CN104807239A - Absorption heat pump of fourth class and absorption heat pump of fifth class - Google Patents

Absorption heat pump of fourth class and absorption heat pump of fifth class Download PDF

Info

Publication number
CN104807239A
CN104807239A CN201510144105.9A CN201510144105A CN104807239A CN 104807239 A CN104807239 A CN 104807239A CN 201510144105 A CN201510144105 A CN 201510144105A CN 104807239 A CN104807239 A CN 104807239A
Authority
CN
China
Prior art keywords
generator
communicated
newly
increased
solution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201510144105.9A
Other languages
Chinese (zh)
Other versions
CN104807239B (en
Inventor
李华玉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201510144105.9A priority Critical patent/CN104807239B/en
Publication of CN104807239A publication Critical patent/CN104807239A/en
Application granted granted Critical
Publication of CN104807239B publication Critical patent/CN104807239B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • F25B15/12—Sorption machines, plants or systems, operating continuously, e.g. absorption type with resorber
    • 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
    • F25B30/00—Heat pumps
    • F25B30/04—Heat pumps of the sorption type
    • 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
    • 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
    • F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
    • 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
    • F25B27/00—Machines, plants or systems, using particular sources of energy
    • F25B27/02—Machines, plants or systems, using particular sources of energy using waste heat, e.g. from internal-combustion engines
    • 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
    • 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
    • Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • 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

Landscapes

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

Abstract

The invention provides an absorption heat pump of fourth class and an absorption heat pump of fifth class, and belongs to the technical field of waste-heat utilization and heat pump. An absorber is connected with a second absorber through a solution heat exchanger, and the second absorber is connected with a generator through a solution pump and a second solution heat exchanger; the generator is connected with a second generator through the solution heat exchanger, and the second generator is connected with the absorber through a second solution pump and the second solution heat exchanger; the generator is connected with a condenser through a refrigerant steam channel, the second generator is connected with the second absorber through the refrigerant steam channel, the condenser is connected with an evaporator through the second generator and a throttle valve, and the condenser is connected with the absorber through the refrigerant steam channel; the generator has a drive thermal medium pipeline for connecting to the external, the absorber and the condenser have heated thermal medium pipeline for connecting to the external, the evaporator has waste heat medium pipeline for connecting to the external, the second condenser has a cooling medium pipeline for connecting to the external for forming the absorption heat pump of fourth class; a waste heat medium pipeline is arranged on the second generator for connecting with external for forming the absorption heat pump of fifth class.

