple-effect the 3rd class absorption heat pump shown in Figure 33 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 26, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, to increase the first generator A newly and the concentrated solution pipeline be arranged through the 3rd solution pump 16, newly-increased solution heat exchanger B and absorption-generator 17 with divide steam chest 18 to be communicated with to be adjusted into the newly-increased first generator A to have concentrated solution pipeline warp to increase the second solution heat exchanger F newly to be communicated with the newly-increased second generator E, the newly-increased second generator E also has the concentrated solution pipeline through the 3rd solution pump 16, the newly-increased second solution heat exchanger F, the newly-increased first solution heat exchanger B and absorption-generator 17 are communicated with dividing steam chest 18, to increase the first generator A newly has the refrigerant vapour passage to be communicated with second condenser 9 to be adjusted into the newly-increased first generator A to have the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with second condenser 9, to increase the second generator E newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and makes to drive thermal medium, and the concentrated solution of the newly-increased first generator A enters the newly-increased second generator E through the newly-increased second solution heat exchanger F; Refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, flow through again after the 3rd solution pump 16, the newly-increased second solution heat exchanger F and newly-increased first solution heat exchanger B absorption-generator 17, heat absorbing part of the concentrated solution of the newly-increased second generator E vaporized and entered branch steam chest 18, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enters second condenser 9 through the newly-increased second choke valve G again, forms single-action-back-heating type triple-effect the 3rd class absorption heat pump.
Single-action-back-heating type triple-effect the 3rd class absorption heat pump shown in Figure 34 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 27, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, to increase the first generator A newly has the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with the newly-increased second generator E through increasing the second solution heat exchanger F newly through the 3rd solution pump 16 and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into the newly-increased first generator A, the newly-increased second generator E also has the concentrated solution pipeline through the 3rd solution pump 16, the newly-increased second solution heat exchanger F and absorption-generator 17 are communicated with dividing steam chest 18, to increase the first generator A newly has the refrigerant vapour passage to be communicated with second condenser 9 to be adjusted into the newly-increased first generator A to have the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with second condenser 9, to increase the second generator E newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and makes to drive thermal medium, and the concentrated solution of the newly-increased first generator A enters the newly-increased second generator E through the newly-increased second solution heat exchanger F; Refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, flow through again after the 3rd solution pump 16 and newly-increased second solution heat exchanger F absorption-generator 17, heat absorbing part of the concentrated solution of the newly-increased second generator E vaporized and entered branch steam chest 18, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enters second condenser 9 through the newly-increased second choke valve G again, forms single-action-back-heating type triple-effect the 3rd class absorption heat pump.
Single-action-back-heating type triple-effect the 3rd class absorption heat pump shown in Figure 35 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 34, with second solution heat exchanger 7 have the concentrated solution pipeline through the newly-increased first solution heat exchanger B is communicated with second generator 2 be adjusted into second solution heat exchanger 7 have the concentrated solution pipeline through the newly-increased second solution heat exchanger F with increase the first solution heat exchanger B newly and be communicated with second generator 2, to increase the second generator E newly and the concentrated solution pipeline be arranged through the 3rd solution pump 16, the newly-increased second solution heat exchanger F and absorption-generator 17 have the concentrated solution pipeline to be communicated with branch steam chest 18 through the 3rd solution pump 16 and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into the newly-increased second generator E, second generator 2 are had the refrigerant vapour passage to be communicated with absorption-generator 17 to be adjusted into increase the first generator A newly and have the refrigerant vapour passage to be communicated with absorption-generator 17.
2. on the flow process, the concentrated solution of first generator 1 is through first solution heat exchanger 6, second solution heat exchanger 7, the newly-increased second solution heat exchanger F and the newly-increased first solution heat exchanger B enter second generator 2, the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and absorption-generator 17 respectively, refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of the newly-increased second generator E absorption-generator 17 of after the 3rd solution pump 16, flowing through again, the heat absorbing part vaporization enters branch steam chest 18, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enter second condenser 9 through the newly-increased second choke valve G again, form single-action-back-heating type triple-effect the 3rd class absorption heat pump.
Single-action-back-heating type triple-effect the 3rd class absorption heat pump shown in Figure 36 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 28, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased solution pump, having the concentrated solution pipeline to be communicated with the newly-increased first generator A through the newly-increased first solution heat exchanger B second solution heat exchanger 7 is adjusted into second solution heat exchanger 7 and has concentrated solution pipeline warp to increase the second solution heat exchanger F newly to be communicated with the newly-increased second generator E, the newly-increased second generator E also has the concentrated solution pipeline through newly-increased solution pump D, the newly-increased second solution heat exchanger F and the newly-increased first solution heat exchanger B are communicated with the newly-increased first generator A, to increase the first generator A newly has the refrigerant vapour passage to be communicated with second condenser 9 to be adjusted into the newly-increased first generator A to have the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with second condenser 9, to increase the second generator E newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, the concentrated solution of first generator 1 is through first solution heat exchanger 6, second solution heat exchanger 7 and the newly-increased second solution heat exchanger F enter the newly-increased second generator E, the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and makes to drive thermal medium, refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of the newly-increased second generator E is through newly-increased solution pump D, the newly-increased second solution heat exchanger F and the newly-increased first solution heat exchanger B enter the newly-increased first generator A, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enter second condenser 9 through the newly-increased second choke valve G again, form single-action-back-heating type triple-effect the 3rd class absorption heat pump.
Single-action-back-heating type triple-effect the 3rd class absorption heat pump shown in Figure 37 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 29, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased solution pump, there is the concentrated solution pipeline to be communicated with the newly-increased first generator A to be adjusted into second solution heat exchanger 7 to have the concentrated solution pipeline to be communicated with the newly-increased second generator E through the newly-increased second solution heat exchanger F second solution heat exchanger 7, the newly-increased second generator E also has the concentrated solution pipeline to be communicated with the newly-increased first generator A through newly-increased solution pump D and the newly-increased second solution heat exchanger F, to increase the first generator A newly has the refrigerant vapour passage to be communicated with second condenser 9 to be adjusted into the newly-increased first generator A to have the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with second condenser 9, to increase the second generator E newly and also have the refrigerant vapour passage to be communicated with second condenser 9.
2. on the flow process, first generator, 1 concentrated solution is through first solution heat exchanger 6, second solution heat exchanger 7 and the newly-increased second solution heat exchanger F enter the newly-increased second generator E, the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and makes to drive thermal medium, refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of the newly-increased second generator E enters the newly-increased first generator A through newly-increased solution pump D and the newly-increased second solution heat exchanger F, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enter second condenser 9 through the newly-increased second choke valve G again, form single-action-back-heating type triple-effect the 3rd class absorption heat pump.
Single-action-back-heating type triple-effect the 3rd class absorption heat pump shown in Figure 38 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 37, having the concentrated solution pipeline to be communicated with the newly-increased second generator E through the newly-increased second solution heat exchanger F second solution heat exchanger 7 is adjusted into second solution heat exchanger 7 and has the concentrated solution pipeline directly to be communicated with the newly-increased second generator E, there is the concentrated solution pipeline to have concentrated solution pipeline warp to increase the first solution heat exchanger B newly through the newly-increased first solution heat exchanger B and absorption-generator 17 with dividing steam chest 18 to be communicated with to be adjusted into second generator 2 in second generator 2, the newly-increased second solution heat exchanger F and absorption-generator 17 are communicated with dividing steam chest 18, second generator 2 are had the refrigerant vapour passage to be communicated with absorption-generator 17 to be adjusted into increase the first generator A newly and have the refrigerant vapour passage to be communicated with absorption-generator 17.
2. on the flow process, the absorption-generator 17 of flowing through again after the newly-increased first solution heat exchanger B of the concentrated solution of second generator 2 warp and the newly-increased second solution heat exchanger F, heat absorbing part are vaporized and are entered branch steam chest 18; First generator, 1 concentrated solution enters the newly-increased second generator E through first solution heat exchanger 6 and second solution heat exchanger 7, the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and absorption-generator 17 respectively, refrigerant vapour is flowed through and is increased the second generator E newly, heating enters its interior solution release and provides refrigerant vapour to second condenser 9, the concentrated solution of the newly-increased second generator E enters the newly-increased first generator A through newly-increased solution pump D and the newly-increased second solution heat exchanger F, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enter second condenser 9 through the newly-increased second choke valve G again, form single-action-back-heating type triple-effect the 3rd class absorption heat pump.
Single-action shown in Figure 39-1.5 grade the 3rd class absorption heat pump is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 2, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, having the weak solution pipeline to be communicated with first solution heat exchanger 6 through first solution pump 4 absorber 3 is adjusted into absorber 3 and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter L through newly-increased solution heat exchanger B, newly-increased absorption-evaporimeter L also has the weak solution pipeline to be communicated with first solution heat exchanger 6 through first solution pump 4 and newly-increased solution heat exchanger B, evaporimeter 10 had the refrigerant vapour passage to be communicated with absorber 3 to be adjusted into evaporimeter 10 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter L, evaporimeter 10 set up the cryogen liquid pipeline through newly-increased cryogen liquid pump M with increase absorption-evaporimeter L newly after newly-increased absorption-evaporimeter L is communicated with and have the refrigerant vapour passage to be communicated with absorber 3 again.
