CN102287961B - Three-generating-three-absorbing system and third-kind absorption-type heat pump - Google Patents

Three-generating-three-absorbing system and third-kind absorption-type heat pump Download PDF

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CN102287961B
CN102287961B CN2011101956023A CN201110195602A CN102287961B CN 102287961 B CN102287961 B CN 102287961B CN 2011101956023 A CN2011101956023 A CN 2011101956023A CN 201110195602 A CN201110195602 A CN 201110195602A CN 102287961 B CN102287961 B CN 102287961B
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generator
communicated
solution
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heat exchanger
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CN102287961A (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

Abstract

The invention provides a three-generating-three-absorbing system and a third-kind absorption-type heat pump, which belong to the technical field of absorption-type heat pumps. The three-generating-three-absorbing system comprises a first generator, a second generator, an absorber-generator, a first absorber, a second absorber, a gas-distributing chamber, a first solution pump, a second solution pump, a third solution pump, a first solution-heat exchanger, a second solution-heat exchanger and a third solution-heat exchanger, wherein the first generator is used for realizing a first low-temperature generating process, the absorber-generator is used for realizing a second low-temperature generating process with a reheating flow, the second generator and the second absorber are used for realizing a high-temperature generating process, and heat loads are mainly provided for the outside through the first absorber and the second absorber; and other parts including a condenser, an evaporator and a refrigerant-liquid pump are added to form a series of reheating-type third-kind absorption-type heat pumps.

Description

Three-three absorption systems and the 3rd class absorption heat pump take place
Technical field:
The invention belongs to low temperature exhaust heat and utilize technical field of heat pumps.
Background technology:
The 3rd class absorption heat pump between several of different effects or different progression, their running parameter interval is disjunct, at performance index bigger difference is arranged.
From workflow, for improving the highest heat supply temperature of the 3rd class absorption heat pump, key is to improve the solution concentration that enters external heat supply usefulness absorber; In order to utilize the more residual heat resources of low temperature, key is to reduce the weak solution concentration that low temperature drives generator exports.Take rational technical measures, when entering external heat supply with the solution concentration of absorber, raising keeps or reduces entering the solution concentration that low temperature drives generator, and the amplitude that can select solution concentration to improve or reduce within the specific limits according to demand, this will have very important meaning.
In order to promote the heat supply temperature of the 3rd class absorption heat pump, in order to make it have rational performance index, in order to realize between the 3rd class absorption heat pump running parameter and the linking of the free of discontinuities between the performance index, the present invention adopts absorption-generator to realize backheat in the low temperature generating process, in the high temperature generating process, adopt second generator and second absorber to realize backheat, set up three generations-three absorption systems with backheat flow process, increase again and comprise condenser, evaporimeter and cryogen liquid pump are at interior associated components, obtain the different numbers and different progression of imitating, the 3rd class absorption heat pump with single or two backheat flow processs, make each running parameter interval that the 3rd corresponding class absorption heat pump be arranged, realize the serialization of the 3rd class absorption heat pump on the running parameter interval, realize the serialization of the 3rd class absorption heat pump on performance index.
Summary of the invention:
Main purpose of the present invention provides three-three absorption systems and the 3rd class absorption heat pump takes place, and concrete summary of the invention subitem is described below:
1. three-three absorption systems take place, and it mainly is made up of first generator, second generator, absorption-generator, first absorber, second absorber, branch steam chest, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; First generator has the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator are communicated with dividing steam chest, divide steam chest to also have the concentrated solution pipeline to be communicated with second generator through second solution pump and second solution heat exchanger, second generator also has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger, first absorber also has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and the 3rd solution heat exchanger, second absorber also has the weak solution pipeline to be communicated with absorption-generator through second solution heat exchanger, absorption-generator also has the weak solution pipeline to be communicated with first generator through first solution heat exchanger, first generator also have surplus heat respectively medium pipeline and external communications and refrigerant vapour passage and external communications arranged, second generator also has the thermal medium of driving pipeline respectively with external communications and has the refrigerant vapour passage to be communicated with second absorber, absorption-generator also has refrigerant vapour passage and external communications, first absorber also has heated medium pipeline and external communications respectively and refrigerant vapour passage and external communications is arranged, absorption-generator and second absorber also have heated medium pipeline and external communications respectively, divide steam chest to also have refrigerant vapour passage and external communications, form three-three absorption systems take place.
2. three-three absorption systems take place, and it mainly is made up of first generator, second generator, absorption-generator, first absorber, second absorber, branch steam chest, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; First generator has the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator are communicated with dividing steam chest, divide steam chest to also have the concentrated solution pipeline to be communicated with second generator through second solution pump and second solution heat exchanger, second generator also has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger, first absorber also has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and the 3rd solution heat exchanger, second absorber also has the weak solution pipeline to be communicated with absorption-generator through second solution heat exchanger, absorption-generator also has the weak solution pipeline to be communicated with first generator through first solution heat exchanger, first generator also have surplus heat respectively medium pipeline and external communications and refrigerant vapour passage and external communications arranged, second generator also has the thermal medium of driving pipeline respectively with external communications and has the refrigerant vapour passage to be communicated with second absorber, absorption-generator also has refrigerant vapour passage and external communications, first absorber also has heated medium pipeline and external communications respectively and refrigerant vapour passage and external communications is arranged, second absorber also has heated medium pipeline and external communications, divide steam chest to also have refrigerant vapour passage and external communications, form three-three absorption systems take place.
3. three-three absorption systems take place, be to take place in-three absorption systems at the 1st described three, first generator there is the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with absorption-generator through first solution pump and first solution heat exchanger with dividing steam chest to be communicated with to be adjusted into first generator, having the weak solution pipeline to be communicated with absorption-generator through second solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with dividing steam chest through second solution heat exchanger and absorption-generator to be communicated with formation three generations-three absorption systems.
4. three-three absorption systems take place, be to take place in-three absorption systems at the 2nd described three, first generator there is the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with absorption-generator through first solution pump and first solution heat exchanger with dividing steam chest to be communicated with to be adjusted into first generator, having the weak solution pipeline to be communicated with absorption-generator through second solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with dividing steam chest through second solution heat exchanger and absorption-generator to be communicated with formation three generations-three absorption systems.
5. the 3rd class absorption heat pump, be to take place in-three absorption systems at 1-2 item described arbitrary three, increase by first condenser, second condenser, evaporimeter, the first cryogen liquid pump and the second 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 the first cryogen liquid pump, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest 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 second cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, to absorb-generator has refrigerant vapour passage and external communications to be defined as evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, first condenser and second condenser also have cooling medium pipeline and external communications respectively, evaporimeter also have surplus heat medium pipeline and external communications form the 3rd class absorption heat pump; Wherein, when not having second condenser, divide steam chest to have the refrigerant vapour passage to be communicated with first condenser.
6. the 3rd class absorption heat pump, be to take place in-three absorption systems at 1-2 item described arbitrary three, increase condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 condenser, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with condenser, condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the first cryogen liquid pump, condenser also has the cryogen liquid pipeline to be communicated with second evaporimeter through the second cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, condenser also has cooling medium pipeline and external communications, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form the 3rd class absorption heat pump.
7. the 3rd class absorption heat pump, be to take place in-three absorption systems at the 2nd described three, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 first evaporimeter through the first cryogen liquid pump, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser has the cryogen liquid pipeline to be communicated with second evaporimeter through the second cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, first condenser and second condenser also have cooling medium pipeline and external communications respectively, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form the 3rd class absorption heat pump.
8. the 3rd class absorption heat pump, be to take place in-three absorption systems at 3-4 item described arbitrary three, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 second evaporimeter through the first cryogen liquid pump, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the second cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, first condenser and second condenser also have cooling medium pipeline and external communications respectively, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form the 3rd class absorption heat pump; Wherein: when 1. not having second evaporimeter, first condenser has the cryogen liquid pipeline to be communicated with first evaporimeter through the first 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 and second condenser, divide steam chest to have the refrigerant vapour passage to be communicated with first condenser, first condenser has the cryogen liquid pipeline to be communicated with first evaporimeter through the first cryogen liquid pump, and first evaporimeter is set up the refrigerant vapour passage and is communicated with absorption-generator.
9. the 3rd class absorption heat pump, be to take place in-three absorption systems at the 4th described three, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 first evaporimeter through the first cryogen liquid pump, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser has the cryogen liquid pipeline to be communicated with second evaporimeter through the second cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, first condenser and second condenser also have cooling medium pipeline and external communications respectively, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form the 3rd class absorption heat pump.
10. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 5-7 item, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, first generator there is the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with the branch steam chest through first solution heat exchanger and absorption-generator with dividing steam chest to be communicated with to be adjusted into first generator, absorption-generator is set up the weak solution pipeline and is communicated with the 3rd generator through the 4th solution heat exchanger, the 3rd generator also has the concentrated solution pipeline through first solution pump, 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 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 single-action-economic benefits and social benefits the 3rd class absorption heat pump.
11. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 5-7 item, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, having the concentrated solution pipeline to be communicated with first solution heat exchanger through first solution pump 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 first solution heat exchanger through first solution pump and 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 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 refrigerant vapour passage first to be communicated with condenser, forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
12. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 5-7 item, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with the 3rd generator through first solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with first generator through first solution pump and the 4th solution heat exchanger, having the concentrated solution pipeline to be communicated with first solution heat exchanger through first solution pump in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with first solution heat exchanger through 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 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 single-action-economic benefits and social benefits the 3rd class absorption heat pump.
13. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 8-9 item, increase by the 3rd generator, the 4th solution heat exchanger, choke valve and the 4th solution pump, absorption-generator is set up the weak solution pipeline and is communicated with the 3rd generator through the 4th solution heat exchanger, the 3rd generator also has the concentrated solution pipeline through the 4th solution pump, after the 4th solution heat exchanger with first generator through first solution pump, concentrated solution pipeline after first solution heat exchanger converges, 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 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 single-action-economic benefits and social benefits the 3rd class absorption heat pump.
14. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 8-9 item, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, having the concentrated solution pipeline to be communicated with first solution heat exchanger through first solution pump 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 first solution heat exchanger through first solution pump and 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 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 refrigerant vapour passage first to be communicated with condenser, forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
15. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 8-9 item, increase by the 3rd generator, the 4th solution heat exchanger, choke valve and the 4th solution pump, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with the 3rd generator through 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 first solution heat exchanger through first solution pump in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with first solution heat exchanger through the 4th solution heat exchanger and first solution pump, 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 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 single-action-economic benefits and social benefits the 3rd class absorption heat pump.
16. the 3rd class absorption heat pump, be described at the 5-7 item, absorption-generator does not have in arbitrary the 3rd class absorption heat pump of heated medium pipeline and external communications, cancel the refrigerant vapour passage that first evaporimeter or second evaporimeter are communicated with absorption-generator, first generator is set up the refrigerant vapour passage and is communicated with absorption-generator, increase by the 3rd generator, choke valve and solution choke valve, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline directly to be communicated with first generator, first generator there is the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with the branch steam chest through solution choke valve and absorption-generator with dividing steam chest to be communicated with to be adjusted into first generator, absorption-generator is set up the weak solution pipeline and is communicated with the 3rd generator through first solution heat exchanger, the 3rd generator also has the concentrated solution pipeline through first solution pump, converge with the concentrated solution pipeline of first generator after the solution choke valve after first 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 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 single-action-economic benefits and social benefits the 3rd class absorption heat pump.
17. the 3rd class absorption heat pump, be described at the 5-7 item, absorption-generator does not have in arbitrary the 3rd class absorption heat pump of heated medium pipeline and external communications, cancel the refrigerant vapour passage that first evaporimeter or second evaporimeter are communicated with absorption-generator, first generator is set up the refrigerant vapour passage and is communicated with absorption-generator, increase the 3rd generator and choke valve, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline directly to be communicated with first generator, first generator there is the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with the 3rd generator through first solution heat exchanger with dividing steam chest to be communicated with to be adjusted into first generator, the 3rd generator also has the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator are communicated with dividing steam chest, 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 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 single-action-economic benefits and social benefits the 3rd class absorption heat pump.
18. the 3rd class absorption heat pump, be described at the 5-7 item, absorption-generator does not have in arbitrary the 3rd class absorption heat pump of heated medium pipeline and external communications, cancel the refrigerant vapour passage that first evaporimeter or second evaporimeter are communicated with absorption-generator, first generator is set up the refrigerant vapour passage and is communicated with absorption-generator, increase by the 3rd generator, choke valve and solution choke valve, first generator there is the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with the branch steam chest through solution choke valve and absorption-generator with dividing steam chest to be communicated with to be adjusted into first generator, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with the 3rd generator through first solution heat exchanger, the 3rd generator also has the concentrated solution pipeline to be communicated with first generator through first solution pump and first 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 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 single-action-economic benefits and social benefits the 3rd class absorption heat pump.
19. the 3rd class absorption heat pump, be in the 10th described arbitrary the 3rd class absorption heat pump, increase by the 4th generator, the 5th solution heat exchanger and second choke valve, the 3rd generator there is the concentrated solution pipeline through first solution pump, the 4th solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with the branch steam chest through the 4th solution heat exchanger and absorption-generator with dividing steam chest to be communicated with to be adjusted into the 3rd generator, absorption-generator is set up the weak solution pipeline and is communicated with the 4th generator through the 5th solution heat exchanger, the 4th generator also has the concentrated solution pipeline through first solution pump, 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 second choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-action-triple effect the 3rd class absorption heat pump.
20. the 3rd class absorption heat pump, be in the 11st described arbitrary the 3rd class absorption heat pump, increase by the 4th generator, the 5th solution heat exchanger and second choke valve, having the concentrated solution pipeline to be communicated with first solution heat exchanger through first solution pump and the 4th 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 through first solution pump, the 5th solution heat exchanger and the 4th solution heat exchanger are communicated with first 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 second choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-action-triple effect the 3rd class absorption heat pump.
21 the 3rd class absorption heat pumps, be in the 12nd described arbitrary the 3rd class absorption heat pump, increase by the 4th generator, the 5th solution heat exchanger, second choke valve and the 4th solution pump, to absorb-generator has the weak solution pipeline to be communicated with the 3rd generator through first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with the 4th generator through 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 5th solution heat exchanger, having the concentrated solution pipeline to be communicated with first solution heat exchanger through the 4th solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with first solution heat exchanger through the 4th solution heat exchanger and 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 second choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-action-triple effect the 3rd class absorption heat pump.
22. the 3rd class absorption heat pump, be in the 13rd described arbitrary the 3rd class absorption heat pump, increase by the 4th generator, the 5th solution heat exchanger, second choke valve and the 5th solution pump, absorption-generator is set up the weak solution pipeline and is communicated with the 4th generator through the 5th solution heat exchanger, the 4th generator also has the concentrated solution pipeline through the 5th solution pump, after the 5th solution heat exchanger with first generator through first solution pump, concentrated solution pipeline after first solution heat exchanger converges, 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 second choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-action-triple effect the 3rd class absorption heat pump.
23. the 3rd class absorption heat pump, be in the 14th described arbitrary the 3rd class absorption heat pump, increase by the 4th generator, the 5th solution heat exchanger and second choke valve, having the concentrated solution pipeline to be communicated with first solution heat exchanger through first solution pump and the 4th 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 through first solution pump, the 5th solution heat exchanger and the 4th solution heat exchanger are communicated with first 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 second choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-action-triple effect the 3rd class absorption heat pump.
24. the 3rd class absorption heat pump, be in the 15th described arbitrary the 3rd class absorption heat pump, increase by the 4th generator, the 5th solution heat exchanger, second choke valve and the 5th solution pump, to absorb-generator has the weak solution pipeline to be communicated with the 3rd generator through first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with the 4th generator through 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, having the concentrated solution pipeline to be communicated with first solution heat exchanger through the 4th solution heat exchanger and first solution pump in first generator is adjusted into first generator and the concentrated solution pipeline is arranged through the 4th solution heat exchanger, the 5th solution heat exchanger and first solution pump are communicated with first 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 second choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-action-triple effect the 3rd class absorption heat pump.
25. the 3rd class absorption heat pump, be in the 16th described arbitrary the 3rd class absorption heat pump, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, the 3rd generator there is the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with the branch steam chest through first solution heat exchanger and absorption-generator with dividing steam chest to be communicated with to be adjusted into the 3rd generator, absorption-generator is set up the weak solution pipeline and is communicated with the 4th generator through the 3rd solution heat exchanger, the 4th generator also has the concentrated solution pipeline through first solution pump, the 4th solution heat exchanger and absorption-generator are communicated with dividing steam chest, 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 second choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-action-triple effect the 3rd class absorption heat pump.
26. the 3rd class absorption heat pump, be in the 25th described arbitrary the 3rd class absorption heat pump, to absorb-generator has the weak solution pipeline directly to be communicated with the 3rd generator through first solution heat exchanger with the first generator connected sum respectively to be adjusted into absorption-generator and to have the weak solution pipeline to distinguish directly to be communicated with first generator through first solution heat exchanger with the 3rd generator connected sum, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with the branch steam chest through first solution heat exchanger and absorption-generator through solution choke valve and absorption-generator with dividing steam chest to be communicated with to be adjusted into first generator in first generator, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with the branch steam chest through solution choke valve and absorption-generator through first solution heat exchanger and absorption-generator with dividing steam chest to be communicated with to be adjusted into the 3rd generator in the 3rd generator, cancel the refrigerant vapour passage that first generator is communicated with absorption-generator, the 3rd generator is set up the refrigerant vapour passage and is communicated with absorption-generator, forms single-action-triple effect the 3rd class absorption heat pump.
27. the 3rd class absorption heat pump, be in the 17th described arbitrary the 3rd class absorption heat pump, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, the 3rd generator there is the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with the 4th generator through the 4th solution heat exchanger with dividing steam chest to be communicated with to be adjusted into the 3rd generator, the 4th generator also has the concentrated solution pipeline through first solution pump, the 4th solution heat exchanger, first solution heat exchanger and absorption-generator are communicated with dividing steam chest, 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 second choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-action-triple effect the 3rd class absorption heat pump.
28. the 3rd class absorption heat pump, be in the 27th described arbitrary the 3rd class absorption heat pump, increase by the 4th solution pump, to absorb-generator has the weak solution pipeline directly to be communicated with first generator to be adjusted into absorption-generator has the weak solution pipeline to be communicated with first generator through the 4th solution pump and first solution heat exchanger, the 4th generator there is the concentrated solution pipeline through first solution pump, the 4th solution heat exchanger, first solution heat exchanger and absorption-generator have the concentrated solution pipeline through first solution pump with dividing steam chest to be communicated with to be adjusted into the 4th generator, the 4th solution heat exchanger and absorption-generator are communicated with dividing steam chest, there is the refrigerant vapour passage to be communicated with absorption-generator to be adjusted into the 3rd generator to set up the refrigerant vapour passage in first generator and is communicated with absorption-generator, form single-action-triple effect the 3rd class absorption heat pump.
29. the 3rd class absorption heat pump, be in the 18th described arbitrary the 3rd class absorption heat pump, increase by the 4th generator, the 4th solution heat exchanger, the 4th solution pump and second choke valve, to absorb-generator has the weak solution pipeline to be communicated with the 3rd generator through first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with the 4th generator through first solution heat exchanger and the 4th 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, 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 second choke valve again, the 4th generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-action-triple effect the 3rd class absorption heat pump.
30-the 3rd class absorption heat pump, be in the 29th described arbitrary the 3rd class absorption heat pump, cancellation solution choke valve, to absorb-generator has the weak solution pipeline to be communicated with the 4th generator through first solution heat exchanger and the 4th solution heat exchanger to be adjusted into the weak solution pipeline and to be communicated with the 4th generator through the 4th solution heat exchanger, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with the branch steam chest through first solution heat exchanger and absorption-generator through solution choke valve and absorption-generator with dividing steam chest to be communicated with to be adjusted into first generator in first generator, cancel the refrigerant vapour passage that first generator is communicated with absorption-generator, the 3rd generator is set up the refrigerant vapour passage and is communicated with absorption-generator, forms single-action-triple effect the 3rd class absorption heat pump.
31. the 3rd class absorption heat pump, be described at the 5th, do not have in arbitrary the 3rd class absorption heat pump of second condenser, keep the second cryogen liquid pump, increase absorption-evaporimeter, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline directly to be communicated with absorption-evaporimeter, absorption-evaporimeter also has the weak solution pipeline to be communicated with first generator with solution heat exchanger through, evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, condenser is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with first absorber through the second cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again, forms single-action-1.5 grade the 3rd class absorption heat pump.