Description

4th class absorption heat pump and the 5th class absorption heat pump
Technical field:
The invention belongs to absorption heat pump and technical field of waste heat utilization.
Background technology:
In absorption heat pump technical field, have respectively with the temperature difference between high temperature driven thermal medium and heated medium for driving the first-class absorption type heat pump (Absorption Refrigerator) of the temperature difference, be the second-kind absorption-type heat pump driving the temperature difference with the temperature difference between waste heat medium and cold environment (cooling medium), and simultaneously with aforementioned two kinds of temperature difference for driving the 3rd class absorption heat pump of the temperature difference.According to existing understanding or viewpoint, in the absorption heat pump of this three types, high temperature driven thermic load is discharged in cold environment (cooling medium), using the temperature difference between high temperature driven thermal medium and cold environment (cooling medium) as the driving temperature difference of absorption heat pump be irrational; Same reason, high temperature driven heat cools under heated medium temperature, and makes this temperature drop also be mysterious as the driving temperature difference of absorption heat pump.
In the first-class absorption type heat pump that high-temperature hot load is provided and the 3rd class absorption heat pump, those skilled in the art encounter such technical barrier: in the absorption heat pump flow process being representative with TFE-TDE pyrosol, and high-temperature generator discharges refrigerant vapour and heat release forms cryogen liquid after heated medium within the condenser; Refrigerant vapour latent heat is little, and cryogen liquid temp is high, sensible heat is relatively large, this causes the performance index of absorption heat pump very low, heat utilization rate is not high, and the application making first-class absorption type heat pump and the 3rd class absorption heat pump carry out freezing in high-temperature heat supply field or application high-temperature hot load is extremely restricted.
Inventor recognizes the problems referred to above, and have developed the technology new departure solved the problem, and has had and has comprised with high-temperature hot load two kinds of temperature drops for driving the 4th class absorption heat pump and the 5th class absorption heat pump of the temperature difference; The invention provides and utilize the second generator and the second absorber to realize poor many moneys the 4th class absorption heat pump and the 5th class absorption heat pump being utilized as basis of cryogen liquid temperature.
Summary of the invention:
Main purpose of the present invention to provide the 4th class absorption heat pump and the 5th class absorption heat pump, and concrete summary of the invention subitem is described below:
1. the 4th class absorption heat pump, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, choke valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, absorber has weak solution pipeline to be communicated with the second absorber through solution heat exchanger, second absorber also has weak solution pipeline to be communicated with generator with the second solution heat exchanger through solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second solution pump, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second absorber, condenser also have cryogen liquid pipeline be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, evaporimeter also has refrigerant steam channel to be communicated with absorber, generator also has driving heat medium pipeline and ft connection, absorber and condenser also have heated medium pipeline and ft connection respectively, evaporimeter also has surplus heat medium pipeline and ft connection, second absorber also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
2. the 4th class absorption heat pump, in the 4th class absorption heat pump described in the 1st, cancel choke valve, had by the second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve and be adjusted to the second generator and have cryogen liquid pipeline to be communicated with evaporimeter, formation the 4th class absorption heat pump.
3. the 4th class absorption heat pump, in the 4th class absorption heat pump described in the 1st, increase by the 3rd generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, second absorber is set up weak solution pipeline and is communicated with the 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 3rd generator also has concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline again through heat exchanger, second generator is communicated with evaporimeter with second throttle, 3rd generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
4. the 4th class absorption heat pump, in the 4th class absorption heat pump described in the 1st, increase by the 3rd generator, second throttle, 3rd solution heat exchanger and heat exchanger, had by second absorber weak solution pipeline to be communicated with generator through solution pump and the second solution heat exchanger to be adjusted to the second absorber and to have weak solution pipeline through solution pump, second solution heat exchanger is communicated with generator with the 3rd solution heat exchanger, had by generator concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger again, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline again through heat exchanger, second generator is communicated with evaporimeter with second throttle, 3rd generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
5. the 4th class absorption heat pump, in the 4th class absorption heat pump described in the 1st, increase by the 3rd generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, had by second absorber weak solution pipeline to be communicated with generator through solution pump and the second solution heat exchanger to be adjusted to the second absorber and to have weak solution pipeline to be communicated with the 3rd generator with the second solution heat exchanger through solution pump, 3rd generator has concentrated solution pipeline to be communicated with generator with the 3rd solution heat exchanger through the 3rd solution pump again, had by generator concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through the 3rd solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline again through heat exchanger, second generator is communicated with evaporimeter with second throttle, 3rd generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
6. the 4th class absorption heat pump, in arbitrary 4th class absorption heat pump described in 3-5 item, cancel choke valve and second throttle, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, there is by second generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 4th class absorption heat pump.
7. the 4th class absorption heat pump, in the 4th class absorption heat pump described in the 3rd, increase by the 4th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, second absorber is set up weak solution pipeline and is communicated with the 4th generator with the 4th solution heat exchanger through the 4th solution pump, 4th generator also has concentrated solution pipeline to be communicated with the second generator through the 4th solution heat exchanger, 4th generator also has refrigerant steam channel to be communicated with condenser, had by 3rd generator refrigerant steam channel to be communicated with condenser to be adjusted to the 3rd generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline again through the second heat exchanger, second generator is communicated with evaporimeter with the 3rd choke valve, 3rd generator there is cryogen liquid pipeline through heat exchanger, second generator and second throttle are communicated with evaporimeter and are adjusted to the 3rd generator and have cryogen liquid pipeline through the 4th generator, heat exchanger, second generator is communicated with evaporimeter with second throttle, second heat exchanger also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
8. the 4th class absorption heat pump, in the 4th class absorption heat pump described in the 4th, increase by the 4th generator, 3rd choke valve, 4th solution heat exchanger and the second heat exchanger, second absorber there is weak solution pipeline through solution pump, second solution heat exchanger and the 3rd solution heat exchanger are communicated with generator and are adjusted to the second absorber and have weak solution pipeline through solution pump, 4th solution heat exchanger, second solution heat exchanger is communicated with generator with the 3rd solution heat exchanger, had by 3rd generator concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger to be adjusted to the 3rd generator and to have concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger, 4th generator has concentrated solution pipeline to be communicated with the second generator through the 4th solution heat exchanger again, 4th generator also has refrigerant steam channel to be communicated with condenser, had by 3rd generator refrigerant steam channel to be communicated with condenser to be adjusted to the 3rd generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline again through the second heat exchanger, second generator is communicated with evaporimeter with the 3rd choke valve, 3rd generator there is cryogen liquid pipeline through heat exchanger, second generator and second throttle are communicated with evaporimeter and are adjusted to the 3rd generator and have cryogen liquid pipeline through the 4th generator, heat exchanger, second generator is communicated with evaporimeter with second throttle, second heat exchanger also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
9. the 4th class absorption heat pump, in the 4th class absorption heat pump described in the 5th, increase by the 4th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, had by second absorber weak solution pipeline to be communicated with the 3rd generator through solution pump and the second solution heat exchanger to be adjusted to the second absorber and to have weak solution pipeline to be communicated with the 4th generator with the second solution heat exchanger through solution pump, 4th generator has concentrated solution pipeline to be communicated with the 3rd generator with the 4th solution heat exchanger through the 4th solution pump again, had by generator concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger and the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline through the 3rd solution heat exchanger, 4th solution heat exchanger is communicated with the second generator with the second solution heat exchanger, 4th generator also has refrigerant steam channel to be communicated with condenser, had by 3rd generator refrigerant steam channel to be communicated with condenser to be adjusted to the 3rd generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline again through the second heat exchanger, second generator is communicated with evaporimeter with the 3rd choke valve, 3rd generator there is cryogen liquid pipeline through heat exchanger, second generator and second throttle are communicated with evaporimeter and are adjusted to the 3rd generator and have cryogen liquid pipeline through the 4th generator, heat exchanger, second generator is communicated with evaporimeter with second throttle, second heat exchanger also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
10. the 4th class absorption heat pump, in arbitrary 4th class absorption heat pump described in 7-9 item, cancel choke valve, second throttle and the 3rd choke valve, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through the 3rd choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 4th class absorption heat pump.
11. the 4th class absorption heat pumps, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 3rd generator, the 3rd solution pump, the 3rd solution heat exchanger and the 3rd absorber, absorber has weak solution pipeline to be communicated with the second absorber through solution heat exchanger, second absorber also has weak solution pipeline to be communicated with the 3rd absorber with the second solution heat exchanger through solution pump, 3rd absorber also has weak solution pipeline to be communicated with generator with the 3rd solution heat exchanger through the 3rd solution pump, generator also has concentrated solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second solution pump, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second absorber, 3rd generator also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also have cryogen liquid pipeline be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, evaporimeter also has refrigerant steam channel to be communicated with absorber, generator and the 3rd generator also have driving heat medium pipeline and ft connection respectively, absorber, condenser and the 3rd absorber also have heated medium pipeline and ft connection respectively, evaporimeter also has surplus heat medium pipeline and ft connection, second absorber also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
12. the 4th class absorption heat pumps, in the 4th class absorption heat pump described in the 11st, cancel choke valve, had by the second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve and be adjusted to the second generator and have cryogen liquid pipeline to be communicated with evaporimeter, formation the 4th class absorption heat pump.
13. the 4th class absorption heat pumps, in the 4th class absorption heat pump described in the 11st, increase by the 4th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, 3rd absorber is set up weak solution pipeline and is communicated with the 4th generator with the 4th solution heat exchanger through the 4th solution pump, 4th generator also has concentrated solution pipeline to be communicated with the 3rd generator through the 4th generator, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline again through heat exchanger, second generator is communicated with evaporimeter with second throttle, 4th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
14. the 4th class absorption heat pumps, in the 4th class absorption heat pump described in the 11st, increase by the 4th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by 3rd absorber weak solution pipeline to be communicated with generator through the 3rd solution pump and the 3rd solution heat exchanger to be adjusted to the 3rd absorber and to have weak solution pipeline through the 3rd solution pump, 3rd solution heat exchanger is communicated with generator with the 4th solution heat exchanger, had by generator concentrated solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 4th generator through the 4th solution heat exchanger, 4th generator has concentrated solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger again, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline again through heat exchanger, second generator is communicated with evaporimeter with second throttle, 4th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
15. the 4th class absorption heat pumps, in the 4th class absorption heat pump described in the 11st, increase by the 4th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, had by 3rd absorber weak solution pipeline to be communicated with generator through the 3rd solution pump and the 3rd solution heat exchanger to be adjusted to the 3rd absorber and to have weak solution pipeline to be communicated with the 4th generator with the 3rd solution heat exchanger through the 3rd solution pump, 4th generator also has concentrated solution pipeline to be communicated with generator with the 4th solution heat exchanger through the 4th solution pump, had by generator concentrated solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 3rd generator with the 3rd solution heat exchanger through the 4th solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline again through heat exchanger, second generator is communicated with evaporimeter with second throttle, 4th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
16. the 4th class absorption heat pumps are in arbitrary 4th class absorption heat pump described in 13-15 item, and the 4th generator is set up and driven heat medium pipeline and ft connection, forms the 4th class absorption heat pump.
17. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in 13-16 item, cancel choke valve and second throttle, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, there is by second generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 4th class absorption heat pump.
18. the 4th class absorption heat pumps, in the 4th class absorption heat pump described in the 1st or the 11st, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber weak solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with the second absorber with solution heat exchanger through newly-increased solution pump again, had by second generator concentrated solution pipeline to be communicated with absorber through the second solution pump and solution heat exchanger to be adjusted to the second generator and to have concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber with newly-increased solution heat exchanger through the second solution pump again, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased absorber, second generator is had cryogen liquid pipeline through choke valve to be communicated with evaporimeter be adjusted to the second generator have cryogen liquid pipeline to be communicated with newly-increased generator after newly-increased generator have cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, newly-increased absorber also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
19. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in the 18th, cancel choke valve, had by newly-increased generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve and be adjusted to newly-increased generator and have cryogen liquid pipeline to be communicated with evaporimeter, formation the 4th class absorption heat pump.
20. the 4th class absorption heat pumps, at 3-5, in arbitrary 4th class absorption heat pump described in 13-16 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber weak solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with the second absorber with solution heat exchanger through newly-increased solution pump again, had by second generator concentrated solution pipeline to be communicated with absorber through the second solution pump and solution heat exchanger to be adjusted to the second generator and to have concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber with newly-increased solution heat exchanger through the second solution pump again, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased absorber, second generator is had cryogen liquid pipeline through choke valve to be communicated with evaporimeter be adjusted to the second generator have cryogen liquid pipeline to be communicated with newly-increased generator after newly-increased generator have cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, second generator is had cryogen liquid pipeline through second throttle to be communicated with evaporimeter be adjusted to the second generator have cryogen liquid pipeline to be communicated with newly-increased generator after newly-increased generator have cryogen liquid pipeline to be communicated with evaporimeter through second throttle again, newly-increased absorber also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
21. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in the 20th, cancel choke valve and second throttle, had by newly-increased generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to newly-increased generator and to have cryogen liquid pipeline to be communicated with evaporimeter, there is by newly-increased generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to newly-increased generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 4th class absorption heat pump.
22. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in 7-9 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber weak solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with the second absorber with solution heat exchanger through newly-increased solution pump again, had by second generator concentrated solution pipeline to be communicated with absorber through the second solution pump and solution heat exchanger to be adjusted to the second generator and to have concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber with newly-increased solution heat exchanger through the second solution pump again, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased absorber, second generator is had cryogen liquid pipeline through choke valve to be communicated with evaporimeter be adjusted to the second generator have cryogen liquid pipeline to be communicated with newly-increased generator after newly-increased generator have cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, second generator is had cryogen liquid pipeline through second throttle to be communicated with evaporimeter be adjusted to the second generator have cryogen liquid pipeline to be communicated with newly-increased generator after newly-increased generator have cryogen liquid pipeline to be communicated with evaporimeter through second throttle again, second generator is had cryogen liquid pipeline through the 3rd choke valve to be communicated with evaporimeter be adjusted to the second generator have cryogen liquid pipeline to be communicated with newly-increased generator after newly-increased generator have cryogen liquid pipeline to be communicated with evaporimeter through the 3rd choke valve again, newly-increased absorber also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
23. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in the 22nd, cancel choke valve, second throttle and the 3rd choke valve, had by newly-increased generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to newly-increased generator and to have cryogen liquid pipeline to be communicated with evaporimeter, had by newly-increased generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to newly-increased generator and to have cryogen liquid pipeline to be communicated with evaporimeter, had by newly-increased generator cryogen liquid pipeline to be communicated with evaporimeter through the 3rd choke valve to be adjusted to newly-increased generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 4th class absorption heat pump.
24. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in 1-17 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to evaporimeter has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with absorber, newly-increased generator also has driving heat medium pipeline and ft connection, newly-increased absorber also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
25. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in 18-23 item, increase newly-increased second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, being had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to evaporimeter has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased second absorber through newly-increased second solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with absorber, newly-increased second generator also has driving heat medium pipeline and ft connection, newly-increased second absorber also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
26. the 4th class absorption heat pumps, at 1-2, in arbitrary 4th class absorption heat pump described in 11-12 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with condenser, newly-increased generator also has driving heat medium pipeline and ft connection, newly-increased absorber also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
27. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in 18-19 item, increase newly-increased second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, being had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased second absorber through newly-increased second solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with condenser, newly-increased second generator also has driving heat medium pipeline and ft connection, newly-increased second absorber also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
28. the 4th class absorption heat pumps, in the 4th class absorption heat pump described in the 1st or the 11st, cancel the cooling medium pipeline of the second absorber and ft connection, there is by second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter with the second absorber through choke valve, form the 4th class absorption heat pump.
29. the 4th class absorption heat pumps, at 3-5, in arbitrary 4th class absorption heat pump described in 13-16 item, cancel the cooling medium pipeline of the second absorber and ft connection, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter with the second absorber through choke valve, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter with the second absorber through second throttle, form the 4th class absorption heat pump.
30. the 4th class absorption heat pumps, at 3-5, in arbitrary 4th class absorption heat pump described in 13-16 item, cancel the cooling medium pipeline of the second absorber and ft connection, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter with the second absorber through choke valve, or to be had by the second generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter with the second absorber through second throttle, form the 4th class absorption heat pump.
31. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in 7-9 item, cancel the cooling medium pipeline of the second absorber and ft connection, and the one-out-three, three of carrying out in following Adjusted Option selects two or three to select three, obtaining the 4th class absorption heat pump: Adjusted Option one, is had by the second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter with the second absorber through choke valve; Adjusted Option two is had by the second generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter with the second absorber through second throttle; Adjusted Option three is had by the second generator cryogen liquid pipeline to be communicated with evaporimeter through the 3rd choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter with the second absorber through the 3rd choke valve.
32. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in the 18th, cancel the cooling medium pipeline of the second absorber and ft connection, cancel the cooling medium pipeline of newly-increased absorber and ft connection, there is by newly-increased generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to newly-increased generator and to have cryogen liquid pipeline to be communicated with evaporimeter with newly-increased absorber through choke valve, the second absorber, form the 4th class absorption heat pump.
33. the 4th class absorption heat pumps, be the 1st, 3-5,7-9,11, in arbitrary 4th class absorption heat pump described in 13-16 item, cancel the cooling medium pipeline of the second absorber and ft connection, 1. circulating pump is increased, the finisher that circulating pump is communicated with the second absorber and evaporimeter successively by circulatory mediator pipeline is communicated with shape by circulatory mediator pipeline with circulating pump again and forms closed circuit, forms the 4th class absorption heat pump; 2. increase intermediate heat exchanger, intermediate heat exchanger is communicated with the second absorber and evaporimeter, forms the 4th class absorption heat pump.
34. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in the 18th, 20,22, increase circulating pump, cancel the cooling medium pipeline of the second absorber and ft connection, cancel the cooling medium pipeline of newly-increased absorber and ft connection, circulating pump is communicated with newly-increased absorber successively by circulatory mediator pipeline, the finisher of the second absorber and evaporimeter is communicated with shape by circulatory mediator pipeline with circulating pump again and forms closed circuit, forms the 4th class absorption heat pump.
35. the 5th class absorption heat pumps, in the 4th class absorption heat pump described in the 1st or the 11st, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber weak solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with the second absorber with solution heat exchanger through newly-increased solution pump again, had by second generator concentrated solution pipeline to be communicated with absorber through the second solution pump and solution heat exchanger to be adjusted to the second generator and to have concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber with newly-increased solution heat exchanger through the second solution pump again, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased generator also has surplus heat medium pipeline and ft connection, newly-increased absorber also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
36. the 5th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in the 35th, cancel choke valve, had by the second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve and be adjusted to the second generator and have cryogen liquid pipeline to be communicated with evaporimeter, formation the 5th class absorption heat pump.
37. the 5th class absorption heat pumps, at 3-5, in arbitrary 5th class absorption heat pump described in 13-16 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber weak solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with the second absorber with solution heat exchanger through newly-increased solution pump again, had by second generator concentrated solution pipeline to be communicated with absorber through the second solution pump and solution heat exchanger to be adjusted to the second generator and to have concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber with newly-increased solution heat exchanger through the second solution pump again, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased generator also has surplus heat medium pipeline and ft connection, newly-increased absorber also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
38. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in the 37th, cancel choke valve and second throttle, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, there is by second generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 5th class absorption heat pump.
39. the 5th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in 7-9 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber weak solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased absorber has weak solution pipeline to be communicated with the second absorber with solution heat exchanger through newly-increased solution pump again, had by second generator concentrated solution pipeline to be communicated with absorber through the second solution pump and solution heat exchanger to be adjusted to the second generator and to have concentrated solution pipeline to be communicated with newly-increased generator through solution heat exchanger, newly-increased generator has concentrated solution pipeline to be communicated with absorber with newly-increased solution heat exchanger through the second solution pump again, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased generator also has surplus heat medium pipeline and ft connection, newly-increased absorber also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
40. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in the 39th, cancel choke valve, second throttle and the 3rd choke valve, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, had by second generator cryogen liquid pipeline to be communicated with evaporimeter through the 3rd choke valve to be adjusted to the second generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 5th class absorption heat pump.
41. the 5th class absorption heat pumps are that the second generator sets up waste heat medium pipeline and ft connection in arbitrary 4th class absorption heat pump described in 1-17,28-34 item, form the 5th class absorption heat pump.
42. the 5th class absorption heat pumps are that the second generator and newly-increased generator set up waste heat medium pipeline and ft connection respectively in arbitrary 4th class absorption heat pump described in 18-23 item, form the 5th class absorption heat pump.
43. the 5th class absorption heat pumps are that the second generator or newly-increased generator set up waste heat medium pipeline and ft connection in arbitrary 4th class absorption heat pump described in 18-23 item, form the 5th class absorption heat pump.
44. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in the 41st, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to evaporimeter has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with absorber, newly-increased generator also has driving heat medium pipeline and ft connection, newly-increased absorber also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
45. the 5th class absorption heat pumps, at 35-38, in arbitrary 5th class absorption heat pump described in 42-43 item, increase newly-increased second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, being had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to evaporimeter has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased second absorber through newly-increased second solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with absorber, newly-increased second generator also has driving heat medium pipeline and ft connection, newly-increased second absorber also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
46. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 1-17 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by second generator refrigerant steam channel to be communicated with the second absorber to be adjusted to the second generator has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with the second absorber, newly-increased generator also has surplus heat medium pipeline and ft connection, newly-increased absorber also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
47. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 35-40 item, increase newly-increased second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, being had by newly-increased generator refrigerant steam channel to be communicated with newly-increased absorber to be adjusted to newly-increased generator has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased second absorber through newly-increased second solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased second generator also has surplus heat medium pipeline and ft connection, newly-increased second absorber also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
48. the 5th class absorption heat pumps are that the second generator sets up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in 45-47 item, form the 5th class absorption heat pump.
49. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 18-23 item, increase newly-increased second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, being had by newly-increased generator refrigerant steam channel to be communicated with newly-increased absorber to be adjusted to newly-increased generator has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased second absorber through newly-increased second solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased second generator also has surplus heat medium pipeline and ft connection, newly-increased second absorber also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
50. the 5th class absorption heat pumps are that the second generator and newly-increased generator set up waste heat medium pipeline and ft connection respectively in arbitrary 5th class absorption heat pump described in the 49th, form the 5th class absorption heat pump.
51. the 5th class absorption heat pumps are that the second generator or newly-increased generator set up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in the 49th, form the 5th class absorption heat pump.
Essence of the present invention is further illustrated below for the 5th class absorption heat pump shown in the 4th class absorption heat pump and Figure 17 shown in Fig. 1:
(1) high temperature driven heat is transferred in its refrigerant vapour discharged by generator 1, wherein in heated medium, thus will realize the utilization of the temperature difference between high temperature driven thermal medium and heated medium by a part of heat trnasfer by condenser 5; Because the latent heat of high-temperature medium is relatively little, then to make in the cryogen liquid of condenser 5 containing the sensible heat of relative abundance, take the technological means directly entering evaporimeter 6 through choke valve 7 throttling will cause the significantly reduction of UTILIZATION OF VESIDUAL HEAT IN amount.
(2) in Fig. 1, sensible heat in cryogen liquid is delivered in cooling medium by the second generator 2 and the second absorber 4, and the second time temperature drop of part high temperature driven heat is played a role---and reduce the solution concentration that enters generator 1 or improve the solution concentration entering absorber 3.
(3) in Figure 17, cryogen liquid flows through the second generator 2 heat release in solution to be made it discharge low pressure refrigerant vapour to provide to the second absorber 4, cryogen liquid flows through the second absorber 4 again and absorbs heat and components vaporize after choke valve 7 reducing pressure by regulating flow, and such high temperature driven heat is cooled to evaporating temperature again; This temperature difference plays a role---and reduce the solution concentration that enters generator 1 or improve the solution concentration entering absorber 3, this temperature difference belongs to the driving temperature difference equally.
Like this with two of high temperature driven heat kinds of temperature drops for drive the temperature difference, comprise the absorption heat pump that can realize the cold environment utilization of resources, be different from existing first-class absorption type heat pump, second-kind absorption-type heat pump and the 3rd class absorption heat pump, belong to new type; The time occurred according to technology and consideration naming order, to claim with two of high temperature driven heat kinds of temperature drops for driving the absorption heat pump of the temperature difference to be the 4th class absorption heat pump, claiming to increase the temperature difference between waste heat and cold environment on the 4th class absorption heat pump basis is drive the absorption heat pump of the temperature difference to be the 5th class absorption heat pump.
Accompanying drawing illustrates:
Fig. 1 is according to the 4th class absorption heat pump provided by the present invention 1st kind of structure and schematic flow sheet.
Fig. 2 is according to the 4th class absorption heat pump provided by the present invention 2nd kind of structure and schematic flow sheet.
Fig. 3 is according to the 4th class absorption heat pump provided by the present invention 3rd kind of structure and schematic flow sheet.
Fig. 4 is according to the 4th class absorption heat pump provided by the present invention 4th kind of structure and schematic flow sheet.
Fig. 5 is according to the 4th class absorption heat pump provided by the present invention 5th kind of structure and schematic flow sheet.
Fig. 6 is according to the 4th class absorption heat pump provided by the present invention 6th kind of structure and schematic flow sheet.
Fig. 7 is according to the 4th class absorption heat pump provided by the present invention 7th kind of structure and schematic flow sheet.
Fig. 8 is according to the 4th class absorption heat pump provided by the present invention 8th kind of structure and schematic flow sheet.
Fig. 9 is according to the 4th class absorption heat pump provided by the present invention 9th kind of structure and schematic flow sheet.
Figure 10 is according to the 4th class absorption heat pump provided by the present invention 10th kind of structure and schematic flow sheet.
Figure 11 is according to the 4th class absorption heat pump provided by the present invention 11st kind of structure and schematic flow sheet.
Figure 12 is according to the 4th class absorption heat pump provided by the present invention 12nd kind of structure and schematic flow sheet.
Figure 13 is according to the 4th class absorption heat pump provided by the present invention 13rd kind of structure and schematic flow sheet.
Figure 14 is according to the 4th class absorption heat pump provided by the present invention 14th kind of structure and schematic flow sheet.
Figure 15 is according to the 4th class absorption heat pump provided by the present invention 15th kind of structure and schematic flow sheet.
Figure 16 is according to the 4th class absorption heat pump provided by the present invention 16th kind of structure and schematic flow sheet.
Figure 17 is according to the 4th class absorption heat pump provided by the present invention 17th kind of structure and schematic flow sheet.
Figure 18 is according to the 4th class absorption heat pump provided by the present invention 18th kind of structure and schematic flow sheet.
Figure 19 is according to the 5th class absorption heat pump provided by the present invention 1st kind of structure and schematic flow sheet.
Figure 20 is according to the 5th class absorption heat pump provided by the present invention 2nd kind of structure and schematic flow sheet.
Figure 21 is according to the 5th class absorption heat pump provided by the present invention 3rd kind of structure and schematic flow sheet.
In figure, 1-generator, 2-second generator, 3-absorber, 4-second absorber, 5-condenser, 6-evaporimeter, 7-choke valve, 8-solution pump, 9-second solution pump, 10-solution heat exchanger, 11-second solution heat exchanger, 12-the 3rd generator, 13-the 3rd choke valve, 14-the 3rd solution pump, 15-the 3rd solution heat exchanger, 16-heat exchanger, 17-the 4th generator, 18-the 3rd choke valve, 19-the 4th solution pump, 20-the 4th solution heat exchanger, 21-second heat exchanger, 22-the 3rd absorber; A-increases generator newly, and B-increases absorber newly, and C-increases solution pump newly, and D-increases solution heat exchanger newly, E-circulating pump.
Here it is noted that
(1) for the 4th class absorption heat pump shown in accompanying drawing 1, the choke valve 7 arranged in cryogen liquid pipeline, available gravitational pressure drop substitutes; When coolant temperature is lower, when the cryogen liquid temp flowing through the second generator 2 is cooled to the evaporating temperature of evaporimeter 6 inside, choke valve 7 is not set, and power pressure reduction is used in the second generator 2 inner heat exchanger pipeline.
(2) for the 4th class absorption heat pump shown in Figure 17, for freeze occasion time, the waste heat medium flowing through evaporimeter 6 is called cooled medium traditionally, and the 4th class absorption heat pump is now called Absorption Refrigerator traditionally; In the present invention, unification is referred to as the 4th class absorption heat pump.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, do not repeat in inessential situation; Apparent flow process is not stated.The present invention is described in detail below in conjunction with accompanying drawing and example.
The 4th class absorption heat pump shown in Fig. 1 is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, choke valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, absorber 3 has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 10, second absorber 4 also has weak solution pipeline to be communicated with generator 1 with the second solution heat exchanger 11 through solution pump 8, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 11, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 10 through the second solution pump 9, generator 1 also has refrigerant steam channel to be communicated with condenser 5, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, condenser 5 also have cryogen liquid pipeline be communicated with the second generator 2 after the second generator 2 have cryogen liquid pipeline to be communicated with evaporimeter 6 through choke valve 7 again, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, generator 1 also has driving heat medium pipeline and ft connection, absorber 3 and condenser 5 also have heated medium pipeline and ft connection respectively, evaporimeter 6 also has surplus heat medium pipeline and ft connection, second absorber 4 also has cooling medium pipeline and ft connection.
(2) in flow process, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 10, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 8 and the second solution heat exchanger 11, drive heat medium flow through generator 1, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of generator 1 enters the second generator 2 through the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 9 and solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in heated medium, and cryogen liquid enters evaporimeter 6 through choke valve 7 throttling again after flowing through the second generator 2 heat release cooling, absorbs heat into refrigerant vapour and provide to absorber 3, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Fig. 2 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase by the 3rd generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, second absorber 4 is set up weak solution pipeline and is communicated with the 3rd generator 12 with the 3rd solution heat exchanger 15 through the 3rd solution pump 14, 3rd generator 12 also has concentrated solution pipeline to be communicated with the second generator 2 through the 3rd solution heat exchanger 15, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 3rd generator 12 after the 3rd generator 12 have cryogen liquid pipeline again through heat exchanger 16, second generator 2 is communicated with evaporimeter 6 with second throttle 13, 3rd generator 12 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 16 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 3rd generator 12 and does to drive thermal medium, the part weak solution of the second absorber 4 enters the 3rd generator 12 through the 3rd solution pump 14 and the 3rd solution heat exchanger 15, refrigerant vapour flows through the 3rd generator 12, heating enters the solution release refrigerant vapour in it and provides to condenser 5, and the concentrated solution of the 3rd generator 12 enters the second generator 2 through the 3rd solution heat exchanger 15; The refrigerant vapour heat release flowing through the 3rd generator 12 flows through heat exchanger 16 and the second generator 2 and progressively heat release cooling successively after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Fig. 3 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase by the 3rd generator, second throttle, 3rd solution heat exchanger and heat exchanger, had by second absorber 4 weak solution pipeline to be communicated with generator 1 through solution pump 8 and the second solution heat exchanger 11 to be adjusted to the second absorber 4 and to have weak solution pipeline through solution pump 8, second solution heat exchanger 11 is communicated with generator 1 with the 3rd solution heat exchanger 15, had by generator 1 concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 11 to be adjusted to generator 1 and to have concentrated solution pipeline to be communicated with the 3rd generator 12 through the 3rd solution heat exchanger 15, 3rd generator 12 has concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 11 again, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 3rd generator 12 after the 3rd generator 12 have cryogen liquid pipeline again through heat exchanger 16, second generator 2 is communicated with evaporimeter 6 with second throttle 13, 3rd generator 12 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 16 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 3rd generator 12 and does to drive thermal medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 8, second solution heat exchanger 11 and the 3rd solution heat exchanger 15, the concentrated solution of generator 1 enters the 3rd generator 12 through the 3rd solution heat exchanger 15, refrigerant vapour flows through the 3rd generator 12, heating enters the solution release refrigerant vapour in it and provides to condenser 5, and the concentrated solution of the 3rd generator 12 enters the second generator 2 through the second solution heat exchanger 11; The refrigerant vapour heat release flowing through the 3rd generator 12 flows through heat exchanger 16 and the second generator 2 and progressively heat release cooling successively after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Fig. 4 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase by the 3rd generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, had by second absorber 4 weak solution pipeline to be communicated with generator 1 through solution pump 8 and the second solution heat exchanger 11 to be adjusted to the second absorber 4 and to have weak solution pipeline to be communicated with the 3rd generator 12 with the second solution heat exchanger 11 through solution pump 8, 3rd generator 12 has concentrated solution pipeline to be communicated with generator 1 with the 3rd solution heat exchanger 15 through the 3rd solution pump 14 again, had by generator 1 concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 11 to be adjusted to generator 1 and to have concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 11 through the 3rd solution heat exchanger 15, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 3rd generator 12 after the 3rd generator 12 have cryogen liquid pipeline again through heat exchanger 16, second generator 2 is communicated with evaporimeter 6 with second throttle 13, 3rd generator 12 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 16 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 3rd generator 12 and does to drive thermal medium, the weak solution of the second absorber 4 enters the 3rd generator 12 through solution pump 8 and the second solution heat exchanger 11, refrigerant vapour flows through the 3rd generator 12, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 3rd generator 12 enters generator 1 through the 3rd solution pump 14 and the 3rd solution heat exchanger 15, and the concentrated solution of generator 1 enters the second generator 2 through the 3rd solution heat exchanger 15 and the second solution heat exchanger 11; The refrigerant vapour heat release flowing through the 3rd generator 12 flows through heat exchanger 16 and the second generator 2 and progressively heat release cooling successively after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Fig. 5 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 2, increase by the 4th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, second absorber 4 is set up weak solution pipeline and is communicated with the 4th generator 17 with the 4th solution heat exchanger 20 through the 4th solution pump 19, 4th generator 17 also has concentrated solution pipeline to be communicated with the second generator 2 through the 4th solution heat exchanger 20, 4th generator 17 also has refrigerant steam channel and condenser 5, had by 3rd generator 12 refrigerant steam channel to be communicated with condenser 5 to be adjusted to the 3rd generator 12 have refrigerant steam channel be communicated with the 4th generator 17 after the 4th generator 17 have cryogen liquid pipeline again through the second heat exchanger 21, second generator 2 is communicated with evaporimeter 6 with the 3rd choke valve 18, 3rd generator 12 there is cryogen liquid pipeline through heat exchanger 16, second generator 2 and second throttle 13 are communicated with evaporimeter 6 and are adjusted to the 3rd generator 12 and have cryogen liquid pipeline through the 4th generator 17, heat exchanger 16, second generator 2 is communicated with evaporimeter 6 with second throttle 13, second heat exchanger 21 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that 3rd generator 12 produces and cryogen liquid are supplied to the 4th generator 17 and do to drive thermal medium, the part weak solution of the second absorber 4 enters the 4th generator 17 through the 4th solution pump 19 and the 4th solution heat exchanger 20, refrigerant vapour and cryogen liquid flow through the 4th generator 17, heating enters the solution