2. on the flow process, the weak solution of absorber 3 enters newly-increased absorption-evaporimeter L, the refrigerant vapour that absorbs flash-pot 10 and heat release in the cryogen liquid of the newly-increased absorption-evaporimeter L that flows through through newly-increased solution heat exchanger B, and the weak solution of newly-increased absorption-evaporimeter L enters first generator 1 through first solution pump 4, newly-increased solution heat exchanger B and first solution heat exchanger 6; The cryogen liquid of evaporimeter 10 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to newly-increased absorption-evaporimeter L, the second the tunnel flows through after newly-increased cryogen liquid pump M pressurization again increases absorption-evaporimeter L newly, absorbs heat into refrigerant vapour and formation single-action-1.5 grade the 3rd class absorption heat pump is provided to absorber 3.
Single-action shown in Figure 40-1.5 grade the 3rd class absorption heat pump is achieved in that
In the 3rd class absorption heat pump shown in Figure 39, there is the concentrated solution pipeline to be communicated with absorber 3 to be adjusted into second solution heat exchanger 7 to have the concentrated solution pipeline to be communicated with absorber 3 through newly-increased solution heat exchanger B second solution heat exchanger 7, to increase absorption-evaporimeter L newly has the weak solution pipeline to be communicated with first solution heat exchanger 6 through first solution pump 4 and newly-increased solution heat exchanger B to be adjusted into newly-increased absorptions-evaporimeter L and to have the weak solution pipeline to be communicated with first solution heat exchanger 6 through first solution pump 4, formation single-action-1.5 grade the 3rd class absorption heat pump.
Single-action shown in Figure 41-1.5 grade the 3rd class absorption heat pump is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 39, increase newly-increased solution pump, second solution heat exchanger 7 had the concentrated solution pipeline to be communicated with absorber 3 to be adjusted into second solution heat exchanger 7 has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter L, to increase absorption-evaporimeter L newly has the weak solution pipeline to be communicated with first solution heat exchanger 6 through first solution pump 4 and newly-increased solution heat exchanger B to be adjusted into newly-increased absorptions-evaporimeter L and to have the weak solution pipeline to be communicated with absorber 3 through first solution pump 4 and newly-increased solution heat exchanger B, has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter L and to be adjusted into absorber 3 and to have weak solution pipeline warp to increase solution heat exchanger B newly and newly-increased solution pump D is communicated with first solution heat exchanger 6 through increasing solution heat exchanger B newly absorber 3.
2. on the flow process, the concentrated solution of second generator 2 enters newly-increased absorption-evaporimeter L through second solution pump 5 and second solution heat exchanger 7, absorb refrigerant vapour and the heat release of flash-pot 10 to increase the cryogen liquid of absorption-evaporimeter L newly in flowing through, the weak solution of newly-increased absorption-evaporimeter L enters absorber 3 through first solution pump 4 and newly-increased solution heat exchanger B, absorption from the refrigerant vapour of newly-increased absorption-evaporimeter L and heat release in heated medium, the weak solution of absorber 3 is through newly-increased solution heat exchanger B, newly-increased solution pump D and first solution heat exchanger 6 enter first generator 1, form single-action-1.5 grade the 3rd class absorption heat pump.
Single-action shown in Figure 42-1.5 grade the 3rd class absorption heat pump is achieved in that
In the 3rd class absorption heat pump shown in Figure 41, there is the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter L to be adjusted into second solution heat exchanger 7 to have the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter L through newly-increased solution heat exchanger B second solution heat exchanger 7, having the weak solution pipeline to be communicated with first solution heat exchanger 6 through newly-increased solution heat exchanger B and newly-increased solution pump D absorber 3 is adjusted into absorber 3 and has the weak solution pipeline to be communicated with first solution heat exchanger 6 through increasing solution pump D newly, formation single-action-1.5 grade the 3rd class absorption heat pump.
1.5 grade of the 3rd class absorption heat pump of single-action-back-heating type shown in Figure 43 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, having the weak solution pipeline to be communicated with first solution heat exchanger 6 through first solution pump 4 absorber 3 is adjusted into absorber 3 and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter L through newly-increased solution heat exchanger B, newly-increased absorption-evaporimeter L also has the weak solution pipeline to be communicated with first solution heat exchanger 6 through first solution pump 4 and newly-increased solution heat exchanger B, evaporimeter 10 had the refrigerant vapour passage to be communicated with absorber 3 to be adjusted into evaporimeter 10 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter L, evaporimeter 10 set up the cryogen liquid pipeline through newly-increased cryogen liquid pump M with increase absorption-evaporimeter L newly after newly-increased absorption-evaporimeter L is communicated with and have the refrigerant vapour passage to be communicated with absorber 3 again.
2. on the flow process, the weak solution of absorber 3 enters newly-increased absorption-evaporimeter L, the refrigerant vapour that absorbs flash-pot 10 and heat release in the cryogen liquid of the newly-increased absorption-evaporimeter L that flows through through newly-increased solution heat exchanger B, and the weak solution of newly-increased absorption-evaporimeter L enters first generator 1 through first solution pump 4, newly-increased solution heat exchanger B and first solution heat exchanger 6; The cryogen liquid of evaporimeter 10 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to newly-increased absorption-evaporimeter L, the second the tunnel flows through after newly-increased cryogen liquid pump M pressurization again increases absorption-evaporimeter L newly, absorbs heat into refrigerant vapour and 1.5 grade of the 3rd class absorption heat pump of formation single-action-back-heating type is provided to absorber 3.
1.5 grade of the 3rd class absorption heat pump of single-action-back-heating type shown in Figure 44 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 4, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, having the weak solution pipeline to be communicated with absorption-generator 17 through the 4th solution pump 27 and the 3rd solution heat exchanger 14 absorber 3 is adjusted into absorber 3 and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter L through newly-increased solution heat exchanger B, newly-increased absorption-evaporimeter L also has the weak solution pipeline through the 4th solution pump 27, newly-increased solution heat exchanger B and the 3rd solution heat exchanger 14 are communicated with absorption-generator 17, evaporimeter 10 had the refrigerant vapour passage to be communicated with absorber 3 to be adjusted into evaporimeter 10 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter L, evaporimeter 10 set up the cryogen liquid pipeline through newly-increased cryogen liquid pump M with increase absorption-evaporimeter L newly after newly-increased absorption-evaporimeter L is communicated with and have the refrigerant vapour passage to be communicated with absorber 3 again.
2. on the flow process, the weak solution of absorber 3 enters newly-increased absorption-evaporimeter L, the refrigerant vapour that absorbs flash-pot 10 and heat release in the cryogen liquid of the newly-increased absorption-evaporimeter L that flows through through newly-increased solution heat exchanger B, and the weak solution of newly-increased absorption-evaporimeter L enters absorption-generator 17 through the 4th solution pump 27, newly-increased solution heat exchanger B and the 3rd solution heat exchanger 14; The cryogen liquid of evaporimeter 10 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to newly-increased absorption-evaporimeter L, the second the tunnel flows through after newly-increased cryogen liquid pump M pressurization again increases absorption-evaporimeter L newly, absorbs heat into refrigerant vapour and 1.5 grade of the 3rd class absorption heat pump of formation single-action-back-heating type is provided to absorber 3.
The effect that the technology of the present invention can realize---the 3rd class absorption-generation systems and the 3rd class absorption heat pump proposed by the invention have following effect and advantage:
1. the 3rd class absorption-generation systems of Ti Chuing, structure and flow process advantages of simple; Two kinds of driving forces are applied in the absorption-generation systems, are that the basis has been set up in the generation of the 3rd class absorption heat pump; Be conducive to bring extra power into play action of thermal difference between resource and the cooling medium is conducive to reduce the requirement to the high temperature driven heat medium temperature.
2. series the 3rd class absorption heat pump of Ti Chuing has the high and excellent double grading of the second class absorption heat pump performance index of first kind absorption heat pump heat supply temperature, can improve the residual heat resources utilization rate.
3. series the 3rd class absorption heat pump of Ti Chuing has good creativeness, novelty and practicality, has further enriched the diversity of absorption heat pump kind, can realize the mutual coupling between heat pump heat supply and the user's request better.
4. series the 3rd class absorption heat pump of Ti Chuing, when the temperature difference between residual heat resources and the cooler environment was big, the effect of the resource that is conducive to bring extra power into play was correspondingly further brought into play the effect of high temperature driven heat or is reduced temperature requirement to high temperature driven heat.
5. utilize the 3rd class absorption heat pump of the present invention, residual heat resources than horn of plenty, especially exist based on latent heat enrich residual heat resources the time, can realize the further lifting of waste heat supply temperature; Can utilize the waste heat of low temperature more and provide the heat supply of higher temperature to the user, enlarge the temperature operation interval of absorption heat pump, expand and enriched the range of application of absorption heat pump.