32. the 3rd class absorption heat pump, be in the 31st described arbitrary the 3rd class absorption heat pump, increase by the 3rd cryogen liquid pump, second evaporimeter and the 4th solution heat exchanger, condenser is set up the cryogen liquid pipeline and is communicated with second evaporimeter through the 3rd cryogen liquid pump, first evaporimeter had the refrigerant vapour passage to be communicated with absorption-generator to be adjusted into second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, to absorb-generator has the weak solution pipeline directly to be communicated with absorption-evaporimeter to be adjusted into absorption-generator has the weak solution pipeline to be communicated with absorption-evaporimeter through the 4th solution heat exchanger, first generator there is the concentrated solution pipeline through first solution pump, first solution heat exchanger and absorption-generator have the concentrated solution pipeline through first solution pump with dividing steam chest to be communicated with to be adjusted into first generator, first solution heat exchanger, the 4th solution heat exchanger and absorption-generator are communicated with dividing steam chest, second evaporimeter also have surplus heat medium pipeline and external communications form single-action-1.5 grade the 3rd class absorption heat pump.
33. the 3rd class absorption heat pump, be in the 31st described arbitrary the 3rd class absorption heat pump, increase choke valve and second condenser, to divide steam chest to have the refrigerant vapour passage to be communicated with first condenser to be adjusted into the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser has the cryogen liquid pipeline to be communicated with first condenser through choke valve, second condenser also has cooling medium pipeline and external communications, forms single-action-1.5 grade the 3rd class absorption heat pump.
34. the 3rd class absorption heat pump, be in the 6th described arbitrary the 3rd class absorption heat pump, increase choke valve or the 3rd cryogen liquid pump, the 4th solution heat exchanger and absorption-evaporimeter, having the weak solution pipeline to be communicated with absorption-generator through second solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with absorption-evaporimeter through second solution heat exchanger, absorption-evaporimeter also has the weak solution pipeline to be communicated with absorption-generator through the 4th solution heat exchanger, to divide steam chest to have the concentrated solution pipeline to be communicated with second generator through second solution pump and second solution heat exchanger is adjusted into the branch steam chest and the concentrated solution pipeline is arranged through second solution pump, the 4th solution heat exchanger and second solution heat exchanger are communicated with second generator, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, condenser is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with first absorber through the 3rd cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again, or first evaporimeter set up the cryogen liquid pipeline and be communicated with second evaporimeter and condenser had the cryogen liquid pipeline be communicated with second evaporimeter through the second cryogen liquid pump through choke valve and be adjusted into condenser and have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with first absorber through the second cryogen liquid pump again with absorption-evaporimeter after absorption-evaporimeter is communicated with, form single-action-1.5 grade the 3rd class absorption heat pump.
35. the 3rd class absorption heat pump, be described at the 8th, do not have in arbitrary the 3rd class absorption heat pump of second evaporimeter, increase absorption-evaporimeter, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline directly to be communicated with absorption-evaporimeter, absorption-evaporimeter also has the weak solution pipeline to be communicated with first generator through first solution heat exchanger, evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, having the cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump second condenser is adjusted into second condenser and has the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with first absorber through the second cryogen liquid pump again with absorption-evaporimeter after absorption-evaporimeter is communicated with, form single-action-1.5 grade the 3rd class absorption heat pump.
36. the 3rd class absorption heat pump, be in the 8th described arbitrary the 3rd class absorption heat pump, increase choke valve or the 3rd cryogen liquid pump, absorption-evaporimeter and the 4th solution heat exchanger, there is the weak solution pipeline to have the weak solution pipeline to be communicated with absorption-evaporimeter through second solution heat exchanger through second solution heat exchanger and absorption-generator with dividing steam chest to be communicated with to be adjusted into second absorber second absorber, absorption-evaporimeter also has the weak solution pipeline to be communicated with dividing steam chest through the 4th solution heat exchanger and absorption-generator, to divide steam chest to have the concentrated solution pipeline to be communicated with second generator through second solution pump and second solution heat exchanger is adjusted into the branch steam chest and the concentrated solution pipeline is arranged through second solution pump, the 4th solution heat exchanger and second solution heat exchanger are communicated with second generator, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with absorption-evaporimeter, second condenser is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with first absorber through the 3rd cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again, or second the cryogen liquid pump set up the cryogen liquid pipeline and be communicated with back absorptions-evaporimeter with absorption-evaporimeter and have the refrigerant vapour passage to be communicated with first absorber more also simultaneously the second cryogen liquid pump to be had the cryogen liquid pipeline to be communicated with first evaporimeter and be adjusted into the second cryogen liquid pump and have the cryogen liquid pipeline to be communicated with first evaporimeter through choke valve, formation single-action-1.5 grade the 3rd class absorption heat pump.
37. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 31-34 item, cancel the refrigerant vapour passage that second evaporimeter 18 and second evaporimeter 18 be communicated with absorption-generator 3 or cancel the refrigerant vapour passage that first evaporimeter 15 is communicated with absorption-generator 3, absorption-evaporimeter 27 is set up the refrigerant vapour passage and is communicated with absorption-generator 3, forms single-action-two-stage the 3rd class absorption heat pump.
38. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 5-37 item, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, second solution heat exchanger is set up the concentrated solution pipeline and is communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with first absorber through newly-increased solution heat exchanger, having the refrigerant vapour passage to be communicated with second absorber to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with economic benefits and social benefits is the 3rd class absorption heat pump of high temperature generation flow process.
39. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 5-37 item, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, 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 second generator through newly-increased solution heat exchanger second solution heat exchanger, having the concentrated solution pipeline to be communicated with first absorber 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 newly-increased solution heat exchanger, newly-increased generator has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger again, having the refrigerant vapour passage to be communicated with second absorber to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with economic benefits and social benefits is the 3rd class absorption heat pump of high temperature generation flow process.
40. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 5-37 item, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, 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 newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with first absorber through newly-increased solution heat exchanger and the 3rd solution heat exchanger, having the refrigerant vapour passage to be communicated with second absorber to be adjusted into second generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased choke valve again, newly-increased generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with economic benefits and social benefits is the 3rd class absorption heat pump of high temperature generation flow process.
41. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 5-37 item, increase newly-increased first generator, newly-increased second generator, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first throttle valve and newly-increased second choke valve, second solution heat exchanger is set up the concentrated solution pipeline and is communicated with newly-increased second generator through newly-increased second solution heat exchanger with the newly-increased first generator connected sum through newly-increased first solution heat exchanger respectively, newly-increased first generator also has the concentrated solution pipeline to be communicated with first absorber through newly-increased first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with first absorber through newly-increased second solution heat exchanger, having the refrigerant vapour passage to be communicated with second absorber to be adjusted into second generator to have the refrigerant vapour passage to be communicated with newly-increased first generator in back with newly-increased first generator in second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased first throttle valve again, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased second choke valve again, newly-increased second generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with the triple effect is the 3rd class absorption heat pump of high temperature generation flow process.
42. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 5-37 item, increase newly-increased first generator, newly-increased second generator, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first throttle valve and newly-increased second choke valve, 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 second generator through newly-increased second solution heat exchanger and newly-increased first solution heat exchanger second solution heat exchanger, having the concentrated solution pipeline to be communicated with first absorber 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 first generator through newly-increased first solution heat exchanger, newly-increased first generator also has 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 first absorber through the 3rd solution heat exchanger, having the refrigerant vapour passage to be communicated with second absorber to be adjusted into second generator to have the refrigerant vapour passage to be communicated with newly-increased first generator in back with newly-increased first generator in second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased first throttle valve again, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased second choke valve again, newly-increased second generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with the triple effect is the 3rd class absorption heat pump of high temperature generation flow process.
43. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 5-37 item, increase newly-increased first generator, newly-increased second generator, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution pump and newly-increased second solution pump, 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 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, newly-increased first generator also has the concentrated solution pipeline to be communicated with second generator through newly-increased first solution pump and newly-increased first solution heat exchanger, having the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger in second generator is adjusted into second generator and the concentrated solution pipeline is arranged through newly-increased first solution heat exchanger, newly-increased second solution heat exchanger and the 3rd solution heat exchanger are communicated with first absorber, having the refrigerant vapour passage to be communicated with second absorber to be adjusted into second generator to have the refrigerant vapour passage to be communicated with newly-increased first generator in back with newly-increased first generator in second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased first throttle valve again, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased second choke valve again, newly-increased second generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with the triple effect is the 3rd class absorption heat pump of high temperature generation flow process.
44. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 5-37 item, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, 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 absorber, newly-increased absorber also has the weak solution pipeline to be communicated with second generator through newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with first absorber through 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 newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger, newly-increased generator also has the thermal medium of driving pipeline respectively with external communications and has the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, and forming with the back-heating type single-action is the 3rd class absorption heat pump of high temperature generation flow process.
45. the 3rd class absorption heat pump, be in the 44th described arbitrary the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased choke valve, newly-increased 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 newly-increased first generator through newly-increased second solution heat exchanger, having the refrigerant vapour passage to be communicated with second absorber to be adjusted into second generator to have the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator in second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased choke valve again, newly-increased second generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with the backheating type double-effect is the 3rd class absorption heat pump of high temperature generation flow process.
46. the 3rd class absorption heat pump, be in the 44th described arbitrary the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased choke valve, to increase absorber newly has the weak solution pipeline to be communicated with second generator through newly-increased solution pump and newly-increased first solution heat exchanger to be adjusted into newly-increased absorber and to have weak solution pipeline warp to increase solution pump newly, newly-increased second solution heat exchanger and newly-increased first solution heat exchanger are communicated with second generator, having the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased first solution heat exchanger in second generator is adjusted into second generator and has 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 newly-increased first generator through newly-increased second solution heat exchanger, having the refrigerant vapour passage to be communicated with second absorber to be adjusted into second generator to have the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator in second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased choke valve again, newly-increased second generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with the backheating type double-effect is the 3rd class absorption heat pump of high temperature generation flow process.
47. the 3rd class absorption heat pump, be in the 44th described arbitrary the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased choke valve and newly-increased second solution pump, to increase newly absorber have the weak solution pipeline through newly-increased first solution pump and newly-increased first solution heat exchanger is communicated with second generator be adjusted into newly-increased absorber have the weak solution pipeline through newly-increased first solution pump with increase first solution heat exchanger newly and be communicated with newly-increased second generator, newly-increased second generator also has the concentrated solution pipeline to be communicated with second generator through newly-increased second solution pump and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased first solution heat exchanger in second generator is adjusted into second generator and the concentrated solution pipeline is arranged through increasing second solution heat exchanger newly and increasing first solution heat exchanger newly and be communicated with newly-increased first generator, having the refrigerant vapour passage to be communicated with second absorber to be adjusted into second generator to have the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator in second generator has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased choke valve again, newly-increased second generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with the backheating type double-effect is the 3rd class absorption heat pump of high temperature generation flow process.
48. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of 45-47 item, the driving thermal medium pipeline of newly-increased first generator of cancellation and external communications, increase newly-increased second choke valve, second generator is set up the refrigerant vapour passage and is communicated with newly-increased first generator in back with newly-increased first generator and has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased second choke valve again, and formation is the 3rd class absorption heat pump of high temperature generation flow process with the backheating type double-effect.
49. the 3rd class absorption heat pump, be in the 45th described arbitrary the 3rd class absorption heat pump, increase newly-increased the 3rd generator, newly-increased the 3rd solution heat exchanger and newly-increased second choke valve, newly-increased solution pump is set up the weak solution pipeline and is communicated with newly-increased the 3rd generator through newly-increased the 3rd solution heat exchanger, newly-increased the 3rd generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased the 3rd solution heat exchanger, to increase second generator newly has the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased second generator to have the refrigerant vapour passage to be communicated with the back with newly-increased the 3rd generator to increase the 3rd generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with first evaporimeter, newly-increased the 3rd generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of high temperature generation flow process.
50. the 3rd class absorption heat pump, be in the 46th described arbitrary the 3rd class absorption heat pump, increase newly-increased the 3rd generator, newly-increased the 3rd solution heat exchanger and newly-increased second choke valve, to increase absorber newly and the weak solution pipeline be arranged through newly-increased solution pump, newly-increased second solution heat exchanger and newly-increased first solution heat exchanger are communicated with second generator and are adjusted into newly-increased absorber and have weak solution pipeline warp to increase solution pump newly, newly-increased the 3rd solution heat exchanger, newly-increased second solution heat exchanger and newly-increased first solution heat exchanger are communicated with second generator, to increase second generator newly has the concentrated solution pipeline to be communicated with newly-increased first generator to be adjusted into through newly-increased second solution heat exchanger to increase second generator newly and have concentrated solution pipeline warp to increase second solution heat exchanger newly to be communicated with newly-increased the 3rd generator, newly-increased the 3rd generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased the 3rd solution heat exchanger, to increase second generator newly has the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased second generator to have the refrigerant vapour passage to be communicated with the back with newly-increased the 3rd generator to increase the 3rd generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with first evaporimeter, newly-increased the 3rd generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of high temperature generation flow process.
51. the 3rd class absorption heat pump, be in the 47th described arbitrary the 3rd class absorption heat pump, increase newly-increased the 3rd generator, newly-increased the 3rd solution heat exchanger, newly-increased second choke valve and newly-increased the 3rd solution pump, to increase absorber newly has the weak solution pipeline to be communicated with newly-increased second generator through newly-increased first solution pump and newly-increased first solution heat exchanger to be adjusted into newly-increased absorber and the weak solution pipeline to be arranged through increasing first solution pump newly and increasing first solution heat exchanger newly and be communicated with newly-increased the 3rd generator, newly-increased the 3rd generator also has the concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased the 3rd solution pump and newly-increased the 3rd solution heat exchanger, having the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased second solution heat exchanger and newly-increased first solution heat exchanger in second generator is adjusted into second generator and has concentrated solution pipeline warp to increase second solution heat exchanger newly, newly-increased the 3rd solution heat exchanger and newly-increased first solution heat exchanger are communicated with newly-increased first generator, to increase second generator newly has the refrigerant vapour passage to be communicated with second absorber to be adjusted into newly-increased second generator to have the refrigerant vapour passage to be communicated with the back with newly-increased the 3rd generator to increase the 3rd generator newly and have cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with first evaporimeter, newly-increased the 3rd generator also has the refrigerant vapour passage to be communicated with second absorber, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of high temperature generation flow process.
52. the 3rd class absorption heat pump, be to ask in described the 3rd arbitrary class absorption heat pump at 49-51, increase newly-increased the 3rd choke valve, the driving thermal medium pipeline of newly-increased first generator of cancellation and external communications, second generator is set up the refrigerant vapour passage and is communicated with newly-increased first generator in back with newly-increased first generator and has the cryogen liquid pipeline to be communicated with first evaporimeter through newly-increased the 3rd choke valve again, and formation is the 3rd class absorption heat pump of high temperature generation flow process with the back-heating type triple-effect.
53. the 3rd class absorption heat pump, be to ask in described the 3rd arbitrary class absorption heat pump at 49-51, increase newly-increased the 3rd choke valve, the driving thermal medium pipeline of newly-increased first generator of cancellation and external communications, newly-increased second generator is set up the refrigerant vapour passage and is communicated with newly-increased first generator in back with newly-increased first generator and has cryogen liquid pipeline warp to increase the 3rd choke valve newly again to be communicated with first evaporimeter, and formation is the 3rd class absorption heat pump of high temperature generation flow process with the back-heating type triple-effect.
Description of drawings:
-three absorption systems the 1st kind of structure and schematic flow sheet take place according to provided by the invention three in Fig. 1.
-three absorption systems the 2nd kind of structure and schematic flow sheet take place according to provided by the invention three in Fig. 2.
Fig. 3 is according to the 3rd class absorption heat pump provided by the invention the 1st kind of structure and schematic flow sheet.
Fig. 4 is according to the 3rd class absorption heat pump provided by the invention the 2nd kind of structure and schematic flow sheet.
Fig. 5 is according to the 3rd class absorption heat pump provided by the invention the 3rd kind of structure and schematic flow sheet.
Fig. 6 is according to the 3rd class absorption heat pump provided by the invention the 4th kind of structure and schematic flow sheet.
Fig. 7 is according to the 3rd class absorption heat pump provided by the invention the 5th kind of structure and schematic flow sheet.
Fig. 8 is according to single-action-economic benefits and social benefits the 3rd class absorption heat pump provided by the invention the 1st kind of structure and schematic flow sheet.
Fig. 9 is according to single-action-economic benefits and social benefits the 3rd class absorption heat pump provided by the invention the 2nd kind of structure and schematic flow sheet.
Figure 10 is according to single-action-economic benefits and social benefits the 3rd class absorption heat pump provided by the invention the 3rd kind of structure and schematic flow sheet.
Figure 11 is according to single-action-economic benefits and social benefits the 3rd class absorption heat pump provided by the invention the 4th kind of structure and schematic flow sheet.
Figure 12 is according to single-action-economic benefits and social benefits the 3rd class absorption heat pump provided by the invention the 5th kind of structure and schematic flow sheet.
Figure 13 is according to single-action-economic benefits and social benefits the 3rd class absorption heat pump provided by the invention the 6th kind of structure and schematic flow sheet.
Figure 14 is according to single-action-triple effect the 3rd class absorption heat pump provided by the invention the 1st kind of structure and schematic flow sheet.
Figure 15 is according to single-action-triple effect the 3rd class absorption heat pump provided by the invention the 2nd kind of structure and schematic flow sheet.
Figure 16 is according to single-action-triple effect the 3rd class absorption heat pump provided by the invention the 3rd kind of structure and schematic flow sheet.
Figure 17 is according to single-action-triple effect the 3rd class absorption heat pump provided by the invention the 4th kind of structure and schematic flow sheet.
Figure 18 is according to single-action-triple effect the 3rd class absorption heat pump provided by the invention the 5th kind of structure and schematic flow sheet.
Figure 19 is according to single-action-triple effect the 3rd class absorption heat pump provided by the invention the 6th kind of structure and schematic flow sheet.
Figure 20 is according to single-action-triple effect the 3rd class absorption heat pump provided by the invention the 7th kind of structure and schematic flow sheet.
Figure 21 is according to single-action-triple effect the 3rd class absorption heat pump provided by the invention the 8th kind of structure and schematic flow sheet.
Figure 22 is according to single-action-triple effect the 3rd class absorption heat pump provided by the invention the 9th kind of structure and schematic flow sheet.
Figure 23 is according to single-action provided by the invention-1.5 grade the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet.
Figure 24 is according to single-action provided by the invention-1.5 grade the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet.
Figure 25 is according to single-action provided by the invention-1.5 grade the 3rd class absorption heat pump the 3rd kind of structure and schematic flow sheet.
Figure 26 is according to single-action provided by the invention-1.5 grade the 3rd class absorption heat pump the 4th kind of structure and schematic flow sheet.
Figure 27 be according to provided by the invention be the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet of high temperature generation flow process with economic benefits and social benefits.
Figure 28 be according to provided by the invention be the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet of high temperature generation flow process with economic benefits and social benefits.
Figure 29 be according to provided by the invention be the 3rd class absorption heat pump the 3rd kind of structure and schematic flow sheet of high temperature generation flow process with economic benefits and social benefits.
Figure 30 be according to provided by the invention be the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet of high temperature generation flow process with the triple effect.
Figure 31 be according to provided by the invention be the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet of high temperature generation flow process with the triple effect.
Figure 32 be according to provided by the invention be the 3rd class absorption heat pump the 3rd kind of structure and schematic flow sheet of high temperature generation flow process with the triple effect.
Figure 33 be according to provided by the invention be the 3rd class absorption heat pump structure and schematic flow sheet of high temperature generation flow process with the back-heating type single-action.
Figure 34 be according to provided by the invention be the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet of high temperature generation flow process with the backheating type double-effect.
Figure 35 be according to provided by the invention be the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet of high temperature generation flow process with the backheating type double-effect.
Figure 36 be according to provided by the invention be the 3rd class absorption heat pump the 3rd kind of structure and schematic flow sheet of high temperature generation flow process with the backheating type double-effect.
Figure 37 be according to provided by the invention be the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet of high temperature generation flow process with the back-heating type triple-effect.
Figure 38 be according to provided by the invention be the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet of high temperature generation flow process with the back-heating type triple-effect.
Figure 39 be according to provided by the invention be the 3rd class absorption heat pump the 3rd kind of structure and schematic flow sheet of high temperature generation flow process with the back-heating type triple-effect.
Among the figure, 1-first generator, 2-second generator, 3-absorption-generator, 4-first absorber, 5-second absorber, 6-divides steam chest, 7-first solution pump, 8-second solution pump, 9-the 3rd solution pump, 10-first solution heat exchanger, 11-second solution heat exchanger, 12-the 3rd solution heat exchanger; 13-condenser/first condenser, 14-second condenser, 15-evaporimeter/first evaporimeter, the 16-cryogen liquid pump/first cryogen liquid pump, the 17-second cryogen liquid pump, 18-second evaporimeter, 19-choke valve/first throttle valve, 20-the 3rd generator, 21-the 4th solution heat exchanger, 22-the 4th solution pump, 23-second choke valve, 24-the 4th generator, 25-the 5th solution heat exchanger, 26-the 5th solution pump, 27-absorption-evaporimeter, 28-the 3rd cryogen liquid pump, 29-solution choke valve; A-increases generator/newly-increased the-generator newly, and B-increases solution heat exchanger/newly-increased first solution heat exchanger newly, and 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, and F-increases second solution heat exchanger newly, and G-increases second choke valve newly, H-increases second solution pump newly, I-increases absorber newly, and J-increases the 3rd generator newly, and K-increases the 3rd choke valve newly, L-increases the 3rd solution heat exchanger newly, and M-increases the 3rd solution pump newly.
What need indicate is:
(1) naming method 1---name from high temperature driven heat and the hot effect of the solution generating process, bringing into play of low temperature driving.Be example with " single-action-economic benefits and social benefits ", " single-action " refers to that high temperature driven (generation) process adopts the single-action flow process, and " economic benefits and social benefits " refer to that low temperature drives (generations) process employing double-effect process.
(2) naming method 2---and temperature height difference is named from the solution generating process, as " be three class absorption heat pump of high temperature generation flow process with economic benefits and social benefits ", refers to that solution high temperature generating process is double-effect process.
When (3) employing was the working media of representative with the ammonia spirit, generator was called rectifying column; In case of necessity, first rectifying column increases heated medium pipeline and external communications, and the involved branch steam chest 6 of ammonia spirit increases cooling medium pipeline and external communications.
(4) setting of solution pump---among Fig. 1, the setting of first solution pump 7 is on first generator 1 and divide pressure differential and flow of solution resistance between the steam chest 6 to decide; Also can make the solution pressure for vaporization be lower than the pressure of first generator 1 in the reality, to omit first solution pump 7.
(5) the 3rd class absorption heat pump shown in Figure 27-39 is to adopt economic benefits and social benefits, triple effect, back-heating type single-action, backheating type double-effect and back-heating type triple-effect as the representative of high temperature generation flow process respectively; Each the 3rd class absorption heat pump shown in Fig. 3-26 also can adopt each the high temperature generation flow process shown in Figure 27-39.
(6) with Fig. 8 be example, divide the refrigerant vapour pressure of steam chest 6 releases and the refrigerant vapour pressure of the 3rd generator 20 releases to approach; By contrast, the refrigerant vapour pressure that first generator 1 discharges is much higher, in this solution pipeline solution pump is not set, and first solution heat exchanger 10 also plays hypotensive effect.
The specific embodiment:
Describe the present invention in detail below in conjunction with accompanying drawing and example.In the instantiation statement, do not repeat to explain structure and flow process under the inessential situation, for apparent and have other embodiment not do the flow process statement can be for reference the time yet.
Three generations-three absorption systems shown in Figure 1 are achieved in that
1. on the structure, it mainly is made up of first generator, second generator, absorption-generator, first absorber, second absorber, branch steam chest, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; First generator 1 has the concentrated solution pipeline through first solution pump 7, first solution heat exchanger 10 and absorption-generator 3 are communicated with dividing steam chest 6, divide steam chest 6 to also have the concentrated solution pipeline to be communicated with second generator 2 through second solution pump 8 and second solution heat exchanger 11, second generator 2 also has the concentrated solution pipeline to be communicated with first absorber 4 through the 3rd solution heat exchanger 12, first absorber 4 also has the weak solution pipeline to be communicated with second absorber 5 through the 3rd solution pump 9 and the 3rd solution heat exchanger 12, second absorber 5 also has the weak solution pipeline to be communicated with absorption-generator 3 through second solution heat exchanger 11, absorption-generator 3 also has the weak solution pipeline to be communicated with first generator 1 through first solution heat exchanger 10, first generator 1 also have surplus heat respectively medium pipeline and external communications and refrigerant vapour passage and external communications arranged, second generator 2 also has the thermal medium of driving pipeline respectively with external communications and has the refrigerant vapour passage to be communicated with second absorber 5, absorption-generator 3 also has refrigerant vapour passage and external communications, absorption-generator 3 or also have heated medium pipeline and external communications, first absorber 4 also has heated medium pipeline and external communications respectively and refrigerant vapour passage and external communications is arranged, second absorber 5 also has heated medium pipeline and external communications, divides steam chest 6 to also have refrigerant vapour passage and external communications.
2. on the flow process, the waste heat MEDIA FLOW is through first generator 1, heating enters the solution release in it and refrigerant vapour externally is provided, the concentrated solution of the first generator 1 absorption-generator 3 of behind first solution pump 7 and first solution heat exchanger 10, flowing through again, the heat absorbing part vaporization enters branch steam chest 6, divide steam chest 6 that refrigerant vapour externally is provided, divide the concentrated solution of steam chest 6 to enter second generator 2 through second solution pump 8 and second solution heat exchanger 11, drive heat medium flow through second generator 2, heating enters its interior solution release and provides refrigerant vapour to second absorber 5, the concentrated solution of second generator 2 enters first absorber 4 through the 3rd solution heat exchanger 12, absorption from the refrigerant vapour of outside and heat release in heated medium, the weak solution of first absorber 4 enters second absorber 5 through the 3rd solution pump 9 and the 3rd solution heat exchanger 12, absorption from the refrigerant vapour of second generator 2 and heat release in heated medium, the weak solution of second absorber 5 is advanced absorption-generator 3 through second solution heat exchanger 11, absorption from the refrigerant vapour of outside and respectively heat release in solution and the heated medium of the absorption-generator 3 of flowing through, the weak solution of absorption-generator 3 enters first generator 1 through first solution heat exchanger 10, forms three-three absorption systems take place.
Three generations-three absorption systems shown in Figure 2 are achieved in that
1. on the structure, in three generations-three absorption systems shown in Figure 1, first generator 1 there is the concentrated solution pipeline through first solution pump 7, first solution heat exchanger 10 and absorption-generator 3 have the concentrated solution pipeline to be communicated with absorption-generator 3 through first solution pump 7 and first solution heat exchanger 10 with dividing steam chest 6 to be communicated with to be adjusted into first generator 1, have the weak solution pipeline to be communicated with absorption-generator 3 through second solution heat exchanger 11 second absorber 5 and are adjusted into second absorber 5 and have the weak solution pipeline to be communicated with branch steam chest 6 through second solution heat exchanger 11 and 3 connections of absorption-generator.
2. on the flow process, the waste heat MEDIA FLOW enters the solution release in it and refrigerant vapour externally is provided through first generator 1, heating, the concentrated solution of first generator 1 enters absorption-generator 3, absorbs from the refrigerant vapour of outside and heat release is in solution and the heated medium of the absorption-generator 3 of flowing through respectively through first solution pump 7 and first solution heat exchanger 10, and the weak solution of absorption-generator 3 enters first generator 1 through first solution heat exchanger 10; The weak solution of the second absorber 5 absorption-generator 3 of after 11 heat releases of second solution heat exchanger and step-down, flowing through again, the heat absorbing part vaporization enters branch steam chest 6, divide steam chest 6 that refrigerant vapour externally is provided, divide the concentrated solution of steam chest 6 to enter second generator 2 through second solution pump 8 and second solution heat exchanger 11, drive heat medium flow through second generator 2, heating enters its interior solution release and provides refrigerant vapour to second absorber 5, the concentrated solution of second generator 2 enters first absorber 4 through the 3rd solution heat exchanger 12, absorption from the refrigerant vapour of outside and heat release in heated medium, the weak solution of first absorber 4 enters second absorber 5 through the 3rd solution pump 9 and the 3rd solution heat exchanger 12, absorption, forms three-three absorption systems takes place in heated medium from the refrigerant vapour of second generator 2 and heat release.
The 3rd class absorption heat pump shown in Figure 3 is achieved in that
1. on the structure, in three generations-three absorption systems shown in Figure 1, increase by first condenser, second condenser, evaporimeter, the first cryogen liquid pump and the second 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 13, first condenser 13 also has the cryogen liquid pipeline to be communicated with evaporimeter 15 through the first cryogen liquid pump 16, to divide steam chest 6 to have refrigerant vapour passage and external communications to be defined as branch steam chest 6 has the refrigerant vapour passage to be communicated with second condenser 14, second condenser 14 also has the cryogen liquid pipeline to be communicated with evaporimeter 15 through the second cryogen liquid pump 17, having refrigerant vapour passage and external communications to be defined as evaporimeter 15 first absorber 4 has the refrigerant vapour passage to be communicated with first absorber 4, to absorb-generator 3 has refrigerant vapour passage and external communications to be defined as evaporimeter 15 has the refrigerant vapour passage to be communicated with absorption-generator 3, first condenser 13 and second condenser 14 also have cooling medium pipeline and external communications respectively, evaporimeter 15 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 13, heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of first condenser 13 enters evaporimeter 15 through 16 pressurizations of the first cryogen liquid pump; The refrigerant vapour that divides steam chest 6 to discharge enters second condenser 14, heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of second condenser 14 enters evaporimeter 15 through 17 pressurizations of the second cryogen liquid pump; Cryogen liquid in the evaporimeter 15 absorbs waste heat and becomes refrigerant vapour also to provide to first absorber 4 and absorption-generator 3 respectively, forms the 3rd class absorption heat pump.
In the embodiment shown in Figure 3, when the condensing pressure of first condenser 13 was higher than the condensing pressure of second condenser 14, first solution pump 7 can omit; Flow through again after 10 step-downs of first solution heat exchanger absorption-generator 3, heat absorption vaporization of the concentrated solution of first generator 1 enters branch steam chest 6.
The 3rd class absorption heat pump shown in Figure 4 is achieved in that
1. on the structure, in three generations-three absorption systems shown in Figure 1, the heated medium pipeline of cancellation absorption-generator 3 and external communications, increase condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 condenser 13, to divide steam chest 6 to have refrigerant vapour passage and external communications to be defined as branch steam chest 6 has the refrigerant vapour passage to be communicated with condenser 13, condenser 13 also has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through the first cryogen liquid pump 16, condenser 13 also has the cryogen liquid pipeline to be communicated with second evaporimeter 18 through the second cryogen liquid pump 17, having refrigerant vapour passage and external communications to be defined as first evaporimeter 15 first absorber 4 has the refrigerant vapour passage to be communicated with first absorber 4, to absorb-generator 3 has refrigerant vapour passage and external communications to be defined as second evaporimeter 18 has the refrigerant vapour passage to be communicated with absorption-generator 3, condenser 13 also has cooling medium pipeline and external communications, first evaporimeter 15 and second evaporimeter 18 also have surplus heat respectively medium pipeline and external communications.
2. on the flow process, first generator 1 enters first condenser 13 with the refrigerant vapour that divides steam chest 6 to produce, heat release becomes cryogen liquid in cooling medium, the cryogen liquid of first condenser 13 is divided into two-way---and the first via enters evaporimeter 15, absorbs waste heat and become refrigerant vapour and provide to first absorber 4 through the pressurization of the first cryogen liquid pump 16, the second the tunnel enters second evaporimeter 18, absorbs waste heat and become refrigerant vapour and provide to absorption-generator 3 through the pressurization of the second cryogen liquid pump 17, forms the 3rd class absorption heat pump.
The 3rd class absorption heat pump shown in Figure 5 is achieved in that
1. on the structure, in three generations-three absorption systems shown in Figure 2, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 13, first condenser 13 also has the cryogen liquid pipeline to be communicated with second evaporimeter 18 through the first cryogen liquid pump 16, to absorb-generator 3 has refrigerant vapour passage and external communications to be defined as second evaporimeter 18 has the refrigerant vapour passage to be communicated with absorption-generator 3, to divide steam chest 6 to have refrigerant vapour passage and external communications to be defined as branch steam chest 6 has the refrigerant vapour passage to be communicated with second condenser 14, second condenser 14 also has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through the second cryogen liquid pump 17, having refrigerant vapour passage and external communications to be defined as first evaporimeter 15 first absorber 4 has the refrigerant vapour passage to be communicated with first absorber 4, first condenser 13 and second condenser 14 also have cooling medium pipeline and external communications respectively, first evaporimeter 15 and second evaporimeter 18 also have surplus heat respectively medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces enters first condenser 13, heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of first condenser 13 enters second evaporimeter 18, absorbs waste heat and become refrigerant vapour and provide to absorption-generator 3 through 16 pressurization of the first cryogen liquid pump; The refrigerant vapour that divides steam chest 6 to produce enters second condenser 14, heat release becomes cryogen liquid in cooling medium, the cryogen liquid of second condenser 14 enters first evaporimeter 15, absorbs waste heat and become refrigerant vapour and provide to first absorber 4 through the pressurization of the second cryogen liquid pump 17, forms the 3rd class absorption heat pump.
The 3rd class absorption heat pump shown in Figure 6 is achieved in that
In the 3rd class absorption heat pump shown in Figure 5, the heated medium pipeline of cancellation absorption-generator 3 and external communications, cancel second evaporimeter 18, first condenser 13 has the cryogen liquid pipeline to be communicated with evaporimeter 15 through the first cryogen liquid pump 16, evaporimeter 15 is set up the refrigerant vapour passage and is communicated with absorption-generator 3, forms the 3rd class absorption heat pump.
The 3rd class absorption heat pump shown in Figure 7 is achieved in that
1. on the structure, in three generations-three absorption systems shown in Figure 2, the heated medium pipeline of cancellation absorption-generator 3 and external communications, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 13, first condenser 13 also has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through the first cryogen liquid pump 16, to divide steam chest 6 to have refrigerant vapour passage and external communications to be defined as branch steam chest 6 has the refrigerant vapour passage to be communicated with second condenser 14, second condenser 14 has the cryogen liquid pipeline to be communicated with second evaporimeter 18 through the second cryogen liquid pump 17, having refrigerant vapour passage and external communications to be defined as first evaporimeter 15 first absorber 4 has the refrigerant vapour passage to be communicated with first absorber 4, to absorb-generator 3 has refrigerant vapour passage and external communications to be defined as second evaporimeter 18 has the refrigerant vapour passage to be communicated with absorption-generator 3, first condenser 13 and second condenser 14 also have cooling medium pipeline and external communications respectively, first evaporimeter 15 and second evaporimeter 18 also have surplus heat respectively medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 1 produces enters first condenser 13, heat release becomes cryogen liquid in cooling medium, the cryogen liquid of first condenser 13 enters first evaporimeter 15 through 16 pressurizations of the first cryogen liquid pump, the absorption waste heat becomes refrigerant vapour and provides to first absorber 4, the refrigerant vapour that divides steam chest 6 to produce enters second condenser 14, heat release becomes cryogen liquid in cooling medium, the cryogen liquid of second condenser 14 enters second evaporimeter 18 through 17 pressurizations of the second cryogen liquid pump, the absorption waste heat becomes refrigerant vapour and provides to absorption-generator 3, forms the 3rd class absorption heat pump.
Single-action-economic benefits and social benefits 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 3, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, first generator 1 there is the concentrated solution pipeline through first solution pump 7, first solution heat exchanger 10 and absorption-generator 3 have the concentrated solution pipeline to be communicated with branch steam chest 6 through first solution heat exchanger 10 and absorption-generator 3 with dividing steam chest 6 to be communicated with to be adjusted into first generator 1, absorption-generator 3 is set up the weak solution pipeline and is communicated with the 3rd generator 20 through the 4th solution heat exchanger 21, the 3rd generator 20 also has the concentrated solution pipeline through first solution pump 7, converge with the concentrated solution pipeline of first generator 1 after first solution heat exchanger 10 after the 4th solution heat exchanger 21, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 20 with the 3rd generator 20 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 13 through choke valve 19 again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, and the 3rd generator 20 refrigerant vapour passage in addition is communicated with first condenser 13.
2. on the flow process, the refrigerant vapour that first generator 1 produces provides to drive thermal medium as it to the 3rd generator 20, the concentrated solution of the first generator 1 absorption-generator 3 of after first solution heat exchanger 10, flowing through again, the heat absorbing part vaporization enters branch steam chest 6, the part weak solution of absorption-generator 3 enters the 3rd generator 20 through the 4th solution heat exchanger 21, refrigerant vapour the 3rd generator 20 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 13, the concentrated solution of the 3rd generator 20 absorption-generator 3 of after first solution pump 7 and the 4th solution heat exchanger 21, flowing through again, the heat absorbing part vaporization enters branch steam chest 6, the refrigerant vapour heat release of the 3rd generator 20 of flowing through becomes cryogen liquid, enter first condenser 13 through choke valve 19 throttlings 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 9 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, having the concentrated solution pipeline to be communicated with first solution heat exchanger 10 through first solution pump 7 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with the 3rd generator 20 through the 4th solution heat exchanger 21, the 3rd generator 20 also has the concentrated solution pipeline to be communicated with first solution heat exchanger 10 through first solution pump 7 and the 4th solution heat exchanger 21, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 20 with the 3rd generator 20 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 13 through choke valve 19 again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, and the 3rd generator 20 refrigerant vapour passage first in addition is communicated with condenser 13.
2. on the flow process, the refrigerant vapour that first generator 1 produces provides to drive thermal medium as it to the 3rd generator 20, the concentrated solution of first generator 1 enters the 3rd generator 20 through the 4th solution heat exchanger 21, refrigerant vapour the 3rd generator 20 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 13, the concentrated solution of the 3rd generator 20 is through first solution pump 7, absorption-the generator 3 of flowing through again after the 4th solution heat exchanger 21 and first solution heat exchanger 10, the heat absorbing part vaporization enters branch steam chest 6, the refrigerant vapour heat release of the 3rd generator 20 of flowing through becomes cryogen liquid, enter first condenser 13 through choke valve 19 throttlings 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 10 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 1 through first solution heat exchanger 10 to be adjusted into absorption-generator 3 and to have the weak solution pipeline to be communicated with the 3rd generator 20 through first solution heat exchanger 10, the 3rd generator 20 also has the concentrated solution pipeline to be communicated with first generator 1 through first solution pump 7 and the 4th solution heat exchanger 21, having the concentrated solution pipeline to be communicated with first solution heat exchanger 10 through first solution pump 7 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with first solution heat exchanger 10 through the 4th solution heat exchanger 21, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 20 with the 3rd generator 20 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 13 through choke valve 19 again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, and the 3rd generator 20 refrigerant vapour passage in addition is communicated with first condenser 13.
2. on the flow process, the refrigerant vapour that first generator 1 produces provides to the 3rd generator 20, the weak solution of absorption-generator 3 enters the 3rd generator 20 through first solution heat exchanger 10, refrigerant vapour the 3rd generator 20 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 13, the concentrated solution of the 3rd generator 20 enters first generator 1 through first solution pump 7 and the 4th solution heat exchanger 21, the refrigerant vapour heat release of the 3rd generator 20 of flowing through becomes cryogen liquid, enter first condenser 13 through choke valve 19 throttlings again, the concentrated solution of the first generator 1 absorption-generator 3 of after the 4th solution heat exchanger 21 and first solution heat exchanger 10, flowing through again, the heat absorbing part vaporization enters branch steam chest 6, 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 11 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, the heated medium pipeline of cancellation absorption-generator 3 and external communications, the refrigerant vapour passage that cancellation evaporimeter 15 is communicated with absorption-generator 3, increase by the 3rd generator, choke valve and solution choke valve, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 1 through first solution heat exchanger 10 to be adjusted into absorption-generator 3 and to have the weak solution pipeline directly to be communicated with first generator 1, first generator 1 there is the concentrated solution pipeline through first solution pump 7, first solution heat exchanger 10 and absorption-generator 3 have the concentrated solution pipeline to be communicated with branch steam chest 6 through solution choke valve 29 and absorption-generator 3 with dividing steam chest 6 to be communicated with to be adjusted into first generator 1, absorption-generator 3 is set up the weak solution pipeline and is communicated with the 3rd generator 20 through first solution heat exchanger 10, the 3rd generator 20 also has the concentrated solution pipeline through first solution pump 7, converge with the concentrated solution pipeline of first generator 1 after solution choke valve 29 after first solution heat exchanger 10, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 20 with the 3rd generator 20 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 13 through choke valve 19 again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator 20 also has the refrigerant vapour passage to be communicated with first condenser 13, and first generator 1 is set up the refrigerant vapour passage and is communicated with absorption-generator 3.
2. on the flow process, the weak solution of absorption-generator 3 directly enters first generator 1 respectively and enters the 3rd generator 20 through first solution heat exchanger 10, the refrigerant vapour that first generator 1 produces provides to absorptions-generator 3 and the 3rd generator 20 respectively, and flow through the 3rd generator 20, heating of refrigerant vapour enters solution release in it and provide refrigerant vapour to first condenser 13; Absorption-generator 3, the heat absorbing part vaporization of flowing through again after solution choke valve 29 of the concentrated solution of first generator 1 enters branch steam chest 6, absorption-generator 3, the heat absorbing part vaporization of flowing through again after first solution pump 7 and first solution heat exchanger 10 of the concentrated solution of the 3rd generator 20 enters branch steam chest 6, the refrigerant vapour heat release of the 3rd generator 20 of flowing through becomes cryogen liquid, enters first condenser 13 through choke valve 19 throttlings 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 12 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, the heated medium pipeline of cancellation absorption-generator 3 and external communications, the refrigerant vapour passage that cancellation evaporimeter 15 is communicated with absorption-generator 3, increase the 3rd generator and choke valve, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 1 through first solution heat exchanger 10 to be adjusted into absorption-generator 3 and to have the weak solution pipeline directly to be communicated with first generator 1, first generator 1 there is the concentrated solution pipeline through first solution pump 7, first solution heat exchanger 10 and absorption-generator 3 have the concentrated solution pipeline to be communicated with the 3rd generator 20 through first solution heat exchanger 10 with dividing steam chest 6 to be communicated with to be adjusted into first generator 1, the 3rd generator 20 also has the concentrated solution pipeline through first solution pump 7, first solution heat exchanger 10 and absorption-generator 3 are communicated with dividing steam chest 6, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 20 with the 3rd generator 20 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 13 through choke valve 19 again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator 20 also has the refrigerant vapour passage to be communicated with first condenser 13, and first generator 1 is set up the refrigerant vapour passage and is communicated with absorption-generator 3.
2. on the flow process, the weak solution of absorption-generator 3 directly enters first generator 1, the refrigerant vapour that first generator 1 produces provides to absorption-generator 3 and the 3rd generator 20 respectively, and the concentrated solution of first generator 1 enters the 3rd generator 20 through first solution heat exchanger 10; Flow through the 3rd generator 20, heating of refrigerant vapour enters solution in it and discharges and provide refrigerant vapour to first condenser 13, absorption-generator 3, the heat absorbing part vaporization of flowing through again after first solution pump 7 and first solution heat exchanger 10 of the concentrated solution of the 3rd generator 20 enters branch steam chest 6, the refrigerant vapour heat release of the 3rd generator 20 of flowing through becomes cryogen liquid, enters first condenser 13 through choke valve 19 throttlings 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 13 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 3, the heated medium pipeline of cancellation absorption-generator 3 and external communications, the refrigerant vapour passage that cancellation evaporimeter 15 is communicated with absorption-generator 3, increase by the 3rd generator, choke valve and solution choke valve, first generator 1 there is the concentrated solution pipeline through first solution pump 7, first solution heat exchanger 10 and absorption-generator 3 have the concentrated solution pipeline to be communicated with branch steam chest 6 through solution choke valve 29 and absorption-generator 3 with dividing steam chest 6 to be communicated with to be adjusted into first generator 1, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 1 through first solution heat exchanger 10 to be adjusted into absorption-generator 3 and to have the weak solution pipeline to be communicated with the 3rd generator 20 through first solution heat exchanger 10, the 3rd generator 20 also has the concentrated solution pipeline to be communicated with first generator 1 through first solution pump 7 and first solution heat exchanger 10, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 20 with the 3rd generator 20 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 13 through choke valve 19 again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator 20 also has the refrigerant vapour passage to be communicated with first condenser 13, and first generator 1 is set up the refrigerant vapour passage and is communicated with absorption-generator 3.
2. on the flow process, the refrigerant vapour that first generator 1 produces provides to absorption-generator 3 and the 3rd generator 20 respectively, the weak solution of absorption-generator 3 enters the 3rd generator 20 through first solution heat exchanger 10, refrigerant vapour the 3rd generator 20 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 13, the concentrated solution of the 3rd generator 20 enters first generator 1 through first solution pump 7 and first solution heat exchanger 10, the concentrated solution of the first generator 1 absorption-generator 3 of after solution choke valve 29, flowing through again, the heat absorbing part vaporization enters branch steam chest 6, forms 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 14 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 6, increase by the 3rd generator, the 4th generator, the 4th solution heat exchanger, the 5th solution heat exchanger, the first throttle valve, second choke valve, the 4th solution pump and the 5th solution pump, absorption-generator 3 is set up the weak solution pipeline and is communicated with the 4th generator 24 through the 5th solution heat exchanger 25 with the 3rd generator 20 connected sums through the 4th solution heat exchanger 21 respectively, the 3rd generator 20 also has the concentrated solution pipeline through the 4th solution pump 22, after the 4th solution heat exchanger 21 with first generator 1 through first solution pump 7, concentrated solution pipeline after first solution heat exchanger 10 converges, the 4th generator 24 also has the concentrated solution pipeline through the 5th solution pump 26, after the 5th solution heat exchanger 25 with first generator 1 through first solution pump 7, concentrated solution pipeline after first solution heat exchanger 10 converges, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 20 with the 3rd generator 20 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 13 through first throttle valve 19 again, the 3rd generator 20 also has the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 has the cryogen liquid pipeline to be communicated with first condenser 13 through second choke valve 23 again, and the 4th generator 24 also has the refrigerant vapour passage to be communicated with first condenser 13.
2. on the flow process, the refrigerant vapour that first generator 1 produces provides to drive thermal medium as it to the 3rd generator 20, and the refrigerant vapour that the 3rd generator 20 produces provides to drive thermal medium as it to the 4th generator 24; The part weak solution of absorption-generator 3 enters the 3rd generator 20 through the 4th solution heat exchanger 21, flow through the 3rd generator 20, heating of refrigerant vapour enters solution in it and discharges and provide refrigerant vapour to the 4th generator 24, the concentrated solution of the 3rd generator 20 enters absorption-generator 3 through the 4th solution pump 22 and the 4th solution heat exchanger 21, and the refrigerant vapour heat release of the 3rd generator 20 of flowing through becomes cryogen liquid, enters first condenser 13 through 19 throttlings of first throttle valve again; The part weak solution of absorption-generator 3 enters the 4th generator 24 through the 5th solution heat exchanger 25, flow through the 4th generator 24, heating of refrigerant vapour enters solution in it and discharges and provide refrigerant vapour to first condenser 13, the concentrated solution of the 4th generator 24 enters absorption-generator 3 through the 5th solution pump 26 and the 5th solution heat exchanger 25, the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enters first condenser 13 through 23 throttlings of second choke valve again, forms single-action-triple effect the 3rd class absorption heat pump.
Single-action-triple effect 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 6, increase by the 3rd generator, the 4th generator, the 4th solution heat exchanger, the 5th solution heat exchanger, first throttle valve and second choke valve, having the concentrated solution pipeline to be communicated with first solution heat exchanger 10 through first solution pump 7 in first generator 1 is adjusted into first generator 1 and has the concentrated solution pipeline to be communicated with the 3rd generator 20 through the 4th solution heat exchanger 21, the 3rd generator 20 also has the concentrated solution pipeline to be communicated with the 4th generator 24 through the 5th solution heat exchanger 25, the 4th generator 24 also has the concentrated solution pipeline through first solution pump 7, the 5th solution heat exchanger 25 and the 4th solution heat exchanger 21 are communicated with first solution heat exchanger 10, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 20 with the 3rd generator 20 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 13 through first throttle valve 19 again, the 3rd generator 20 also has the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 has the cryogen liquid pipeline to be communicated with first condenser 13 through second choke valve 23 again, and the 4th generator 24 also has the refrigerant vapour passage to be communicated with first condenser 13.
2. on the flow process, the refrigerant vapour that first generator 1 produces provides to drive thermal medium as it to the 3rd generator 20, the concentrated solution of first generator 1 enters the 3rd generator 20 through the 4th solution heat exchanger 21, flow through the 3rd generator 20, heating of refrigerant vapour enters solution in it and discharges and provide refrigerant vapour to the 4th generator 24, the concentrated solution of the 3rd generator 20 enters the 4th generator 24 through the 5th solution heat exchanger 25, and the refrigerant vapour heat release of the 3rd generator 20 of flowing through becomes cryogen liquid, enters first condenser 13 through 19 throttlings of first throttle valve again; Flow through the 4th generator 24, heating of refrigerant vapour enters solution in it and discharges and provide refrigerant vapour to first condenser 13, the concentrated solution of the 4th generator 24 enters absorption-generator 3 through first solution pump 7, the 5th solution heat exchanger 25, the 4th solution heat exchanger 21 and first solution heat exchanger 10, the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enters first condenser 13 through second choke valve 23 again, forms single-action-triple effect the 3rd class absorption heat pump.
Single-action-triple effect 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 6, increase by the 3rd generator, the 4th generator, the 4th solution heat exchanger, the 5th solution heat exchanger, the first throttle valve, second choke valve, the 4th solution pump and the 5th solution pump, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 1 through first solution heat exchanger 10 to be adjusted into absorption-generator 3 and to have the weak solution pipeline to be communicated with the 4th generator 24 through first solution heat exchanger 10, the 4th generator 24 also has the concentrated solution pipeline to be communicated with the 3rd generator 20 through the 5th solution pump 26 and the 5th solution heat exchanger 25, the 3rd generator 20 also has the concentrated solution pipeline to be communicated with first generator 1 through the 4th solution pump 22 and the 4th solution heat exchanger 21, having the concentrated solution pipeline to be communicated with first solution heat exchanger 10 through first solution pump 7 in first generator 1 is adjusted into first generator 1 and the concentrated solution pipeline is arranged through the 4th solution heat exchanger 21, the 5th solution heat exchanger 25 and first solution pump 7 are communicated with first solution heat exchanger 10, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into first generator 1 to have the refrigerant vapour passage to be communicated with back the 3rd generator 20 with the 3rd generator 20 in first generator 1 has the cryogen liquid pipeline to be communicated with first condenser 13 through first throttle valve 19 again, the 3rd generator 20 also has the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 has the cryogen liquid pipeline to be communicated with first condenser 13 through second choke valve 23 again, and the 4th generator 24 also has the refrigerant vapour passage to be communicated with first condenser 13.
2. on the flow process, the refrigerant vapour that first generator 1 produces provides to drive thermal medium as it to the 3rd generator 20, and the refrigerant vapour that the 3rd generator 20 produces provides to drive thermal medium as it to the 4th generator 24; The weak solution of absorption-generator 3 enters the 4th generator 24 through first solution heat exchanger 10, flow through the 4th generator 24, heating of refrigerant vapour enters solution in it and discharges and provide refrigerant vapour to first condenser 13, the concentrated solution of the 4th generator 24 enters the 3rd generator 20 through the 5th solution pump 26 and the 5th solution heat exchanger 25, and the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enters first condenser 13 through second choke valve 23 again; Flow through the 3rd generator 20, heating of refrigerant vapour enters solution in it and discharges and provide refrigerant vapour to the 4th generator 24, the concentrated solution of the 3rd generator 20 enters first generator 1 through the 4th solution pump 22 and the 4th solution heat exchanger 21, and the refrigerant vapour heat release of the 3rd generator 20 of flowing through becomes cryogen liquid, enters first condenser 13 through 19 throttlings of first throttle valve again; The concentrated solution of first generator 1 enters absorption-generator 3 through the 4th solution heat exchanger 21, the 5th solution heat exchanger 25, first solution pump 7 and first solution heat exchanger 10, forms single-action-triple effect the 3rd class absorption heat pump.
Single-action-triple effect 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 11, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, the 3rd generator 20 there is the concentrated solution pipeline through first solution pump 7, first solution heat exchanger 10 and absorption-generator 3 have the concentrated solution pipeline to be communicated with branch steam chest 6 through first solution heat exchanger 10 and absorption-generator 3 with dividing steam chest 6 to be communicated with to be adjusted into the 3rd generator 20, absorption-generator 3 is set up the weak solution pipeline and is communicated with the 4th generator 24 through the 3rd solution heat exchanger 21, the 4th generator 24 also has the concentrated solution pipeline through first solution pump 7, the 4th solution heat exchanger 21 and absorption-generator 3 are communicated with dividing steam chest 6, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into the 3rd generator 20 to have the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 in the 3rd generator 20 has the cryogen liquid pipeline to be communicated with first condenser 13 through second choke valve 23 again, and the 4th generator 24 refrigerant vapour passage in addition is communicated with first condenser 13.
2. on the flow process, the weak solution of absorption-generator 3 directly enters first generator 1 respectively, enter the 3rd generator 2 and enter the 4th generator 24 through the 4th solution heat exchanger 21 through first solution heat exchanger 10, the concentrated solution of the first generator 1 absorption-generator 3 of after the 29 throttling step-downs of solution choke valve, flowing through again, the heat absorbing part vaporization enters branch steam chest 6, the concentrated solution of the second generator 2 absorption-generator 3 of after first solution heat exchanger 10 heat absorption step-downs, flowing through again, the concentrated solution that heat absorbing part vaporization enters branch steam chest 6, the four generators 24 absorption-generator 3 of after first solution pump 7 and the 4th solution heat exchanger 21, flowing through again, the heat absorbing part vaporization enters branch steam chest 6; The refrigerant vapour that first generator 1 produces provides to absorption-generator 3 and the 3rd generator 20 respectively, the refrigerant vapour that the 3rd generator 20 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 13, the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enters first condenser 13 through 23 throttlings of second choke valve again, forms single-action-triple effect 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 17, to absorb-generator 3 has the weak solution pipeline directly to be communicated with the 3rd generator 20 through first solution heat exchanger 10 with first generator, 1 connected sum respectively to be adjusted into absorption-generator 3 and to have the weak solution pipeline to distinguish directly to be communicated with first generator 1 through first solution heat exchanger 10 with the 3rd generator 20 connected sums, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest 6 through first solution heat exchanger 10 and absorption-generator 3 through solution choke valve 29 and absorption-generator 3 with dividing steam chest 6 to be communicated with to be adjusted into first generator 1 in first generator 1, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest 6 through solution choke valve 29 and absorption-generator 3 through first solution heat exchanger 10 and absorption-generator 3 with dividing steam chest 6 to be communicated with to be adjusted into the 3rd generator 20 in the 3rd generator 20, cancel the refrigerant vapour passage that first generator 1 is communicated with absorption-generator 3, the 3rd generator 20 is set up the refrigerant vapour passage and is communicated with absorption-generator 3.
2. on the flow process, the weak solution of absorption-generator 3 enters first generator 1 through first solution heat exchanger 10 respectively, directly enter the 3rd generator 2 and enter the 4th generator 24 through the 4th solution heat exchanger 21, absorption-the generator 3 of flowing through again after concentrated solution first solution heat exchanger 10 step-downs of first generator 1 cooling, the heat absorbing part vaporization enters branch steam chest 6, the concentrated solution of the second generator 2 absorption-generator 3 of after the 29 throttling step-downs of solution choke valve, flowing through again, the concentrated solution that heat absorbing part vaporization enters branch steam chest 6, the four generators 24 absorption-generator 3 of after first solution pump 7 and the 4th solution heat exchanger 21, flowing through, the heat absorbing part vaporization enters branch steam chest 6; The refrigerant vapour that first generator 1 produces provides to the 3rd generator 20, the refrigerant vapour that the 3rd generator 20 produces provides to absorption-generator 3 and the 4th generator 24 respectively, the 4th generator 24 discharges and provides refrigerant vapour to first condenser 13, forms 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 12, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, the 3rd generator 20 there is the concentrated solution pipeline through first solution pump 7, first solution heat exchanger 10 and absorption-generator 3 have the concentrated solution pipeline to be communicated with the 4th generator 24 through the 4th solution heat exchanger 21 with dividing steam chest 6 to be communicated with to be adjusted into the 3rd generator 20, the 4th generator 24 also has the concentrated solution pipeline through first solution pump 7, the 4th solution heat exchanger 21, first solution heat exchanger 10 and absorption-generator 3 are communicated with dividing steam chest 6, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into the 3rd generator 20 to have the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 in the 3rd generator 20 has the cryogen liquid pipeline to be communicated with first condenser 13 through second choke valve 23 again, and the 4th generator 24 refrigerant vapour passage in addition is communicated with first condenser 13.
2. on the flow process, the refrigerant vapour that the 3rd generator 20 produces offers the 4th generator 24, the concentrated solution of the 3rd generator 20 enters the 4th generator 24 through the 4th solution heat exchanger 21, refrigerant vapour the 4th generator 24 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 13, the concentrated solution of the 4th generator 24 is through first solution pump 7, absorption-the generator 3 of flowing through again after the 4th solution heat exchanger 21 and first solution heat exchanger 10, the heat absorbing part vaporization enters branch steam chest 6, the refrigerant vapour heat release of the 4th generator 24 of flowing through becomes cryogen liquid, enter first condenser 13 through 23 throttlings of second choke valve 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 19, increase by the 4th solution pump, to absorb-generator 3 has the weak solution pipeline directly to be communicated with first generator 1 to be adjusted into absorption-generator 3 has the weak solution pipeline to be communicated with first generator 1 through the 4th solution pump 22 and first solution heat exchanger 10, the 4th generator 24 there is the concentrated solution pipeline through first solution pump 7, the 4th solution heat exchanger 21, first solution heat exchanger 10 and absorption-generator 3 have the concentrated solution pipeline through first solution pump 7 with dividing steam chest 6 to be communicated with to be adjusted into the 4th generator 24, the 4th solution heat exchanger 21 and absorption-generator 3 are communicated with dividing steam chest 6, have the refrigerant vapour passage to be communicated with absorption-generator 3 to be adjusted into the 3rd generator 20 to set up the refrigerant vapour passage in first generator 1 and are communicated with absorption-generator 3.
2. on the flow process, the weak solution of absorption-generator 3 enters first generator 1 through the 4th solution pump 22 and first solution heat exchanger 10, the refrigerant vapour that the 3rd generator produces provides to absorption-generator 3 and the 4th generator 24 respectively, absorption-generator 3, the heat absorbing part vaporization of flowing through again after first solution pump 7 and the 4th solution heat exchanger 21 of the concentrated solution of the 4th generator 24 enters branch steam chest 6, forms single-action-triple effect the 3rd class absorption heat pump.
Single-action-triple 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 13, increase by the 4th generator, the 4th solution heat exchanger, the 4th solution pump and second choke valve, to absorb-generator 3 has the weak solution pipeline to be communicated with the 3rd generator 20 through first solution heat exchanger 10 to be adjusted into absorption-generator 3 and to have the weak solution pipeline to be communicated with the 4th generator 24 through first solution heat exchanger 10 and the 4th solution heat exchanger 21, the 4th generator 24 also has the concentrated solution pipeline to be communicated with the 3rd generator 20 through the 4th solution pump 22 and the 4th solution heat exchanger 21, having the refrigerant vapour passage to be communicated with first condenser 13 to be adjusted into the 3rd generator 20 to have the refrigerant vapour passage to be communicated with back the 4th generator 24 with the 4th generator 24 in the 3rd generator 20 has the cryogen liquid pipeline to be communicated with first condenser 13 through second choke valve 23 again, and the 4th generator 24 refrigerant vapour passage in addition is communicated with first condenser 13.
2. on the flow process, the refrigerant vapour that the 3rd generator 20 produces offers the 4th generator 24, the weak solution of absorption-generator 3 enters the 4th generator 24 through first solution heat exchanger 10 and the 4th solution heat exchanger 21, refrigerant vapour the 4th generator 24 of flowing through, heating enters its interior solution release and provides refrigerant vapour to first condenser 13, the concentrated solution of the 4th generator 24 enters the 3rd generator 20 through the 4th solution pump 22 and the 4th solution heat exchanger 21, refrigerant vapour heat release through the 4th generator 24 becomes cryogen liquid, enter first condenser 13 through 23 throttlings of second choke valve 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 22 is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 21, cancellation solution choke valve, to absorb-generator 3 has the weak solution pipeline to be communicated with the 4th generator 24 through first solution heat exchanger 10 and the 4th solution heat exchanger 21 to be adjusted into the weak solution pipeline and to be communicated with the 4th generator 24 through the 4th solution heat exchanger 21, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest 6 through first solution heat exchanger 10 and absorption-generator 3 through solution choke valve 29 and absorption-generator 3 with dividing steam chest 6 to be communicated with to be adjusted into first generator 1 in first generator 1, cancel the refrigerant vapour passage that first generator 11 is communicated with absorption-generator 3, the 3rd generator 20 is set up the refrigerant vapour passage and is communicated with absorption-generator 3.
2. on the flow process, the weak solution of absorption-generator 3 enters the 4th generator 24 through the 4th solution heat exchanger 21, the concentrated solution of the 4th generator 24 enters the 3rd generator 20 through the 4th solution pump 22 and the 4th solution heat exchanger 21, flow through again after first solution heat exchanger 10 absorption-generator 3, heat absorbing part vaporization of the concentrated solution that the concentrated solution of the 3rd generator 20 enters first generator, 1, the first generator 1 through first solution pump 7 and first solution heat exchanger 10 enters branch steam chest 6; The refrigerant vapour that the 3rd generator 20 produces offers absorption-generator 3 and the 4th generator 24 respectively, forms single-action-triple effect the 3rd class absorption heat pump.
Single-action shown in Figure 23-1.5 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 4, cancel second evaporimeter 18, keep the second cryogen liquid pump 17, evaporimeter 15 is set up the refrigerant vapour passage and is communicated with absorption-generator 3; Increase absorption-evaporimeter again, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 1 through first solution heat exchanger 10 to be adjusted into absorption-generator 3 and to have the weak solution pipeline to be communicated with absorption-evaporimeter 27, absorption-evaporimeter 27 also has the weak solution pipeline to be communicated with first generator 1 through the 4th solution heat exchanger 21, evaporimeter 15 had the refrigerant vapour passage to be communicated with first absorber 4 to be adjusted into evaporimeter 15 has the refrigerant vapour passage to be communicated with absorption-evaporimeter 27, and condenser 13 is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with first absorber 4 through the second cryogen liquid pump 17 with absorption-evaporimeter 27 after absorption-evaporimeter 27 is communicated with again.
2. on the flow process, the weak solution of absorption-generator 3 enters absorption-evaporimeter 27, the refrigerant vapour that absorbs flash-pot 15 and heat release in the cryogen liquid of the absorption-evaporimeter 27 of flowing through, and the weak solution of absorption-evaporimeter 27 enters first generator 1 through the 4th solution heat exchanger 21; The cryogen liquid of condenser 13 is divided into two-way---and the first via enters evaporimeter 15, absorbs waste heat and become refrigerant vapour and provide to absorption-evaporimeter 27 and absorption-generator 3 respectively through the first cryogen liquid pump 16, the second the tunnel after the pressurization of the second cryogen liquid pump 17, flow through absorptions-evaporimeter 27, absorb heat into refrigerant vapour and formation single-action-1.5 grade the 3rd class absorption heat pump be provided to first absorber 4.
Single-action shown in Figure 24-1.5 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 4, increase choke valve, the 4th solution heat exchanger and absorption-evaporimeter, having the weak solution pipeline to be communicated with absorption-generator 3 through second solution heat exchanger 11 second absorber 5 is adjusted into second absorber 5 and has the weak solution pipeline to be communicated with absorption-evaporimeter 27 through second solution heat exchanger 11, absorption-evaporimeter 27 also has the weak solution pipeline to be communicated with absorption-generator 3 through the 4th solution heat exchanger 21, to divide steam chest 6 to have the concentrated solution pipeline to be communicated with second generator 2 through second solution pump 8 and second solution heat exchanger 11 is adjusted into branch steam chest 6 and the concentrated solution pipeline is arranged through second solution pump 8, the 4th solution heat exchanger 21 and second solution heat exchanger 11 are communicated with second generator 2, first evaporimeter 15 had the refrigerant vapour passage to be communicated with first absorber 4 to be adjusted into first evaporimeter 15 has the refrigerant vapour passage to be communicated with absorption-evaporimeter 27, first evaporimeter 15 is set up the cryogen liquid pipeline and is communicated with second evaporimeter 18 through choke valve 19, has the cryogen liquid pipeline to be communicated with second evaporimeter 18 through the second cryogen liquid pump 17 condenser 13 and is adjusted into condenser 13 and has the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with first absorber 4 through the second cryogen liquid pump 17 again with absorption-evaporimeter 27 after absorption-evaporimeter 27 is communicated with.
2. on the flow process, the weak solution of second absorber 5 enters absorption-evaporimeter 27, absorbs from the refrigerant vapour of first evaporimeter 15 and heat release in the cryogen liquid of the absorption-evaporimeter 27 of flowing through through second solution heat exchanger 11, the weak solution of absorption-evaporimeter 27 enters absorption-generator 3 through the 4th solution heat exchanger 21, divides the concentrated solution of steam chest 6 to enter second generator 2 through second solution pump 8, the 4th solution heat exchanger 21 and second solution heat exchanger 11; The cryogen liquid of condenser 13 is divided into two-way---the first via through the first cryogen liquid pump 16 enter first evaporimeter 15, the second tunnel after the pressurization of the second cryogen liquid pump 17, flow through absorption-evaporimeter 27, absorb heat into refrigerant vapour and provide to first absorber 4; The cryogen liquid of first evaporimeter 15 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to absorption-evaporimeter 27, the second the tunnel enters second evaporimeter 18, absorbs waste heat and become refrigerant vapour and formation single-action-1.5 grade the 3rd class absorption heat pump is provided to absorptions-generator 3 through choke valve 19.
Single-action shown in Figure 25-1.5 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 6, increase absorption-evaporimeter, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 1 through first solution heat exchanger 10 to be adjusted into absorption-generator 3 and to have the weak solution pipeline to be communicated with absorption-evaporimeter 27, absorption-evaporimeter 27 also has the weak solution pipeline to be communicated with first generator 1 through first solution heat exchanger 10, evaporimeter 15 had the refrigerant vapour passage to be communicated with first absorber 4 to be adjusted into evaporimeter 15 has the refrigerant vapour passage to be communicated with absorption-evaporimeter 27, has the cryogen liquid pipeline to be communicated with evaporimeter 15 through the second cryogen liquid pump 17 second condenser 14 and is adjusted into second condenser 14 and has the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with first absorber 4 through the second cryogen liquid pump 17 again with absorption-evaporimeter 27 after absorption-evaporimeter 27 is communicated with.
2. on the flow process, the weak solution of absorption-generator 3 enters absorption-evaporimeter 27, the refrigerant vapour that absorbs flash-pot 15 and heat release in the cryogen liquid of the absorption-evaporimeter 27 of flowing through, and the weak solution of absorption-evaporimeter 27 enters first generator 1 through first solution heat exchanger 10; The cryogen liquid of first condenser 13 pressurizes through the first cryogen liquid pump 16 and enters evaporimeter 15, the absorption waste heat becomes refrigerant vapour also to provide to absorption-evaporimeter 27 and absorption-generator 23 respectively, the cryogen liquid of second condenser 14 after the pressurization of the second cryogen liquid pump 17, flow through absorptions-evaporimeter 27, absorb heat into refrigerant vapour and formation single-action-1.5 grade the 3rd class absorption heat pump be provided to first absorber 4.
Single-action shown in Figure 26-1.5 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 5, increase absorption-evaporimeter, the 4th solution heat exchanger and the 3rd cryogen liquid pump, there is the weak solution pipeline to have the weak solution pipeline to be communicated with absorption-evaporimeter 27 through second solution heat exchanger 11 through second solution heat exchanger 11 and absorption-generator 3 with dividing steam chest 6 to be communicated with to be adjusted into second absorber 5 second absorber 5, absorption-evaporimeter 27 also has the weak solution pipeline to be communicated with dividing steam chest 6 through the 4th solution heat exchanger 21 and absorption-generator 3, to divide steam chest 6 to have the concentrated solution pipeline to be communicated with second generator 2 through second solution pump 8 and second solution heat exchanger 11 is adjusted into branch steam chest 6 and the concentrated solution pipeline is arranged through second solution pump 8, the 4th solution heat exchanger 21 and second solution heat exchanger 11 are communicated with second generator 2, first evaporimeter 15 had the refrigerant vapour passage to be communicated with first absorber 4 to be adjusted into first evaporimeter 15 has the refrigerant vapour passage to be communicated with absorption-evaporimeter 27, and second condenser 14 is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with first absorber 4 through the 3rd cryogen liquid pump 28 with absorption-evaporimeter 27 after absorption-evaporimeter 27 is communicated with again.
2. on the flow process, the weak solution of second absorber 5 enters absorption-evaporimeter 27, absorbs from the refrigerant vapour of first evaporimeter 15 and heat release in the cryogen liquid of the absorption-evaporimeter 27 of flowing through through second solution heat exchanger 11, absorption-generator 3, the heat absorbing part vaporization of flowing through again after the 4th solution heat exchanger 21 of the weak solution of absorption-evaporimeter 27 enters branch steam chest 6, divides the concentrated solution of steam chest 6 to enter second generator 2 through second solution pump 8, the 4th solution heat exchanger 21 and second solution heat exchanger 11; The cryogen liquid of second condenser 14 is divided into two-way---and the first via enters first evaporimeter 15, absorbs waste heat and become refrigerant vapour and provide to absorption-evaporimeter 27 through the second cryogen liquid pump 17, the second the tunnel after the pressurization of the 3rd cryogen liquid pump 28, flow through absorptions-evaporimeter 27, absorb heat into refrigerant vapour and formation single-action-1.5 grade the 3rd class absorption heat pump be provided to first absorber 4.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 27 with economic benefits and social benefits is 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, second solution heat exchanger 11 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 first absorber 4 through newly-increased solution heat exchanger B, having the refrigerant vapour passage to be communicated with second absorber 5 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 evaporimeter 15 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second absorber 5.
2. on the flow process, divide the concentrated solution of steam chest 6 after second solution pump 8 and second solution heat exchanger 11, to be divided into two-way---the first via directly enters second generator 2, the second tunnel 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 absorber 5, the concentrated solution of newly-increased generator A enters first absorber 4 through newly-increased solution heat exchanger B, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enters evaporimeter 15 through newly-increased choke valve C throttling again, and forming with economic benefits and social benefits is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 28 with economic benefits and social benefits is 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 be communicated with second generator 2 to be adjusted into second solution heat exchanger 11 to have the concentrated solution pipeline to be communicated with second generator 2 through newly-increased solution heat exchanger B second solution heat exchanger 11, having the concentrated solution pipeline to be communicated with first absorber 4 through the 3rd solution heat exchanger 12 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased solution heat exchanger B, newly-increased generator A has the concentrated solution pipeline to be communicated with first absorber 4 through the 3rd solution heat exchanger 12 again, having the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into second generator 2 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second absorber 5.
2. on the flow process, divide the concentrated solution of steam chest 6 through second solution pump 8, second solution heat exchanger 11 and newly-increased solution heat exchanger B enter second generator 2, the refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, the concentrated solution of second generator 2 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 absorber 5, the concentrated solution of newly-increased generator A enters first absorber 4 through the 3rd solution heat exchanger 12, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enter first evaporimeter 15 through newly-increased choke valve C throttling again, forming with economic benefits and social benefits is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 29 with economic benefits and social benefits is 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 pump, second solution heat exchanger 11 had the concentrated solution pipeline to be communicated with second generator 2 to be adjusted into second solution heat exchanger 11 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 newly-increased solution pump D and newly-increased solution heat exchanger B, having the concentrated solution pipeline to be communicated with first absorber 4 through the 3rd solution heat exchanger 12 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with first absorber 4 through newly-increased solution heat exchanger B and the 3rd solution heat exchanger 12, having the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into second generator 2 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through newly-increased choke valve C again, increases generator A newly and also have the refrigerant vapour passage to be communicated with second absorber 5.
2. on the flow process, the refrigerant vapour that second generator 2 produces offers newly-increased generator A and makes to drive thermal medium, divide the concentrated solution of steam chest 6 to enter newly-increased generator A through second solution pump 8 and second solution heat exchanger 11, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to second absorber 5, newly-increased generator A concentrated solution enters second generator 2 through newly-increased solution pump D and newly-increased solution heat exchanger B, the concentrated solution of second generator 2 enters first absorber 4 through newly-increased solution heat exchanger B and the 3rd solution heat exchanger 12, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enter first evaporimeter 15 through newly-increased choke valve C throttling again, forming with economic benefits and social benefits is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 30 with the triple effect is is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 5, increase newly-increased first generator, newly-increased second generator, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first throttle valve and newly-increased second choke valve, second solution heat exchanger 11 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 with the newly-increased first generator A connected sum through the newly-increased first solution heat exchanger B respectively, the newly-increased first generator A also has the concentrated solution pipeline to be communicated with first absorber 4 through the newly-increased first solution heat exchanger B, the newly-increased second generator E also has the concentrated solution pipeline to be communicated with first absorber 4 through the newly-increased second solution heat exchanger F, having the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into second generator 2 to have the refrigerant vapour passage to be communicated with the newly-increased first generator A in back with the newly-increased first generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through newly-increased first throttle valve C again, the newly-increased first generator A also has the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through the newly-increased second choke valve G again, and the newly-increased second generator E also has the refrigerant vapour passage to be communicated with second absorber 5.
2. on the flow process, divide the concentrated solution of steam chest 6 after second solution pump 8 and second solution heat exchanger 11, to be divided into three the tunnel---the first via directly enters second generator 2, the newly-increased first solution heat exchanger B of the second road warp enters the newly-increased first generator A, and Third Road enters through the newly-increased second solution heat exchanger F and increases the second generator E newly; The refrigerant vapour that second generator 2 produces offers the newly-increased first generator A and makes to drive thermal medium, refrigerant vapour is flowed through and is increased the first generator A newly, heating enters its interior solution release and provides refrigerant vapour to the newly-increased second generator E, the concentrated solution of the newly-increased first generator A enters first absorber 4 through the newly-increased first solution heat exchanger B, and the refrigerant vapour heat release of the newly-increased first generator A that flows through becomes cryogen liquid, enters first evaporimeter 15 through newly-increased first throttle valve C throttling again; Enter solution in it and discharge and provide refrigerant vapour to second absorber 5 from the flow through newly-increased second generator E, heating of the refrigerant vapour of the newly-increased first generator A, the concentrated solution of the newly-increased second generator E enters first absorber 4 through 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, enters first evaporimeter 15 through the newly-increased second choke valve G throttling again, and forming with the triple effect is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 31 with the triple effect is is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 5, increase newly-increased first generator, newly-increased second generator, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first throttle valve and newly-increased second choke valve, there is the concentrated solution pipeline to be communicated with second generator 2 to be adjusted into second solution heat exchanger 11 to have the concentrated solution pipeline to be communicated with second generator 2 through the newly-increased second solution heat exchanger F and the newly-increased first solution heat exchanger B second solution heat exchanger 11, having the concentrated solution pipeline to be communicated with first absorber 4 through the 3rd solution heat exchanger 12 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with the newly-increased first generator A through the newly-increased first solution heat exchanger B, the newly-increased first generator A also has the concentrated solution pipeline to be 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 first absorber 4 through the 3rd solution heat exchanger 12, having the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into second generator 2 to have the refrigerant vapour passage to be communicated with the newly-increased first generator A in back with the newly-increased first generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through newly-increased first throttle valve C again, the newly-increased first generator A also has the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through the newly-increased second choke valve G again, and the newly-increased second generator E also has the refrigerant vapour passage to be communicated with second absorber 5.
2. on the flow process, divide the concentrated solution of steam chest 6 through second solution pump 8, second solution heat exchanger 11, 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 second generator 2 produces offers the newly-increased first generator A and makes to drive thermal medium, the concentrated solution of second generator 2 enters the newly-increased first generator A through the newly-increased first solution heat exchanger B, refrigerant vapour is flowed through and is increased the first generator A newly, heating enters its interior solution release and provides refrigerant vapour to the newly-increased second generator E, 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, and the refrigerant vapour heat release of the newly-increased first generator A that flows through becomes cryogen liquid, enter first evaporimeter 15 through newly-increased first throttle valve C throttling again; Enter solution in it and discharge and provide refrigerant vapour to second absorber 5 from the flow through newly-increased second generator E, heating of the refrigerant vapour of the newly-increased first generator A, the concentrated solution of the newly-increased second generator E enters first absorber 4 through the 3rd solution heat exchanger 12, the refrigerant vapour heat release that increases the second generator E newly of flowing through becomes cryogen liquid, enters first evaporimeter 15 through the newly-increased second choke valve G throttling again, and forming with the triple effect is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 32 with the triple effect is is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 5, increase newly-increased first generator, newly-increased second generator, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution pump and newly-increased second solution pump, second solution heat exchanger 11 had the concentrated solution pipeline to be communicated with second generator 2 to be adjusted into second solution heat exchanger 11 has the concentrated solution pipeline 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 the newly-increased first generator A through the newly-increased second solution pump H and the newly-increased second solution heat exchanger F, the newly-increased first generator A also has the concentrated solution pipeline to be communicated with second generator 2 through the newly-increased first solution pump D and the newly-increased first solution heat exchanger B, having the concentrated solution pipeline to be communicated with first absorber 4 through the 3rd solution heat exchanger 12 in second generator 2 is adjusted into second generator 2 and the concentrated solution pipeline is arranged through the newly-increased first solution heat exchanger B, the newly-increased second solution heat exchanger F and the 3rd solution heat exchanger 12 are communicated with first absorber 4, having the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into second generator 2 to have the refrigerant vapour passage to be communicated with the newly-increased first generator A in back with the newly-increased first generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through newly-increased first throttle valve C again, the newly-increased first generator A also has the refrigerant vapour passage to be communicated with the newly-increased second generator E in back with the newly-increased second generator E has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through the newly-increased second choke valve G again, and the newly-increased second generator E also has the refrigerant vapour passage to be communicated with second absorber 5.
2. on the flow process, the refrigerant vapour that second generator 2 produces offers the newly-increased first generator A and makes to drive thermal medium, and the refrigerant vapour that the newly-increased first generator A produces offers the newly-increased second generator E and makes to drive thermal medium; Divide the concentrated solution of steam chest 6 to enter the newly-increased second generator E through second solution pump 8 and second solution heat exchanger 11, 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 absorber 5, 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, and the refrigerant vapour heat release of the newly-increased second generator E that flows through becomes cryogen liquid, enters first evaporimeter 15 through the newly-increased second choke valve G throttling again; Refrigerant vapour is flowed through and is increased the first generator A newly, heating enters its interior solution release and provides refrigerant vapour to the newly-increased second generator E, the newly-increased first generator A concentrated solution enters second generator 2 through the newly-increased first solution pump D and the newly-increased first solution heat exchanger B, the refrigerant vapour heat release that increases the first generator A newly of flowing through becomes cryogen liquid, enter first evaporimeter 15 through newly-increased first throttle valve C throttling again, the concentrated solution of second generator 2 is through the newly-increased first solution heat exchanger B, the newly-increased second solution heat exchanger F and the 3rd solution heat exchanger 12 enter first absorber 4, and forming with the triple effect is the 3rd class absorption heat pump of high temperature generation flow process.
Shown in Figure 33 is that the 3rd class absorption heat pump of high temperature generation flow process is achieved in that with the back-heating type single-action
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 solution pump and newly-increased absorber, second solution heat exchanger 11 had the concentrated solution pipeline to be communicated with second generator 2 to be adjusted into second solution heat exchanger 11 has the concentrated solution pipeline to be communicated with newly-increased absorber I, newly-increased absorber I also has the weak 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 first absorber 4 through the 3rd solution heat exchanger 12 in second generator 2 is adjusted into second generator 2 and has the concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased solution heat exchanger B, newly-increased generator A also has the concentrated solution pipeline to be communicated with first absorber 4 through the 3rd solution heat exchanger 12, newly-increased generator A also has the thermal medium of driving pipeline respectively with external communications and has the refrigerant vapour passage to be communicated with newly-increased absorber I, and newly-increased absorber I also has heated medium pipeline and external communications.
2. on the flow process, divide the concentrated solution of steam chest 6 to enter newly-increased absorber I through second solution pump 8 and second solution heat exchanger 11, absorption from the refrigerant vapour of newly-increased generator A and heat release in heated medium, the weak solution of newly-increased absorber I enters second generator 2 through newly-increased solution pump D and newly-increased solution heat exchanger B, the refrigerant vapour that second generator 2 produces enters second absorber 5, the concentrated solution of second generator 2 enters newly-increased generator A through newly-increased solution heat exchanger B, drive heat medium flow through newly-increased generator A, heating enters its interior solution release and provides refrigerant vapour to newly-increased absorber I, the concentrated solution of newly-increased generator A enters first absorber 4 through the 3rd solution heat exchanger 12, and forming with the back-heating type single-action is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 34 with the backheating type double-effect is is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 33, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased choke valve, newly-increased solution pump D sets up the weak 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 the newly-increased first generator A through the newly-increased second solution heat exchanger F, having the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into second generator 2 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 in second generator 2 has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through newly-increased choke valve C again, increases the second generator E newly and also have the refrigerant vapour passage to be communicated with second absorber 5.
2. on the flow process, the refrigerant vapour that second generator 2 produces is given provides the newly-increased second generator E to make to drive thermal medium, the part weak solution of newly-increased absorber I enters the newly-increased second generator E through newly-increased solution pump D and 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 absorber 5, the concentrated solution of the newly-increased second generator E enters the newly-increased first generator A through 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 first evaporimeter 15 through newly-increased choke valve C again, forming with the backheating type double-effect is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 35 with the backheating type double-effect is is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 33, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased choke valve, to increase absorber I newly has the weak solution pipeline to be communicated with second generator 2 through newly-increased solution pump D and the newly-increased first solution heat exchanger B to be adjusted into newly-increased absorber I and to have weak solution pipeline warp to increase solution pump D newly, the newly-increased second solution heat exchanger F and the newly-increased first solution heat exchanger B are communicated with second generator 2, having the concentrated solution pipeline to be communicated with the newly-increased first generator A through the newly-increased first solution heat exchanger B in second generator 2 is adjusted into second generator 2 and has 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 the newly-increased first generator A through the newly-increased second solution heat exchanger F, having the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into second generator 2 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 in second generator 2 has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through newly-increased choke valve C again, increases the second generator E newly and also have the refrigerant vapour passage to be communicated with second absorber 5.
2. on the flow process, the weak solution of newly-increased absorber I 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 second generator 2, the refrigerant vapour that second generator 2 produces offers the newly-increased second generator E and makes to drive thermal medium, the concentrated solution of second generator 2 enters the newly-increased second generator E through the newly-increased first solution heat exchanger B, 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 absorber 5, the concentrated solution of the newly-increased second generator E enters the newly-increased first generator A through 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 first evaporimeter 15 through newly-increased choke valve C again, forming with the backheating type double-effect is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 36 with the backheating type double-effect is is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 33, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased choke valve and newly-increased second solution pump, to increase newly absorber I have the weak solution pipeline through the newly-increased first solution pump D and the newly-increased first solution heat exchanger B is communicated with second generator 2 be adjusted into newly-increased absorber I have the weak solution pipeline through the newly-increased first solution pump D with increase the first solution heat exchanger B newly and 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 second generator 2 through the newly-increased second solution pump H and the newly-increased second solution heat exchanger F, having the concentrated solution pipeline to be communicated with the newly-increased first generator A through the newly-increased first solution heat exchanger B in second generator 2 is adjusted into second generator 2 and the concentrated solution pipeline is arranged through increasing the second solution heat exchanger F newly and increasing the first solution heat exchanger B newly and be communicated with the newly-increased first generator A, having the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into second generator 2 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 in second generator 2 has the cryogen liquid pipeline to be communicated with first evaporimeter 15 through newly-increased choke valve C again, increases the second generator E newly and also have the refrigerant vapour passage to be communicated with second absorber 5; The driving thermal medium pipeline of the newly-increased first generator A of cancellation and external communications, increase newly-increased second choke valve, second generator 2 is set up the refrigerant vapour passage and is communicated with the back with the newly-increased first generator A and increases the first generator A newly and have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with evaporimeter 15.
2. on the flow process, the refrigerant vapour that second generator 2 produces offers the newly-increased first generator A respectively and the newly-increased second generator E makes to drive thermal medium, the weak solution of newly-increased absorber I enters the newly-increased second generator E through the newly-increased first solution pump D and the newly-increased first solution heat exchanger B, 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 absorber 5, the concentrated solution of the newly-increased second generator E enters second generator 2 through the newly-increased second solution pump H and the newly-increased second solution heat exchanger F, and the refrigerant vapour heat release of the newly-increased second generator E that flows through becomes cryogen liquid, enter first evaporimeter 15 through newly-increased first throttle valve C again; The concentrated solution of first generator 1 enters the newly-increased first generator A through the newly-increased second solution heat exchanger F and the newly-increased first solution heat exchanger B, refrigerant vapour is flowed through and is increased the first generator A newly, heating enters its interior solution release and provides refrigerant vapour to newly-increased absorber I, the refrigerant vapour heat release that increases the first generator A newly of flowing through becomes cryogen liquid, enters first evaporimeter 15 through the newly-increased second choke valve G throttling again, and forming with the backheating type double-effect is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 37 with the back-heating type triple-effect is is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 34, increase newly-increased the 3rd generator, newly-increased the 3rd solution heat exchanger and newly-increased second choke valve, newly-increased solution pump D sets up the weak solution pipeline and is communicated with newly-increased the 3rd generator J through newly-increased the 3rd solution heat exchanger L, newly-increased the 3rd generator J also has the concentrated solution pipeline to be communicated with the newly-increased first generator A through newly-increased the 3rd solution heat exchanger L, to increase the second generator E newly has the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into the newly-increased second generator E to have the refrigerant vapour passage to be communicated with newly-increased the 3rd generator J in back with newly-increased the 3rd generator J to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with first evaporimeter 15, to increase the 3rd generator J newly and also have the refrigerant vapour passage to be communicated with second absorber 5.
2. on the flow process, the refrigerant vapour that the newly-increased second generator E produces offers newly-increased the 3rd generator J and makes to drive thermal medium, the part weak solution of newly-increased absorber I enters newly-increased the 3rd generator J through newly-increased solution pump D and newly-increased the 3rd solution heat exchanger L, refrigerant vapour is flowed through and is increased the 3rd generator J newly, heating enters its interior solution release and provides refrigerant vapour to second absorber 5, the concentrated solution of newly-increased the 3rd generator J enters the newly-increased first generator A through newly-increased the 3rd solution heat exchanger L, the refrigerant vapour heat release that increases the 3rd generator J newly of flowing through becomes cryogen liquid, enter first evaporimeter 15 through the newly-increased second choke valve G throttling again, forming with the back-heating type triple-effect is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 38 with the back-heating type triple-effect is is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 35, increase newly-increased the 3rd generator, newly-increased the 3rd solution heat exchanger and newly-increased second choke valve, to increase absorber I newly and the weak solution pipeline be arranged 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 second generator 2 and are adjusted into newly-increased absorber I and have weak solution pipeline warp to increase solution pump D newly, newly-increased the 3rd solution heat exchanger L, the newly-increased second solution heat exchanger F and the newly-increased first solution heat exchanger B are communicated with second generator 2, to increase the second generator E newly has the concentrated solution pipeline to be communicated with the newly-increased first generator A to be adjusted into through the newly-increased second solution heat exchanger F to increase the second generator E newly and have concentrated solution pipeline warp to increase the second solution heat exchanger F newly to be communicated with newly-increased the 3rd generator J, newly-increased the 3rd generator J also has the concentrated solution pipeline to be communicated with the newly-increased first generator A through newly-increased the 3rd solution heat exchanger L, to increase the second generator E newly has the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into the newly-increased second generator E to have the refrigerant vapour passage to be communicated with newly-increased the 3rd generator J in back with newly-increased the 3rd generator J to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with first evaporimeter 15, to increase the 3rd generator J newly and also have the refrigerant vapour passage to be communicated with second absorber 5; Increase newly-increased the 3rd choke valve again, increasing the first generator A after the driving thermal medium pipeline of the newly-increased first generator A of cancellation and external communications, the newly-increased second generator E are set up the refrigerant vapour passage and be communicated with the newly-increased first generator A newly has cryogen liquid pipeline warp to increase the 3rd choke valve K newly to be communicated with first evaporimeter 15 again.
2. on the flow process, the weak solution of newly-increased absorber I is through newly-increased solution pump D, newly-increased the 3rd solution heat exchanger L, the newly-increased second solution heat exchanger F and the newly-increased first solution heat exchanger B enter second generator 2, the concentrated solution of second generator 2 enters the newly-increased second generator E through the newly-increased first solution heat exchanger B, refrigerant vapour is flowed through and is increased the second generator E newly, heating enters the solution release in it and provides refrigerant vapour to drive thermal medium as it to the newly-increased first generator A and newly-increased the 3rd generator J respectively, the concentrated solution of the newly-increased second generator E enters newly-increased the 3rd generator J through the newly-increased second solution heat exchanger F, refrigerant vapour is flowed through and is increased the 3rd generator J newly, heating enters its interior solution release and provides refrigerant vapour to second absorber 5, the concentrated solution of newly-increased the 3rd generator J enters the newly-increased first generator A through newly-increased the 3rd solution heat exchanger L, and the refrigerant vapour heat release of newly-increased the 3rd generator J that flows through becomes cryogen liquid, enter first evaporimeter 15 through the newly-increased second choke valve G throttling again; Refrigerant vapour is flowed through and is increased the first generator A newly, heating enters its interior solution release and provides refrigerant vapour to newly-increased absorber I, the refrigerant vapour heat release that increases the first generator A newly of flowing through becomes cryogen liquid, enters first evaporimeter 15 through newly-increased the 3rd choke valve K throttling again, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of high temperature generation flow process.
The 3rd class absorption heat pump of high temperature generation flow process that shown in Figure 39 with the back-heating type triple-effect is is achieved in that
1. on the structure, in the 3rd class absorption heat pump shown in Figure 36, to increase the second choke valve G newly and change to the 3rd choke valve K, increase newly-increased the 3rd generator, newly-increased the 3rd solution heat exchanger, newly-increased second choke valve and newly-increased the 3rd solution pump, to increase absorber I newly has the weak solution pipeline to be communicated with the newly-increased second generator E through the newly-increased first solution pump D and the newly-increased first solution heat exchanger B to be adjusted into newly-increased absorber I and the weak solution pipeline to be arranged through increasing the first solution pump D newly and increasing the first solution heat exchanger B newly and be communicated with newly-increased the 3rd generator J, newly-increased the 3rd generator J also has the concentrated solution pipeline to be communicated with the newly-increased second generator E through newly-increased the 3rd solution pump M and newly-increased the 3rd solution heat exchanger L, having the concentrated solution pipeline to be communicated with the newly-increased first generator A through the newly-increased second solution heat exchanger F and the newly-increased first solution heat exchanger B in second generator 2 is adjusted into second generator 2 and has concentrated solution pipeline warp to increase the second solution heat exchanger F newly, newly-increased the 3rd solution heat exchanger L and the newly-increased first solution heat exchanger B are communicated with the newly-increased first generator A, to increase the second generator E newly has the refrigerant vapour passage to be communicated with second absorber 5 to be adjusted into the newly-increased second generator E to have the refrigerant vapour passage to be communicated with newly-increased the 3rd generator J in back with newly-increased the 3rd generator J to have cryogen liquid pipeline warp to increase the second choke valve G newly again to be communicated with first evaporimeter 15, to increase the 3rd generator J newly and also have the refrigerant vapour passage to be communicated with second absorber 5; Having the refrigerant vapour passage to be communicated with the newly-increased first generator A in back with the newly-increased first generator A in second generator 2 has the cryogen liquid pipeline to be communicated with first evaporimeter 15 to be adjusted into through newly-increased the 3rd choke valve K to increase the first generator A after the newly-increased second generator E sets up the refrigerant vapour passage and the newly-increased first generator A is communicated with newly and have cryogen liquid pipeline warp to increase the 3rd choke valve K newly again to be communicated with first evaporimeter 15 again.
2. on the flow process, the refrigerant vapour that the newly-increased second generator E produces offers the newly-increased first generator A respectively and newly-increased the 3rd generator J makes to drive thermal medium, the weak solution of newly-increased absorber I enters newly-increased the 3rd generator J through the newly-increased first solution pump D and the newly-increased first solution heat exchanger B, refrigerant vapour is flowed through and is increased the 3rd generator J newly, heating enters its interior solution release and provides refrigerant vapour to second absorber 5, the concentrated solution of newly-increased the 3rd generator J enters the newly-increased second generator E through newly-increased the 3rd solution pump M and newly-increased the 3rd solution heat exchanger L, and the refrigerant vapour heat release of newly-increased the 3rd generator J that flows through becomes cryogen liquid, enter first evaporimeter 15 through the newly-increased second choke valve G throttling again; The concentrated solution of second generator 2 enters the newly-increased first generator A through the newly-increased second solution heat exchanger F, newly-increased the 3rd solution heat exchanger L and the newly-increased first solution heat exchanger B, refrigerant vapour is flowed through and is increased the first generator A newly, heating enters its interior solution release and provides refrigerant vapour to newly-increased absorber I, the refrigerant vapour heat release that increases the first generator A newly of flowing through becomes cryogen liquid, enters first evaporimeter 15 through newly-increased the 3rd choke valve K throttling again, and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of high temperature generation flow process.
The effect that the technology of the present invention can realize---three generation-three absorption systems and the 3rd class absorption heat pumps proposed by the invention have following effect and advantage:
1. three generations-three absorption systems that propose, structure and flow process advantages of simple have high temperature driven solution generating process and drive the solution generating process with the low temperature that has the backheat flow process, are that the generation of the 3rd class absorption heat pump provides the foundation.
2. series the 3rd class absorption heat pump of Ti Chuing, the backheat amplitude can be regulated, and can realize taking full advantage of waste heat and high temperature driven heat.
3. the 3rd class absorption heat pump of Ti Chuing has the high and high two-fold advantage of the second class absorption heat pump performance index of first kind absorption heat pump heat supply temperature.
4. the 3rd class absorption heat pump of Ti Chuing, its first absorber is the second class absorption heat pump flow process heat supply end, is conducive to take full advantage of the temperature difference between waste heat and the cooling medium, improves the residual heat resources utilization rate.
5. series the 3rd class absorption heat pump of Ti Chuing has further enriched the diversity of absorption heat pump kind, can realize the mutual coupling between heat pump heat supply and the user's heat better.
Residual heat resources than horn of plenty, especially exist based on latent heat enrich residual heat resources the time, utilize the 3rd class absorption heat pump of the present invention, 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 (53)

1. three-three absorption systems take place, and it mainly is made up of first generator, second generator, absorption-generator, first absorber, second absorber, branch steam chest, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; First generator (1) has the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (6), divide steam chest (6) to also have the concentrated solution pipeline to be communicated with second generator (2) through second solution pump (8) and second solution heat exchanger (11), second generator (2) also has the concentrated solution pipeline to be communicated with first absorber (4) through the 3rd solution heat exchanger (12), first absorber (4) also has the weak solution pipeline to be communicated with second absorber (5) through the 3rd solution pump (9) and the 3rd solution heat exchanger (12), second absorber (5) also has the weak solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (11), absorption-generator (3) also has the weak solution pipeline to be communicated with first generator (1) through first solution heat exchanger (10), first generator (1) also have surplus heat respectively medium pipeline and external communications and refrigerant vapour passage and external communications arranged, second generator (2) also has the thermal medium of driving pipeline respectively with external communications and has the refrigerant vapour passage to be communicated with second absorber (5), absorption-generator (3) also has refrigerant vapour passage and external communications, first absorber (4) also has heated medium pipeline and external communications respectively and refrigerant vapour passage and external communications is arranged, absorption-generator (3) and second absorber (5) also have heated medium pipeline and external communications respectively, divide steam chest (6) to also have refrigerant vapour passage and external communications, form three-three absorption systems take place.
2. three-three absorption systems take place, and it mainly is made up of first generator, second generator, absorption-generator, first absorber, second absorber, branch steam chest, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; First generator (1) has the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (6), divide steam chest (6) to also have the concentrated solution pipeline to be communicated with second generator (2) through second solution pump (8) and second solution heat exchanger (11), second generator (2) also has the concentrated solution pipeline to be communicated with first absorber (4) through the 3rd solution heat exchanger (12), first absorber (4) also has the weak solution pipeline to be communicated with second absorber (5) through the 3rd solution pump (9) and the 3rd solution heat exchanger (12), second absorber (5) also has the weak solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (11), absorption-generator (3) also has the weak solution pipeline to be communicated with first generator (1) through first solution heat exchanger (10), first generator (1) also have surplus heat respectively medium pipeline and external communications and refrigerant vapour passage and external communications arranged, second generator (2) also has the thermal medium of driving pipeline respectively with external communications and has the refrigerant vapour passage to be communicated with second absorber (5), absorption-generator (3) also has refrigerant vapour passage and external communications, first absorber (4) also has heated medium pipeline and external communications respectively and refrigerant vapour passage and external communications is arranged, second absorber (5) also has heated medium pipeline and external communications, divide steam chest (6) to also have refrigerant vapour passage and external communications, form three-three absorption systems take place.
3. three-three absorption systems take place, be to take place in-three absorption systems in claim 1 described three, first generator (1) there is the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution pump (7) and first solution heat exchanger (10) with dividing steam chest (6) to be communicated with to be adjusted into first generator (1), having the weak solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (11) second absorber (5) is adjusted into second absorber (5) and has the weak solution pipeline to be communicated with dividing steam chest (6) through second solution heat exchanger (11) and absorption-generator (3) to be communicated with formation three generations-three absorption systems.
4. three-three absorption systems take place, be to take place in-three absorption systems in claim 2 described three, first generator (1) there is the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution pump (7) and first solution heat exchanger (10) with dividing steam chest (6) to be communicated with to be adjusted into first generator (1), having the weak solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (11) second absorber (5) is adjusted into second absorber (5) and has the weak solution pipeline to be communicated with dividing steam chest (6) through second solution heat exchanger (11) and absorption-generator (3) to be communicated with formation three generations-three absorption systems.
5. the 3rd class absorption heat pump, be to take place in-three absorption systems at claim 1-2 described arbitrary three, increase by first condenser, second condenser, evaporimeter, the first cryogen liquid pump and the second 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 (13), first condenser (13) also has the cryogen liquid pipeline to be communicated with evaporimeter (15) through the first cryogen liquid pump (16), to divide steam chest (6) to have refrigerant vapour passage and external communications to be defined as branch steam chest (6) has the refrigerant vapour passage to be communicated with second condenser (14), second condenser (14) also has the cryogen liquid pipeline to be communicated with evaporimeter (15) through the second cryogen liquid pump (17), having refrigerant vapour passage and external communications to be defined as evaporimeter (15) first absorber (4) has the refrigerant vapour passage to be communicated with first absorber (4), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as evaporimeter (15) to have the refrigerant vapour passage to be communicated with absorption-generator (3), first condenser (13) and second condenser (14) also have cooling medium pipeline and external communications respectively, evaporimeter (15) also have surplus heat medium pipeline and external communications form the 3rd class absorption heat pump; Wherein, when not having second condenser, divide steam chest (6) to have the refrigerant vapour passage to be communicated with first condenser (13).
6. the 3rd class absorption heat pump, be to take place in-three absorption systems at claim 1-2 described arbitrary three, increase condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 condenser (13), to divide steam chest (6) to have refrigerant vapour passage and external communications to be defined as branch steam chest (6) has the refrigerant vapour passage to be communicated with condenser (13), condenser (13) also has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through the first cryogen liquid pump (16), condenser (13) also has the cryogen liquid pipeline to be communicated with second evaporimeter (18) through the second cryogen liquid pump (17), having refrigerant vapour passage and external communications to be defined as first evaporimeter (15) first absorber (4) has the refrigerant vapour passage to be communicated with first absorber (4), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (18) to have the refrigerant vapour passage to be communicated with absorption-generator (3), condenser (13) also has cooling medium pipeline and external communications, first evaporimeter (15) and second evaporimeter (18) also have surplus heat respectively medium pipeline and external communications form the 3rd class absorption heat pump.
7. the 3rd class absorption heat pump, be to take place in-three absorption systems in claim 2 described three, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 (13), first condenser (13) also has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through the first cryogen liquid pump (16), to divide steam chest (6) to have refrigerant vapour passage and external communications to be defined as branch steam chest (6) has the refrigerant vapour passage to be communicated with second condenser (14), second condenser (14) has the cryogen liquid pipeline to be communicated with second evaporimeter (18) through the second cryogen liquid pump (17), having refrigerant vapour passage and external communications to be defined as first evaporimeter (15) first absorber (4) has the refrigerant vapour passage to be communicated with first absorber (4), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (18) to have the refrigerant vapour passage to be communicated with absorption-generator (3), first condenser (13) and second condenser (14) also have cooling medium pipeline and external communications respectively, first evaporimeter (15) and second evaporimeter (18) also have surplus heat respectively medium pipeline and external communications form the 3rd class absorption heat pump.
8. the 3rd class absorption heat pump, be to take place in-three absorption systems at claim 3-4 described arbitrary three, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 (13), first condenser (13) also has the cryogen liquid pipeline to be communicated with second evaporimeter (18) through the first cryogen liquid pump (16), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (18) to have the refrigerant vapour passage to be communicated with absorption-generator (3), to divide steam chest (6) to have refrigerant vapour passage and external communications to be defined as branch steam chest (6) has the refrigerant vapour passage to be communicated with second condenser (14), second condenser (14) also has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through the second cryogen liquid pump (17), having refrigerant vapour passage and external communications to be defined as first evaporimeter (15) first absorber (4) has the refrigerant vapour passage to be communicated with first absorber (4), first condenser (13) and second condenser (14) also have cooling medium pipeline and external communications respectively, first evaporimeter (15) and second evaporimeter (18) also have surplus heat respectively medium pipeline and external communications form the 3rd class absorption heat pump; Wherein: when 1. not having second evaporimeter, first condenser (13) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through the first cryogen liquid pump (16), and first evaporimeter (15) is set up the refrigerant vapour passage and is communicated with absorption-generator (3); When 2. not having second evaporimeter and second condenser, divide steam chest (6) to have the refrigerant vapour passage to be communicated with first condenser (13), first condenser (13) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through the first cryogen liquid pump (16), and first evaporimeter (15) is set up the refrigerant vapour passage and is communicated with absorption-generator.
9. the 3rd class absorption heat pump, be to take place in-three absorption systems in claim 4 described three, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first cryogen liquid pump and the second 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 (13), first condenser (13) also has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through the first cryogen liquid pump (16), to divide steam chest (6) to have refrigerant vapour passage and external communications to be defined as branch steam chest (6) has the refrigerant vapour passage to be communicated with second condenser (14), second condenser (14) has the cryogen liquid pipeline to be communicated with second evaporimeter (18) through the second cryogen liquid pump (17), having refrigerant vapour passage and external communications to be defined as first evaporimeter (15) first absorber (4) has the refrigerant vapour passage to be communicated with first absorber (4), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (18) to have the refrigerant vapour passage to be communicated with absorption-generator (3), first condenser (13) and second condenser (14) also have cooling medium pipeline and external communications respectively, first evaporimeter (15) and second evaporimeter (18) also have surplus heat respectively medium pipeline and external communications form the 3rd class absorption heat pump.
10. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 5-7, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, first generator (1) there is the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with branch steam chest (6) through first solution heat exchanger (10) and absorption-generator (3) with dividing steam chest (6) to be communicated with to be adjusted into first generator (1), absorption-generator (3) is set up the weak solution pipeline and is communicated with the 3rd generator (20) through the 4th solution heat exchanger (21), the 3rd generator (20) also has the concentrated solution pipeline through first solution pump (7), the 4th solution heat exchanger (21) converges through first solution heat exchanger (10) concentrated solution pipeline afterwards with first generator (1) afterwards, having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (20) with the 3rd generator (20) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (13) through choke valve (19) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (20) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
11. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 5-7, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, having the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through first solution pump (7) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with the 3rd generator (20) through the 4th solution heat exchanger (21), the 3rd generator (20) also has the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through first solution pump (7) and the 4th solution heat exchanger (21), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (20) with the 3rd generator (20) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (13) through choke valve (19) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (20) also has refrigerant vapour passage first to be communicated with condenser (13), forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
12. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 5-7, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (1) through first solution heat exchanger (10) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with the 3rd generator (20) through first solution heat exchanger (10), the 3rd generator (20) also has the concentrated solution pipeline to be communicated with first generator (1) through first solution pump (7) and the 4th solution heat exchanger (21), having the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through first solution pump (7) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through the 4th solution heat exchanger (21), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (20) with the 3rd generator (20) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (13) through choke valve (19) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (20) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
13. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 8-9, increase by the 3rd generator, the 4th solution heat exchanger, choke valve and the 4th solution pump, absorption-generator (3) is set up the weak solution pipeline and is communicated with the 3rd generator (20) through the 4th solution heat exchanger (21), the 3rd generator (20) also has the concentrated solution pipeline through the 4th solution pump (22), the 4th solution heat exchanger (21) afterwards with first generator (1) through first solution pump (7), first solution heat exchanger (10) concentrated solution pipeline afterwards converges, having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (20) with the 3rd generator (20) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (13) through choke valve (19) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (20) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
14. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 8-9, increase by the 3rd generator, the 4th solution heat exchanger and choke valve, having the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through first solution pump (7) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with the 3rd generator (20) through the 4th solution heat exchanger (21), the 3rd generator (20) also has the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through first solution pump (7) and the 4th solution heat exchanger (21), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (20) with the 3rd generator (20) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (13) through choke valve (19) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (20) also has refrigerant vapour passage first to be communicated with condenser (13), forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
15. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 8-9, increase by the 3rd generator, the 4th solution heat exchanger, choke valve and the 4th solution pump, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (1) through first solution heat exchanger (10) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with the 3rd generator (20) through first solution heat exchanger (10), the 3rd generator (20) also has the concentrated solution pipeline to be communicated with first generator (1) through the 4th solution pump (22) and the 4th solution heat exchanger (21), having the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through first solution pump (7) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through the 4th solution heat exchanger (21) and first solution pump (7), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (20) with the 3rd generator (20) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (13) through choke valve (19) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (20) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
16. the 3rd class absorption heat pump, be described at claim 5-7, absorption-generator does not have in arbitrary the 3rd class absorption heat pump of heated medium pipeline and external communications, cancel the refrigerant vapour passage that first evaporimeter (15) or second evaporimeter (18) are communicated with absorption-generator (3), first generator (1) is set up the refrigerant vapour passage and is communicated with absorption-generator (3), increase by the 3rd generator, choke valve and solution choke valve, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (1) through first solution heat exchanger (10) to be adjusted into absorption-generator (3) and to have the weak solution pipeline directly to be communicated with first generator (1), first generator (1) there is the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with branch steam chest (6) through solution choke valve (29) and absorption-generator (3) with dividing steam chest (6) to be communicated with to be adjusted into first generator (1), absorption-generator (3) is set up the weak solution pipeline and is communicated with the 3rd generator (20) through first solution heat exchanger (10), the 3rd generator (20) also has the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) converges through solution choke valve (29) concentrated solution pipeline afterwards with first generator (1) afterwards, having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (20) with the 3rd generator (20) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (13) through choke valve (19) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (20) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
17. the 3rd class absorption heat pump, be described at claim 5-7, absorption-generator does not have in arbitrary the 3rd class absorption heat pump of heated medium pipeline and external communications, cancel the refrigerant vapour passage that first evaporimeter (15) or second evaporimeter (18) are communicated with absorption-generator (3), first generator (1) is set up the refrigerant vapour passage and is communicated with absorption-generator (3), increase the 3rd generator and choke valve, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (1) through first solution heat exchanger (10) to be adjusted into absorption-generator (3) and to have the weak solution pipeline directly to be communicated with first generator (1), first generator (1) there is the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with the 3rd generator (20) through first solution heat exchanger (10) with dividing steam chest (6) to be communicated with to be adjusted into first generator (1), the 3rd generator (20) also has the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (6), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (20) with the 3rd generator (20) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (13) through choke valve (19) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (20) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
18. the 3rd class absorption heat pump, be described at claim 5-7, absorption-generator does not have in arbitrary the 3rd class absorption heat pump of heated medium pipeline and external communications, cancel the refrigerant vapour passage that first evaporimeter (15) or second evaporimeter (18) are communicated with absorption-generator (3), first generator (1) is set up the refrigerant vapour passage and is communicated with absorption-generator (3), increase by the 3rd generator, choke valve and solution choke valve, first generator (1) there is the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with branch steam chest (6) through solution choke valve (29) and absorption-generator (3) with dividing steam chest (6) to be communicated with to be adjusted into first generator (1), to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (1) through first solution heat exchanger (10) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with the 3rd generator (20) through first solution heat exchanger (10), the 3rd generator (20) also has the concentrated solution pipeline to be communicated with first generator (1) through first solution pump (7) and first solution heat exchanger (10), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into first generator (1) to have the refrigerant vapour passage to be communicated with back the 3rd generator (20) with the 3rd generator (20) in first generator (1) has the cryogen liquid pipeline to be communicated with first condenser (13) through choke valve (19) again---and the refrigerant vapour of first generator generation is as the driving thermal medium of the 3rd generator, the 3rd generator (20) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-economic benefits and social benefits the 3rd class absorption heat pump.
19. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 10, increase by the 4th generator, the 5th solution heat exchanger and second choke valve, the 3rd generator (20) there is the concentrated solution pipeline through first solution pump (7), the 4th solution heat exchanger (21) and absorption-generator (3) have the concentrated solution pipeline to be communicated with branch steam chest (6) through the 4th solution heat exchanger (21) and absorption-generator (3) with dividing steam chest (6) to be communicated with to be adjusted into the 3rd generator (20), absorption-generator (3) is set up the weak solution pipeline and is communicated with the 4th generator (24) through the 5th solution heat exchanger (25), the 4th generator (24) also has the concentrated solution pipeline through first solution pump (7), the 5th solution heat exchanger (25) converges through first solution heat exchanger (10) concentrated solution pipeline afterwards with first generator (1) afterwards, having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into the 3rd generator (20) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (20) has the cryogen liquid pipeline to be communicated with first condenser (13) through second choke valve (23) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-triple effect the 3rd class absorption heat pump.
20. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 11, increase by the 4th generator, the 5th solution heat exchanger and second choke valve, having the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through first solution pump (7) and the 4th solution heat exchanger (21) in the 3rd generator (20) is adjusted into the 3rd generator (21) and has the concentrated solution pipeline to be communicated with the 4th generator (24) through the 5th solution heat exchanger (25), the 4th generator (24) also has the concentrated solution pipeline through first solution pump (7), the 5th solution heat exchanger (25) and the 4th solution heat exchanger (21) are communicated with first solution heat exchanger (10), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into the 3rd generator (20) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (20) has the cryogen liquid pipeline to be communicated with first condenser (13) through second choke valve (23) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-triple effect the 3rd class absorption heat pump.
21. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 12, increase by the 4th generator, the 5th solution heat exchanger, second choke valve and the 4th solution pump, to absorb-generator (3) has the weak solution pipeline to be communicated with the 3rd generator (20) through first solution heat exchanger (10) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with the 4th generator (24) through first solution heat exchanger (10), the 4th generator (24) also has the concentrated solution pipeline to be communicated with the 3rd generator (20) through the 4th solution pump (22) and the 5th solution heat exchanger (25), having the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through the 4th solution heat exchanger (21) in first generator (1) is adjusted into first generator (1) and has the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through the 4th solution heat exchanger (21) and the 5th solution heat exchanger (25), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into the 3rd generator (20) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (20) has the cryogen liquid pipeline to be communicated with first condenser (13) through second choke valve (23) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-triple effect the 3rd class absorption heat pump.
22. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 13, increase by the 4th generator, the 5th solution heat exchanger, second choke valve and the 5th solution pump, absorption-generator (3) is set up the weak solution pipeline and is communicated with the 4th generator (24) through the 5th solution heat exchanger (25), the 4th generator (24) also has the concentrated solution pipeline through the 5th solution pump (26), the 5th solution heat exchanger (25) afterwards with first generator (1) through first solution pump (7), first solution heat exchanger (10) concentrated solution pipeline afterwards converges, having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into the 3rd generator (20) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (20) has the cryogen liquid pipeline to be communicated with first condenser (13) through second choke valve (23) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-triple effect the 3rd class absorption heat pump.
23. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 14, increase by the 4th generator, the 5th solution heat exchanger and second choke valve, having the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through first solution pump (7) and the 4th solution heat exchanger (21) in the 3rd generator (20) is adjusted into the 3rd generator (21) and has the concentrated solution pipeline to be communicated with the 4th generator (24) through the 5th solution heat exchanger (25), the 4th generator (24) also has the concentrated solution pipeline through first solution pump (7), the 5th solution heat exchanger (25) and the 4th solution heat exchanger (21) are communicated with first solution heat exchanger (10), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into the 3rd generator (20) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (20) has the cryogen liquid pipeline to be communicated with first condenser (13) through second choke valve (23) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-triple effect the 3rd class absorption heat pump.
24. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 15, increase by the 4th generator, the 5th solution heat exchanger, second choke valve and the 5th solution pump, to absorb-generator (3) has the weak solution pipeline to be communicated with the 3rd generator (20) through first solution heat exchanger (10) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with the 4th generator (24) through first solution heat exchanger (10), the 4th generator (24) also has the concentrated solution pipeline to be communicated with the 3rd generator (20) through the 5th solution pump (26) and the 5th solution heat exchanger (25), having the concentrated solution pipeline to be communicated with first solution heat exchanger (10) through the 4th solution heat exchanger (21) and first solution pump (7) in first generator (1) is adjusted into first generator (1) and the concentrated solution pipeline is arranged through the 4th solution heat exchanger (21), the 5th solution heat exchanger (25) and first solution pump (7) are communicated with first solution heat exchanger (10), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into the 3rd generator (20) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (20) has the cryogen liquid pipeline to be communicated with first condenser (13) through second choke valve (23) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-triple effect the 3rd class absorption heat pump.
25. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 16, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, the 3rd generator (20) there is the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with branch steam chest (6) through first solution heat exchanger (10) and absorption-generator (3) with dividing steam chest (6) to be communicated with to be adjusted into the 3rd generator (20), absorption-generator (3) is set up the weak solution pipeline and is communicated with the 4th generator (24) through the 3rd solution heat exchanger (21), the 4th generator (24) also has the concentrated solution pipeline through first solution pump (7), the 4th solution heat exchanger (21) and absorption-generator (3) are communicated with dividing steam chest (6), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into the 3rd generator (20) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (20) has the cryogen liquid pipeline to be communicated with first condenser (13) through second choke valve (23) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-triple effect the 3rd class absorption heat pump.
26. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 25, to absorb-generator (3) has the weak solution pipeline to be communicated with the 3rd generator (20) through first solution heat exchanger (10) with first generator (1) connected sum respectively directly to be adjusted into absorption-generator (3) and to have the weak solution pipeline to distinguish directly to be communicated with first generator (1) through first solution heat exchanger (10) with the 3rd generator (20) connected sum, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest (6) through first solution heat exchanger (10) and absorption-generator (3) through solution choke valve (29) and absorption-generator (3) with dividing steam chest (6) to be communicated with to be adjusted into first generator (1) in first generator (1), there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest (6) through solution choke valve (29) and absorption-generator (3) through first solution heat exchanger (10) and absorption-generator (3) with dividing steam chest (6) to be communicated with to be adjusted into the 3rd generator (20) in the 3rd generator (20), cancel the refrigerant vapour passage that first generator (1) is communicated with absorption-generator (3), the 3rd generator (20) is set up the refrigerant vapour passage and is communicated with absorption-generator (3), forms single-action-triple effect the 3rd class absorption heat pump.
27. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 17, increase by the 4th generator, the 4th solution heat exchanger and second choke valve, the 3rd generator (20) there is the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with the 4th generator (24) through the 4th solution heat exchanger (21) with dividing steam chest (6) to be communicated with to be adjusted into the 3rd generator (20), the 4th generator (24) also has the concentrated solution pipeline through first solution pump (7), the 4th solution heat exchanger (21), first solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (6), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into the 3rd generator (20) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (20) has the cryogen liquid pipeline to be communicated with first condenser (13) through second choke valve (23) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-triple effect the 3rd class absorption heat pump.
28. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 27, increase by the 4th solution pump, to absorb-generator (3) has the weak solution pipeline directly to be communicated with first generator (1) to be adjusted into absorption-generator (3) and has the weak solution pipeline to be communicated with first generator (1) through the 4th solution pump (22) and first solution heat exchanger (10), the 4th generator (24) there is the concentrated solution pipeline through first solution pump (7), the 4th solution heat exchanger (21), first solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline through first solution pump (7) with dividing steam chest (6) to be communicated with to be adjusted into the 4th generator (24), the 4th solution heat exchanger (21) and absorption-generator (3) are communicated with dividing steam chest (6), there is the refrigerant vapour passage to be communicated with absorption-generator (3) to be adjusted into the 3rd generator (20) to set up the refrigerant vapour passage in first generator (1) and is communicated with absorption-generator (3), form single-action-triple effect the 3rd class absorption heat pump.
29. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 18, increase by the 4th generator, the 4th solution heat exchanger, the 4th solution pump and second choke valve, to absorb-generator (3) has the weak solution pipeline to be communicated with the 3rd generator (20) through first solution heat exchanger (10) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with the 4th generator (24) through first solution heat exchanger (10) and the 4th solution heat exchanger (21), the 4th generator (24) also has the concentrated solution pipeline to be communicated with the 3rd generator (20) through the 4th solution pump (22) and the 4th solution heat exchanger (21), having the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into the 3rd generator (20) to have the refrigerant vapour passage to be communicated with back the 4th generator (24) with the 4th generator (24) in the 3rd generator (20) has the cryogen liquid pipeline to be communicated with first condenser (13) through second choke valve (23) again, the 4th generator (24) also has the refrigerant vapour passage to be communicated with first condenser (13), forms single-action-triple effect the 3rd class absorption heat pump.
30. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 29, cancellation solution choke valve, to absorb-generator (3) has the weak solution pipeline to be communicated with the 4th generator (24) through first solution heat exchanger (10) and the 4th solution heat exchanger (21) to be adjusted into the weak solution pipeline and to be communicated with the 4th generator (24) through the 4th solution heat exchanger (21), there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with branch steam chest (6) through first solution heat exchanger (10) and absorption-generator (3) through solution choke valve (29) and absorption-generator (3) with dividing steam chest (6) to be communicated with to be adjusted into first generator (1) in first generator (1), cancel the refrigerant vapour passage that first generator (11) is communicated with absorption-generator (3), the 3rd generator (20) is set up the refrigerant vapour passage and is communicated with absorption-generator (3), forms single-action-triple effect the 3rd class absorption heat pump.
31. the 3rd class absorption heat pump, be described in claim 5, do not have in arbitrary the 3rd class absorption heat pump of second condenser, keep the second cryogen liquid pump, increase absorption-evaporimeter, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (1) through first solution heat exchanger (10) to be adjusted into absorption-generator (3) and to have the weak solution pipeline directly to be communicated with absorption-evaporimeter (27), absorption-evaporimeter (27) also has the weak solution pipeline to be communicated with first generator (1) with solution heat exchanger (10) through the, evaporimeter (15) had the refrigerant vapour passage to be communicated with first absorber (4) to be adjusted into evaporimeter (15) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (27), condenser (13) is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with first absorber (4) through the second cryogen liquid pump (17) with absorption-evaporimeter (27) after absorption-evaporimeter (27) is communicated with again, forms single-action-1.5 grade the 3rd class absorption heat pump.
32. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 31, increase by the 3rd cryogen liquid pump, second evaporimeter and the 4th solution heat exchanger, condenser (13) is set up the cryogen liquid pipeline and is communicated with second evaporimeter (18) through the 3rd cryogen liquid pump (28), first evaporimeter (15) had the refrigerant vapour passage to be communicated with absorption-generator (3) to be adjusted into second evaporimeter (18) has the refrigerant vapour passage to be communicated with absorption-generator (3), to absorb-generator (3) has the weak solution pipeline directly to be communicated with absorption-evaporimeter (27) to be adjusted into absorption-generator (3) and has the weak solution pipeline to be communicated with absorption-evaporimeter (27) through the 4th solution heat exchanger (21), first generator (1) there is the concentrated solution pipeline through first solution pump (7), first solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline through first solution pump (7) with dividing steam chest (6) to be communicated with to be adjusted into first generator (1), first solution heat exchanger (10), the 4th solution heat exchanger (21) and absorption-generator (3) are communicated with dividing steam chest (6), second evaporimeter (18) also have surplus heat medium pipeline and external communications form single-action-1.5 grade the 3rd class absorption heat pump.
33. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 31, increase choke valve and second condenser, to divide steam chest (6) to have the refrigerant vapour passage to be communicated with first condenser (13) to be adjusted into branch steam chest (6) has the refrigerant vapour passage to be communicated with second condenser (14), second condenser (14) has the cryogen liquid pipeline to be communicated with first condenser (13) through choke valve (19), second condenser (14) also has cooling medium pipeline and external communications, forms single-action-1.5 grade the 3rd class absorption heat pump.
34. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 6, increase choke valve or the 3rd cryogen liquid pump, the 4th solution heat exchanger and absorption-evaporimeter, having the weak solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (11) second absorber (5) is adjusted into second absorber (5) and has the weak solution pipeline to be communicated with absorption-evaporimeter (27) through second solution heat exchanger (11), absorption-evaporimeter (27) also has the weak solution pipeline to be communicated with absorption-generator (3) through the 4th solution heat exchanger (21), to divide steam chest (6) to have the concentrated solution pipeline to be communicated with second generator (2) through second solution pump (8) and second solution heat exchanger (11) is adjusted into branch steam chest (6) and the concentrated solution pipeline is arranged through second solution pump (8), the 4th solution heat exchanger (21) and second solution heat exchanger (11) are communicated with second generator (2), first evaporimeter (15) had the refrigerant vapour passage to be communicated with first absorber (4) to be adjusted into first evaporimeter (15) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (27), condenser (13) is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with first absorber (4) through the 3rd cryogen liquid pump (28) with absorption-evaporimeter (27) after absorption-evaporimeter (27) is communicated with again, or first evaporimeter (15) set up the cryogen liquid pipeline and be communicated with second evaporimeter (18) and condenser (13) had the cryogen liquid pipeline be communicated with second evaporimeter (18) through the second cryogen liquid pump (17) through choke valve (19) and be adjusted into condenser (13) and have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with first absorber (4) through the second cryogen liquid pump (17) again with absorption-evaporimeter (27) after absorption-evaporimeter (27) is communicated with, form single-action-1.5 grade the 3rd class absorption heat pump.
35. the 3rd class absorption heat pump, be described in claim 8, do not have in arbitrary the 3rd class absorption heat pump of second evaporimeter, increase absorption-evaporimeter, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (1) through first solution heat exchanger (10) to be adjusted into absorption-generator (3) and to have the weak solution pipeline directly to be communicated with absorption-evaporimeter (27), absorption-evaporimeter (27) also has the weak solution pipeline to be communicated with first generator (1) through first solution heat exchanger (10), evaporimeter (15) had the refrigerant vapour passage to be communicated with first absorber (4) to be adjusted into evaporimeter (15) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (27), having the cryogen liquid pipeline to be communicated with evaporimeter (15) through the second cryogen liquid pump (17) second condenser (14) is adjusted into second condenser (14) and has the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with first absorber (4) through the second cryogen liquid pump (17) again with absorption-evaporimeter (27) after absorption-evaporimeter (27) is communicated with, form single-action-1.5 grade the 3rd class absorption heat pump.
36. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 8, increase choke valve or the 3rd cryogen liquid pump, absorption-evaporimeter and the 4th solution heat exchanger, there is the weak solution pipeline to have the weak solution pipeline to be communicated with absorption-evaporimeter (27) through second solution heat exchanger (11) through second solution heat exchanger (11) and absorption-generator (3) with dividing steam chest (6) to be communicated with to be adjusted into second absorber (5) second absorber (5), absorption-evaporimeter (27) also has the weak solution pipeline to be communicated with dividing steam chest (6) through the 4th solution heat exchanger (21) and absorption-generator (3), to divide steam chest (6) to have the concentrated solution pipeline to be communicated with second generator (2) through second solution pump (8) and second solution heat exchanger (11) is adjusted into branch steam chest (6) and the concentrated solution pipeline is arranged through second solution pump (8), the 4th solution heat exchanger (21) and second solution heat exchanger (11) are communicated with second generator (2), first evaporimeter (15) had the refrigerant vapour passage to be communicated with first absorber (4) to be adjusted into first evaporimeter (15) has the refrigerant vapour passage to be communicated with absorption-evaporimeter (27), second condenser (14) is set up the cryogen liquid pipeline has the refrigerant vapour passage to be communicated with first absorber (4) through the 3rd cryogen liquid pump (28) with absorption-evaporimeter (27) after absorption-evaporimeter (27) is communicated with again, or second cryogen liquid pump (17) set up the cryogen liquid pipeline and be communicated with back absorptions-evaporimeter (27) with absorption-evaporimeter (27) and have the refrigerant vapour passage to be communicated with first absorber (4) more also simultaneously the second cryogen liquid pump (17) to be had the cryogen liquid pipeline to be communicated with first evaporimeter (15) and be adjusted into the second cryogen liquid pump (17) and have the cryogen liquid pipeline to be communicated with first evaporimeter (15) through choke valve (19), formation single-action-1.5 grade the 3rd class absorption heat pump.
37. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 31-34, cancel the refrigerant vapour passage that second evaporimeter 18 and second evaporimeter 18 be communicated with absorption-generator 3 or cancel the refrigerant vapour passage that first evaporimeter 15 is communicated with absorption-generator 3, absorption-evaporimeter 27 is set up the refrigerant vapour passage and is communicated with absorption-generator 3, forms single-action-two-stage the 3rd class absorption heat pump.
38. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 5-37, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, second solution heat exchanger (11) 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 first absorber (4) through newly-increased solution heat exchanger (B), having the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with economic benefits and social benefits is the 3rd class absorption heat pump of high temperature generation flow process.
39. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 5-37, increase newly-increased generator, newly-increased solution heat exchanger and newly-increased choke valve, there is the concentrated solution pipeline to be communicated with second generator (2) to be adjusted into second solution heat exchanger (11) to have the concentrated solution pipeline to be communicated with second generator (2) through newly-increased solution heat exchanger (B) second solution heat exchanger (11), having the concentrated solution pipeline to be communicated with first absorber (4) through the 3rd solution heat exchanger (12) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (B), newly-increased generator (A) has the concentrated solution pipeline to be communicated with first absorber (4) through the 3rd solution heat exchanger (12) again, having the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with economic benefits and social benefits is the 3rd class absorption heat pump of high temperature generation flow process.
40. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 5-37, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased choke valve and newly-increased solution pump, second solution heat exchanger (11) had the concentrated solution pipeline to be communicated with second generator (2) to be adjusted into second solution heat exchanger (11) 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 newly-increased solution pump (D) and newly-increased solution heat exchanger (B), having the concentrated solution pipeline to be communicated with first absorber (4) through the 3rd solution heat exchanger (12) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with first absorber (4) through newly-increased solution heat exchanger (B) and the 3rd solution heat exchanger (12), having the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased choke valve (C) again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with economic benefits and social benefits is the 3rd class absorption heat pump of high temperature generation flow process.
41. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 5-37, increase newly-increased first generator, newly-increased second generator, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first throttle valve and newly-increased second choke valve, second solution heat exchanger (11) is set up the concentrated solution pipeline and is communicated with newly-increased second generator (E) through newly-increased second solution heat exchanger (F) with newly-increased first generator (A) connected sum through newly-increased first solution heat exchanger (B) respectively, newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with first absorber (4) through newly-increased first solution heat exchanger (B), newly-increased second generator (E) also has the concentrated solution pipeline to be communicated with first absorber (4) through newly-increased second solution heat exchanger (F), having the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with newly-increased first generator (A) in back with newly-increased first generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased first throttle valve (C) again, newly-increased first generator (A) also has the refrigerant vapour passage to be communicated with newly-increased second generator (E) in back with newly-increased second generator (E) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased second choke valve (G) again, newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with the triple effect is the 3rd class absorption heat pump of high temperature generation flow process.
42. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 5-37, increase newly-increased first generator, newly-increased second generator, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first throttle valve and newly-increased second choke valve, having the concentrated solution pipeline to be communicated with second generator (2) to be adjusted into second solution heat exchanger (11) the concentrated solution pipeline to be arranged through newly-increased second solution heat exchanger (F) and increase first solution heat exchanger (B) newly second solution heat exchanger (11) is communicated with second generator (2), having the concentrated solution pipeline to be communicated with first absorber (4) through the 3rd solution heat exchanger (12) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased first solution heat exchanger (B), newly-increased first generator (A) also has 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 first absorber (4) through the 3rd solution heat exchanger (12), having the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with newly-increased first generator (A) in back with newly-increased first generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased first throttle valve (C) again, newly-increased first generator (A) also has the refrigerant vapour passage to be communicated with newly-increased second generator (E) in back with newly-increased second generator (E) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased second choke valve (G) again, newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with the triple effect is the 3rd class absorption heat pump of high temperature generation flow process.
43. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 5-37, increase newly-increased first generator, newly-increased second generator, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution pump and newly-increased second solution pump, second solution heat exchanger (11) had the concentrated solution pipeline to be communicated with second generator (2) to be adjusted into second solution heat exchanger (11) has the concentrated solution pipeline to be 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), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with second generator (2) through newly-increased first solution pump (D) and newly-increased first solution heat exchanger (B), having the concentrated solution pipeline to be communicated with first absorber (4) through the 3rd solution heat exchanger (12) in second generator (2) is adjusted into second generator (2) and the concentrated solution pipeline is arranged through newly-increased first solution heat exchanger (B), newly-increased second solution heat exchanger (F) and the 3rd solution heat exchanger (12) are communicated with first absorber (4), having the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with newly-increased first generator (A) in back with newly-increased first generator (A) in second generator (2) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased first throttle valve (C) again, newly-increased first generator (A) also has the refrigerant vapour passage to be communicated with newly-increased second generator (E) in back with newly-increased second generator (E) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased second choke valve (G) again, newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with the triple effect is the 3rd class absorption heat pump of high temperature generation flow process.
44. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 5-37, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, second solution heat exchanger (11) had the concentrated solution pipeline to be communicated with second generator (2) to be adjusted into second solution heat exchanger (11) has the concentrated solution pipeline to be communicated with newly-increased absorber (I), newly-increased absorber (I) also has the weak 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 first absorber (4) through the 3rd solution heat exchanger (12) in second generator (2) is adjusted into second generator (2) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (B), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with first absorber (4) through the 3rd solution heat exchanger (12), newly-increased generator (A) also has the thermal medium of driving pipeline respectively with external communications and has the refrigerant vapour passage to be communicated with newly-increased absorber (I), newly-increased absorber (I) also has heated medium pipeline and external communications, and forming with the back-heating type single-action is the 3rd class absorption heat pump of high temperature generation flow process.
45. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 44, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased choke valve, newly-increased solution pump (D) 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 newly-increased first generator (A) through newly-increased second solution heat exchanger (F), having the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with newly-increased second generator (E) in back with newly-increased second generator (E) in second generator (2) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased choke valve (C) again, newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with the backheating type double-effect is the 3rd class absorption heat pump of high temperature generation flow process.
46. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 44, increase newly-increased second generator, newly-increased second solution heat exchanger and newly-increased choke valve, to increase absorber (I) newly has the weak solution pipeline to be communicated with second generator (2) through newly-increased solution pump (D) and newly-increased first solution heat exchanger (B) to be adjusted into newly-increased absorber (I) and to have weak solution pipeline warp to increase solution pump (D) newly, newly-increased second solution heat exchanger (F) and newly-increased first solution heat exchanger (B) are communicated with second generator (2), having the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased first solution heat exchanger (B) in second generator (2) is adjusted into second generator (2) and has 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 newly-increased first generator (A) through newly-increased second solution heat exchanger (F), having the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with newly-increased second generator (E) in back with newly-increased second generator (E) in second generator (2) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased choke valve (C) again, newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with the backheating type double-effect is the 3rd class absorption heat pump of high temperature generation flow process.
47. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 44, increase newly-increased second generator, newly-increased second solution heat exchanger, newly-increased choke valve and newly-increased second solution pump, to increase absorber (I) newly has the weak solution pipeline to be communicated with second generator (2) through newly-increased first solution pump (D) and newly-increased first solution heat exchanger (B) to be adjusted into newly-increased absorber (I) and to have weak solution pipeline warp to increase first solution pump (D) newly and increase first solution heat exchanger (B) newly and be communicated with newly-increased second generator (E), newly-increased second generator (E) also has the concentrated solution pipeline to be communicated with second generator (2) through newly-increased second solution pump (H) and newly-increased second solution heat exchanger (F), having the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased first solution heat exchanger (B) in second generator (2) is adjusted into second generator (2) and has concentrated solution pipeline warp to increase second solution heat exchanger (F) newly and increase first solution heat exchanger (B) newly and be communicated with newly-increased first generator (A), having the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into second generator (2) to have the refrigerant vapour passage to be communicated with newly-increased second generator (E) in back with newly-increased second generator (E) in second generator (2) has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased choke valve (C) again, newly-increased second generator (E) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with the backheating type double-effect is the 3rd class absorption heat pump of high temperature generation flow process.
48. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 45-47, the driving thermal medium pipeline of newly-increased first generator (A) of cancellation and external communications, increase newly-increased second choke valve, second generator (2) is set up the refrigerant vapour passage and is communicated with newly-increased first generator (A) in back with newly-increased first generator (A) and has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased second choke valve (G) again, and formation is the 3rd class absorption heat pump of high temperature generation flow process with the backheating type double-effect.
49. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 45, increase newly-increased the 3rd generator, newly-increased the 3rd solution heat exchanger and newly-increased second choke valve, newly-increased solution pump (D) is set up the weak solution pipeline and is communicated with newly-increased the 3rd generator (J) through newly-increased the 3rd solution heat exchanger (L), newly-increased the 3rd generator (J) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased the 3rd solution heat exchanger (L), to increase second generator (E) newly has the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased second generator (E) to have the refrigerant vapour passage to be communicated with the back with newly-increased the 3rd generator (J) to increase the 3rd generator (J) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with first evaporimeter (15), newly-increased the 3rd generator (J) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of high temperature generation flow process.
50. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 46, increase newly-increased the 3rd generator, newly-increased the 3rd solution heat exchanger and newly-increased second choke valve, to increase absorber (I) newly and the weak solution pipeline be arranged through newly-increased solution pump (D), newly-increased second solution heat exchanger (F) and newly-increased first solution heat exchanger (B) are communicated with second generator (2) and are adjusted into newly-increased absorber (I) and have weak solution pipeline warp to increase solution pump (D) newly, newly-increased the 3rd solution heat exchanger (L), newly-increased second solution heat exchanger (F) and newly-increased first solution heat exchanger (B) are communicated with second generator (2), to increase second generator (E) newly has the concentrated solution pipeline to be communicated with newly-increased first generator (A) to be adjusted into through newly-increased second solution heat exchanger (F) to increase second generator (E) newly and have concentrated solution pipeline warp to increase second solution heat exchanger (F) newly to be communicated with newly-increased the 3rd generator (J), newly-increased the 3rd generator (J) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased the 3rd solution heat exchanger (L), to increase second generator (E) newly has the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased second generator (E) to have the refrigerant vapour passage to be communicated with the back with newly-increased the 3rd generator (J) to increase the 3rd generator (J) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with first evaporimeter (15), newly-increased the 3rd generator (J) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of high temperature generation flow process.
51. the 3rd class absorption heat pump, be in described arbitrary the 3rd class absorption heat pump of claim 47, increase newly-increased the 3rd generator, newly-increased the 3rd solution heat exchanger, newly-increased second choke valve and newly-increased the 3rd solution pump, to increase absorber (I) newly has the weak solution pipeline to be communicated with newly-increased second generator (E) through newly-increased first solution pump (D) and newly-increased first solution heat exchanger (B) to be adjusted into newly-increased absorber (I) and to have weak solution pipeline warp to increase first solution pump (D) newly and increase first solution heat exchanger (B) newly and be communicated with newly-increased the 3rd generator (J), newly-increased the 3rd generator (J) also has the concentrated solution pipeline to be communicated with newly-increased second generator (E) through newly-increased the 3rd solution pump (M) and newly-increased the 3rd solution heat exchanger (L), having the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased second solution heat exchanger (F) and newly-increased first solution heat exchanger (B) in second generator (2) is adjusted into second generator (2) and has concentrated solution pipeline warp to increase second solution heat exchanger (F) newly, newly-increased the 3rd solution heat exchanger (L) and newly-increased first solution heat exchanger (B) are communicated with newly-increased first generator (A), to increase second generator (E) newly has the refrigerant vapour passage to be communicated with second absorber (5) to be adjusted into newly-increased second generator (E) to have the refrigerant vapour passage to be communicated with the back with newly-increased the 3rd generator (J) to increase the 3rd generator (J) newly and have cryogen liquid pipeline warp to increase second choke valve (G) newly again to be communicated with first evaporimeter (15), newly-increased the 3rd generator (J) also has the refrigerant vapour passage to be communicated with second absorber (5), and forming with the back-heating type triple-effect is the 3rd class absorption heat pump of high temperature generation flow process.
52. the 3rd class absorption heat pump, be to ask in described the 3rd arbitrary class absorption heat pump at claim 49-51, increase newly-increased the 3rd choke valve, the driving thermal medium pipeline of newly-increased first generator (A) of cancellation and external communications, second generator (2) is set up the refrigerant vapour passage and is communicated with newly-increased first generator (A) in back with newly-increased first generator (A) and has the cryogen liquid pipeline to be communicated with first evaporimeter (15) through newly-increased the 3rd choke valve (K) again, and formation is the 3rd class absorption heat pump of high temperature generation flow process with the back-heating type triple-effect.
53. the 3rd class absorption heat pump, be to ask in described the 3rd arbitrary class absorption heat pump at claim 49-51, increase newly-increased the 3rd choke valve, the driving thermal medium pipeline of newly-increased first generator (A) of cancellation and external communications, newly-increased second generator (E) is set up the refrigerant vapour passage and is communicated with newly-increased first generator (A) in back with newly-increased first generator (A) and has cryogen liquid pipeline warp to increase the 3rd choke valve (K) newly again to be communicated with first evaporimeter (15), and formation is the 3rd class absorption heat pump of high temperature generation flow process with the back-heating type triple-effect.
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Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102538279B (en) * 2012-02-03 2014-05-14 李华玉 Triple-generation double absorption system and third-class absorption heat pump
CN102563953B (en) * 2012-02-03 2014-07-30 李华玉 Three-generation-three-absorption system and class III absorption heat pump
CN102538278B (en) * 2012-02-12 2014-06-25 李华玉 Fractional condensation third-class absorption heat pump
CN102589185B (en) * 2012-02-19 2014-07-30 李华玉 Third type absorption heat pump with regenerative cooling end
CN102645051B (en) * 2012-03-27 2014-10-29 李华玉 Double-effect back-heating absorbing-generating system and back-heating second-class absorption heat pump
CN102706027B (en) * 2012-04-01 2014-07-30 李华玉 Double-effect regeneration absorption-generation system and regeneration third-class absorption heat pump
CN102635970B (en) * 2012-04-09 2015-02-04 李华玉 Grading condensation third-type absorption heat pump
CN102679615B (en) * 2012-05-04 2014-09-03 李华玉 Sectional heat return third-class absorption heat pump

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1624400A (en) * 2003-06-18 2005-06-08 三洋电机株式会社 Single/double effect absorption refrigerating machine, and its operation control method
JP4143562B2 (en) * 2004-03-15 2008-09-03 三菱製紙株式会社 Inkjet recording material for pigment ink
JP2011127857A (en) * 2009-12-21 2011-06-30 Kawasaki Thermal Engineering Co Ltd Method and device for controlling absorption water heater/cooler utilizing exhaust gas of dispersion type power generating system

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04143562A (en) * 1990-10-05 1992-05-18 Nippon Telegr & Teleph Corp <Ntt> Low temperature waste heat utilizing absorption type refrigerating plant and controlling method therefor
CN2525445Y (en) * 2001-12-04 2002-12-11 江苏双良空调设备股份有限公司 Two purpose second class lithium bromide absorptice heat pump
JP2004257705A (en) * 2003-02-27 2004-09-16 Sanyo Electric Co Ltd Concentration device using absorption heat pump
CN101464068A (en) * 2009-01-11 2009-06-24 李华玉 Method for improving heat supply temperature of second-kind absorption type heat pump and high temperature type heat pump thereof
WO2011091560A1 (en) * 2010-01-30 2011-08-04 Li Huayu Combined absorption-generation system and third-type absorption heat pump
CN101968286B (en) * 2010-10-10 2011-11-02 李华玉 Double absorption-double generation system and multi-terminal heat supply third kind absorption heat pumps

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1624400A (en) * 2003-06-18 2005-06-08 三洋电机株式会社 Single/double effect absorption refrigerating machine, and its operation control method
JP4143562B2 (en) * 2004-03-15 2008-09-03 三菱製紙株式会社 Inkjet recording material for pigment ink
JP2011127857A (en) * 2009-12-21 2011-06-30 Kawasaki Thermal Engineering Co Ltd Method and device for controlling absorption water heater/cooler utilizing exhaust gas of dispersion type power generating system

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