release refrigerant vapour in it and provides to condenser 5, and the concentrated solution of the 4th generator 17 enters the second generator 2 through the 4th solution heat exchanger 20; The refrigerant vapour heat release flowing through the 4th generator 17 flows through the second heat exchanger 21 and the second generator 2 and progressively heat release cooling successively after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 6 through the 3rd choke valve 18 throttling; The cryogen liquid of the 3rd generator 12 flows through the 4th generator 17, heat exchanger 16 and the second generator 2 heat release cooling successively, and the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Fig. 6 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 3, increase by the 4th generator, 3rd choke valve, 4th solution heat exchanger and the second heat exchanger, second absorber 4 there is weak solution pipeline through solution pump 8, second solution heat exchanger 11 and the 3rd solution heat exchanger 15 are communicated with generator 1 and are adjusted to the second absorber 4 and have weak solution pipeline through solution pump 8, 4th solution heat exchanger 20, second solution heat exchanger 11 is communicated with generator 1 with the 3rd solution heat exchanger 15, had by 3rd generator 12 concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 11 to be adjusted to the 3rd generator 12 and to have concentrated solution pipeline to be communicated with the 4th generator 17 through the second solution heat exchanger 11, 4th generator 17 has concentrated solution pipeline to be communicated with the second generator 2 through the 4th solution heat exchanger 20 again, 4th generator 17 also has refrigerant steam channel and condenser 5, had by 3rd generator 12 refrigerant steam channel to be communicated with condenser 5 to be adjusted to the 3rd generator 12 have refrigerant steam channel be communicated with the 4th generator 17 after the 4th generator 17 have cryogen liquid pipeline again through the second heat exchanger 21, second generator 2 is communicated with evaporimeter 6 with the 3rd choke valve 18, 3rd generator 12 there is cryogen liquid pipeline through heat exchanger 16, second generator 2 and second throttle 13 are communicated with evaporimeter 6 and are adjusted to the 3rd generator 12 and have cryogen liquid pipeline through the 4th generator 17, heat exchanger 16, second generator 2 is communicated with evaporimeter 6 with second throttle 13, second heat exchanger 21 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that 3rd generator 12 produces and cryogen liquid are supplied to the 4th generator 17 and do to drive thermal medium, the weak solution of the second absorber 4 is through solution pump 8, 4th solution heat exchanger 20, second solution heat exchanger 11 and the 3rd solution heat exchanger 15 enter generator 1, the concentrated solution of generator 1 enters the 3rd generator 12 through the 3rd solution heat exchanger 15, the concentrated solution of the 3rd generator 12 enters the 4th generator 17 through the second solution heat exchanger 11, refrigerant vapour and cryogen liquid flow through the 4th generator 17, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 4th generator 17 enters the second generator 2 through the 4th solution heat exchanger 20, the refrigerant vapour heat release flowing through the 4th generator 17 flows through the second heat exchanger 21 and the second generator 2 and progressively heat release cooling successively after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 6 through the 3rd choke valve 18 throttling, the cryogen liquid of the 3rd generator 12 flows through the 4th generator 17, heat exchanger 16 and the second generator 2 heat release cooling successively, and the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Fig. 7 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 4, increase by the 4th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, had by second absorber 4 weak solution pipeline to be communicated with the 3rd generator 12 through solution pump 8 and the second solution heat exchanger 11 to be adjusted to the second absorber 4 and to have weak solution pipeline to be communicated with the 4th generator 17 with the second solution heat exchanger 11 through solution pump 8, 4th generator 17 has concentrated solution pipeline to be communicated with the 3rd generator 12 with the 4th solution heat exchanger 20 through the 4th solution pump 19 again, had by generator 1 concentrated solution pipeline to be communicated with the second generator 2 through the 3rd solution heat exchanger 15 and the second solution heat exchanger 11 to be adjusted to generator 1 and to have concentrated solution pipeline through the 3rd solution heat exchanger 15, 4th solution heat exchanger 20 is communicated with the second generator 2 with the second solution heat exchanger 11, 4th generator 17 also has refrigerant steam channel and condenser 5, had by 3rd generator 12 refrigerant steam channel to be communicated with condenser 5 to be adjusted to the 3rd generator 12 have refrigerant steam channel be communicated with the 4th generator 17 after the 4th generator 17 have cryogen liquid pipeline again through the second heat exchanger 21, second generator 2 is communicated with evaporimeter 6 with the 3rd choke valve 18, 3rd generator 12 there is cryogen liquid pipeline through heat exchanger 16, second generator 2 and second throttle 13 are communicated with evaporimeter 6 and are adjusted to the 3rd generator 12 and have cryogen liquid pipeline through the 4th generator 17, heat exchanger 16, second generator 2 is communicated with evaporimeter 6 with second throttle 13, second heat exchanger 21 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that 3rd generator 12 produces and cryogen liquid are supplied to the 4th generator 17 and do to drive thermal medium, the weak solution of the second absorber 4 enters the 4th generator 17 through solution pump 8 and the second solution heat exchanger 11, refrigerant vapour and cryogen liquid flow through the 4th generator 17, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 4th generator 17 enters the 3rd generator 12 through the 4th solution pump 19 and the 4th solution heat exchanger 20, the concentrated solution of the 3rd generator 12 enters generator 1 through the 3rd solution pump 14 and the 3rd solution heat exchanger 15, the concentrated solution of generator 1 is through the 3rd solution heat exchanger 15, 4th solution heat exchanger 20 and the second solution heat exchanger 11 enter the second generator 2, the refrigerant vapour heat release flowing through the 4th generator 17 flows through the second heat exchanger 21 and the second generator 2 and progressively heat release cooling successively after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 6 through the 3rd choke valve 18 throttling, the cryogen liquid of the 3rd generator 12 flows through the 4th generator 17, heat exchanger 16 and the second generator 2 heat release cooling successively, and the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Fig. 8 is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 3rd generator, the 3rd solution pump, the 3rd solution heat exchanger and the 3rd absorber, absorber 3 has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 10, second absorber 4 also has weak solution pipeline to be communicated with the 3rd absorber 22 with the second solution heat exchanger 11 through solution pump 8, 3rd absorber 22 also has weak solution pipeline to be communicated with generator 1 with the 3rd solution heat exchanger 15 through the 3rd solution pump 14, generator 1 also has concentrated solution pipeline to be communicated with the 3rd generator 12 through the 3rd solution heat exchanger 15, 3rd generator 12 also has concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 11, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 10 through the second solution pump 9, generator 1 also has refrigerant steam channel to be communicated with condenser 5, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, 3rd generator 12 also has refrigerant steam channel to be communicated with the 3rd absorber 22, condenser 5 also have cryogen liquid pipeline be communicated with the second generator 2 after the second generator 2 have cryogen liquid pipeline to be communicated with evaporimeter 6 through choke valve 7 again, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, generator 1 and the 3rd generator 12 also have driving heat medium pipeline and ft connection respectively, absorber 3, condenser 5 and the 3rd absorber 22 also have heated medium pipeline and ft connection respectively, evaporimeter 6 also has surplus heat medium pipeline and ft connection, second absorber 4 also has cooling medium pipeline and ft connection.
(2) in flow process, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 10, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 4 enters the 3rd absorber 22 through solution pump 8 and the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 22 enters generator 1 through the 3rd solution pump 14 and the 3rd solution heat exchanger 15, drive heat medium flow through generator 1, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of generator 1 enters the 3rd generator 12 through the 3rd solution heat exchanger 15, drive heat medium flow through the 3rd generator 12, heating enters the solution release refrigerant vapour in it and provides to the 3rd absorber 22, the concentrated solution of the 3rd generator 12 enters the second generator 2 through the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 9 and solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in heated medium, and cryogen liquid enters evaporimeter 6 through choke valve 7 throttling again after flowing through the second generator 2 heat release cooling, absorbs heat into refrigerant vapour and provide to absorber 3, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Fig. 9 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 8, increase by the 4th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, 3rd absorber 22 is set up weak solution pipeline and is communicated with the 4th generator 17 with the 4th solution heat exchanger 20 through the 4th solution pump 19, 4th generator 17 also has concentrated solution pipeline to be communicated with the 3rd generator 12 through the 4th generator 20, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 4th generator 17 after the 4th generator 17 have cryogen liquid pipeline again through heat exchanger 16, second generator 2 is communicated with evaporimeter 6 with second throttle 13, 4th generator 17 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 16 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 4th generator 17 and does to drive thermal medium, the part weak solution of the 3rd absorber 22 enters the 4th generator 17 through the 4th solution pump 19 and the 4th solution heat exchanger 20, refrigerant vapour flows through the 4th generator 17, heating enters the solution release refrigerant vapour in it and provides to condenser 5, and the concentrated solution of the 4th generator 17 enters the 3rd generator 12 through the 4th solution heat exchanger 20; The refrigerant vapour heat release flowing through the 4th generator 17 flows through heat exchanger 16 and the second generator 2 and progressively heat release cooling successively after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Figure 10 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 8, increase by the 4th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by 3rd absorber 22 weak solution pipeline to be communicated with generator 1 through the 3rd solution pump 14 and the 3rd solution heat exchanger 15 to be adjusted to the 3rd absorber 22 and to have weak solution pipeline through the 3rd solution pump 14, 3rd solution heat exchanger 15 is communicated with generator 1 with the 4th solution heat exchanger 20, had by generator 1 concentrated solution pipeline to be communicated with the 3rd generator 12 through the 3rd solution heat exchanger 15 to be adjusted to generator 1 and to have concentrated solution pipeline to be communicated with the 4th generator 17 through the 4th solution heat exchanger 20, 4th generator 17 has concentrated solution pipeline to be communicated with the 3rd generator 12 through the 3rd solution heat exchanger 15 again, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 4th generator 17 after the 4th generator 17 have cryogen liquid pipeline again through heat exchanger 16, second generator 2 is communicated with evaporimeter 6 with second throttle 13, 4th generator 17 also has refrigerant steam channel to be communicated with condenser 5, 4th generator 17 also has driving heat medium pipeline and ft connection, heat exchanger 16 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour driving thermal medium and generator 1 to produce provides driving thermic load to the 4th generator 17, the weak solution of the 3rd absorber 22 is through the 3rd solution pump 14, 3rd solution heat exchanger 15 and the 4th solution heat exchanger 20 enter generator 1, the concentrated solution of generator 1 enters the 4th generator 17 through the 4th solution heat exchanger 20, refrigerant vapour and driving heat medium flow are through the 4th generator 17, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 4th generator 17 enters the 3rd generator 12 through the 3rd solution heat exchanger 15, the refrigerant vapour heat release flowing through the 4th generator 17 flows through heat exchanger 16 and the second generator 2 and progressively heat release cooling successively after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Figure 11 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 8, increase by the 4th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, had by 3rd absorber 22 weak solution pipeline to be communicated with generator 1 through the 3rd solution pump 14 and the 3rd solution heat exchanger 15 to be adjusted to the 3rd absorber 22 and to have weak solution pipeline to be communicated with the 4th generator 17 with the 3rd solution heat exchanger 15 through the 3rd solution pump 14,4th generator 17 also has concentrated solution pipeline to be communicated with generator 1 with the 4th solution heat exchanger 20 through the 4th solution pump 19, had by generator 1 concentrated solution pipeline to be communicated with the 3rd generator 12 through the 3rd solution heat exchanger 15 to be adjusted to generator 1 and to have concentrated solution pipeline to be communicated with the 3rd generator 12 with the 3rd solution heat exchanger 15 through the 4th solution heat exchanger 20, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 4th generator 17 after the 4th generator 17 have cryogen liquid pipeline again through heat exchanger 16, second generator 2 is communicated with evaporimeter 6 with second throttle 13,4th generator 17 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 16 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 4th generator 17 and does to drive thermal medium, the weak solution of the 3rd absorber 22 enters the 4th generator 17 through the 3rd solution pump 14 and the 3rd solution heat exchanger 15, refrigerant vapour flows through the 4th generator 17, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 4th generator 17 enters generator 1 through the 4th solution pump 19 and the 4th solution heat exchanger 20, the concentrated solution of generator 1 enters the 3rd generator 12 through the 4th solution heat exchanger 20 and the 3rd solution heat exchanger 15, the refrigerant vapour heat release flowing through the 4th generator 17 flows through heat exchanger 16 and the second generator 2 and progressively heat release cooling successively after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Figure 12 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber 3 weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 10 to be adjusted to absorber 3 and to have weak solution pipeline to be communicated with newly-increased absorber B through newly-increased solution heat exchanger D, newly-increased absorber B has weak solution pipeline to be communicated with the second absorber 4 with solution heat exchanger 10 through newly-increased solution pump C again, had by second generator 2 concentrated solution pipeline to be communicated with absorber 3 through the second solution pump 9 and solution heat exchanger 10 to be adjusted to the second generator 2 and to have concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 10, newly-increased generator A has concentrated solution pipeline to be communicated with absorber 3 with newly-increased solution heat exchanger D through the second solution pump 9 again, newly-increased generator A also has refrigerant steam channel to be communicated with newly-increased absorber B, second generator 2 is had cryogen liquid pipeline through choke valve 7 to be communicated with evaporimeter 6 be adjusted to the second generator 2 have cryogen liquid pipeline to be communicated with newly-increased generator A after newly-increased generator A have cryogen liquid pipeline to be communicated with evaporimeter 6 through choke valve 7 again, newly-increased absorber B also has cooling medium pipeline and ft connection.