Claims (70)

1. the 3rd class absorption-generation systems mainly is made up of first generator, second generator, absorber, first solution pump, second solution pump, first solution heat exchanger and second solution heat exchanger; Absorber (3) has the weak solution pipeline to be communicated with first generator (1) through first solution pump (4) and first solution heat exchanger (6), first generator (1) also has the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7), second generator (2) also has the concentrated solution pipeline to be communicated with absorber (3) through second solution pump (5) and second solution heat exchanger (7), first generator (1) also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, second generator (2) also has refrigerant vapour passage and external communications respectively and have surplus heat medium pipeline and external communications, absorber (3) also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, and forms the 3rd class absorption-generation systems.
2. the 3rd class absorption heat pump, be in described the 3rd class absorption-generation systems of claim 1, increase by first condenser, second condenser, evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator (1) in first generator (1) has the refrigerant vapour passage to be communicated with first condenser (8), first condenser (8) also has the cryogen liquid pipeline to be communicated with evaporimeter (10) through choke valve (11), having refrigerant vapour passage and external communications to be defined as second generator (2) in second generator (2) has the refrigerant vapour passage to be communicated with second condenser (9), second condenser (9) also has the cryogen liquid pipeline to be communicated with evaporimeter (10) through cryogen liquid pump (12), having refrigerant vapour passage and external communications to be defined as evaporimeter (10) absorber (3) has the refrigerant vapour passage to be communicated with absorber (3), first condenser (8) also has heated medium pipeline and external communications, second condenser (9) also has cooling medium pipeline and external communications, evaporimeter (10) also have surplus heat medium pipeline and external communications form the 3rd class absorption heat pump.
3. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 2, increase by the 3rd generator, the 3rd solution heat exchanger, second absorber and the 3rd solution pump, having the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with second absorber (15) through first solution heat exchanger (6) and second solution heat exchanger (7), second absorber (15) also has the weak solution pipeline to be communicated with second generator (2) through the 3rd solution pump (16) and the 3rd solution heat exchanger (14), having the concentrated solution pipeline to be communicated with absorber (3) through second solution pump (5) and second solution heat exchanger (7) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with the 3rd generator (13) through the 3rd solution heat exchanger (14), the 3rd generator (13) also has the concentrated solution pipeline to be communicated with absorber (3) through second solution pump (5) and second solution heat exchanger (7), the 3rd generator (13) also has refrigerant vapour passage and second absorber (15) connected sum have surplus heat medium pipeline and external communications respectively, second absorber (15) also has cooling medium pipeline and external communications, forms back-heating type the 3rd class absorption heat pump.
4. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 2, increase absorption-generator, divide steam chest, the 3rd condenser, second evaporimeter, the second cryogen liquid pump, the 3rd solution heat exchanger, the 3rd solution pump and the 4th solution pump, having the weak solution pipeline to be communicated with first generator (1) through first solution pump (4) and first solution heat exchanger (6) absorber (3) is adjusted into absorber (3) and has the weak solution pipeline to be communicated with absorption-generator (17) through the 4th solution pump (27) and the 3rd solution heat exchanger (14), absorption-generator (17) also has the weak solution pipeline through first solution pump (4), the 3rd solution heat exchanger (14) and first solution heat exchanger (6) are communicated with first generator (1), having the concentrated solution pipeline to be communicated with absorber (3) through second solution pump (5) and second solution heat exchanger (7) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with dividing steam chest (18) through the 3rd solution pump (16) and absorption-generator (17), divide steam chest (18) to also have the concentrated solution pipeline to be communicated with absorber (3) through second solution pump (5) and second solution heat exchanger (7), divide steam chest (18) to also have the refrigerant vapour passage to be communicated with the 3rd condenser (19), the 3rd condenser (19) also has the cryogen liquid pipeline to be communicated with second evaporimeter (20) through the second cryogen liquid pump (21), second evaporimeter (20) also has the refrigerant vapour passage to be communicated with absorption-generator (17), the 3rd condenser (19) also has cooling medium pipeline and external communications, second evaporimeter (20) also have surplus heat medium pipeline and external communications, absorption-generator (17) or also have heated medium pipeline and external communications forms back-heating type the 3rd class absorption heat pump; Wherein: when 1. not having second evaporimeter, the 3rd condenser (19) has the cryogen liquid pipeline to be communicated with first evaporimeter (10) through the second cryogen liquid pump (21), and first evaporimeter (10) is set up the refrigerant vapour passage and is communicated with absorption-generator (17); When 2. not having second evaporimeter, second condenser, the 3rd solution pump and the second cryogen liquid pump, second generator (2) has the concentrated solution pipeline to be communicated with dividing steam chest (18) through absorption-generator (17), divide steam chest (18) to have the refrigerant vapour passage to be communicated with first condenser (9), first evaporimeter (10) is set up the refrigerant vapour passage and is communicated with absorption-generator (17).
5. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 2, increase by the 3rd generator, the 3rd solution heat exchanger and second choke valve, first solution pump (4) is set up the weak solution pipeline and is communicated with the 3rd generator (13) through the 3rd solution heat exchanger (14), the 3rd generator (13) also has the concentrated solution pipeline to converge through first solution heat exchanger (6) concentrated solution pipeline afterwards with first generator (1) afterwards through the 3rd solution heat exchanger (14), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (13) with the 3rd generator (13) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (8) through second choke valve (23) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (13) also has the refrigerant vapour passage to be communicated with first condenser (8), forms economic benefits and social benefits-single-action the 3rd class absorption heat pump.
6. the 3rd class absorption heat pump, be in claim 2 the 3rd class absorption heat pump, increase by the 3rd generator, the 3rd solution heat exchanger and second choke valve, having the weak solution pipeline to be communicated with first generator (1) through first solution pump (4) and first solution heat exchanger (6) absorber (3) is adjusted into absorber (3) and the weak solution pipeline is arranged through first solution pump (4), first solution heat exchanger (6) and the 3rd solution heat exchanger (14) are communicated with first generator (1), having the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with the 3rd generator (13) through the 3rd solution heat exchanger (14), the 3rd generator (13) also has the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (13) with the 3rd generator (13) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (8) through second choke valve (23) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (13) also has the refrigerant vapour passage to be communicated with first condenser (8), forms economic benefits and social benefits-single-action the 3rd class absorption heat pump.
7. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 6, increase the solution choke valve, absorber (3) there is the weak solution pipeline through first solution pump (4), first solution heat exchanger (6) and the 3rd solution heat exchanger (14) are communicated with first generator (1) and are adjusted into absorber (3) and the weak solution pipeline are arranged through first solution pump (4), first solution heat exchanger (6) is communicated with first generator (1) through the 3rd solution heat exchanger (14) with the 3rd generator (13) connected sum through solution choke valve (22) respectively afterwards more again, forms economic benefits and social benefits-single-action the 3rd class absorption heat pump.
8. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 2, increase by the 3rd generator, the 3rd solution heat exchanger, the 3rd solution pump and second choke valve, having the weak solution pipeline to be communicated with first generator (1) through first solution pump (4) and first solution heat exchanger (6) absorber (3) is adjusted into absorber (3) and has the weak solution pipeline to be communicated with the 3rd generator (13) through first solution pump (4) and first solution heat exchanger (6), the 3rd generator (13) also has the concentrated solution pipeline to be communicated with first generator (1) through the 3rd solution pump (16) and the 3rd solution heat exchanger (14), having the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7) in first generator (1) is adjusted into first generator (1) and the concentrated solution pipeline is arranged through the 3rd solution heat exchanger (14), first solution heat exchanger (6) and second solution heat exchanger (7) are communicated with second generator (2), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (13) with the 3rd generator (13) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (8) through second choke valve (23) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (13) also has the refrigerant vapour passage to be communicated with first condenser (8), forms economic benefits and social benefits-single-action the 3rd class absorption heat pump.
9. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 8, increase the solution choke valve, having the weak solution pipeline to be communicated with the 3rd generator (13) through first solution pump (4) and first solution heat exchanger (6) absorber (3) is adjusted into absorber (3) and has the weak solution pipeline directly to be communicated with the 3rd generator (13) through solution choke valve (22) with first generator (1) connected sum respectively afterwards through first solution pump (4) and first solution heat exchanger (6) again, form economic benefits and social benefits-single-action the 3rd class absorption heat pump.
10. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 5, increase by the 4th generator, the 4th solution heat exchanger and the 3rd choke valve, first solution pump (4) is set up the weak solution pipeline and is communicated with the 4th generator (24) through the 4th solution heat exchanger (25), the 4th generator (24) also has the concentrated solution pipeline to converge through first solution heat exchanger (6) concentrated solution pipeline afterwards with first generator (1) afterwards through the 4th solution heat exchanger (25), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into the 3rd generator (13) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (13) has the cryogen liquid pipeline to be communicated with first condenser (8) through the 3rd choke valve (26) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (8), forms triple effect-single-action the 3rd class absorption heat pump.
11. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 6, increase by the 4th generator, the 4th solution heat exchanger and the 3rd choke valve, absorber (3) there is the weak solution pipeline through first solution pump (4), first solution heat exchanger (6) and the 3rd solution heat exchanger (14) are communicated with first generator (1) and are adjusted into absorber (3) and the weak solution pipeline are arranged through first solution pump (4), first solution heat exchanger (6), the 4th solution heat exchanger (25) and the 3rd solution heat exchanger (14) are communicated with first generator (1), having the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7) in the 3rd generator (13) is adjusted into the 3rd generator (13) and has the concentrated solution pipeline to be communicated with the 4th generator (24) through the 4th solution heat exchanger (25), the 4th generator (24) also has the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into the 3rd generator (13) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (13) has the cryogen liquid pipeline to be communicated with first condenser (8) through the 3rd choke valve (26) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (8), forms triple effect-single-action the 3rd class absorption heat pump.
12. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 8, increase by the 4th generator, the 4th solution heat exchanger, the 3rd choke valve and the 4th solution pump, having the weak solution pipeline to be communicated with the 3rd generator (13) through first solution pump (4) and first solution heat exchanger (6) absorber (3) is adjusted into absorber (3) and has the weak solution pipeline to be communicated with the 4th generator (24) through first solution pump (4) and first solution heat exchanger (6), the 4th generator (24) also has the concentrated solution pipeline to be communicated with the 3rd generator (13) through the 4th solution pump (27) and the 4th solution heat exchanger (25), first generator (1) there is the concentrated solution pipeline through the 3rd solution heat exchanger (14), first solution heat exchanger (6) and second solution heat exchanger (7) are communicated with second generator (2) and are adjusted into first generator (1) and the concentrated solution pipeline are arranged through the 3rd solution heat exchanger (14), the 4th solution heat exchanger (25), first solution heat exchanger (6) and second solution heat exchanger (7) are communicated with second generator (2), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into the 3rd generator (13) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (13) has the cryogen liquid pipeline to be communicated with first condenser (8) through the 3rd choke valve (26) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (8), forms triple effect-single-action the 3rd class absorption heat pump.
13. the 3rd class absorption heat pump, be in described the 3rd class absorption-generation systems of claim 3, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, first solution pump (4) is set up the weak solution pipeline and is communicated with the 4th generator (24) through the 4th solution heat exchanger (25), the 4th generator (24) also has the concentrated solution pipeline to converge through first solution heat exchanger (6) concentrated solution pipeline afterwards with first generator (1) afterwards through the 4th solution heat exchanger (25), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (8) through second choke valve (23) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 4th generator, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (8), forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
14. the 3rd class absorption heat pump, be in claim 3 the 3rd class absorption heat pump, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, having the weak solution pipeline to be communicated with first generator (1) through first solution pump (4) and first solution heat exchanger (6) absorber (3) is adjusted into absorber (3) and the weak solution pipeline is arranged through first solution pump (4), first solution heat exchanger (6) and the 4th solution heat exchanger (25) are communicated with first generator (1), having the concentrated solution pipeline to be communicated with second absorber (15) through first solution heat exchanger (6) and second solution heat exchanger (7) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with the 4th generator (24) through the 4th solution heat exchanger (25), the 4th generator (24) also has the concentrated solution pipeline to be communicated with second absorber (15) through first solution heat exchanger (6) and second solution heat exchanger (7), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (8) through second choke valve (23) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 4th generator, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (8), forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
15. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 14, increase the solution choke valve, absorber (3) there is the weak solution pipeline through first solution pump (4), first solution heat exchanger (6) and the 4th solution heat exchanger (25) are communicated with first generator (1) and are adjusted into absorber (3) and the weak solution pipeline are arranged through first solution pump (4), first solution heat exchanger (6) is communicated with first generator (1) through the 4th solution heat exchanger (25) with the 4th generator (24) connected sum through solution choke valve (22) respectively afterwards more again, forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
16. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 3, increase by the 4th generator, the 4th solution heat exchanger, second choke valve and the 4th solution pump, having the weak solution pipeline to be communicated with first generator (1) through first solution pump (4) and first solution heat exchanger (6) absorber (3) is adjusted into absorber (3) and has the weak solution pipeline to be communicated with the 4th generator (24) through first solution pump (4) and first solution heat exchanger (6), the 4th generator (24) also has the concentrated solution pipeline to be communicated with first generator (1) through the 4th solution pump (27) and the 4th solution heat exchanger (25), having the concentrated solution pipeline to be communicated with second absorber (15) through first solution heat exchanger (6) and second solution heat exchanger (7) in first generator (1) is adjusted into first generator (1) and the concentrated solution pipeline is arranged through the 4th solution heat exchanger (25), first solution heat exchanger (6) and second solution heat exchanger (7) are communicated with second absorber (15), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (8) through second choke valve (23) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 4th generator, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (8), forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
17. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 16, increase the solution choke valve, having the weak solution pipeline to be communicated with the 4th generator (24) through first solution pump (4) and first solution heat exchanger (6) absorber (3) is adjusted into absorber (3) and has the weak solution pipeline directly to be communicated with the 4th generator (24) through solution choke valve (22) with first generator (1) connected sum respectively afterwards through first solution pump (4) and first solution heat exchanger (6) again, form economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
18. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 13, increase by the 5th generator, the 3rd choke valve and the 5th solution heat exchanger, first solution pump (4) is set up the weak solution pipeline and is communicated with the 5th generator through the 5th solution heat exchanger, the 5th generator also has the concentrated solution pipeline to converge through first solution heat exchanger (6) concentrated solution pipeline afterwards through the 5th solution heat exchanger and first generator (1), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into the 4th generator (24) to have the refrigerant vapour passage to be communicated with back the 5th generator with the 5th generator in the 4th generator (24) has the cryogen liquid pipeline to be communicated with first condenser (8) through the 3rd choke valve (26) again, the 5th generator also has the refrigerant vapour passage to be communicated with first condenser (8), forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
19. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 14, increase by the 5th generator, the 3rd choke valve and the 5th solution heat exchanger, absorber (3) there is the weak solution pipeline through first solution pump (4), first solution heat exchanger (6) and the 4th solution heat exchanger (25) are communicated with first generator (1) and are adjusted into absorber (3) and the weak solution pipeline are arranged through first solution pump (4), first solution heat exchanger (6), the 5th solution heat exchanger and the 4th solution heat exchanger (25) are communicated with first generator (1), having the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7) in the 4th generator (24) is adjusted into the 4th generator (24) and has the concentrated solution pipeline to be communicated with the 5th generator through the 5th solution heat exchanger, the 5th generator also has the concentrated solution pipeline to be communicated with second absorber (15) through first solution heat exchanger (6) and second solution heat exchanger (7), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into the 4th generator (24) to have the refrigerant vapour passage to be communicated with back the 5th generator with the 5th generator in the 4th generator (24) has the cryogen liquid pipeline to be communicated with first condenser (8) through the 3rd choke valve (26) again, the 5th generator also has the refrigerant vapour passage to be communicated with first condenser (8), forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
20. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 16, increase by the 5th generator, the 3rd choke valve, the 5th solution pump and the 5th solution heat exchanger, having the weak solution pipeline to be communicated with the 4th generator (24) through first solution pump (4) and first solution heat exchanger (6) absorber (3) is adjusted into absorber (3) and has the weak solution pipeline to be communicated with the 5th generator through first solution pump (4) and first solution heat exchanger (6), the 5th generator also has the concentrated solution pipeline to be communicated with the 4th generator (24) through the 5th solution pump and the 5th solution heat exchanger, first generator (1) there is the concentrated solution pipeline through the 4th solution heat exchanger (25), first solution heat exchanger (6) and second solution heat exchanger (7) are communicated with second absorber (15) and are adjusted into first generator (1) and the concentrated solution pipeline are arranged through the 4th solution heat exchanger (25), the 5th solution heat exchanger, first solution heat exchanger (6) and second solution heat exchanger (7) are communicated with second absorber (15), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into the 4th generator (24) to have the refrigerant vapour passage to be communicated with back the 5th generator with the 5th generator in the 4th generator (24) has the cryogen liquid pipeline to be communicated with first condenser (8) through the 3rd choke valve (26) again, the 5th generator also has the refrigerant vapour passage to be communicated with first condenser (8), forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
21. the 3rd class absorption heat pump, be in described the 3rd class absorption-generation systems of claim 4, increase by the 3rd generator, the 4th solution heat exchanger and second choke valve, first solution pump (4) is set up the weak solution pipeline through the 3rd solution heat exchanger (14) and also is communicated with the 3rd generator (13) through the 4th solution heat exchanger (25) again, the 3rd generator (13) also has the concentrated solution pipeline to converge through first solution heat exchanger (6) concentrated solution pipeline afterwards with first generator (1) afterwards through the 4th solution heat exchanger (25), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (13) with the 3rd generator (13) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (8) through second choke valve (23) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (13) also has the refrigerant vapour passage to be communicated with first condenser (8), forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
22. the 3rd class absorption heat pump, be in claim 4 the 3rd class absorption heat pump, increase by the 3rd generator, the 4th solution heat exchanger and second choke valve, having the weak solution pipeline to be communicated with first generator (1) through the 3rd solution heat exchanger (14) and first solution heat exchanger (6) first solution pump (4) is adjusted into first solution pump (4) and the weak solution pipeline is arranged through the 3rd solution heat exchanger (14), first solution heat exchanger (6) and the 4th solution heat exchanger (25) are communicated with first generator (1), having the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with the 3rd generator (13) through the 4th solution heat exchanger (25), the 3rd generator (13) also has the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (13) with the 3rd generator (13) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (8) through second choke valve (23) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (13) also has the refrigerant vapour passage to be communicated with first condenser (8), forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
23. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 22, increase the solution choke valve, first solution pump (4) there is the weak solution pipeline through the 3rd solution heat exchanger (14), first solution heat exchanger (6) and the 4th solution heat exchanger (25) are communicated with first generator (1) and are adjusted into first solution pump (4) and the weak solution pipeline are arranged through the 3rd solution heat exchanger (14), first solution heat exchanger (6) is communicated with first generator (1) through the 4th solution heat exchanger (25) with the 3rd generator (13) connected sum through solution choke valve (22) respectively afterwards more again, forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
24. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 4, increase by the 3rd generator, the 4th solution heat exchanger, the 4th solution pump and second choke valve, having the weak solution pipeline to be communicated with first generator (1) through the 3rd solution heat exchanger (14) and first solution heat exchanger (6) first solution pump (4) is adjusted into first solution pump (4) and has the weak solution pipeline to be communicated with the 3rd generator (13) through the 3rd solution heat exchanger (14) and first solution heat exchanger (6), the 3rd generator (13) also has the concentrated solution pipeline to be communicated with first generator (1) through the 4th solution pump (27) and the 4th solution heat exchanger (25), having the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7) in first generator (1) is adjusted into first generator (1) and the concentrated solution pipeline is arranged through the 4th solution heat exchanger (25), first solution heat exchanger (6) and second solution heat exchanger (7) are communicated with second generator (2), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (13) with the 3rd generator (13) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (8) through second choke valve (23) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (13) also has the refrigerant vapour passage to be communicated with first condenser (8), forms economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
25. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 24, increase the solution choke valve, having the weak solution pipeline to be communicated with the 3rd generator (13) through the 3rd solution heat exchanger (14) and first solution heat exchanger (6) first solution pump (4) is adjusted into first solution pump (4) and has the weak solution pipeline directly to be communicated with the 3rd generator (13) through solution choke valve (22) with first generator (1) connected sum respectively afterwards through the 3rd solution heat exchanger (14) and first solution heat exchanger (6) again, form economic benefits and social benefits-back-heating type single-action the 3rd class absorption heat pump.
26. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 21, increase by the 4th generator, the 5th solution heat exchanger and the 3rd choke valve, first solution pump (4) is set up the weak solution pipeline through the 3rd solution heat exchanger (14) and also is communicated with the 4th generator (24) through the 5th solution heat exchanger again, the 4th generator (24) also has the concentrated solution pipeline to converge through first solution heat exchanger (6) concentrated solution pipeline afterwards with first generator (1) after the 5th solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into the 3rd generator (13) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (13) has the cryogen liquid pipeline to be communicated with first condenser (8) through the 3rd choke valve (26) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (8), forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
27. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 22, increase by the 4th generator, the 5th solution heat exchanger and the 3rd choke valve, first solution pump (4) there is the weak solution pipeline through the 3rd solution heat exchanger (14), first solution heat exchanger (6) and the 4th solution heat exchanger (25) are communicated with first generator (1) and are adjusted into first solution pump (4) and the weak solution pipeline are arranged through the 3rd solution heat exchanger (14), first solution heat exchanger (6), the 5th solution heat exchanger and the 4th solution heat exchanger (25) are communicated with first generator (1), having the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7) in the 3rd generator (13) is adjusted into the 3rd generator (13) and has the concentrated solution pipeline to be communicated with the 4th generator (24) through the 5th solution heat exchanger, the 4th generator (24) also has the concentrated solution pipeline to be communicated with second generator (2) through first solution heat exchanger (6) and second solution heat exchanger (7), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into the 3rd generator (13) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (13) has the cryogen liquid pipeline to be communicated with first condenser (8) through the 3rd choke valve (26) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (8), forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
28. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 24, increase by the 4th generator, the 5th solution heat exchanger, the 3rd choke valve and the 5th solution pump, having the weak solution pipeline to be communicated with the 3rd generator (13) through the 3rd solution heat exchanger (14) and first solution heat exchanger (6) first solution pump (4) is adjusted into first solution pump (4) and has the weak solution pipeline to be communicated with the 4th generator (24) through the 3rd solution heat exchanger (14) and first solution heat exchanger (6), the 4th generator (24) also has the concentrated solution pipeline to be communicated with the 3rd generator (13) through the 5th solution pump and the 5th solution heat exchanger, first generator (1) there is the concentrated solution pipeline through the 4th solution heat exchanger (25), first solution heat exchanger (6) and second solution heat exchanger (7) are communicated with second generator (2) and are adjusted into first generator (1) and the concentrated solution pipeline are arranged through the 4th solution heat exchanger (25), the 5th solution heat exchanger, first solution heat exchanger (6) and second solution heat exchanger (7) are communicated with second generator (2), having the refrigerant vapour passage to be communicated with first condenser (8) to be adjusted into the 3rd generator (13) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (13) has the cryogen liquid pipeline to be communicated with first condenser (8) through the 3rd choke valve (26) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (8), forms triple effect-back-heating type single-action the 3rd class absorption heat pump.
29. the 3rd class absorption heat pump, be in claim 2, in interior described the 3rd class absorption heat pump of arbitrary claim of 5-12, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, concentrated solution provides device to set up the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (B), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with absorber (3) through newly-increased solution pump (D) and newly-increased solution heat exchanger (B), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with economic benefits and social benefits is the 3rd class absorption heat pump of low temperature generation flow process.
30. the 3rd class absorption heat pump, be in claim 2, in interior described the 3rd class absorption heat pump of arbitrary claim of 5-12, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, providing device to have the concentrated solution pipeline to be communicated with second generator (2) through second solution heat exchanger (7) concentrated solution is adjusted into concentrated solution and provides device to have the concentrated solution pipeline to be communicated with second generator (2) through newly-increased solution heat exchanger (B) and second solution heat exchanger (7), having the concentrated solution pipeline to be communicated with absorber (3) through second solution pump (5) and second solution heat exchanger (7) 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 (7), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with absorber (3) through second solution pump (5) and newly-increased solution heat exchanger (B), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with economic benefits and social benefits is the 3rd class absorption heat pump of low temperature generation flow process.
31. the 3rd class absorption heat pump, be in claim 2, in interior described the 3rd class absorption heat pump of arbitrary claim of 5-12, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, providing device to have the concentrated solution pipeline to be communicated with second generator (2) through second solution heat exchanger (7) concentrated solution is adjusted into concentrated solution and provides device to have the concentrated solution pipeline to be communicated with newly-increased generator (A) through second solution heat exchanger (7) and newly-increased solution heat exchanger (B), 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 (B), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with economic benefits and social benefits is the 3rd class absorption heat pump of low temperature generation flow process.
32. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 29, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased second solution pump, concentrated solution provides device to set up the concentrated solution pipeline to be communicated with newly-increased second generator (E) through newly-increased second solution heat exchanger (F), newly-increased second generator (E) also has the concentrated solution pipeline to be communicated with absorber (3) through newly-increased second solution pump (H) and newly-increased second solution heat exchanger (F), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the triple effect is the 3rd class absorption heat pump of low temperature generation flow process.
33. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 30, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, providing device to have the concentrated solution pipeline to be communicated with second generator (2) through newly-increased first solution heat exchanger (B) and second solution heat exchanger (7) concentrated solution is adjusted into concentrated solution and provides device to have concentrated solution pipeline warp to increase second solution heat exchanger (F) newly, newly-increased first solution heat exchanger (B) and second solution heat exchanger (7) are communicated with second generator (2), to increase first generator (A) newly has the concentrated solution pipeline to be communicated with absorber (3) through second solution pump (5) and newly-increased first solution heat exchanger (B) to be adjusted into newly-increased first generator (A) and to have concentrated solution pipeline warp to increase first solution heat exchanger (B) newly to be communicated with newly-increased second generator (E), newly-increased second generator (E) also has the concentrated solution pipeline to be communicated with absorber (3) through second solution pump (5) and newly-increased second solution heat exchanger (F), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the triple effect is the 3rd class absorption heat pump of low temperature generation flow process.
34. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 31, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased second solution pump, providing device to have the concentrated solution pipeline to be communicated with newly-increased first generator (A) through second solution heat exchanger (7) and newly-increased first solution heat exchanger (B) concentrated solution is adjusted into concentrated solution and provides device the concentrated solution pipeline to be arranged through second solution heat exchanger (7), newly-increased first solution heat exchanger (B) and newly-increased second solution heat exchanger (F) are communicated with newly-increased second generator (E), newly-increased second generator (E) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased second solution pump (H) and newly-increased second solution heat exchanger (F), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the triple effect is the 3rd class absorption heat pump of low temperature generation flow process.