(2) in flow process, the weak solution of absorber 3 enters newly-increased absorber B through newly-increased solution heat exchanger D, absorb refrigerant vapour and heat release in cooling medium, the weak solution of newly-increased absorber B enters the second absorber 4 through newly-increased solution pump C and solution heat exchanger 10; The concentrated solution of the second generator 2 enters newly-increased generator A through solution heat exchanger 10, absorbing heat discharges refrigerant vapour and provide to newly-increased absorber B, and the concentrated solution of newly-increased generator A enters absorber 3 through the second solution pump 9 and newly-increased solution heat exchanger D; The cryogen liquid of condenser 5 flows through the second generator 2 and newly-increased generator A also progressively heat release cooling successively, and the cryogen liquid after cooling enters evaporimeter 6 through choke valve 7 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Figure 13 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 2, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber 3 weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 10 to be adjusted to absorber 3 and to have weak solution pipeline to be communicated with newly-increased absorber B through newly-increased solution heat exchanger D, newly-increased absorber B has weak solution pipeline to be communicated with the second absorber 4 with solution heat exchanger 10 through newly-increased solution pump C again, had by second generator 2 concentrated solution pipeline to be communicated with absorber 3 through the second solution pump 9 and solution heat exchanger 10 to be adjusted to the second generator 2 and to have concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 10, newly-increased generator A has concentrated solution pipeline to be communicated with absorber 3 with newly-increased solution heat exchanger D through the second solution pump 9 again, newly-increased generator A also has refrigerant steam channel to be communicated with newly-increased absorber B, second generator 2 is had cryogen liquid pipeline through choke valve 7 to be communicated with evaporimeter 6 be adjusted to the second generator 2 have cryogen liquid pipeline to be communicated with newly-increased generator A after newly-increased generator A have cryogen liquid pipeline to be communicated with evaporimeter 6 through choke valve 7 again, second generator 2 is had cryogen liquid pipeline through second throttle 13 to be communicated with evaporimeter 6 be adjusted to the second generator 2 have cryogen liquid pipeline to be communicated with newly-increased generator A after newly-increased generator A have cryogen liquid pipeline to be communicated with evaporimeter 6 through second throttle 13 again, newly-increased absorber B also has cooling medium pipeline and ft connection.
(2) in flow process, the weak solution of absorber 3 enters newly-increased absorber B through newly-increased solution heat exchanger D, absorb refrigerant vapour and heat release in cooling medium, the weak solution of newly-increased absorber B enters the second absorber 4 through newly-increased solution pump C and solution heat exchanger 10; The concentrated solution of the second generator 2 enters newly-increased generator A through solution heat exchanger 10, absorbing heat discharges refrigerant vapour and provide to newly-increased absorber B, and the concentrated solution of newly-increased generator A enters absorber 3 through the second solution pump 9 and newly-increased solution heat exchanger D; The cryogen liquid of condenser 5 flows through the second generator 2 and newly-increased generator A also progressively heat release cooling successively, and the cryogen liquid after cooling enters evaporimeter 6 through choke valve 7 throttling; The cryogen liquid that 3rd generator 12 produces flows through heat exchanger 16, second generator 2 and newly-increased generator A also progressively heat release cooling successively, and the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Figure 14 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 5, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber 3 weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 10 to be adjusted to absorber 3 and to have weak solution pipeline to be communicated with newly-increased absorber B through newly-increased solution heat exchanger D, newly-increased absorber B has weak solution pipeline to be communicated with the second absorber 4 with solution heat exchanger 10 through newly-increased solution pump C again, had by second generator 2 concentrated solution pipeline to be communicated with absorber 3 through the second solution pump 9 and solution heat exchanger 10 to be adjusted to the second generator 2 and to have concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 10, newly-increased generator A has concentrated solution pipeline to be communicated with absorber 3 with newly-increased solution heat exchanger D through the second solution pump 9 again, newly-increased generator A also has refrigerant steam channel to be communicated with newly-increased absorber B, second generator 2 is had cryogen liquid pipeline through choke valve 7 to be communicated with evaporimeter 6 be adjusted to the second generator 2 have cryogen liquid pipeline to be communicated with newly-increased generator A after newly-increased generator A have cryogen liquid pipeline to be communicated with evaporimeter 6 through choke valve 7 again, second generator 2 is had cryogen liquid pipeline through second throttle 13 to be communicated with evaporimeter 6 be adjusted to the second generator 2 have cryogen liquid pipeline to be communicated with newly-increased generator A after newly-increased generator A have cryogen liquid pipeline to be communicated with evaporimeter 6 through second throttle 13 again, second generator 2 is had cryogen liquid pipeline through the 3rd choke valve 18 to be communicated with evaporimeter 6 be adjusted to the second generator 2 have cryogen liquid pipeline to be communicated with newly-increased generator A after newly-increased generator A have cryogen liquid pipeline to be communicated with evaporimeter 6 through the 3rd choke valve 18 again, newly-increased absorber B also has cooling medium pipeline and ft connection.
(2) in flow process, the weak solution of absorber 3 enters newly-increased absorber B through newly-increased solution heat exchanger D, absorb refrigerant vapour and heat release in cooling medium, the weak solution of newly-increased absorber B enters the second absorber 4 through newly-increased solution pump C and solution heat exchanger 10; The concentrated solution of the second generator 2 enters newly-increased generator A through solution heat exchanger 10, absorbing heat discharges refrigerant vapour and provide to newly-increased absorber B, and the concentrated solution of newly-increased generator A enters absorber 3 through the second solution pump 9 and newly-increased solution heat exchanger D; The cryogen liquid of condenser 5 flows through the second generator 2 and newly-increased generator A also progressively heat release cooling successively, and the cryogen liquid after cooling enters evaporimeter 6 through choke valve 7 throttling; The cryogen liquid that 3rd generator 12 produces flows through the 4th generator 17, heat exchanger 16, second generator 2 and newly-increased generator A and progressively heat release cooling successively, and the cryogen liquid after cooling enters evaporimeter 6 through second throttle 13 throttling; The cryogen liquid that 4th generator 17 produces flows through the second heat exchanger 21, second generator 2 and newly-increased generator A also progressively heat release cooling successively, and the cryogen liquid after cooling enters evaporimeter 6 through the 3rd choke valve 18 throttling, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Figure 15 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by evaporimeter 6 refrigerant steam channel to be communicated with absorber 3 to be adjusted to evaporimeter 6 has refrigerant steam channel to be communicated with newly-increased absorber B, newly-increased absorber B also has weak solution pipeline to be communicated with newly-increased generator A with newly-increased solution heat exchanger D through newly-increased solution pump C, newly-increased generator A also has concentrated solution pipeline to be communicated with newly-increased absorber B through newly-increased solution heat exchanger D, newly-increased generator A also has refrigerant steam channel to be communicated with absorber 3, newly-increased generator A also has driving heat medium pipeline and ft connection, newly-increased absorber B also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that evaporimeter 6 produces enters newly-increased absorber B, the weak solution of newly-increased absorber B enters newly-increased generator A through newly-increased solution pump C and newly-increased solution heat exchanger D, heat medium flow is driven to enter the solution release refrigerant vapour in it through newly-increased generator A, heating and provide to absorber 3, the concentrated solution of newly-increased generator A enters newly-increased absorber B through newly-increased solution heat exchanger D, absorb refrigerant vapour and heat release in heated medium, form the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Figure 16 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 has refrigerant steam channel to be communicated with newly-increased absorber B, newly-increased absorber B also has weak solution pipeline to be communicated with newly-increased generator A with newly-increased solution heat exchanger D through newly-increased solution pump C, newly-increased generator A also has concentrated solution pipeline to be communicated with newly-increased absorber B through newly-increased solution heat exchanger D, newly-increased generator A also has refrigerant steam channel to be communicated with condenser 5, newly-increased generator A also has driving heat medium pipeline and ft connection, newly-increased absorber B also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces enters newly-increased absorber B, the weak solution of newly-increased absorber B enters newly-increased generator A through newly-increased solution pump C and newly-increased solution heat exchanger D, heat medium flow is driven to enter the solution release refrigerant vapour in it through newly-increased generator A, heating and provide to condenser 5, the concentrated solution of newly-increased generator A enters newly-increased absorber B through newly-increased solution heat exchanger D, absorb refrigerant vapour and heat release in heated medium, form the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Figure 17 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, cancel the cooling medium pipeline of the second absorber 4 and ft connection, had by the second generator 2 cryogen liquid pipeline to be communicated with evaporimeter 6 through choke valve 7 and be adjusted to the second generator 2 and have cryogen liquid pipeline to be communicated with evaporimeter 6 with the second absorber 4 through choke valve 7.
(2), in flow process, the cryogen liquid of condenser 5 flows through again through choke valve 7 reducing pressure by regulating flow after the second generator 2 heat release is lowered the temperature, and cryogen liquid flows through the second absorber 4 and absorbs heat and enter evaporimeter 6 after components vaporize, forms the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Figure 18 is used for refrigeration and is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase circulating pump, cancel the cooling medium pipeline of the second absorber 4 and ft connection, the finisher 6 that circulating pump E is communicated with the second absorber 4 and evaporimeter 6 successively by circulatory mediator pipeline is communicated with shape by circulatory mediator pipeline with circulating pump E again and forms closed circuit.
(2) in flow process, circulating thermal medium flows through the second absorber 4 and absorbs heat, then enters circulating pump E after flowing through evaporimeter 6 heat release, forms the 4th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 19 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, add newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber 3 weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 10 to be adjusted to absorber 3 and to have weak solution pipeline to be communicated with newly-increased absorber B through newly-increased solution heat exchanger D, newly-increased absorber B has weak solution pipeline to be communicated with the second absorber 4 with solution heat exchanger 10 through newly-increased solution pump C again, had by second generator 2 concentrated solution pipeline to be communicated with absorber 3 through the second solution pump 9 and solution heat exchanger 10 to be adjusted to the second generator 2 and to have concentrated solution pipeline to be communicated with newly-increased generator A through solution heat exchanger 10, newly-increased generator A has concentrated solution pipeline to be communicated with absorber 3 with newly-increased solution heat exchanger D through the second solution pump 9 again, newly-increased generator A also has refrigerant steam channel to be communicated with newly-increased absorber B, newly-increased generator A also has surplus heat medium pipeline and ft connection, newly-increased absorber B also has cooling medium pipeline and ft connection.
(1) in structure, the weak solution of absorber 3 enters newly-increased absorber B through newly-increased solution heat exchanger D, absorb refrigerant vapour and heat release in cooling medium, the weak solution of newly-increased absorber B enters the second absorber 4 through newly-increased solution pump C and solution heat exchanger 10; The concentrated solution of the second generator 2 enters newly-increased generator A through solution heat exchanger 10, waste heat medium flows through newly-increased generator A, heating enters the solution release refrigerant vapour in it and provides to newly-increased absorber B, the concentrated solution of newly-increased generator A enters absorber 3 through the second solution pump 9 and newly-increased solution heat exchanger D, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 20 is achieved in that
In the 4th class absorption heat pump shown in Fig. 1, the second generator 2 sets up waste heat medium pipeline and ft connection; Cryogen liquid and waste heat medium provide driving thermic load to the second generator 2 jointly, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 21 is achieved in that
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by second generator 2 refrigerant steam channel to be communicated with the second absorber 4 to be adjusted to the second generator 2 has refrigerant steam channel to be communicated with newly-increased absorber B, newly-increased absorber B also has weak solution pipeline to be communicated with newly-increased generator A with newly-increased solution heat exchanger D through newly-increased solution pump C, newly-increased generator A also has concentrated solution pipeline to be communicated with newly-increased absorber B through newly-increased solution heat exchanger D, newly-increased generator A also has refrigerant steam channel to be communicated with the second absorber 4, newly-increased generator A also has surplus heat medium pipeline and ft connection, newly-increased absorber B also has cooling medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that second generator 2 produces enters newly-increased absorber B, the weak solution of newly-increased absorber B enters newly-increased generator A through newly-increased solution pump C and newly-increased solution heat exchanger D, waste heat medium flows through newly-increased generator A, heating enters the solution release refrigerant vapour in it and provides to the second absorber 4, the concentrated solution of newly-increased generator A enters newly-increased absorber B through newly-increased solution heat exchanger D, absorb refrigerant vapour and heat release in cooling medium, form the 5th class absorption heat pump.
The effect that the technology of the present invention can realize---the 4th class absorption heat pump proposed by the invention and the 5th class absorption heat pump, have following effect and advantage:
(1) propose new approaches, new ideas and new technology that the temperature difference utilizes, will further developing and applying of absorption heat pump technology be promoted.
(2) high temperature cryogen liquid can be solved well to the negative effect of UTILIZATION OF VESIDUAL HEAT IN degree, especially to the absorption heat pump flow process being Typical Representative with TFE-TDE solution, performance index and the utilization rate of waste heat of absorption heat pump can be significantly improved.
(3) temperature difference producing level is expanded under low temperature cold environment or heated medium temperature, further increase the temperature difference and utilize level, and the performance index reduction brought to Environment release heat energy because of cryogen liquid is played to suppression and made up effect.
(4) can reduce the requirement of driving heat medium temperature, or improve the degree of UTILIZATION OF VESIDUAL HEAT IN, maybe can utilize the residual heat resources of lower temperature.
(5) provide multiple concrete technical scheme, numerous different actual state can be tackled, have the wider scope of application.
(6) enriched the type of absorption heat pump, extended the range of application of absorption heat pump, be conducive to adopting absorption heat pump to realize making full use of of the temperature difference better.

Claims (51)

1. the 4th class absorption heat pump, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, choke valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger; absorber (3) has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (10), second absorber (4) also has weak solution pipeline to be communicated with generator (1) with the second solution heat exchanger (11) through solution pump (8), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (11), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (10) through the second solution pump (9), generator (1) also has refrigerant steam channel to be communicated with condenser (5), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), condenser (5) also have cryogen liquid pipeline be communicated with the second generator (2) after the second generator (2) have cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) again, evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), generator (1) also has driving heat medium pipeline and ft connection, absorber (3) and condenser (5) also have heated medium pipeline and ft connection respectively, evaporimeter (6) also has surplus heat medium pipeline and ft connection, second absorber (4) also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
2. the 4th class absorption heat pump, in the 4th class absorption heat pump according to claim 1, cancel choke valve, there is by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 4th class absorption heat pump.
3. the 4th class absorption heat pump, in the 4th class absorption heat pump according to claim 1, increase by the 3rd generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, second absorber (4) is set up weak solution pipeline and is communicated with the 3rd generator (12) with the 3rd solution heat exchanger (15) through the 3rd solution pump (14), 3rd generator (12) also has concentrated solution pipeline to be communicated with the second generator (2) through the 3rd solution heat exchanger (15), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 3rd generator (12) after the 3rd generator (12) have cryogen liquid pipeline again through heat exchanger (16), second generator (2) is communicated with evaporimeter (6) with second throttle (13), 3rd generator (12) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (16) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
4. the 4th class absorption heat pump, in the 4th class absorption heat pump according to claim 1, increase by the 3rd generator, second throttle, 3rd solution heat exchanger and heat exchanger, had by second absorber (4) weak solution pipeline to be communicated with generator (1) through solution pump (8) and the second solution heat exchanger (11) to be adjusted to the second absorber (4) and to have weak solution pipeline through solution pump (8), second solution heat exchanger (11) is communicated with generator (1) with the 3rd solution heat exchanger (15), had by generator (1) concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (11) to be adjusted to generator (1) and to have concentrated solution pipeline to be communicated with the 3rd generator (12) through the 3rd solution heat exchanger (15), 3rd generator (12) has concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (11) again, had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 3rd generator (12) after the 3rd generator (12) have cryogen liquid pipeline again through heat exchanger (16), second generator (2) is communicated with evaporimeter (6) with second throttle (13), 3rd generator (12) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (16) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
5. the 4th class absorption heat pump, in the 4th class absorption heat pump according to claim 1, increase by the 3rd generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, had by second absorber (4) weak solution pipeline to be communicated with generator (1) through solution pump (8) and the second solution heat exchanger (11) to be adjusted to the second absorber (4) and to have weak solution pipeline to be communicated with the 3rd generator (12) with the second solution heat exchanger (11) through solution pump (8), 3rd generator (12) has concentrated solution pipeline to be communicated with generator (1) with the 3rd solution heat exchanger (15) through the 3rd solution pump (14) again, had by generator (1) concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (11) to be adjusted to generator (1) and to have concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (11) through the 3rd solution heat exchanger (15), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 3rd generator (12) after the 3rd generator (12) have cryogen liquid pipeline again through heat exchanger (16), second generator (2) is communicated with evaporimeter (6) with second throttle (13), 3rd generator (12) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (16) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
6. the 4th class absorption heat pump, in arbitrary 4th class absorption heat pump described in claim 3-5, cancel choke valve and second throttle, had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 4th class absorption heat pump.
7. the 4th class absorption heat pump, in the 4th class absorption heat pump according to claim 3, increase by the 4th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, second absorber (4) is set up weak solution pipeline and is communicated with the 4th generator (17) with the 4th solution heat exchanger (20) through the 4th solution pump (19), 4th generator (17) also has concentrated solution pipeline to be communicated with the second generator (2) through the 4th solution heat exchanger (20), 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), had by 3rd generator (12) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 3rd generator (12) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline again through the second heat exchanger (21), second generator (2) is communicated with evaporimeter (6) with the 3rd choke valve (18), 3rd generator (12) there is cryogen liquid pipeline through heat exchanger (16), second generator (2) and second throttle (13) are communicated with evaporimeter (6) and are adjusted to the 3rd generator (12) and have cryogen liquid pipeline through the 4th generator (17), heat exchanger (16), second generator (2) is communicated with evaporimeter (6) with second throttle (13), second heat exchanger (21) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
8. the 4th class absorption heat pump, in the 4th class absorption heat pump according to claim 4, increase by the 4th generator, 3rd choke valve, 4th solution heat exchanger and the second heat exchanger, second absorber (4) there is weak solution pipeline through solution pump (8), second solution heat exchanger (11) and the 3rd solution heat exchanger (15) are communicated with generator (1) and are adjusted to the second absorber (4) and have weak solution pipeline through solution pump (8), 4th solution heat exchanger (20), second solution heat exchanger (11) is communicated with generator (1) with the 3rd solution heat exchanger (15), had by 3rd generator (12) concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (11) to be adjusted to the 3rd generator (12) and to have concentrated solution pipeline to be communicated with the 4th generator (17) through the second solution heat exchanger (11), 4th generator (17) has concentrated solution pipeline to be communicated with the second generator (2) through the 4th solution heat exchanger (20) again, 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), had by 3rd generator (12) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 3rd generator (12) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline again through the second heat exchanger (21), second generator (2) is communicated with evaporimeter (6) with the 3rd choke valve (18), 3rd generator (12) there is cryogen liquid pipeline through heat exchanger (16), second generator (2) and second throttle (13) are communicated with evaporimeter (6) and are adjusted to the 3rd generator (12) and have cryogen liquid pipeline through the 4th generator (17), heat exchanger (16), second generator (2) is communicated with evaporimeter (6) with second throttle (13), second heat exchanger (21) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
9. the 4th class absorption heat pump, in the 4th class absorption heat pump according to claim 5, increase by the 4th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, had by second absorber (4) weak solution pipeline to be communicated with the 3rd generator (12) through solution pump (8) and the second solution heat exchanger (11) to be adjusted to the second absorber (4) and to have weak solution pipeline to be communicated with the 4th generator (17) with the second solution heat exchanger (11) through solution pump (8), 4th generator (17) has concentrated solution pipeline to be communicated with the 3rd generator (12) with the 4th solution heat exchanger (20) through the 4th solution pump (19) again, had by generator (1) concentrated solution pipeline to be communicated with the second generator (2) through the 3rd solution heat exchanger (15) and the second solution heat exchanger (11) to be adjusted to generator (1) and to have concentrated solution pipeline through the 3rd solution heat exchanger (15), 4th solution heat exchanger (20) is communicated with the second generator (2) with the second solution heat exchanger (11), 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), had by 3rd generator (12) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 3rd generator (12) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline again through the second heat exchanger (21), second generator (2) is communicated with evaporimeter (6) with the 3rd choke valve (18), 3rd generator (12) there is cryogen liquid pipeline through heat exchanger (16), second generator (2) and second throttle (13) are communicated with evaporimeter (6) and are adjusted to the 3rd generator (12) and have cryogen liquid pipeline through the 4th generator (17), heat exchanger (16), second generator (2) is communicated with evaporimeter (6) with second throttle (13), second heat exchanger (21) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
10. the 4th class absorption heat pump, in arbitrary 4th class absorption heat pump described in claim 7-9, cancel choke valve, second throttle and the 3rd choke valve, had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through the 3rd choke valve (18) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 4th class absorption heat pump.
11. the 4th class absorption heat pumps, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 3rd generator, the 3rd solution pump, the 3rd solution heat exchanger and the 3rd absorber; absorber (3) has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (10), second absorber (4) also has weak solution pipeline to be communicated with the 3rd absorber (22) with the second solution heat exchanger (11) through solution pump (8), 3rd absorber (22) also has weak solution pipeline to be communicated with generator (1) with the 3rd solution heat exchanger (15) through the 3rd solution pump (14), generator (1) also has concentrated solution pipeline to be communicated with the 3rd generator (12) through the 3rd solution heat exchanger (15), 3rd generator (12) also has concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (11), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (10) through the second solution pump (9), generator (1) also has refrigerant steam channel to be communicated with condenser (5), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), 3rd generator (12) also has refrigerant steam channel to be communicated with the 3rd absorber (22), condenser (5) also have cryogen liquid pipeline be communicated with the second generator (2) after the second generator (2) have cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) again, evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), generator (1) and the 3rd generator (12) also have driving heat medium pipeline and ft connection respectively, absorber (3), condenser (5) and the 3rd absorber (22) also have heated medium pipeline and ft connection respectively, evaporimeter (6) also has surplus heat medium pipeline and ft connection, second absorber (4) also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
12. the 4th class absorption heat pumps, in the 4th class absorption heat pump according to claim 11, cancel choke valve, there is by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 4th class absorption heat pump.
13. the 4th class absorption heat pumps, in the 4th class absorption heat pump according to claim 11, increase by the 4th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, 3rd absorber (22) is set up weak solution pipeline and is communicated with the 4th generator (17) with the 4th solution heat exchanger (20) through the 4th solution pump (19), 4th generator (17) also has concentrated solution pipeline to be communicated with the 3rd generator (12) through the 4th generator (20), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline again through heat exchanger (16), second generator (2) is communicated with evaporimeter (6) with second throttle (13), 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (16) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
14. the 4th class absorption heat pumps, in the 4th class absorption heat pump according to claim 11, increase by the 4th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by 3rd absorber (22) weak solution pipeline to be communicated with generator (1) through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) to be adjusted to the 3rd absorber (22) and to have weak solution pipeline through the 3rd solution pump (14), 3rd solution heat exchanger (15) is communicated with generator (1) with the 4th solution heat exchanger (20), had by generator (1) concentrated solution pipeline to be communicated with the 3rd generator (12) through the 3rd solution heat exchanger (15) to be adjusted to generator (1) and to have concentrated solution pipeline to be communicated with the 4th generator (17) through the 4th solution heat exchanger (20), 4th generator (17) has concentrated solution pipeline to be communicated with the 3rd generator (12) through the 3rd solution heat exchanger (15) again, had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline again through heat exchanger (16), second generator (2) is communicated with evaporimeter (6) with second throttle (13), 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (16) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
15. the 4th class absorption heat pumps, in the 4th class absorption heat pump according to claim 11, increase by the 4th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, had by 3rd absorber (22) weak solution pipeline to be communicated with generator (1) through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) to be adjusted to the 3rd absorber (22) and to have weak solution pipeline to be communicated with the 4th generator (17) with the 3rd solution heat exchanger (15) through the 3rd solution pump (14), 4th generator (17) also has concentrated solution pipeline to be communicated with generator (1) with the 4th solution heat exchanger (20) through the 4th solution pump (19), had by generator (1) concentrated solution pipeline to be communicated with the 3rd generator (12) through the 3rd solution heat exchanger (15) to be adjusted to generator (1) and to have concentrated solution pipeline to be communicated with the 3rd generator (12) with the 3rd solution heat exchanger (15) through the 4th solution heat exchanger (20), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline again through heat exchanger (16), second generator (2) is communicated with evaporimeter (6) with second throttle (13), 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (16) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
16. the 4th class absorption heat pumps are in arbitrary 4th class absorption heat pump described in claim 13-15, and the 4th generator (17) is set up and driven heat medium pipeline and ft connection, forms the 4th class absorption heat pump.
17. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in claim 13-16, cancel choke valve and second throttle, had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 4th class absorption heat pump.
18. the 4th class absorption heat pumps, in claim 1 or the 4th class absorption heat pump according to claim 11, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber (3) weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (10) to be adjusted to absorber (3) and to have weak solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased absorber (B) has weak solution pipeline to be communicated with the second absorber (4) with solution heat exchanger (10) through newly-increased solution pump (C) again, had by second generator (2) concentrated solution pipeline to be communicated with absorber (3) through the second solution pump (9) and solution heat exchanger (10) to be adjusted to the second generator (2) and to have concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (10), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (3) with newly-increased solution heat exchanger (D) through the second solution pump (9) again, newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased absorber (B), second generator (2) is had cryogen liquid pipeline through choke valve (7) to be communicated with evaporimeter (6) be adjusted to the second generator (2) have cryogen liquid pipeline to be communicated with newly-increased generator (A) after newly-increased generator (A) have cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) again, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
19. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump according to claim 18, cancel choke valve, generator (A) will be increased newly have cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to newly-increased generator (A) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 4th class absorption heat pump.
20. the 4th class absorption heat pumps, at claim 3-5, in arbitrary 4th class absorption heat pump described in 13-16, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber (3) weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (10) to be adjusted to absorber (3) and to have weak solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased absorber (B) has weak solution pipeline to be communicated with the second absorber (4) with solution heat exchanger (10) through newly-increased solution pump (C) again, had by second generator (2) concentrated solution pipeline to be communicated with absorber (3) through the second solution pump (9) and solution heat exchanger (10) to be adjusted to the second generator (2) and to have concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (10), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (3) with newly-increased solution heat exchanger (D) through the second solution pump (9) again, newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased absorber (B), second generator (2) is had cryogen liquid pipeline through choke valve (7) to be communicated with evaporimeter (6) be adjusted to the second generator (2) have cryogen liquid pipeline to be communicated with newly-increased generator (A) after newly-increased generator (A) have cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) again, second generator (2) is had cryogen liquid pipeline through second throttle (13) to be communicated with evaporimeter (6) be adjusted to the second generator (2) have cryogen liquid pipeline to be communicated with newly-increased generator (A) after newly-increased generator (A) have cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) again, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
21. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump according to claim 20, cancel choke valve and second throttle, generator (A) will be increased newly have cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to newly-increased generator (A) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), generator (A) will be increased newly have cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) to be adjusted to newly-increased generator (A) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 4th class absorption heat pump.
22. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in claim 7-9, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber (3) weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (10) to be adjusted to absorber (3) and to have weak solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased absorber (B) has weak solution pipeline to be communicated with the second absorber (4) with solution heat exchanger (10) through newly-increased solution pump (C) again, had by second generator (2) concentrated solution pipeline to be communicated with absorber (3) through the second solution pump (9) and solution heat exchanger (10) to be adjusted to the second generator (2) and to have concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (10), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (3) with newly-increased solution heat exchanger (D) through the second solution pump (9) again, newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased absorber (B), second generator (2) is had cryogen liquid pipeline through choke valve (7) to be communicated with evaporimeter (6) be adjusted to the second generator (2) have cryogen liquid pipeline to be communicated with newly-increased generator (A) after newly-increased generator (A) have cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) again, second generator (2) is had cryogen liquid pipeline through second throttle (13) to be communicated with evaporimeter (6) be adjusted to the second generator (2) have cryogen liquid pipeline to be communicated with newly-increased generator (A) after newly-increased generator (A) have cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) again, second generator (2) is had cryogen liquid pipeline through the 3rd choke valve (18) to be communicated with evaporimeter (6) be adjusted to the second generator (2) have cryogen liquid pipeline to be communicated with newly-increased generator (A) after newly-increased generator (A) have cryogen liquid pipeline to be communicated with evaporimeter (6) through the 3rd choke valve (18) again, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
23. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump according to claim 22, cancel choke valve, second throttle and the 3rd choke valve, generator (A) will be increased newly have cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to newly-increased generator (A) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), generator (A) will be increased newly have cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) to be adjusted to newly-increased generator (A) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), generator (A) will be increased newly have cryogen liquid pipeline to be communicated with evaporimeter (6) through the 3rd choke valve (18) to be adjusted to newly-increased generator (A) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 4th class absorption heat pump.
24. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in claim 1-17, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to evaporimeter (6) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with absorber (3), newly-increased generator (A) also has driving heat medium pipeline and ft connection, newly-increased absorber (B) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
25. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in claim 18-23, increase newly-increased second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, being had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to evaporimeter (6) has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased second absorber through newly-increased second solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with absorber (3), newly-increased second generator also has driving heat medium pipeline and ft connection, newly-increased second absorber also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
26. the 4th class absorption heat pumps, at claim 1-2, in arbitrary 4th class absorption heat pump described in 11-12, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with condenser (5), newly-increased generator (A) also has driving heat medium pipeline and ft connection, newly-increased absorber (B) also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
27. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in claim 18-19, increase newly-increased second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, being had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased second absorber through newly-increased second solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with condenser, newly-increased second generator also has driving heat medium pipeline and ft connection, newly-increased second absorber also has heated medium pipeline and ft connection, form the 4th class absorption heat pump.
28. the 4th class absorption heat pumps, in claim 1 or the 4th class absorption heat pump according to claim 11, cancel the cooling medium pipeline of the second absorber (4) and ft connection, there is by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6) with the second absorber (4) through choke valve (7), form the 4th class absorption heat pump.
29. the 4th class absorption heat pumps, at claim 3-5, in arbitrary 4th class absorption heat pump described in 13-16, cancel the cooling medium pipeline of the second absorber (4) and ft connection, had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6) with the second absorber (4) through choke valve (7), had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6) with the second absorber (4) through second throttle (7), form the 4th class absorption heat pump.
30. the 4th class absorption heat pumps, at claim 3-5, in arbitrary 4th class absorption heat pump described in 13-16, cancel the cooling medium pipeline of the second absorber (4) and ft connection, had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6) with the second absorber (4) through choke valve (7), or to be had by the second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6) with the second absorber (4) through second throttle (7), form the 4th class absorption heat pump.
31. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in claim 7-9, cancel the cooling medium pipeline of the second absorber (4) and ft connection, and the one-out-three of carrying out in following Adjusted Option, three select two or three to select three, obtain the 4th class absorption heat pump: Adjusted Option one, had by the second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6) with the second absorber (4) through choke valve (7), Adjusted Option two is had by the second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6) with the second absorber (4) through second throttle (7), Adjusted Option three is had by the second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through the 3rd choke valve (18) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6) with the second absorber (4) through the 3rd choke valve (18).
32. the 4th class absorption heat pumps, in arbitrary 4th class absorption heat pump according to claim 18, cancel the cooling medium pipeline of the second absorber (4) and ft connection, cancel the cooling medium pipeline of newly-increased absorber (B) and ft connection, generator (A) will be increased newly have cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to newly-increased generator (A) and to have cryogen liquid pipeline through choke valve (7), second absorber (4) is communicated with evaporimeter (6) with newly-increased absorber (A), form the 4th class absorption heat pump.
33. the 4th class absorption heat pumps, be claim 1,3-5,7-9,11, in arbitrary 4th class absorption heat pump described in 13-16, cancel the cooling medium pipeline of the second absorber (4) and ft connection, 1. circulating pump is increased, circulating pump (E) has circulatory mediator pipeline to be communicated with the second absorber (4) successively has circulatory mediator pipeline be communicated with shape with circulating pump (E) and form closed circuit with the finisher (6) of evaporimeter (6) again, forms the 4th class absorption heat pump; 2. increase intermediate heat exchanger, intermediate heat exchanger is communicated with the second absorber 4 and evaporimeter 6, forms the 4th class absorption heat pump.
34. the 4th class absorption heat pumps, in claim 18, 20, in arbitrary 4th class absorption heat pump described in 22, increase circulating pump, cancel the cooling medium pipeline of the second absorber (4) and ft connection, cancel the cooling medium pipeline of newly-increased absorber (B) and ft connection, circulating pump (E) has circulatory mediator pipeline to be communicated with newly-increased absorber (B) successively, second absorber (4) has circulatory mediator pipeline be communicated with shape with circulating pump (E) and form closed circuit with the finisher (6) of evaporimeter (6) again, form the 4th class absorption heat pump.
35. the 5th class absorption heat pumps, in claim 1 or the 4th class absorption heat pump according to claim 11, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber (3) weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (10) to be adjusted to absorber (3) and to have weak solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased absorber (B) has weak solution pipeline to be communicated with the second absorber (4) with solution heat exchanger (10) through newly-increased solution pump (C) again, had by second generator (2) concentrated solution pipeline to be communicated with absorber (3) through the second solution pump (9) and solution heat exchanger (10) to be adjusted to the second generator (2) and to have concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (10), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (3) with newly-increased solution heat exchanger (D) through the second solution pump (9) again, newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased generator (A) also has surplus heat medium pipeline and ft connection, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
36. the 5th class absorption heat pumps, in arbitrary 4th class absorption heat pump according to claim 35, cancel choke valve, there is by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 5th class absorption heat pump.
37. the 5th class absorption heat pumps, at claim 3-5, in arbitrary 5th class absorption heat pump described in 13-16, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber (3) weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (10) to be adjusted to absorber (3) and to have weak solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased absorber (B) has weak solution pipeline to be communicated with the second absorber (4) with solution heat exchanger (10) through newly-increased solution pump (C) again, had by second generator (2) concentrated solution pipeline to be communicated with absorber (3) through the second solution pump (9) and solution heat exchanger (10) to be adjusted to the second generator (2) and to have concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (10), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (3) with newly-increased solution heat exchanger (D) through the second solution pump (9) again, newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased generator (A) also has surplus heat medium pipeline and ft connection, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 4th class absorption heat pump.
38. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump according to claim 37, cancel choke valve and second throttle, had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 5th class absorption heat pump.
39. the 5th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in claim 7-9, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, had by absorber (3) weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (10) to be adjusted to absorber (3) and to have weak solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased absorber (B) has weak solution pipeline to be communicated with the second absorber (4) with solution heat exchanger (10) through newly-increased solution pump (C) again, had by second generator (2) concentrated solution pipeline to be communicated with absorber (3) through the second solution pump (9) and solution heat exchanger (10) to be adjusted to the second generator (2) and to have concentrated solution pipeline to be communicated with newly-increased generator (A) through solution heat exchanger (10), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorber (3) with newly-increased solution heat exchanger (D) through the second solution pump (9) again, newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased generator (A) also has surplus heat medium pipeline and ft connection, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
40. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump according to claim 39, cancel choke valve, second throttle and the 3rd choke valve, had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (7) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through second throttle (13) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), had by second generator (2) cryogen liquid pipeline to be communicated with evaporimeter (6) through the 3rd choke valve (18) to be adjusted to the second generator (2) and to have cryogen liquid pipeline to be communicated with evaporimeter (6), form the 5th class absorption heat pump.
41. the 5th class absorption heat pumps are that the second generator (2) sets up waste heat medium pipeline and ft connection in arbitrary 4th class absorption heat pump described in claim 1-17,28-34, form the 5th class absorption heat pump.
42. the 5th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in claim 18-23, second generator (2) and newly-increased generator (A) set up waste heat medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
43. the 5th class absorption heat pumps, in arbitrary 4th class absorption heat pump described in claim 18-23, second generator (2) or newly-increased generator (A) set up waste heat medium pipeline and ft connection, form the 5th class absorption heat pump.
44. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump according to claim 41, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to evaporimeter (6) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with absorber (3), newly-increased generator (A) also has driving heat medium pipeline and ft connection, newly-increased absorber (B) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
45. the 5th class absorption heat pumps, at claim 35-38, in arbitrary 5th class absorption heat pump described in 42-43, increase newly-increased second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, being had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to evaporimeter (6) has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased second absorber through newly-increased second solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with absorber (3), newly-increased second generator also has driving heat medium pipeline and ft connection, newly-increased second absorber also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
46. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 1-17, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by second generator (2) refrigerant steam channel to be communicated with the second absorber (4) to be adjusted to the second generator (2) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with the second absorber (4), newly-increased generator (A) also has surplus heat medium pipeline and ft connection, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
47. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 35-40, increase newly-increased second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, generator (A) will be increased newly have refrigerant steam channel to be communicated with newly-increased absorber (B) to be adjusted to newly-increased generator (A) and have refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased second absorber through newly-increased second solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased second generator also has surplus heat medium pipeline and ft connection, newly-increased second absorber also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
48. the 5th class absorption heat pumps are that the second generator (2) sets up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in claim 45-47, form the 5th class absorption heat pump.
49. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 18-23, increase newly-increased second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, generator (A) will be increased newly have refrigerant steam channel to be communicated with newly-increased absorber (B) to be adjusted to newly-increased generator (A) and have refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased second absorber through newly-increased second solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased second generator also has surplus heat medium pipeline and ft connection, newly-increased second absorber also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
50. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump according to claim 49, second generator (2) and newly-increased generator (A) set up waste heat medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
51. the 5th class absorption heat pumps are that the second generator (2) or newly-increased generator (A) set up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump according to claim 49, form the 5th class absorption heat pump.
CN201510144105.9A 2014-03-27 2015-03-24 4th class absorption heat pump and the 5th class absorption heat pump Active CN104807239B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510144105.9A CN104807239B (en) 2014-03-27 2015-03-24 4th class absorption heat pump and the 5th class absorption heat pump