35. the 3rd class absorption heat pump, be in claim 3, in interior described the 3rd class absorption heat pump of arbitrary claim of 13-20, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, the 3rd solution pump (16) is set up the weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution heat exchanger (B), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with the 3rd generator (13) through newly-increased solution heat exchanger (B), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
36. the 3rd class absorption heat pump, be in claim 3, in interior described the 3rd class absorption heat pump of arbitrary claim of 13-20, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, having the weak solution pipeline to be communicated with second generator (2) through the 3rd solution heat exchanger (14) the 3rd solution pump (16) is adjusted into the 3rd solution pump (16) and has the weak solution pipeline to be communicated with second generator (2) through newly-increased solution heat exchanger (B) and the 3rd solution heat exchanger (14), having the concentrated solution pipeline to be communicated with the 3rd generator (13) through the 3rd solution heat exchanger (14) 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 the 3rd solution heat exchanger (14), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with the 3rd generator (13) through newly-increased solution heat exchanger (B), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
37. the 3rd class absorption heat pump, be in claim 3, in interior described the 3rd class absorption heat pump of arbitrary claim of 13-20, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, having the weak solution pipeline to be communicated with second generator (2) through the 3rd solution heat exchanger (14) the 3rd solution pump (16) is adjusted into the 3rd solution pump (16) and has the weak solution pipeline to be communicated with newly-increased generator (A) through the 3rd solution heat exchanger (14), 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 (B), having the concentrated solution pipeline to be communicated with the 3rd generator (13) through the 3rd solution heat exchanger (14) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with the 3rd generator (13) through newly-increased solution heat exchanger (B) and the 3rd solution heat exchanger (14), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
38. the 3rd class absorption heat pump, be in claim 35-37 in described the 3rd class absorption heat pump of arbitrary claim, cancel the waste heat medium pipeline of the 3rd generator (13) and external communications, increase newly-increased second choke valve, second generator (2) is set up the refrigerant vapour passage and is communicated with back the 3rd generator (13) with the 3rd generator (13) and has the cryogen liquid pipeline to be communicated with second condenser (9) through newly-increased second choke valve (G) again, and formation is the 3rd class absorption heat pump of low temperature generation flow process with the backheating type double-effect.
39. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 35, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, the 3rd solution pump (16) is set up the weak solution pipeline and is communicated with newly-increased second generator (E) through newly-increased second solution heat exchanger (F), newly-increased second generator (E) also has the concentrated solution pipeline to be communicated with the 3rd generator (13) through newly-increased second solution heat exchanger (F), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
40. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 36, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, having the weak solution pipeline to be communicated with second generator (2) through newly-increased first solution heat exchanger (B) and the 3rd solution heat exchanger (14) the 3rd solution pump (16) is adjusted into the 3rd solution pump (16) and has weak solution pipeline warp to increase second solution heat exchanger (F) newly, newly-increased first solution heat exchanger (B) and the 3rd solution heat exchanger (14) are communicated with second generator (2), to increase first generator (A) newly has the concentrated solution pipeline to be communicated with the 3rd generator (13) through newly-increased first solution heat exchanger (B) to be adjusted into newly-increased first generator (A) and to have concentrated solution pipeline warp to increase first solution heat exchanger (B) newly to be communicated with newly-increased second generator (E), newly-increased second generator (E) also has the concentrated solution pipeline to be communicated with the 3rd generator (13) through newly-increased second solution heat exchanger (F), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
41. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 37, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased second solution pump, having the weak solution pipeline to be communicated with newly-increased first generator (A) through the 3rd solution heat exchanger (14) the 3rd solution pump (16) is adjusted into the 3rd solution pump (16) and has the weak solution pipeline to be communicated with through newly-increased second generator (E) of the 3rd solution heat exchanger (14), newly-increased second generator (E) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased second solution pump (H) and newly-increased second solution heat exchanger (F), having the concentrated solution pipeline to be communicated with the 3rd generator (13) through newly-increased solution heat exchanger (B) and the 3rd solution heat exchanger (14) in second generator (2) is adjusted into second generator (2) and has concentrated solution pipeline warp to increase solution heat exchanger (B) newly, newly-increased second solution heat exchanger (F) and the 3rd solution heat exchanger (14) are communicated with the 3rd generator (13), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
42. the 3rd class absorption heat pump, be in claim 39-41 in described the 3rd class absorption heat pump of arbitrary claim, cancel the waste heat medium pipeline of the 3rd generator (13) and external communications, increase newly-increased the 3rd choke valve, second generator (2) is set up the refrigerant vapour passage and is communicated with back the 3rd generator (13) with the 3rd generator (13) and has the cryogen liquid pipeline to be communicated with second condenser (9) through newly-increased the 3rd choke valve again, and formation is back-heating type the 3rd class absorption heat pump of low temperature generation flow process with the triple effect.
43. the 3rd class absorption heat pump, be in claim 39-41 in described the 3rd class absorption heat pump of arbitrary claim, cancel the waste heat medium pipeline of the 3rd generator (13) and external communications, increase newly-increased the 3rd choke valve, newly-increased first generator (A) is set up the refrigerant vapour passage and is communicated with back the 3rd generator (13) with the 3rd generator (13) and has the cryogen liquid pipeline to be communicated with second condenser (9) through increasing the 3rd choke valve newly again, and formation is the 3rd class absorption heat pump of low temperature generation flow process with the back-heating type triple-effect.
44. the 3rd class absorption heat pump, be in claim 4, in interior described the 3rd class absorption heat pump of arbitrary claim of 21-28, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution choke valve, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest (18) through newly-increased solution choke valve (I) and absorption-generator (17) through the 3rd solution pump (16) and absorption-generator (17) with dividing steam chest (18) to be communicated with to be adjusted into second generator (2) in second generator (2), having the concentrated solution pipeline directly to be communicated with second generator (2) to be adjusted into second solution heat exchanger (7) to have the concentrated solution pipeline directly to increase solution heat exchanger (B) newly with second generator (2) connected sum warp respectively second solution heat exchanger (7) is communicated with newly-increased generator (A), newly-increased generator (A) also has the concentrated solution pipeline through the 3rd solution pump (16), newly-increased solution heat exchanger (B) and absorption-generator (17) are communicated with dividing steam chest (18), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
45. the 3rd class absorption heat pump, be in claim 4, in interior described the 3rd class absorption heat pump of arbitrary claim of 21-28, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution choke valve, having the concentrated solution pipeline directly to be communicated with second generator (2) to be adjusted into second solution heat exchanger (7) to have the concentrated solution pipeline to increase solution choke valve (I) through newly-increased solution heat exchanger (B) newly with second generator (2) connected sum warp respectively second solution heat exchanger (7) is communicated with newly-increased generator (A), there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest (18) through newly-increased solution heat exchanger (B) and absorption-generator (17) through the 3rd solution pump (16) and absorption-generator (17) with dividing steam chest (18) to be communicated with to be adjusted into second generator (2) in second generator (2), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with dividing steam chest (18) through the 3rd solution pump (16) and absorption-generator (17), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, increase newly generator (A) in addition the refrigerant vapour passage be communicated with second condenser (9); Cancel the refrigerant vapour passage that first evaporimeter (10) or second evaporimeter (20) are communicated with absorption-generator (17), second generator (2) is set up the refrigerant vapour passage and is communicated with absorption-generator (17), cancel the 4th solution pump, absorber (3) has the weak solution pipeline to be communicated with absorption-generator (17) through the 3rd solution heat exchanger (14), and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
46. the 3rd class absorption heat pump, be in claim 4, in interior described the 3rd class absorption heat pump of arbitrary claim of 21-28, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased generator (A) through increasing solution heat exchanger (B) newly through the 3rd solution pump (16) and absorption-generator (17) with dividing steam chest (18) to be communicated with to be adjusted into second generator (2) in second generator (2), newly-increased generator (A) also has the concentrated solution pipeline through the 3rd solution pump (16), newly-increased solution heat exchanger (B) and absorption-generator (17) are communicated with dividing steam chest (18), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
47. the 3rd class absorption heat pump, be in claim 4, in interior described the 3rd class absorption heat pump of arbitrary claim of 21-28, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, having the concentrated solution pipeline directly to be communicated with second generator (2) to be adjusted into second solution heat exchanger (7) to have concentrated solution pipeline warp to increase solution heat exchanger (B) newly second solution heat exchanger (7) is communicated with second generator (2), there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased generator (A) through increasing solution heat exchanger (B) newly through the 3rd solution pump (16) and absorption-generator (17) with dividing steam chest (18) to be communicated with to be adjusted into second generator (2) in second generator (2), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with dividing steam chest (18) through the 3rd solution pump (16) and absorption-generator (17), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, increase newly generator (A) in addition the refrigerant vapour passage be communicated with second condenser (9); Cancel the refrigerant vapour passage that first evaporimeter (10) or second evaporimeter (20) are communicated with absorption-generator (17), second generator (2) is set up the refrigerant vapour passage and is communicated with absorption-generator (17), cancel the 4th solution pump, absorber (3) has the weak solution pipeline to be communicated with absorption-generator (17) through the 3rd solution heat exchanger (14), and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
48. the 3rd class absorption heat pump, be in claim 4, in interior described the 3rd class absorption heat pump of arbitrary claim of 21-28, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest (18) through newly-increased solution choke valve (I) and absorption-generator (17) through the 3rd solution pump (16) and absorption-generator (17) with dividing steam chest (18) to be communicated with to be adjusted into second generator (2) in second generator (2), there is the concentrated solution pipeline to be communicated with second generator (2) to be adjusted into second solution heat exchanger (7) to have the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (B) second solution heat exchanger (7), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with second generator (2) through the 3rd solution pump (16) and newly-increased solution heat exchanger (B), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
49. the 3rd class absorption heat pump, be in claim 4, in interior described the 3rd class absorption heat pump of arbitrary claim of 21-28, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, second solution heat exchanger (7) had the concentrated solution pipeline to be communicated with second generator (2) to be adjusted into second solution heat exchanger (7) has the concentrated solution pipeline to be communicated with newly-increased generator (A), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with second generator (2) through the 3rd solution pump (16) and newly-increased solution heat exchanger (B), there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest (18) through newly-increased solution heat exchanger (B) and absorption-generator (17) through the 3rd solution pump (16) and absorption-generator (17) with dividing steam chest (18) to be communicated with to be adjusted into second generator (2) in second generator (2), having the refrigerant vapour passage to be communicated with second condenser (9) 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 second condenser (9) through newly-increased choke valve (C) again, increase newly generator (A) in addition the refrigerant vapour passage be communicated with second condenser (9); Cancel the refrigerant vapour passage that first evaporimeter (10) or second evaporimeter (20) are communicated with absorption-generator (17), second generator (2) is set up the refrigerant vapour passage and is communicated with absorption-generator (17), cancel the 4th solution pump, absorber (3) has the weak solution pipeline to be communicated with absorption-generator (17) through the 3rd solution heat exchanger (14), and forming with the backheating type double-effect is the 3rd class absorption heat pump of low temperature generation flow process.
50. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 44, increase newly-increased second generator, newly-increased second choke valve, the newly-increased second solution choke valve and newly-increased the 3rd solution choke valve, having the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (B) second solution heat exchanger (7) is adjusted into second solution heat exchanger (7) and has concentrated solution pipeline warp to increase the second solution choke valve (J) newly to be communicated with newly-increased generator (A), to increase generator (A) newly and the concentrated solution pipeline be arranged through the 3rd solution pump (16), newly-increased solution heat exchanger (B) and absorptions-generator (17) with divide steam chest (18) to be communicated with to be adjusted into newly-increased generator (A) to have concentrated solution pipeline warp to increase the 3rd solution choke valve (K) newly and absorption-generator (17) is communicated with branch steam chest (18), concentrated solution provides device to set up the concentrated solution pipeline through second solution heat exchanger (7) to be communicated with newly-increased second generator (E) through newly-increased solution heat exchanger (B), newly-increased second generator (E) also has the concentrated solution pipeline through the 3rd solution pump (16), newly-increased solution heat exchanger (B) and absorption-generator (17) are communicated with dividing steam chest (18), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
51. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 45, increase newly-increased second generator, newly-increased second choke valve, the newly-increased second solution choke valve and newly-increased the 3rd solution choke valve, to increase first generator (A) newly has the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest (18) through the newly-increased second solution choke valve (J) and absorption-generator (17) through the 3rd solution pump (16) and absorption-generator (17) with dividing steam chest (18) to be communicated with to be adjusted into newly-increased first generator (A), concentrated solution provides device to set up the concentrated solution pipeline through second solution heat exchanger (7) to be communicated with newly-increased second generator (E) through newly-increased the 3rd solution choke valve (K), newly-increased second generator (E) also has the concentrated solution pipeline to be communicated with dividing steam chest (18) through the 3rd solution pump (16) and absorption-generator (17), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
52. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 51, the newly-increased first solution choke valve of cancellation and the newly-increased second solution choke valve, increase newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with newly-increased first generator (A) through the newly-increased first solution choke valve (I) second solution heat exchanger (7) is adjusted into second solution heat exchanger (7) and has concentrated solution pipeline warp to increase second solution heat exchanger (F) newly to be communicated with newly-increased first generator (A), to increase first generator (A) newly has the concentrated solution pipeline to increase first generator (A) newly and have concentrated solution pipeline warp to increase second solution heat exchanger (F) newly and absorption-generator (17) is communicated with branch steam chest (18) with dividing steam chest (18) to be communicated with to be adjusted into through the newly-increased second solution choke valve (J) and absorptions-generator (17), have the refrigerant vapour passage to be communicated with absorption-generator (17) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with absorption-generator (17) in second generator (2), formation is the 3rd class absorption heat pump of low temperature generation flow process with the back-heating type triple-effect.
53. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 46, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, to increase first generator (A) newly and the concentrated solution pipeline be arranged through the 3rd solution pump (16), newly-increased solution heat exchanger (B) and absorptions-generator (17) increase first generator (A) newly and have concentrated solution pipeline warp to increase second solution heat exchanger (F) newly to be communicated with newly-increased second generator (E) with dividing steam chest (18) to be communicated with to be adjusted into, newly-increased second generator (E) also has the concentrated solution pipeline through the 3rd solution pump (16), newly-increased second solution heat exchanger (F), newly-increased first solution heat exchanger (B) and absorption-generator (17) are communicated with dividing steam chest (18), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
54. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 47, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased second choke valve, to increase first generator (A) newly has the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased second generator (E) through increasing second solution heat exchanger (F) newly through the 3rd solution pump (16) and absorption-generator (17) with dividing steam chest (18) to be communicated with to be adjusted into newly-increased first generator (A), newly-increased second generator (E) also has the concentrated solution pipeline through the 3rd solution pump (16), newly-increased second solution heat exchanger (F) and absorption-generator (17) are communicated with dividing steam chest (18), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
55. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 54, having the concentrated solution pipeline to be communicated with second generator (2) through newly-increased first solution heat exchanger (B) second solution heat exchanger (7) is adjusted into second solution heat exchanger (7) and has the concentrated solution pipeline to be communicated with second generator (2) through increasing second solution heat exchanger (F) newly and increasing first solution heat exchanger (B) newly, to increase second generator (E) newly and the concentrated solution pipeline be arranged through the 3rd solution pump (16), newly-increased second solution heat exchanger (F) and absorptions-generator (17) are communicated with branch steam chest (18) to be adjusted into and increase second generator (E) newly and have the concentrated solution pipeline to be communicated with branch steam chest (18) through the 3rd solution pump (16) and absorption-generator (17), have the refrigerant vapour passage to be communicated with absorption-generator (17) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with absorption-generator (17) in second generator (2), formation is the 3rd class absorption heat pump of low temperature generation flow process with the back-heating type triple-effect.
56. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 48, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased solution pump, having the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased first solution heat exchanger (B) second solution heat exchanger (7) is adjusted into second solution heat exchanger (7) and has concentrated solution pipeline warp to increase second solution heat exchanger (F) newly to be communicated with newly-increased second generator (E), newly-increased second generator (E) also has the concentrated solution pipeline through newly-increased solution pump (D), newly-increased second solution heat exchanger (F) and newly-increased first solution heat exchanger (B) are communicated with newly-increased first generator (A), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
57. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 49, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased second choke valve and newly-increased solution pump, there is the concentrated solution pipeline to be communicated with newly-increased first generator (A) to be adjusted into second solution heat exchanger (7) to have the concentrated solution pipeline to be communicated with newly-increased second generator (E) through newly-increased second solution heat exchanger (F) second solution heat exchanger (7), newly-increased second generator (E) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased solution pump (D) and newly-increased second solution heat exchanger (F), to increase first generator (A) newly has the refrigerant vapour passage to be communicated with second condenser (9) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with the back with newly-increased second generator (E) to increase second generator (E) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with second condenser (9), newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second condenser (9), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of low temperature generation flow process.
58. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 57, having the concentrated solution pipeline to be communicated with newly-increased second generator (E) through newly-increased second solution heat exchanger (F) second solution heat exchanger (7) is adjusted into second solution heat exchanger (7) and has the concentrated solution pipeline directly to be communicated with newly-increased second generator (E), having the concentrated solution pipeline to be communicated with branch steam chest (18) through newly-increased first solution heat exchanger (B) and absorptions-generator (17) in second generator (2) is adjusted into second generator (2) and has concentrated solution pipeline warp to increase first solution heat exchanger (B) newly, newly-increased second solution heat exchanger (F) and absorption-generator (17) are communicated with dividing steam chest (18), have the refrigerant vapour passage to be communicated with absorption-generator (17) to be adjusted into newly-increased first generator (A) to have the refrigerant vapour passage to be communicated with absorption-generator (17) in second generator (2), formation is the 3rd class absorption heat pump of low temperature generation flow process with the back-heating type triple-effect.
59. the 3rd class absorption heat pump, be in claim 2, in interior described the 3rd class absorption heat pump of arbitrary claim of 5-12, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, having the weak solution pipeline to be communicated with first solution heat exchanger (6) through first solution pump (4) absorber (3) is adjusted into absorber (3) and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (L) through newly-increased solution heat exchanger (B), newly-increased absorption-evaporimeter (L) also has the weak solution pipeline to be communicated with first solution heat exchanger (6) through first solution pump (4) and newly-increased solution heat exchanger (B), evaporimeter (10) had the refrigerant vapour passage to be communicated with absorber (3) to be adjusted into evaporimeter (10) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (L), evaporimeter (10) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (L) after increasing cryogen liquid pump (M) newly and newly-increased absorption-evaporimeter (L) is communicated with has the refrigerant vapour passage to be communicated with absorber (3) again, and forming with 1.5 grades is the 3rd class absorption heat pump of low temperature generation flow process.
60. the 3rd class absorption heat pump, be in claim 3, in interior described the 3rd class absorption heat pump of arbitrary claim of 13-20, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, having the weak solution pipeline to be communicated with first solution heat exchanger (6) through first solution pump (4) absorber (3) is adjusted into absorber (3) and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (L) through newly-increased solution heat exchanger (B), newly-increased absorption-evaporimeter (L) also has the weak solution pipeline to be communicated with first solution heat exchanger (6) through first solution pump (4) and newly-increased solution heat exchanger (B), evaporimeter (10) had the refrigerant vapour passage to be communicated with absorber (3) to be adjusted into evaporimeter (10) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (L), evaporimeter (10) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (L) after increasing cryogen liquid pump (M) newly and newly-increased absorption-evaporimeter (L) is communicated with has the refrigerant vapour passage to be communicated with absorber (3) again, and forming with 1.5 grades of back-heating types is the 3rd class absorption heat pump of low temperature generation flow process.
61. the 3rd class absorption heat pump, be in claim 4, in interior described the 3rd class absorption heat pump of arbitrary claim of 21-28, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, having the weak solution pipeline to be communicated with absorption-generator (17) through the 4th solution pump (27) and the 3rd solution heat exchanger (14) absorber (3) is adjusted into absorber (3) and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (L) through newly-increased solution heat exchanger (B), newly-increased absorption-evaporimeter (L) also has the weak solution pipeline through the 4th solution pump (27), newly-increased solution heat exchanger (B) and the 3rd solution heat exchanger (14) are communicated with absorption-generator (17), evaporimeter (10) had the refrigerant vapour passage to be communicated with absorber (3) to be adjusted into evaporimeter (10) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (L), evaporimeter (10) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (L) after increasing cryogen liquid pump (M) newly and newly-increased absorption-evaporimeter (L) is communicated with has the refrigerant vapour passage to be communicated with absorber (3) again, and forming with 1.5 grades of back-heating types is the 3rd class absorption heat pump of low temperature generation flow process.
62. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 59, there is the concentrated solution pipeline to be communicated with absorber (3) to be adjusted into second solution heat exchanger (7) to have the concentrated solution pipeline to be communicated with absorber (3) through newly-increased solution heat exchanger (B) second solution heat exchanger (7), to increase absorption-evaporimeter (L) newly has the weak solution pipeline to be communicated with first solution heat exchanger (6) through first solution pump (4) and newly-increased solution heat exchanger (B) to be adjusted into newly-increased absorptions-evaporimeter (L) and to have the weak solution pipeline to be communicated with first solution heat exchanger (6) through first solution pump (4), and formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades.
63. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 60, there is the concentrated solution pipeline to be communicated with absorber (3) to be adjusted into second solution heat exchanger (7) to have the concentrated solution pipeline to be communicated with absorber (3) through newly-increased solution heat exchanger (B) second solution heat exchanger (7), to increase absorption-evaporimeter (L) newly has the weak solution pipeline to be communicated with first solution heat exchanger (6) through first solution pump (4) and newly-increased solution heat exchanger (B) to be adjusted into newly-increased absorptions-evaporimeter (L) and to have the weak solution pipeline to be communicated with first solution heat exchanger (6) through first solution pump (4), and formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
64. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 61, there is the concentrated solution pipeline to be communicated with absorber (3) to be adjusted into second solution heat exchanger (7) to have the concentrated solution pipeline to be communicated with absorber (3) through newly-increased solution heat exchanger (B) second solution heat exchanger (7), to increase absorption-evaporimeter (L) newly has the weak solution pipeline to be communicated with the 3rd solution heat exchanger (14) through the 4th solution pump (27) and newly-increased solution heat exchanger (B) to be adjusted into newly-increased absorptions-evaporimeter (L) and to have the weak solution pipeline to be communicated with the 3rd solution heat exchanger (14) through the 4th solution pump (27), and formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
65. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 59, increase newly-increased solution pump, second solution heat exchanger (7) had the concentrated solution pipeline to be communicated with absorber (3) to be adjusted into second solution heat exchanger (7) has the concentrated solution pipeline to be communicated with absorption-evaporimeter (L), to increase absorption-evaporimeter (L) newly has the weak solution pipeline to be communicated with first solution heat exchanger (6) through first solution pump (4) and newly-increased solution heat exchanger (B) to be adjusted into newly-increased absorption-evaporimeter (L) and to have the weak solution pipeline to be communicated with absorber (3) through first solution pump (4) and newly-increased solution heat exchanger (B), have the weak solution pipeline to be communicated with absorptions-evaporimeter (L) through newly-increased solution heat exchanger (B) absorber (3) and be adjusted into absorber (3) and have weak solution pipeline warp to increase solution heat exchanger (B) newly and newly-increased solution pump (D) is communicated with first solution heat exchanger (6), formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades.
66. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 60, increase newly-increased solution pump, second solution heat exchanger (7) had the concentrated solution pipeline to be communicated with absorber (3) to be adjusted into second solution heat exchanger (7) has the concentrated solution pipeline to be communicated with absorption-evaporimeter (L), to increase absorption-evaporimeter (L) newly has the weak solution pipeline to be communicated with first solution heat exchanger (6) through first solution pump (4) and newly-increased solution heat exchanger (B) to be adjusted into newly-increased absorption-evaporimeter (L) and to have the weak solution pipeline to be communicated with absorber (3) through first solution pump (4) and newly-increased solution heat exchanger (B), have the weak solution pipeline to be communicated with absorptions-evaporimeter (L) through newly-increased solution heat exchanger (B) absorber (3) and be adjusted into absorber (3) and have weak solution pipeline warp to increase solution heat exchanger (B) newly and newly-increased solution pump (D) is communicated with first solution heat exchanger (6), formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
67. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 61, second solution heat exchanger (7) had the concentrated solution pipeline to be communicated with absorber (3) to be adjusted into second solution heat exchanger (7) has the concentrated solution pipeline to be communicated with absorption-evaporimeter (L), to increase absorption-evaporimeter (L) newly has the weak solution pipeline to be communicated with the 3rd solution heat exchanger (14) through first solution pump (4) and newly-increased solution heat exchanger (B) to be adjusted into newly-increased absorption-evaporimeter (L) and to have the weak solution pipeline to be communicated with absorber (3) through first solution pump (4) and newly-increased solution heat exchanger (B), have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter (L) through newly-increased solution heat exchanger (B) absorber (3) and be adjusted into absorber (3) and have weak solution pipeline warp to increase solution heat exchanger (B) newly to be communicated with first solution heat exchanger (6), formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
68. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 65, there is the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (L) to be adjusted into second solution heat exchanger (7) to have the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (L) through newly-increased solution heat exchanger (B) second solution heat exchanger (7), have the weak solution pipeline to be communicated with first solution heat exchanger (6) through newly-increased solution heat exchanger (B) and newly-increased solution pump (D) absorber (3) and be adjusted into absorber (3) and have weak solution pipeline warp to increase solution pump (D) newly to be communicated with first solution heat exchanger (6), formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades.
69. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 66, there is the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (L) to be adjusted into second solution heat exchanger (7) to have the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (L) through newly-increased solution heat exchanger (B) second solution heat exchanger (7), have the weak solution pipeline to be communicated with first solution heat exchanger (6) through newly-increased solution heat exchanger (B) and newly-increased solution pump (D) absorber (3) and be adjusted into absorber (3) and have weak solution pipeline warp to increase solution pump (D) newly to be communicated with first solution heat exchanger (6), formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
70. the 3rd class absorption heat pump, be in described the 3rd class absorption heat pump of claim 67, there is the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (L) to be adjusted into second solution heat exchanger (7) to have the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (L) through newly-increased solution heat exchanger (B) second solution heat exchanger (7), have the weak solution pipeline to be communicated with the 3rd solution heat exchanger (14) through newly-increased solution heat exchanger (B) absorber (3) and be adjusted into absorber (3) and have the weak solution pipeline to be communicated with the 3rd solution heat exchanger (14), formation is the 3rd class absorption heat pump of low temperature generation flow process with 1.5 grades of back-heating types.
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