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CN2014101341997 2014-03-27
CN201410134199 2014-03-27
CN201510144105.9A CN104807239B (en) 2014-03-27 2015-03-24 4th class absorption heat pump and the 5th class absorption heat pump

Publications (2)

Publication Number Publication Date
CN104807239A true CN104807239A (en) 2015-07-29
CN104807239B CN104807239B (en) 2018-05-08

Family

ID=53692292

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510144105.9A Active CN104807239B (en) 2014-03-27 2015-03-24 4th class absorption heat pump and the 5th class absorption heat pump

Country Status (2)

Country Link
CN (1) CN104807239B (en)
WO (1) WO2015143926A1 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106322815A (en) * 2015-09-28 2017-01-11 李华玉 Fifth-class absorption heat pump
CN106369865A (en) * 2016-05-30 2017-02-01 李华玉 Double-effect fourth-class and fifth-class absorption heat pump
CN106403367A (en) * 2015-09-05 2017-02-15 李华玉 Fourth thermally-driven compression-absorption type heat pump
CN106440473A (en) * 2015-09-28 2017-02-22 李华玉 Fifth-type absorption heat pump
CN112984860A (en) * 2020-02-21 2021-06-18 李华玉 Absorption-compression heat pump of the third/fourth type
CN115218536A (en) * 2020-02-21 2022-10-21 李华玉 Third/fourth type heat-driven absorption-compression heat pump
CN115355629A (en) * 2020-02-21 2022-11-18 李华玉 Third/fourth absorption heat pump

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4520634A (en) * 1983-04-13 1985-06-04 Hitachi, Ltd. Multi-stage absorption refrigeration system
CN101182962A (en) * 2007-11-25 2008-05-21 李华玉 Composite absorption heat pump
CN102200358A (en) * 2010-06-29 2011-09-28 上海理工大学 Two-stage double-effect lithium bromide (LiBr) refrigeration-heat pump cycle system
CN102305489A (en) * 2011-08-19 2012-01-04 李华玉 Compound first-class absorption heat pump based on single-effect flow
CN102538279A (en) * 2012-02-03 2012-07-04 李华玉 Triple-generation double absorption system and third-class absorption heat pump
CN102679612A (en) * 2012-05-14 2012-09-19 李华玉 Fractional condensation third-class absorption type heat pump

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101776343A (en) * 2009-11-09 2010-07-14 李华玉 Solution series circulated two-stage first-type absorption heat pump using single effect as first stage
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
CN102419026B (en) * 2011-07-27 2013-11-20 李华玉 Absorption-type heat source temperature changer

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4520634A (en) * 1983-04-13 1985-06-04 Hitachi, Ltd. Multi-stage absorption refrigeration system
CN101182962A (en) * 2007-11-25 2008-05-21 李华玉 Composite absorption heat pump
CN102200358A (en) * 2010-06-29 2011-09-28 上海理工大学 Two-stage double-effect lithium bromide (LiBr) refrigeration-heat pump cycle system
CN102305489A (en) * 2011-08-19 2012-01-04 李华玉 Compound first-class absorption heat pump based on single-effect flow
CN102538279A (en) * 2012-02-03 2012-07-04 李华玉 Triple-generation double absorption system and third-class absorption heat pump
CN102679612A (en) * 2012-05-14 2012-09-19 李华玉 Fractional condensation third-class absorption type heat pump

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106403367A (en) * 2015-09-05 2017-02-15 李华玉 Fourth thermally-driven compression-absorption type heat pump
CN106322815A (en) * 2015-09-28 2017-01-11 李华玉 Fifth-class absorption heat pump
CN106440473A (en) * 2015-09-28 2017-02-22 李华玉 Fifth-type absorption heat pump
CN106440473B (en) * 2015-09-28 2020-06-16 李华玉 Fifth-class absorption heat pump
CN106369865A (en) * 2016-05-30 2017-02-01 李华玉 Double-effect fourth-class and fifth-class absorption heat pump
CN112984860A (en) * 2020-02-21 2021-06-18 李华玉 Absorption-compression heat pump of the third/fourth type
CN115218536A (en) * 2020-02-21 2022-10-21 李华玉 Third/fourth type heat-driven absorption-compression heat pump
CN115355629A (en) * 2020-02-21 2022-11-18 李华玉 Third/fourth absorption heat pump

Also Published As

Publication number Publication date
CN104807239B (en) 2018-05-08
WO2015143926A1 (en) 2015-10-01

Similar Documents

Publication Publication Date Title
CN104807239A (en) Absorption heat pump of fourth class and absorption heat pump of fifth class
CN104807240A (en) Fifth type absorption heat pump
CN106016821A (en) First-class heat drive compression-absorption type heat pump
CN103851823B (en) Compound generation first-class absorption type heat pump
CN104807235A (en) Fifth type absorption heat pump
CN104807241A (en) Class four absorption type heat pump and class five absorption type heat pump
CN104807236A (en) Class five absorption type heat pump
CN104833128A (en) Fourth type absorption heat pump
CN104748439A (en) Heat and power combined supplying system
CN105841401A (en) First-kind heat drive compression-absorption type heat pump
CN105953464A (en) Fourth kind thermal-driving compression-absorption type heat pump
CN209371561U (en) A kind of superhigh temperature non-azeotropic working medium heat pump unit
CN104807238A (en) Absorption heat pump of fourth class and absorption heat pump of fifth class
CN103148631B (en) Compound generation first-class absorption type heat pump
CN105953467A (en) Fourth kind thermal-driving compression-absorption type heat pump
CN105953465A (en) Fourth kind thermal-driving compression-absorption type heat pump
CN105546877A (en) Gravitational field low-grade heat source conversion device and method
CN103486757B (en) Branch-cycle first-class absorption type heat pump
CN103697615B (en) Multiterminal heat supply the 3rd class absorption heat pump
CN104180555A (en) Cool double-effect lithium bromide spray absorption type refrigeration cycle system
CN103148630B (en) Composite-generationsecond second kind absorption type heat pump
CN105928246A (en) Class-V thermally-driven compression-absorption type heat pump
CN102434996B (en) Secondary absorption heat pump adopting classified generation mode
CN105910341A (en) First kind thermal driving compression-absorption heat pump
CN103196256B (en) Composite-generationsecond second kind absorption type heat pump

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
EXSB Decision made by sipo to initiate substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant