CN103940142B - Branch-cycle first-class absorption type heat pump - Google Patents

Branch-cycle first-class absorption type heat pump Download PDF

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CN103940142B
CN103940142B CN201410138252.0A CN201410138252A CN103940142B CN 103940142 B CN103940142 B CN 103940142B CN 201410138252 A CN201410138252 A CN 201410138252A CN 103940142 B CN103940142 B CN 103940142B
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absorber
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increased
solution
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CN103940142A (en
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李华玉
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • 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
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00—Devices or apparatus used for air treatment
    • F24F2203/02—System or Device comprising a heat pump as a subsystem, e.g. combined with humidification/dehumidification, heating, natural energy or with hybrid system
    • F24F2203/026—Absorption - desorption cycle
    • 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

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

Abstract

The present invention provides Branch-cycle first-class absorption type heat pump, belongs to refrigeration and technical field of heat pumps.Absorber connects generator through solution pump with solution heat exchanger, and generator connects absorber through solution heat exchanger, and generator has refrigerant steam channel to connect condenser, and condenser connects vaporizer through choke valve, and vaporizer has refrigerant steam channel to connect absorber；Second absorber connects a point steam chest through the second solution pump, the second solution heat exchanger with absorber, steam chest is divided to connect the second absorber through the second solution heat exchanger, steam chest is divided to have refrigerant steam channel to connect the second condenser, second condenser connects the second vaporizer through second throttle, and the second vaporizer has refrigerant steam channel to connect the second absorber；Generator connection drives heat medium pipeline, and the second absorber, condenser and the second condenser are respectively communicated with heated medium pipeline, vaporizer and the second vaporizer and are respectively communicated with waste heat medium pipeline, forms Branch-cycle first-class absorption type heat pump.

Description

Branch-cycle first-class absorption type heat pump
Technical field:
The invention belongs to low temperature heat and absorption type heat pump.
Background technology:
Utilize in terms of angle from the temperature difference, first-class absorption type heat pump is to drive the temperature difference between thermal medium and heated medium as driving force, should use twice when driving the temperature difference bigger or repeatedly the temperature difference utilizes flow process to improve the degree that the temperature difference utilizes, thus realize the high efficiency of heat energy utilization；And from the point of view of working media, the working media of absorption heat pump is solution, being limited by physical property, each solution has its working range being suitable for；So, when driving the temperature of thermal medium and temperature drop beyond the working range of single solution, different solution should be used to carry out Branch-cycle and to complete driving the temperature difference to make full use of, the effect i.e. driving the temperature difference is embodied in respectively in different solution circulation loop, it is achieved drive the rationalization that the temperature difference utilizes.
While considering to make full use of the temperature difference, the circulation process of first-class absorption type heat pump also to realize more requirement, and these requirements include: thermodynamic parameter smooth change, heating parameter scalable, it is possible to preferably adaptation condition change, has optimal performance index；It is capable of the deep exploitation to high temperature heat source, or utilizes the thermal source of different grade to realize its comprehensive utilization etc..
Summary of the invention:
Present invention is primarily intended to Branch-cycle first-class absorption type heat pump to be provided, use two-way or three road solution circulations, the making full use of of the temperature difference is done step-by-step, concrete summary of the invention subitem is described below:
1. Branch-cycle first-class absorption type heat pump, is mainly made up of generator, absorber, the second absorber, condenser, the second condenser, vaporizer, the second vaporizer, solution pump, the second solution pump, choke valve, second throttle, solution heat exchanger, the second solution heat exchanger and a point steam chest；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, generator also has refrigerant steam channel to connect with condenser, condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer also has refrigerant steam channel to connect with absorber；Second absorber has weak solution pipeline to connect with a point steam chest through the second solution pump, the second solution heat exchanger and absorber, steam chest is divided to also have concentrated solution pipeline to connect through the second solution heat exchanger and the second absorber, steam chest is divided to also have refrigerant steam channel to connect with the second condenser, second condenser also has cryogen liquid pipeline to connect with the second vaporizer through second throttle, and the second vaporizer also has refrigerant steam channel to connect with the second absorber；Generator also has driving heat medium pipeline and ft connection, second absorber, condenser and the second condenser have heated medium pipeline and ft connection the most respectively, vaporizer and the second vaporizer have surplus heat medium pipeline and ft connection the most respectively, form Branch-cycle first-class absorption type heat pump.
2. Branch-cycle first-class absorption type heat pump, it is in the 1st described Branch-cycle first-class absorption type heat pump, increase by the 3rd generator, 3rd choke valve and the 3rd solution heat exchanger, solution pump is set up weak solution pipeline and is connected through the 3rd solution heat exchanger and the 3rd generator, 3rd generator also has concentrated solution pipeline to connect with absorber through the 3rd solution heat exchanger, generator has refrigerant steam channel connect with condenser be adjusted to the 3rd generator after generator has refrigerant steam channel to connect with the 3rd generator and have cryogen liquid pipeline to connect with condenser through the 3rd choke valve again, 3rd generator also has refrigerant steam channel to connect with condenser, form Branch-cycle first-class absorption type heat pump.
null3. Branch-cycle first-class absorption type heat pump，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd choke valve and the 3rd solution heat exchanger，Absorber has weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber and have weak solution pipeline through solution pump、3rd solution heat exchanger connects with generator with solution heat exchanger，Generator has concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to generator and have concentrated solution pipeline to connect through solution heat exchanger and the 3rd generator，3rd generator has concentrated solution pipeline to connect with absorber through the 3rd solution heat exchanger again，Generator has refrigerant steam channel connect with condenser be adjusted to the 3rd generator after generator has refrigerant steam channel to connect with the 3rd generator and have cryogen liquid pipeline to connect with condenser through the 3rd choke valve again，3rd generator also has refrigerant steam channel to connect with condenser，Form Branch-cycle first-class absorption type heat pump.
null4. Branch-cycle first-class absorption type heat pump，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd choke valve、3rd solution heat exchanger and the 3rd solution pump，Absorber has weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber and have weak solution pipeline through solution pump and the second solution heat exchanger and the connection of the 3rd generator，3rd generator has concentrated solution pipeline to connect with generator through the 3rd solution pump and the 3rd solution heat exchanger again，Generator has concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to generator and have concentrated solution pipeline to connect with absorber through the 3rd solution heat exchanger and solution heat exchanger，Generator has refrigerant steam channel connect with condenser be adjusted to the 3rd generator after generator has refrigerant steam channel to connect with the 3rd generator and have cryogen liquid pipeline to connect with condenser through the 3rd choke valve again，3rd generator also has refrigerant steam channel to connect with condenser，Form Branch-cycle first-class absorption type heat pump.
null5. Branch-cycle first-class absorption type heat pump，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd choke valve、3rd solution heat exchanger and the 3rd condenser，Absorber has weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber and have weak solution pipeline through solution pump、3rd solution heat exchanger connects with generator with solution heat exchanger，Generator has concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to generator and have concentrated solution pipeline to connect through solution heat exchanger and the 3rd generator，3rd generator has concentrated solution pipeline to connect with absorber through the 3rd solution heat exchanger again，3rd generator also has refrigerant steam channel to connect with the 3rd condenser，3rd condenser also has cryogen liquid pipeline to connect with vaporizer through the 3rd choke valve，3rd generator also has driving heat medium pipeline and ft connection，3rd condenser also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump；Wherein, or by condenser have cryogen liquid pipeline to connect with vaporizer through choke valve to be adjusted to condenser and have cryogen liquid pipeline to connect through choke valve and the 3rd condenser.
null6. Branch-cycle first-class absorption type heat pump，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Absorber has weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber and have weak solution pipeline through solution pump and the 3rd solution heat exchanger and the connection of the 3rd absorber，3rd absorber has weak solution pipeline to connect with generator with solution heat exchanger through the 3rd solution pump again，Generator has concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to generator and have concentrated solution pipeline to connect through solution heat exchanger and the 3rd generator，3rd generator has concentrated solution pipeline to connect with absorber through the 3rd solution heat exchanger again，3rd generator also has refrigerant steam channel to connect with the 3rd absorber，3rd generator also has driving heat medium pipeline and ft connection，3rd absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null7. Branch-cycle first-class absorption type heat pump，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Absorber has weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber and have weak solution pipeline through solution pump and the 3rd solution heat exchanger and the connection of the 3rd absorber，3rd absorber has weak solution pipeline to connect with generator with solution heat exchanger through the 3rd solution pump again，Generator has concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to generator and have concentrated solution pipeline to connect through solution heat exchanger and the 3rd generator，3rd generator has concentrated solution pipeline to connect with absorber through the 3rd solution heat exchanger again，3rd generator also has refrigerant steam channel to connect with the 3rd absorber，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest，3rd generator also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null8. Branch-cycle first-class absorption type heat pump，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd absorber、3rd solution pump、Second point of steam chest、Solution choke valve and the second solution choke valve，Absorber has weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber and have weak solution pipeline through solution pump and solution heat exchanger and the connection of the 3rd absorber，3rd absorber has weak solution pipeline to connect with generator through the second solution choke valve again，Generator has concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to generator and have concentrated solution pipeline to connect through the 3rd solution pump and the 3rd generator，3rd generator also has concentrated solution pipeline through solution choke valve and the 3rd absorber and second point of steam chest connection，Second point of steam chest has concentrated solution pipeline to connect with absorber through solution heat exchanger again，3rd generator also has refrigerant steam channel to connect with the 3rd absorber，Second point of steam chest also has refrigerant steam channel to connect with condenser，3rd generator also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null9. Branch-cycle first-class absorption type heat pump，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd absorber、Second point of steam chest and solution choke valve，Absorber has weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber and have weak solution pipeline through solution pump and solution heat exchanger and the connection of the 3rd absorber，3rd absorber also has weak solution pipeline and the connection of the 3rd generator，3rd generator has concentrated solution pipeline to connect with generator through solution choke valve again，Generator has concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to generator and have concentrated solution pipeline through the 3rd absorber and second point of steam chest connection，Second point of steam chest has concentrated solution pipeline to connect with absorber through solution heat exchanger again，3rd generator also has refrigerant steam channel to connect with the 3rd absorber，Second point of steam chest also has refrigerant steam channel to connect with condenser，3rd generator also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump；Wherein, arranging for convenience of parts, or increase by the 3rd solution pump, the 3rd absorber has weak solution pipeline and the connection of the 3rd generator are adjusted to the 3rd absorber has weak solution pipeline to connect through the 3rd solution pump and the 3rd generator.
null10. Branch-cycle first-class absorption type heat pump，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and second point of steam chest，Absorber has weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber and have weak solution pipeline through solution pump、Solution heat exchanger and the 3rd solution heat exchanger and the 3rd absorber connect，3rd absorber also has weak solution pipeline and the connection of the 3rd generator，3rd generator has concentrated solution pipeline to connect with generator through the 3rd solution heat exchanger again，Generator has concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to generator and have concentrated solution pipeline through the 3rd absorber and second point of steam chest connection，Second point of steam chest has concentrated solution pipeline to connect with absorber through solution heat exchanger again，3rd generator also has refrigerant steam channel to connect with the 3rd absorber，Second point of steam chest also has refrigerant steam channel to connect with condenser，3rd generator also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump；Wherein, arranging for convenience of parts, or increase by the 3rd solution pump, the 3rd absorber has weak solution pipeline and the connection of the 3rd generator are adjusted to the 3rd absorber has weak solution pipeline to connect through the 3rd solution pump and the 3rd generator.
null11. Branch-cycle first-class absorption type heat pumps，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd absorber、4th absorber、3rd solution pump、4th solution pump、3rd solution heat exchanger、4th solution heat exchanger、Second point of steam chest and solution choke valve，Absorber has weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber and have weak solution pipeline through solution pump and the 3rd solution heat exchanger and the connection of the 4th absorber，4th absorber also has weak solution pipeline through the 3rd solution pump and the 4th solution heat exchanger and the connection of the 3rd absorber，3rd absorber has weak solution pipeline to connect with generator with solution heat exchanger through the 4th solution pump again，Generator has concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to generator and have concentrated solution pipeline to connect through solution heat exchanger and the 3rd generator，3rd generator also has concentrated solution pipeline through solution choke valve and the 3rd absorber and second point of steam chest connection，Second point of steam chest has concentrated solution pipeline to connect with absorber through the 4th solution heat exchanger and the 3rd solution heat exchanger again，3rd generator also has refrigerant steam channel to connect with the 3rd absorber，Second point of steam chest also has refrigerant steam channel to connect with the 4th absorber，3rd generator also has driving heat medium pipeline and ft connection，3rd absorber or also heated medium pipeline and ft connection，4th absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null12. Branch-cycle first-class absorption type heat pumps，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd absorber、4th absorber、3rd solution pump、4th solution pump、3rd solution heat exchanger、4th solution heat exchanger、Solution choke valve and second point of steam chest，Absorber has weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber and have weak solution pipeline through solution pump and the 3rd solution heat exchanger and the connection of the 4th absorber，4th absorber also has weak solution pipeline through the 3rd solution pump and the 4th solution heat exchanger and the connection of the 3rd absorber，3rd absorber has weak solution pipeline to connect with generator with solution heat exchanger through the 4th solution pump again，Generator has concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to generator and have concentrated solution pipeline to connect through solution heat exchanger and the 3rd generator，3rd generator also has concentrated solution pipeline through solution choke valve and the 3rd absorber and second point of steam chest connection，Second point of steam chest has concentrated solution pipeline to connect with absorber through the 4th solution heat exchanger and the 3rd solution heat exchanger again，3rd generator also has refrigerant steam channel to connect with the 3rd absorber，Second point of steam chest also has refrigerant steam channel to connect with the 4th absorber，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 4th absorber connect with a point steam chest or connect with a point steam chest through the 3rd absorber，3rd generator also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
13. Branch-cycle first-class absorption type heat pumps, it is in the 1st described Branch-cycle first-class absorption type heat pump, increase by the 3rd generator, 3rd absorber, 3rd solution heat exchanger and the 3rd solution pump, generator has refrigerant steam channel connect with condenser be adjusted to generator and have refrigerant steam channel to connect with the 3rd absorber, 3rd absorber also has weak solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger and the connection of the 3rd generator, 3rd generator also has concentrated solution pipeline to connect through the 3rd solution heat exchanger and the 3rd absorber, 3rd generator also has refrigerant steam channel to connect with condenser, 3rd generator also has driving heat medium pipeline and ft connection, 3rd absorber also has heated medium pipeline and ft connection, form Branch-cycle first-class absorption type heat pump.
null14. Branch-cycle first-class absorption type heat pumps，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Generator has refrigerant steam channel connect with condenser be adjusted to generator and have refrigerant steam channel to connect with the 3rd absorber，3rd absorber also has weak solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger and the connection of the 3rd generator，3rd generator also has concentrated solution pipeline to connect through the 3rd solution heat exchanger and the 3rd absorber，3rd generator also has refrigerant steam channel to connect with condenser，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline through the second solution pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest，Absorber sets up heated medium pipeline and ft connection，3rd generator also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null15. Branch-cycle first-class absorption type heat pumps，It is in the 1st described Branch-cycle first-class absorption type heat pump，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Generator has refrigerant steam channel connect with condenser be adjusted to generator and have refrigerant steam channel to connect with the 3rd absorber，3rd absorber also has weak solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger and the connection of the 3rd generator，3rd generator also has concentrated solution pipeline to connect through the 3rd solution heat exchanger and the 3rd absorber，3rd generator also has refrigerant steam channel to connect with condenser，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest，3rd generator also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
16. Branch-cycle first-class absorption type heat pumps, it is in the arbitrary Branch-cycle first-class absorption type heat pump described in 1-15 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, second solution pump is set up weak solution pipeline and is connected with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has concentrated solution pipeline through newly-increased solution heat exchanger and the connection of the second absorber, refrigerant steam channel is had connect with the second condenser to be adjusted to after a point steam chest has refrigerant steam channel to connect with newly-increased generator and increase generator newly and have cryogen liquid pipeline warp to increase choke valve newly again and the second condenser connects a point steam chest, newly-increased generator also has refrigerant steam channel to connect with the second condenser, form Branch-cycle first-class absorption type heat pump.
null17. Branch-cycle first-class absorption type heat pumps，It is at 1-6、8-11、In 13 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased generator、Newly-increased choke valve and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline through the second solution pump、Newly-increased solution heat exchanger、Second solution heat exchanger connects with a point steam chest with absorber，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator has concentrated solution pipeline again through newly-increased solution heat exchanger and the connection of the second absorber，Refrigerant steam channel is had connect with the second condenser to be adjusted to after a point steam chest has refrigerant steam channel to connect with newly-increased generator and increase generator newly and have cryogen liquid pipeline warp to increase choke valve newly again and the second condenser connects a point steam chest，Newly-increased generator also has refrigerant steam channel to connect with the second condenser，Form Branch-cycle first-class absorption type heat pump.
null18. Branch-cycle first-class absorption type heat pumps，It is the 7th、In 15 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased generator、Newly-increased choke valve and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline through the second solution pump、Newly-increased solution heat exchanger、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator has concentrated solution pipeline again through newly-increased solution heat exchanger and the connection of the second absorber，Refrigerant steam channel is had connect with the second condenser to be adjusted to after a point steam chest has refrigerant steam channel to connect with newly-increased generator and increase generator newly and have cryogen liquid pipeline warp to increase choke valve newly again and the second condenser connects a point steam chest，Newly-increased generator also has refrigerant steam channel to connect with the second condenser，Form Branch-cycle first-class absorption type heat pump.
null19. Branch-cycle first-class absorption type heat pumps，It is in the 12nd described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased generator、Newly-increased choke valve and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 4th absorber connects with a point steam chest or have weak solution pipeline through the second solution pump through the 3rd absorber with dividing a steam chest to connect to be adjusted to the second absorber again、Newly-increased solution heat exchanger、Second solution heat exchanger、Absorber and the 4th absorber connect with a point steam chest or connect with a point steam chest through the 3rd absorber，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator has concentrated solution pipeline again through newly-increased solution heat exchanger and the connection of the second absorber，Refrigerant steam channel is had connect with the second condenser to be adjusted to after a point steam chest has refrigerant steam channel to connect with newly-increased generator and increase generator newly and have cryogen liquid pipeline warp to increase choke valve newly again and the second condenser connects a point steam chest，Newly-increased generator also has refrigerant steam channel to connect with the second condenser，Form Branch-cycle first-class absorption type heat pump.
null20. Branch-cycle first-class absorption type heat pumps，It is in the 14th described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased generator、Newly-increased choke valve and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline through the second solution pump、Newly-increased solution heat exchanger、Second solution heat exchanger and the 3rd absorber connect with a point steam chest，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator has concentrated solution pipeline again through newly-increased solution heat exchanger and the connection of the second absorber，Refrigerant steam channel is had connect with the second condenser to be adjusted to after a point steam chest has refrigerant steam channel to connect with newly-increased generator and increase generator newly and have cryogen liquid pipeline warp to increase choke valve newly again and the second condenser connects a point steam chest，Newly-increased generator also has refrigerant steam channel to connect with the second condenser，Form Branch-cycle first-class absorption type heat pump.
null21. Branch-cycle first-class absorption type heat pumps，It is at 1-6、8-11、In 13 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased generator、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased generator through the second solution pump and the second solution heat exchanger，Newly-increased generator has concentrated solution pipeline again through new solubilization liquid pump、Newly-increased solution heat exchanger connects with a point steam chest with absorber，A steam chest will be divided to have concentrated solution pipeline to be adjusted to a point steam chest through the second solution heat exchanger and the connection of the second absorber and to have concentrated solution pipeline through increasing solution heat exchanger and the second solution heat exchanger and the connection of the second absorber newly，Refrigerant steam channel is had connect with the second condenser to be adjusted to after a point steam chest has refrigerant steam channel to connect with newly-increased generator and increase generator newly and have cryogen liquid pipeline warp to increase choke valve newly again and the second condenser connects a point steam chest，Newly-increased generator also has refrigerant steam channel to connect with the second condenser，Form Branch-cycle first-class absorption type heat pump.
null22. Branch-cycle first-class absorption type heat pumps，It is the 7th、In 15 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased generator、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased generator through the second solution pump and the second solution heat exchanger，Newly-increased generator has concentrated solution pipeline again through new solubilization liquid pump、Newly-increased solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest，A steam chest will be divided to have concentrated solution pipeline to be adjusted to a point steam chest through the second solution heat exchanger and the connection of the second absorber and to have concentrated solution pipeline through increasing solution heat exchanger and the second solution heat exchanger and the connection of the second absorber newly，Refrigerant steam channel is had connect with the second condenser to be adjusted to after a point steam chest has refrigerant steam channel to connect with newly-increased generator and increase generator newly and have cryogen liquid pipeline warp to increase choke valve newly again and the second condenser connects a point steam chest，Newly-increased generator also has refrigerant steam channel to connect with the second condenser，Form Branch-cycle first-class absorption type heat pump.
null23. Branch-cycle first-class absorption type heat pumps，It is in the 12nd described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased generator、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 4th absorber connects with a point steam chest or have weak solution pipeline to connect with newly-increased generator through the second solution pump and the second solution heat exchanger through the 3rd absorber with dividing a steam chest to connect to be adjusted to the second absorber again，Newly-increased generator has concentrated solution pipeline again through new solubilization liquid pump、Newly-increased solution heat exchanger、Absorber and the 4th absorber connect with a point steam chest or connect with a point steam chest through the 3rd absorber，A steam chest will be divided to have concentrated solution pipeline to be adjusted to a point steam chest through the second solution heat exchanger and the connection of the second absorber and to have concentrated solution pipeline through increasing solution heat exchanger and the second solution heat exchanger and the connection of the second absorber newly，Refrigerant steam channel is had connect with the second condenser to be adjusted to after a point steam chest has refrigerant steam channel to connect with newly-increased generator and increase generator newly and have cryogen liquid pipeline warp to increase choke valve newly again and the second condenser connects a point steam chest，Newly-increased generator also has refrigerant steam channel to connect with the second condenser，Form Branch-cycle first-class absorption type heat pump.
null24. Branch-cycle first-class absorption type heat pumps，It is in the 14th described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased generator、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased generator through the second solution pump and the second solution heat exchanger，Newly-increased generator has concentrated solution pipeline again through new solubilization liquid pump、Newly-increased solution heat exchanger and the 3rd absorber connect with a point steam chest，A steam chest will be divided to have concentrated solution pipeline to be adjusted to a point steam chest through the second solution heat exchanger and the connection of the second absorber and to have concentrated solution pipeline through increasing solution heat exchanger and the second solution heat exchanger and the connection of the second absorber newly，Refrigerant steam channel is had connect with the second condenser to be adjusted to after a point steam chest has refrigerant steam channel to connect with newly-increased generator and increase generator newly and have cryogen liquid pipeline warp to increase choke valve newly again and the second condenser connects a point steam chest，Newly-increased generator also has refrigerant steam channel to connect with the second condenser，Form Branch-cycle first-class absorption type heat pump.
25. Branch-cycle first-class absorption type heat pumps, it is in the arbitrary Branch-cycle first-class absorption type heat pump described in 1-15 item, increase newly-increased point of steam chest, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, second vaporizer has refrigerant steam channel connect with the second absorber be adjusted to the second vaporizer and have refrigerant steam channel to connect with newly-increased absorber, newly-increased absorber also has weak solution pipeline through new solubilization liquid pump, newly-increased solution heat exchanger connects with a newly-increased point steam chest with absorber, a newly-increased point steam chest also has concentrated solution pipeline to connect with newly-increased absorber through newly-increased solution heat exchanger, a newly-increased point steam chest also has refrigerant steam channel to connect with the second absorber, newly-increased absorber also has heated medium pipeline and ft connection, form Branch-cycle first-class absorption type heat pump.
null26. Branch-cycle first-class absorption type heat pumps，It is at 1-6、8-11、In 13 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased point of steam chest、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased absorber has weak solution pipeline again through new solubilization liquid pump、Second solution heat exchanger connects with a point steam chest with absorber，A steam chest will be divided to have concentrated solution pipeline to be adjusted to a point steam chest through the second solution heat exchanger and the connection of the second absorber has concentrated solution pipeline to connect with a newly-increased point steam chest through the second solution heat exchanger and absorber，A newly-increased point steam chest also has concentrated solution pipeline through newly-increased solution heat exchanger and the connection of the second absorber，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased absorber，Newly-increased absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null27. Branch-cycle first-class absorption type heat pumps，It is the 7th、In 15 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased point of steam chest、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased absorber has weak solution pipeline again through new solubilization liquid pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest、Absorber and the 3rd absorber connect with a newly-increased point steam chest，A newly-increased point steam chest also has concentrated solution pipeline through newly-increased solution heat exchanger and the connection of the second absorber，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased absorber，Newly-increased absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null28. Branch-cycle first-class absorption type heat pumps，It is in the 12nd described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased point of steam chest、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Connect with a point steam chest with absorber and the 4th absorber or have weak solution pipeline to connect with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger through the 3rd absorber with dividing a steam chest to connect to be adjusted to the second absorber again，Newly-increased absorber has weak solution pipeline again through new solubilization liquid pump、Second solution heat exchanger、Absorber and the 4th absorber connect with a point steam chest or connect with a point steam chest through the 3rd absorber，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest、Absorber and the 4th absorber connect with a newly-increased point steam chest or connect with a newly-increased point steam chest through the 3rd absorber，A newly-increased point steam chest also has concentrated solution pipeline through newly-increased solution heat exchanger and the connection of the second absorber，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased absorber，Newly-increased absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null29. Branch-cycle first-class absorption type heat pumps，It is in the 14th described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased point of steam chest、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased absorber has weak solution pipeline again through new solubilization liquid pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest，A steam chest will be divided to have concentrated solution pipeline to be adjusted to a point steam chest through the second solution heat exchanger and the connection of the second absorber has concentrated solution pipeline to connect with a newly-increased point steam chest through the second solution heat exchanger and the 3rd absorber，A newly-increased point steam chest also has concentrated solution pipeline through newly-increased solution heat exchanger and the connection of the second absorber，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased absorber，Newly-increased absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null30. Branch-cycle first-class absorption type heat pumps，It is at 1-6、8-11、In 13 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve、Newly-increased point of steam chest and newly-increased second point of steam chest，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased second absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased second absorber also has weak solution pipeline to connect with newly-increased absorber with newly-increased second solution heat exchanger through new solubilization liquid pump，Newly-increased absorber has weak solution pipeline again through newly-increased second solution pump、Second solution heat exchanger connects with a point steam chest with absorber，A steam chest will be divided to have concentrated solution pipeline to be adjusted to a point steam chest through the second solution heat exchanger and the connection of the second absorber has concentrated solution pipeline to connect with a newly-increased point steam chest through the second solution heat exchanger and absorber，A newly-increased point steam chest also has concentrated solution pipeline to connect with newly-increased second point of steam chest with newly-increased absorber through new solubilization liquid choke valve，Newly-increased second point of steam chest has concentrated solution pipeline to connect with newly-increased solution heat exchanger and the second absorber through newly-increased second solution heat exchanger again，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased absorber，Newly-increased second point of steam chest also has refrigerant steam channel to connect with newly-increased second absorber，Newly-increased absorber or also heated medium pipeline and ft connection，Newly-increased second absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null31. Branch-cycle first-class absorption type heat pumps，It is the 7th、In 15 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve、Newly-increased point of steam chest and newly-increased second point of steam chest，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased second absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased second absorber also has weak solution pipeline to connect with newly-increased absorber with newly-increased second solution heat exchanger through new solubilization liquid pump，Newly-increased absorber has weak solution pipeline again through newly-increased second solution pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest、Absorber and the 3rd absorber connect with a newly-increased point steam chest，A newly-increased point steam chest also has concentrated solution pipeline to connect with newly-increased second point of steam chest with newly-increased absorber through new solubilization liquid choke valve，Newly-increased second point of steam chest has concentrated solution pipeline to connect with newly-increased solution heat exchanger and the second absorber through newly-increased second solution heat exchanger again，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased absorber，Newly-increased second point of steam chest also has refrigerant steam channel to connect with newly-increased second absorber，Newly-increased absorber or also heated medium pipeline and ft connection，Newly-increased second absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null32. Branch-cycle first-class absorption type heat pumps，It is in the 12nd described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve、Newly-increased point of steam chest and newly-increased second point of steam chest，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 4th absorber connects with a point steam chest or have weak solution pipeline to connect with newly-increased second absorber through the second solution pump and newly-increased solution heat exchanger through the 3rd absorber with dividing a steam chest to connect to be adjusted to the second absorber again，Newly-increased second absorber also has weak solution pipeline to connect with newly-increased absorber with newly-increased second solution heat exchanger through new solubilization liquid pump，Newly-increased absorber has weak solution pipeline again through newly-increased second solution pump、Second solution heat exchanger、Absorber and the 4th absorber connect with a point steam chest or connect with a point steam chest through the 3rd absorber，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest、Absorber and the 4th absorber connect with a newly-increased point steam chest or connect with a newly-increased point steam chest through the 3rd absorber，A newly-increased point steam chest also has concentrated solution pipeline to connect with newly-increased second point of steam chest with newly-increased absorber through new solubilization liquid choke valve，Newly-increased second point of steam chest has concentrated solution pipeline to connect with newly-increased solution heat exchanger and the second absorber through newly-increased second solution heat exchanger again，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased absorber，Newly-increased second point of steam chest also has refrigerant steam channel to connect with newly-increased second absorber，Newly-increased absorber or also heated medium pipeline and ft connection，Newly-increased second absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null33. Branch-cycle first-class absorption type heat pumps，It is in the 14th described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve、Newly-increased point of steam chest and newly-increased second point of steam chest，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased second absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased second absorber also has weak solution pipeline to connect with newly-increased absorber with newly-increased second solution heat exchanger through new solubilization liquid pump，Newly-increased absorber has weak solution pipeline again through newly-increased second solution pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest，A steam chest will be divided to have concentrated solution pipeline to be adjusted to a point steam chest through the second solution heat exchanger and the connection of the second absorber has concentrated solution pipeline to connect with a newly-increased point steam chest through the second solution heat exchanger and the 3rd absorber，A newly-increased point steam chest also has concentrated solution pipeline to connect with newly-increased second point of steam chest with newly-increased absorber through new solubilization liquid choke valve，Newly-increased second point of steam chest has concentrated solution pipeline to connect with newly-increased solution heat exchanger and the second absorber through newly-increased second solution heat exchanger again，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased absorber，Newly-increased second point of steam chest also has refrigerant steam channel to connect with newly-increased second absorber，Newly-increased absorber or also heated medium pipeline and ft connection，Newly-increased second absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null34. Branch-cycle first-class absorption type heat pumps，It is at 1-6、8-11、In 13 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased generator、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased absorber has weak solution pipeline again through new solubilization liquid pump、Second solution heat exchanger connects with a point steam chest with absorber，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator has concentrated solution pipeline again through newly-increased solution heat exchanger and the connection of the second absorber，Newly-increased generator also has refrigerant steam channel to connect with newly-increased 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 Branch-cycle first-class absorption type heat pump.
null35. Branch-cycle first-class absorption type heat pumps，It is the 7th、In 15 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased generator、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased absorber has weak solution pipeline again through new solubilization liquid pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator has concentrated solution pipeline again through newly-increased solution heat exchanger and the connection of the second absorber，Newly-increased generator also has refrigerant steam channel to connect with newly-increased 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 Branch-cycle first-class absorption type heat pump.
null36. Branch-cycle first-class absorption type heat pumps，It is in the 12nd described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased generator、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 4th absorber connects with a point steam chest or have weak solution pipeline to connect with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger through the 3rd absorber with dividing a steam chest to connect to be adjusted to the second absorber again，Newly-increased absorber has weak solution pipeline again through new solubilization liquid pump、Second solution heat exchanger、Absorber and the 4th absorber connect with a point steam chest or connect with a point steam chest through the 3rd absorber，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator has concentrated solution pipeline again through newly-increased solution heat exchanger and the connection of the second absorber，Newly-increased generator also has refrigerant steam channel to connect with newly-increased 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 Branch-cycle first-class absorption type heat pump.
null37. Branch-cycle first-class absorption type heat pumps，It is in the 14th described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased generator、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased absorber has weak solution pipeline again through new solubilization liquid pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator has concentrated solution pipeline again through newly-increased solution heat exchanger and the connection of the second absorber，Newly-increased generator also has refrigerant steam channel to connect with newly-increased 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 Branch-cycle first-class absorption type heat pump.
null38. Branch-cycle first-class absorption type heat pumps，It is at 1-6、8-11、In 13 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased generator、Newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve and newly-increased point of steam chest，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased second absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased second absorber also has weak solution pipeline to connect with newly-increased absorber with newly-increased second solution heat exchanger through new solubilization liquid pump，Newly-increased absorber has weak solution pipeline again through newly-increased second solution pump、Second solution heat exchanger connects with a point steam chest with absorber，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator also has concentrated solution pipeline to connect with a newly-increased point steam chest with newly-increased absorber through new solubilization liquid choke valve，A newly-increased point steam chest has concentrated solution pipeline to connect with newly-increased solution heat exchanger and the second absorber through newly-increased second solution heat exchanger again，Newly-increased generator also has refrigerant steam channel to connect with newly-increased absorber，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased second absorber，Newly-increased generator also has driving heat medium pipeline and ft connection，Newly-increased absorber or also heated medium pipeline and ft connection，Newly-increased second absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null39. Branch-cycle first-class absorption type heat pumps，It is the 7th、In 15 described arbitrary Branch-cycle first-class absorption type heat pumps，Increase newly-increased generator、Newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve and newly-increased point of steam chest，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased second absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased second absorber also has weak solution pipeline to connect with newly-increased absorber with newly-increased second solution heat exchanger through new solubilization liquid pump，Newly-increased absorber has weak solution pipeline again through newly-increased second solution pump、Second solution heat exchanger、Absorber and the 3rd absorber connect with a point steam chest，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator also has concentrated solution pipeline to connect with a newly-increased point steam chest with newly-increased absorber through new solubilization liquid choke valve，A newly-increased point steam chest has concentrated solution pipeline to connect with newly-increased solution heat exchanger and the second absorber through newly-increased second solution heat exchanger again，Newly-increased generator also has refrigerant steam channel to connect with newly-increased absorber，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased second absorber，Newly-increased generator also has driving heat medium pipeline and ft connection，Newly-increased absorber or also heated medium pipeline and ft connection，Newly-increased second absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null40. Branch-cycle first-class absorption type heat pumps，It is in the 12nd described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased generator、Newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve and newly-increased point of steam chest，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger、Absorber and the 4th absorber connects with a point steam chest or have weak solution pipeline to connect with newly-increased second absorber through the second solution pump and newly-increased solution heat exchanger through the 3rd absorber with dividing a steam chest to connect to be adjusted to the second absorber again，Newly-increased second absorber also has weak solution pipeline to connect with newly-increased absorber with newly-increased second solution heat exchanger through new solubilization liquid pump，Newly-increased absorber has weak solution pipeline again through newly-increased second solution pump、Second solution heat exchanger、Absorber and the 4th absorber connect with a point steam chest or connect with a point steam chest through the 3rd absorber，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator also has concentrated solution pipeline to connect with a newly-increased point steam chest with newly-increased absorber through new solubilization liquid choke valve，A newly-increased point steam chest has concentrated solution pipeline to connect with newly-increased solution heat exchanger and the second absorber through newly-increased second solution heat exchanger again，Newly-increased generator also has refrigerant steam channel to connect with newly-increased absorber，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased second absorber，Newly-increased generator also has driving heat medium pipeline and ft connection，Newly-increased absorber or also heated medium pipeline and ft connection，Newly-increased second absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null41. Branch-cycle first-class absorption type heat pumps，It is in the 14th described arbitrary Branch-cycle first-class absorption type heat pump，Increase newly-increased generator、Newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve and newly-increased point of steam chest，Second absorber is had weak solution pipeline through the second solution pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest and are adjusted to the second absorber and have weak solution pipeline to connect with newly-increased second absorber through the second solution pump and newly-increased solution heat exchanger，Newly-increased second absorber also has weak solution pipeline to connect with newly-increased absorber with newly-increased second solution heat exchanger through new solubilization liquid pump，Newly-increased absorber has weak solution pipeline again through newly-increased second solution pump、Second solution heat exchanger and the 3rd absorber connect with a point steam chest，Concentrated solution pipeline is had to be adjusted to a point steam chest have concentrated solution pipeline to connect with newly-increased generator through the second solution heat exchanger through the second solution heat exchanger and the connection of the second absorber a point steam chest，Newly-increased generator also has concentrated solution pipeline to connect with a newly-increased point steam chest with newly-increased absorber through new solubilization liquid choke valve，A newly-increased point steam chest has concentrated solution pipeline to connect with newly-increased solution heat exchanger and the second absorber through newly-increased second solution heat exchanger again，Newly-increased generator also has refrigerant steam channel to connect with newly-increased absorber，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased second absorber，Newly-increased generator also has driving heat medium pipeline and ft connection，Newly-increased absorber or also heated medium pipeline and ft connection，Newly-increased second absorber also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
42. Branch-cycle first-class absorption type heat pumps, are in the arbitrary Branch-cycle first-class absorption type heat pump described in 1-41 item, vaporizer and the second vaporizer are united two into one, and form Branch-cycle first-class absorption type heat pump.
43. Branch-cycle first-class absorption type heat pumps, are in the arbitrary Branch-cycle first-class absorption type heat pump described in 1-42 item, condenser and the second condenser are united two into one, and form Branch-cycle first-class absorption type heat pump.
null44. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in 1-15 item，Increase newly-increased generator、Newly-increased absorber、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second vaporizer has refrigerant steam channel connect with the second absorber be adjusted to the second vaporizer and have refrigerant steam channel to connect with newly-increased absorber，Refrigerant steam channel is had connect with the second condenser to be adjusted to after a point steam chest has refrigerant steam channel to connect with newly-increased generator and increase generator newly and have cryogen liquid pipeline warp to increase choke valve newly again to connect with newly-increased vaporizer a point steam chest，Newly-increased vaporizer also has refrigerant steam channel to connect with the second absorber，Newly-increased generator also has concentrated solution pipeline to connect with newly-increased absorber through newly-increased solution heat exchanger，Newly-increased absorber also has weak solution pipeline to connect with newly-increased generator with newly-increased solution heat exchanger through new solubilization liquid pump，Newly-increased generator also has refrigerant steam channel to connect with the second condenser，Newly-increased absorber also has heated medium pipeline and ft connection，Newly-increased vaporizer also has surplus heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null45. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in 1-15 item，Increase newly-increased choke valve、Newly-increased solution heat exchanger、New solubilization liquid pump、Newly-increased absorber、Newly-increased point of steam chest、Newly-increased condenser and newly-increased vaporizer，Cancel the heated medium pipeline of the second absorber and ft connection，Newly-increased absorber has weak solution pipeline through new solubilization liquid pump、Newly-increased solution heat exchanger and the second absorber connect with a newly-increased point steam chest，A newly-increased point steam chest also has concentrated solution to connect with newly-increased absorber through newly-increased solution heat exchanger，A newly-increased point steam chest also has refrigerant steam channel to connect with newly-increased condenser，Newly-increased condenser also has cryogen liquid pipeline to connect with newly-increased vaporizer through newly-increased choke valve，Newly-increased vaporizer also has refrigerant steam channel to connect with newly-increased absorber，Newly-increased absorber and newly-increased condenser have heated medium pipeline and ft connection the most respectively，Newly-increased vaporizer also has surplus heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
46. Branch-cycle first-class absorption type heat pumps, are in the arbitrary Branch-cycle first-class absorption type heat pump described in 44-45 item, are one by vaporizer, the second vaporizer and newly-increased vaporizer conjunction three, form Branch-cycle first-class absorption type heat pump.
47. Branch-cycle first-class absorption type heat pumps, are in the 44th described arbitrary Branch-cycle first-class absorption type heat pump, condenser and the second condenser are united two into one, and form Branch-cycle first-class absorption type heat pump.
48. Branch-cycle first-class absorption type heat pumps, are in the 45th described arbitrary Branch-cycle first-class absorption type heat pump, are one by condenser, the second condenser and newly-increased condenser conjunction three, form Branch-cycle first-class absorption type heat pump.
Feature and the essence of the present invention is further illustrated below in conjunction with Branch-cycle first-class absorption type heat pump shown in Fig. 1, Fig. 7 and Figure 22:
1. drive thermal medium to flow through generator 1, heating enters its interior solution release and to condensation 4 offer refrigerant vapour, drives heat to carry out temperature drop for the first time in first solution circulation loop；The refrigerant vapour that vaporizer 6 produces enters absorber 3, is absorbed by concentrated solution and heat up, and for the generating process of another road solution after intensification, is equal to high temperature driven thermic load and plays twice effect, improve the value of high temperature driven thermal medium.
2. the second absorber 3, condenser 4 and the second common externally heat supply of condenser 5, condenser 4 is single-action flow process heat supply, second absorber 3 and the second condenser 5 are simple double-effect process heat supply, it is particularly suitable for the situation that heated medium range of temperature is wide, be conducive to improving the thermodynamics consummating degree of circulation, obtain higher performance index.
3. for the occasion driving heat to be sensible heat, high-temperature part is used for generator 1, and the driving heat after temperature reduces utilizes for the 3rd generator 15, the 3rd generator 15 and the 3rd absorber 20 composition second time temperature difference, further increases the producing level driving heat.
4. Fig. 7 with Figure 22 combines, the backheat flow process that the 3rd generator 15 and the 3rd absorber 20 are constituted, and the utilization driving the temperature difference is embodied in and provides driving thermic load by absorber 2 to another road solution by it；The backheat flow process that newly-increased generator A and newly-increased absorber E is constituted, remains able to make the driving temperature difference further be utilized, thus realizes driving the temperature difference to make full use of.
Accompanying drawing illustrates:
Fig. 1 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 1st kind of structure and schematic flow sheet.
Fig. 2 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 2nd kind of structure and schematic flow sheet.
Fig. 3 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 3rd kind of structure and schematic flow sheet.
Fig. 4 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 4th kind of structure and schematic flow sheet.
Fig. 5 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 5th kind of structure and schematic flow sheet.
Fig. 6 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 6th kind of structure and schematic flow sheet.
Fig. 7 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 7th kind of structure and schematic flow sheet.
Fig. 8 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 8th kind of structure and schematic flow sheet.
Fig. 9 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 9th kind of structure and schematic flow sheet.
Figure 10 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 10th kind of structure and schematic flow sheet.
Figure 11 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 11st kind of structure and schematic flow sheet.
Figure 12 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 12nd kind of structure and schematic flow sheet.
Figure 13 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 13rd kind of structure and schematic flow sheet.
Figure 14 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 14th kind of structure and schematic flow sheet.
Figure 15 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 15th kind of structure and schematic flow sheet.
Figure 16 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 16th kind of structure and schematic flow sheet.
Figure 17 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 17th kind of structure and schematic flow sheet.
Figure 18 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 18th kind of structure and schematic flow sheet.
Figure 19 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 19th kind of structure and schematic flow sheet.
Figure 20 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 20th kind of structure and schematic flow sheet.
Figure 21 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 21st kind of structure and schematic flow sheet.
Figure 22 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 22nd kind of structure and schematic flow sheet.
Figure 23 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 23rd kind of structure and schematic flow sheet.
Figure 24 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 24th kind of structure and schematic flow sheet.
Figure 25 is based on Branch-cycle first-class absorption type heat pump provided by the present invention 25th kind of structure and schematic flow sheet.
In figure, 1-generator, 2-absorber, 3-the second absorber, 4-condenser, 5-the second condenser, 6-vaporizer, 7-the second vaporizer, 8-solution pump, 9-the second solution pump, 10-choke valve, 11-second throttle, 12-solution heat exchanger, 13-the second solution heat exchanger, 14-divides steam chest, 15-the 3rd generator, 16-the 3rd choke valve, 17-the 3rd solution heat exchanger, 18-the 3rd solution pump, 19-the 3rd condenser, 20-the 3rd absorber, 21-solution choke valve, 22-the second solution choke valve, second point of steam chest of 23-, 24-the 4th absorber, 25-the 4th solution pump, 26-the 4th solution heat exchanger；A-increases generator newly, and B-increases choke valve newly, and C-increases solution heat exchanger newly, D-new solubilization liquid pump, E-increases absorber newly, newly-increased point of steam chest of F-, and G-increases the second solution pump newly, H-increases the second solution heat exchanger newly, I-increases second point of steam chest, J-new solubilization liquid choke valve newly, and K-increases the second absorber newly, L-increases condenser newly, and M-increases vaporizer newly.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, inessential in the case of do not repeat；Obvious flow process is not stated.The present invention is described in detail below in conjunction with the accompanying drawings with example.
Branch-cycle first-class absorption type heat pump shown in Fig. 1 is achieved in that
1., in structure, it is mainly made up of generator, absorber, the second absorber, condenser, the second condenser, vaporizer, the second vaporizer, solution pump, the second solution pump, choke valve, second throttle, solution heat exchanger, the second solution heat exchanger and a point steam chest；Absorber 2 has weak solution pipeline to connect with generator 1 with solution heat exchanger 12 through solution pump 8, generator 1 also concentrated solution pipeline connects with absorber 2 through solution heat exchanger 12, generator 1 also refrigerant steam channel connects with condenser 4, condenser 4 also cryogen liquid pipeline connects with vaporizer 6 through choke valve 10, and vaporizer 6 also refrigerant steam channel connects with absorber 2；Second absorber 3 has weak solution pipeline to connect with a point steam chest 14 with absorber 2 through second solution pump the 9, second solution heat exchanger 13, steam chest 14 also concentrated solution pipeline is divided to connect with the second absorber 3 through the second solution heat exchanger 13, steam chest 14 also refrigerant steam channel is divided to connect with the second condenser 5, second condenser 5 also cryogen liquid pipeline connects with the second vaporizer 7 through second throttle 11, and the second vaporizer 7 also refrigerant steam channel connects with the second absorber 3；Generator 1 also has and drives heat medium pipeline and ft connection, and the second absorber 3, condenser 4 and the second condenser 5 have heated medium pipeline and ft connection, vaporizer 6 and the second vaporizer 7 to have surplus heat the most respectively medium pipeline and ft connection the most respectively.
2. in flow process, the weak solution of absorber 2 enters generator 1 through solution pump 8 and solution heat exchanger 12, drive thermal medium to flow through generator 1, heating enters its interior solution release and provides refrigerant vapour to condenser 4, the concentrated solution of generator 1 enters absorber 2 through solution heat exchanger 12, absorbs refrigerant vapour heat release in flowing through its interior solution, the refrigerant vapour heat release of condenser 4 becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 4 enters vaporizer 6 through choke valve 10 reducing pressure by regulating flow, absorption waste heat becomes refrigerant vapour and provides to absorber 2；The weak solution of the second absorber 3 flows through absorber 2 after the second solution pump 9 and the second solution heat exchanger 13, a point steam chest 14 is entered after heat absorbing part vaporization, the concentrated solution dividing steam chest 14 enters the second absorber 3 through the second solution heat exchanger 13, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour dividing steam chest 14 enters the second condenser 5, heat release becomes cryogen liquid in heated medium, the cryogen liquid of the second condenser 5 enters the second vaporizer 7 through second throttle 11 throttling, absorb waste heat become refrigerant vapour and provide to the second absorber 3, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Fig. 2 is achieved in that
1. in structure, in the Branch-cycle first-class absorption type heat pump shown in Fig. 1, increase by the 3rd generator, 3rd choke valve and the 3rd solution heat exchanger, solution pump 8 is set up weak solution pipeline and is connected with the 3rd generator 15 through the 3rd solution heat exchanger 17, 3rd generator 15 also concentrated solution pipeline connects with absorber 2 through the 3rd solution heat exchanger 17, generator 1 has refrigerant steam channel connect with condenser 4 be adjusted to the 3rd generator 15 after generator 1 has refrigerant steam channel to connect with the 3rd generator 15 and have cryogen liquid pipeline to connect with condenser 4 through the 3rd choke valve 16 again, 3rd generator 15 also refrigerant steam channel connects with condenser 4.
2. in flow process, the refrigerant vapour that generator 1 produces is supplied to the 3rd generator 15 and makees to drive thermal medium, the part weak solution of absorber 2 enters the 3rd generator 15 through solution pump 8 and the 3rd solution heat exchanger 17, refrigerant vapour flows through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to condenser 4, the concentrated solution of the 3rd generator 15 enters absorber 2 through the 3rd solution heat exchanger 17, flow through and enter condenser 4 through the 3rd choke valve 16 throttling again after the refrigerant vapour heat release of the 3rd generator 15 becomes cryogen liquid, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Fig. 3 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd choke valve and the 3rd solution heat exchanger，Absorber 2 has weak solution pipeline connect with generator 1 through solution pump 8 and solution heat exchanger 12 be adjusted to absorber 2 and have weak solution pipeline through solution pump 8、3rd solution heat exchanger 17 connects with generator 1 with solution heat exchanger 12，Generator 1 has concentrated solution pipeline connect with absorber 2 through solution heat exchanger 12 be adjusted to generator 1 and have concentrated solution pipeline to connect with the 3rd generator 15 through solution heat exchanger 12，3rd generator 15 has concentrated solution pipeline to connect with absorber 2 through the 3rd solution heat exchanger 17 again，Generator 1 has refrigerant steam channel connect with condenser 4 be adjusted to the 3rd generator 15 after generator 1 has refrigerant steam channel to connect with the 3rd generator 15 and have cryogen liquid pipeline to connect with condenser 4 through the 3rd choke valve 16 again，3rd generator 15 also refrigerant steam channel connects with condenser 4.
2. in flow process, the refrigerant vapour that generator 1 produces is supplied to the 3rd generator 15 and makees to drive thermal medium, the weak solution of absorber 2 is through solution pump 8, 3rd solution heat exchanger 17 and solution heat exchanger 12 enter generator 1, the concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12, refrigerant vapour flows through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to condenser 4, the concentrated solution of the 3rd generator 15 enters absorber 2 through the 3rd solution heat exchanger 17, flow through and enter condenser 4 through the 3rd choke valve 16 throttling again after the refrigerant vapour heat release of the 3rd generator 15 becomes cryogen liquid, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Fig. 4 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd choke valve、3rd solution heat exchanger and the 3rd solution pump，Absorber 2 has weak solution pipeline connect with generator 1 through solution pump 8 and solution heat exchanger 12 be adjusted to absorber 2 and have weak solution pipeline to connect with the 3rd generator 15 through solution pump 8 and the second solution heat exchanger 12，3rd generator 15 has concentrated solution pipeline to connect with generator 1 with the 3rd solution heat exchanger 17 through the 3rd solution pump 18 again，Generator 1 has concentrated solution pipeline connect with absorber 2 through solution heat exchanger 12 be adjusted to generator 1 and have concentrated solution pipeline to connect with absorber 2 through the 3rd solution heat exchanger 17 and solution heat exchanger 12，Generator 1 has refrigerant steam channel connect with condenser 4 be adjusted to the 3rd generator 15 after generator 1 has refrigerant steam channel to connect with the 3rd generator 15 and have cryogen liquid pipeline to connect with condenser 4 through the 3rd choke valve 16 again，3rd generator 15 also refrigerant steam channel connects with condenser 4.
2. in flow process, the refrigerant vapour that generator 1 produces is supplied to the 3rd generator 15 and makees to drive thermal medium, the weak solution of absorber 2 enters the 3rd generator 15 through solution pump 8 and solution heat exchanger 12, refrigerant vapour flows through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to condenser 4, the concentrated solution of the 3rd generator 15 enters generator 1 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, the concentrated solution of generator 1 enters absorber 2 through the 3rd solution heat exchanger 17 and solution heat exchanger 12, flow through and enter condenser 4 through the 3rd choke valve 16 throttling again after the refrigerant vapour heat release of the 3rd generator 15 becomes cryogen liquid, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Fig. 5 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd choke valve、3rd solution heat exchanger and the 3rd condenser，Absorber 2 has weak solution pipeline connect with generator 1 through solution pump 8 and solution heat exchanger 12 be adjusted to absorber 2 and have weak solution pipeline through solution pump 8、3rd solution heat exchanger 17 connects with generator 1 with solution heat exchanger 12，Generator 1 has concentrated solution pipeline connect with absorber 2 through solution heat exchanger 12 be adjusted to generator 1 and have concentrated solution pipeline to connect with the 3rd generator 15 through solution heat exchanger 12，3rd generator 15 has concentrated solution pipeline to connect with absorber 2 through the 3rd solution heat exchanger 17 again，3rd generator 15 also refrigerant steam channel connects with the 3rd condenser 19，3rd condenser 19 also cryogen liquid pipeline connects with vaporizer 6 through the 3rd choke valve 16，3rd generator 15 also has driving heat medium pipeline and ft connection，3rd condenser 19 also has heated medium pipeline and ft connection.
2. in flow process, the weak solution of absorber 2 enters generator 1 through solution pump the 8, the 3rd solution heat exchanger 17 and solution heat exchanger 12, the concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12, drive thermal medium to flow through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to the 3rd condenser 19, and the concentrated solution of the 3rd generator 15 enters absorber 2 through the 3rd solution heat exchanger 17；The refrigerant vapour heat release of the 3rd condenser 19 becomes cryogen liquid in heated medium, and the cryogen liquid of the 3rd condenser 19 enters vaporizer 6 through the 3rd choke valve 16 throttling, forms Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Fig. 6 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Absorber 2 has weak solution pipeline connect with generator 1 through solution pump 8 and solution heat exchanger 12 be adjusted to absorber 2 and have weak solution pipeline to connect with the 3rd absorber 20 through solution pump 8 and the 3rd solution heat exchanger 17，3rd absorber 20 has weak solution pipeline to connect with generator 1 with solution heat exchanger 12 through the 3rd solution pump 18 again，Generator 1 has concentrated solution pipeline connect with absorber 2 through solution heat exchanger 12 be adjusted to generator 1 and have concentrated solution pipeline to connect with the 3rd generator 15 through solution heat exchanger 12，3rd generator 15 has concentrated solution pipeline to connect with absorber 2 through the 3rd solution heat exchanger 17 again，3rd generator 15 also refrigerant steam channel connects with the 3rd absorber 20，3rd generator 15 also has driving heat medium pipeline and ft connection，3rd absorber 20 also has heated medium pipeline and ft connection.
2. in flow process, the weak solution of absorber 2 enters the 3rd absorber 20 through solution pump 8 and the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 20 enters generator 1 through the 3rd solution pump 18 and solution heat exchanger 12, the concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12, thermal medium is driven to flow through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 enters absorber 2 through the 3rd solution heat exchanger 17, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Fig. 7 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Absorber 2 has weak solution pipeline connect with generator 1 through solution pump 8 and solution heat exchanger 12 be adjusted to absorber 2 and have weak solution pipeline to connect with the 3rd absorber 20 through solution pump 8 and the 3rd solution heat exchanger 17，3rd absorber 20 has weak solution pipeline to connect with generator 1 with solution heat exchanger 12 through the 3rd solution pump 18 again，Generator 1 has concentrated solution pipeline connect with absorber 2 through solution heat exchanger 12 be adjusted to generator 1 and have concentrated solution pipeline to connect with the 3rd generator 15 through solution heat exchanger 12，3rd generator 15 has concentrated solution pipeline to connect with absorber 2 through the 3rd solution heat exchanger 17 again，3rd generator 15 also refrigerant steam channel connects with the 3rd absorber 20，Second absorber 3 there is weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 and absorber 2 connect with a point steam chest 14 and are adjusted to the second absorber 3 and have weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13、Absorber 2 connects with a point steam chest 14 with the 3rd absorber 20，3rd generator 15 also has driving heat medium pipeline and ft connection.
2. in flow process, the weak solution of absorber 2 enters the 3rd absorber 20 through solution pump 8 and the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in flowing through its interior solution, the weak solution of the 3rd absorber 20 enters generator 1 through the 3rd solution pump 18 and solution heat exchanger 12, the concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12, thermal medium is driven to flow through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 enters absorber 2 through the 3rd solution heat exchanger 17；The weak solution of the second absorber 3 enters a point steam chest 14 after flowing through absorber 2 and the 3rd absorber 20, heat absorbing part vaporization successively after the second solution pump 9 and the second solution heat exchanger 13, forms Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Fig. 8 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd absorber、3rd solution pump、Second point of steam chest、Solution choke valve and the second solution choke valve，Absorber 2 has weak solution pipeline connect with generator 1 through solution pump 8 and solution heat exchanger 12 be adjusted to absorber 2 and have weak solution pipeline to connect with the 3rd absorber 20 through solution pump 8 and solution heat exchanger 12，3rd absorber 20 has weak solution pipeline to connect with generator 1 through the second solution choke valve 22 again，Generator 1 has concentrated solution pipeline connect with absorber 2 through solution heat exchanger 12 be adjusted to generator 1 and have concentrated solution pipeline to connect with the 3rd generator 15 through the 3rd solution pump 18，3rd generator 15 also concentrated solution pipeline connects with second point of steam chest 23 with the 3rd absorber 20 through solution choke valve 21，Second point of steam chest 23 has concentrated solution pipeline to connect with absorber 2 through solution heat exchanger 12 again，3rd generator 15 also refrigerant steam channel connects with the 3rd absorber 20，Second point of steam chest 23 also refrigerant steam channel connects with condenser 4，3rd generator 15 also has driving heat medium pipeline and ft connection.
null2. in flow process，The weak solution of absorber 2 enters the 3rd absorber 20 through solution pump 8 and solution heat exchanger 12、Absorb refrigerant vapour heat release in flowing through its interior solution，The weak solution of the 3rd absorber 20 enters generator 1 through the second solution choke valve 22 reducing pressure by regulating flow，The concentrated solution of generator 1 enters the 3rd generator 15 through the 3rd solution pump 18，Thermal medium is driven to flow through the 3rd generator 15、Heating enters its interior solution release and provides refrigerant vapour to the 3rd absorber 20，The concentrated solution of the 3rd generator 15 flows through the 3rd absorber 20 after solution choke valve 21 reducing pressure by regulating flow、Second point of steam chest 23 is entered after heat absorbing part vaporization，The concentrated solution of second point of steam chest 23 enters absorber 3 through solution heat exchanger 12，The refrigerant vapour of second point of steam chest 23 enters condenser 4，Form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Fig. 9 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd absorber、Second point of steam chest and solution choke valve，Absorber 2 has weak solution pipeline connect with generator 1 through solution pump 8 and solution heat exchanger 12 be adjusted to absorber 2 and have weak solution pipeline to connect with the 3rd absorber 20 through solution pump 8 and solution heat exchanger 12，3rd absorber 20 also weak solution pipeline and the 3rd generator 15 connect，3rd generator 15 has concentrated solution pipeline to connect with generator 1 through solution choke valve 21 again，Generator 1 has concentrated solution pipeline connect with absorber 2 through solution heat exchanger 12 be adjusted to generator 1 and have concentrated solution pipeline to connect with second point of steam chest 23 through the 3rd absorber 20，Second point of steam chest 23 has concentrated solution pipeline to connect with absorber 2 through solution heat exchanger 12 again，3rd generator 15 also refrigerant steam channel connects with the 3rd absorber 20，Second point of steam chest 23 also refrigerant steam channel connects with condenser 4，3rd generator 15 also has driving heat medium pipeline and ft connection.
2. in flow process, the weak solution of absorber 2 enters the 3rd absorber 20 through solution pump 8 and solution heat exchanger 12, absorb refrigerant vapour heat release in flowing through its interior solution, the weak solution of the 3rd absorber 20 enters the 3rd generator 15, thermal medium is driven to flow through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 enters generator 1 through solution choke valve 21 reducing pressure by regulating flow, the concentrated solution of generator 1 flows through the 3rd absorber 20, second point of steam chest 23 is entered after heat absorbing part vaporization, the concentrated solution of second point of steam chest 23 enters absorber 2 through solution heat exchanger 12, the refrigerant vapour of second point of steam chest 23 enters condenser 4, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 10 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and second point of steam chest，Absorber 2 has weak solution pipeline connect with generator 1 through solution pump 8 and solution heat exchanger 12 be adjusted to absorber 2 and have weak solution pipeline through solution pump 8、Solution heat exchanger 12 connects with the 3rd absorber 20 with the 3rd solution heat exchanger 17，3rd absorber 20 also weak solution pipeline and the 3rd generator 15 connect，3rd generator 15 has concentrated solution pipeline to connect with generator 1 through the 3rd solution heat exchanger 17 again，Generator 1 has concentrated solution pipeline connect with absorber 2 through solution heat exchanger 12 be adjusted to generator 1 and have concentrated solution pipeline to connect with second point of steam chest 23 through the 3rd absorber 20，Second point of steam chest 23 has concentrated solution pipeline to connect with absorber 2 through solution heat exchanger 12 again，3rd generator 15 also refrigerant steam channel connects with the 3rd absorber 20，Second point of steam chest 23 also refrigerant steam channel connects with condenser 4，3rd generator 15 also has driving heat medium pipeline and ft connection.
2. in flow process, the weak solution of absorber 2 is through solution pump 8, solution heat exchanger 12 and the 3rd solution heat exchanger 17 enter the 3rd absorber 20, absorb refrigerant vapour heat release in flowing through its interior solution, the weak solution of the 3rd absorber 20 enters the 3rd generator 15, thermal medium is driven to flow through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to the 3rd absorber 20, the concentrated solution of the 3rd generator 15 enters generator 1 through the 3rd solution heat exchanger 17, the concentrated solution of generator 1 flows through the 3rd absorber 20, second point of steam chest 23 is entered after heat absorbing part vaporization, the concentrated solution of second point of steam chest 23 enters absorber 2 through solution heat exchanger 12, the refrigerant vapour of second point of steam chest 23 enters condenser 4, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 11 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd absorber、4th absorber、3rd solution pump、4th solution pump、3rd solution heat exchanger、4th solution heat exchanger、Second point of steam chest and solution choke valve，Absorber 2 has weak solution pipeline connect with generator 1 through solution pump 8 and solution heat exchanger 12 be adjusted to absorber 2 and have weak solution pipeline to connect with the 4th absorber 24 through solution pump 8 and the 3rd solution heat exchanger 17，4th absorber 24 also weak solution pipeline connects with the 3rd absorber 20 with the 4th solution heat exchanger 26 through the 3rd solution pump 18，3rd absorber 20 has weak solution pipeline to connect with generator 1 with solution heat exchanger 12 through the 4th solution pump 25 again，Generator 1 has concentrated solution pipeline connect with absorber 2 through solution heat exchanger 12 be adjusted to generator 1 and have concentrated solution pipeline to connect with the 3rd generator 15 through solution heat exchanger 12，3rd generator 15 also concentrated solution pipeline connects with second point of steam chest 23 with the 3rd absorber 20 through solution choke valve 21，Second point of steam chest 23 has concentrated solution pipeline to connect with absorber 2 with the 3rd solution heat exchanger 17 through the 4th solution heat exchanger 26 again，3rd generator 15 also refrigerant steam channel connects with the 3rd absorber 20，Second point of steam chest 23 also refrigerant steam channel connects with the 4th absorber 24，3rd generator 15 also has driving heat medium pipeline and ft connection，4th absorber 24 also has heated medium pipeline and ft connection.
null2. in flow process，The weak solution of absorber 2 enters the 4th absorber 24 through solution pump 8 and the 3rd solution heat exchanger 17、Absorb refrigerant vapour heat release in heated medium，The weak solution of the 4th absorber 24 enters the 3rd absorber 20 through the 3rd solution pump 18 and the 4th solution heat exchanger 26、Absorb refrigerant vapour heat release in flowing through its interior solution，The weak solution of the 3rd absorber 20 enters generator 1 through the 4th solution pump 25 and solution heat exchanger 12，The concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12，Thermal medium is driven to flow through the 3rd generator 15、Heating enters its interior solution release and provides refrigerant vapour to the 3rd absorber 20，The concentrated solution of the 3rd generator 15 flows through the 3rd absorber 20 after solution choke valve 21 reducing pressure by regulating flow、Second point of steam chest 23 is entered after heat absorbing part vaporization，The concentrated solution of second point of steam chest 23 enters absorber 2 through the 4th solution heat exchanger 26 and the 3rd solution heat exchanger 17，The refrigerant vapour of second point of steam chest 23 enters the 4th absorber 24，Form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 12 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd absorber、4th absorber、3rd solution pump、4th solution pump、3rd solution heat exchanger、4th solution heat exchanger、Solution choke valve and second point of steam chest，Absorber 2 has weak solution pipeline connect with generator 1 through solution pump 8 and solution heat exchanger 12 be adjusted to absorber 2 and have weak solution pipeline to connect with the 4th absorber 24 through solution pump 8 and the 3rd solution heat exchanger 17，4th absorber 24 also weak solution pipeline connects with the 3rd absorber 20 with the 4th solution heat exchanger 26 through the 3rd solution pump 18，3rd absorber 20 has weak solution pipeline to connect with generator 1 with solution heat exchanger 12 through the 4th solution pump 25 again，Generator 1 has concentrated solution pipeline connect with absorber 2 through solution heat exchanger 12 be adjusted to generator 1 and have concentrated solution pipeline to connect with the 3rd generator 15 through solution heat exchanger 12，3rd generator 15 also concentrated solution pipeline connects with second point of steam chest 23 with the 3rd absorber 20 through solution choke valve 21，Second point of steam chest 23 has concentrated solution pipeline to connect with absorber 2 with the 3rd solution heat exchanger 17 through the 4th solution heat exchanger 26 again，3rd generator 15 also refrigerant steam channel connects with the 3rd absorber 20，Second point of steam chest 23 also refrigerant steam channel connects with the 4th absorber 24，Second absorber 3 there is weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 and absorber 2 connect with a point steam chest 14 and are adjusted to the second absorber 3 and have weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13、Absorber 2 connects with a point steam chest 14 with the 4th absorber 24，3rd generator 15 also has driving heat medium pipeline and ft connection.
null2. in flow process，The weak solution of absorber 2 enters the 4th absorber 24 through solution pump 8 and the 3rd solution heat exchanger 17、Absorb refrigerant vapour heat release in flowing through its interior solution，The weak solution of the 4th absorber 24 enters the 3rd absorber 20 through the 3rd solution pump 18 and the 4th solution heat exchanger 26、Absorb refrigerant vapour heat release in flowing through its interior solution，The weak solution of the 3rd absorber 20 enters generator 1 through the 4th solution pump 25 and solution heat exchanger 12，The concentrated solution of generator 1 enters the 3rd generator 15 through solution heat exchanger 12，Thermal medium is driven to flow through the 3rd generator 15、Heating enters its interior solution release and provides refrigerant vapour to the 3rd absorber 20，The concentrated solution of the 3rd generator 15 flows through the 3rd absorber 20 after solution choke valve 21 reducing pressure by regulating flow、Second point of steam chest 23 is entered after heat absorbing part vaporization，The concentrated solution of second point of steam chest 23 enters absorber 2 through the 4th solution heat exchanger 26 and the 3rd solution heat exchanger 17，The refrigerant vapour of second point of steam chest 23 enters the 4th absorber 24；The weak solution of the second absorber 3 enters a point steam chest 14 after flowing through absorber 2 and the 4th absorber 24, heat absorbing part vaporization successively after the second solution pump 9 and the second solution heat exchanger 13, forms Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 13 is achieved in that
1. in structure, in the Branch-cycle first-class absorption type heat pump shown in Fig. 1, increase by the 3rd generator, 3rd absorber, 3rd solution heat exchanger and the 3rd solution pump, generator 1 has refrigerant steam channel connect with condenser 4 be adjusted to generator 1 and have refrigerant steam channel to connect with the 3rd absorber 20, 3rd absorber 20 also weak solution pipeline connects with the 3rd generator 15 with the 3rd solution heat exchanger 17 through the 3rd solution pump 18, 3rd generator 15 also concentrated solution pipeline connects with the 3rd absorber 20 through the 3rd solution heat exchanger 17, 3rd generator 15 also refrigerant steam channel connects with condenser 4, 3rd generator 15 also has driving heat medium pipeline and ft connection, 3rd absorber 20 also has heated medium pipeline and ft connection.
2. in flow process, the refrigerant vapour of generator 1 enters the 3rd absorber 20, is absorbed also heat release by concentrated solution in heated medium, the weak solution of the 3rd absorber 20 enters the 3rd generator 15 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, drive thermal medium to flow through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to condenser 4, the concentrated solution of the 3rd generator 15 enters the 3rd absorber 20 through the 3rd solution heat exchanger 17, forms Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 14 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Generator 1 has refrigerant steam channel connect with condenser 4 be adjusted to generator 1 and have refrigerant steam channel to connect with the 3rd absorber 20，3rd absorber 20 also weak solution pipeline connects with the 3rd generator 15 with the 3rd solution heat exchanger 17 through the 3rd solution pump 18，3rd generator 15 also concentrated solution pipeline connects with the 3rd absorber 20 through the 3rd solution heat exchanger 17，3rd generator 15 also refrigerant steam channel connects with condenser 4，Second absorber 3 there is weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 and absorber 2 connect with a point steam chest 14 and are adjusted to the second absorber 3 and have weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 connects with a point steam chest 14 with the 3rd absorber 20，Absorber 2 sets up heated medium pipeline and ft connection，3rd generator 15 also has driving heat medium pipeline and ft connection.
2. in flow process, the refrigerant vapour of generator 1 enters the 3rd absorber 20, absorbed by concentrated solution and heat release is in flowing through its interior solution, the weak solution of the 3rd absorber 20 enters the 3rd generator 15 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, thermal medium is driven to flow through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to condenser 4, the concentrated solution of the 3rd generator 15 enters the 3rd absorber 20 through the 3rd solution heat exchanger 17, the cryogen liquid of condenser 4 enters vaporizer 6 through choke valve 10 reducing pressure by regulating flow, absorb waste heat become refrigerant vapour and pass through to absorber 2, the concentrated solution of generator 1 enters absorber 2 through solution heat exchanger 12, absorb refrigerant vapour heat release in heated medium；The weak solution of the second absorber 3 enters a point steam chest 14 after flowing through the 3rd absorber 20, heat absorbing part vaporization after the second solution pump 9 and the second solution heat exchanger 13, forms Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 15 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Generator 1 has refrigerant steam channel connect with condenser 4 be adjusted to generator 1 and have refrigerant steam channel to connect with the 3rd absorber 20，3rd absorber 20 also weak solution pipeline connects with the 3rd generator 15 with the 3rd solution heat exchanger 17 through the 3rd solution pump 18，3rd generator 15 also concentrated solution pipeline connects with the 3rd absorber 20 through the 3rd solution heat exchanger 17，3rd generator 15 also refrigerant steam channel connects with condenser 4，Second absorber 3 there is weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 and absorber 2 connect with a point steam chest 14 and are adjusted to the second absorber 3 and have weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13、Absorber 2 connects with a point steam chest 14 with the 3rd absorber 20，3rd generator 15 also has driving heat medium pipeline and ft connection.
2. in flow process, the refrigerant vapour of generator 1 enters the 3rd absorber 20, is absorbed also heat release by concentrated solution in flowing through its interior solution, the weak solution of the 3rd absorber 20 enters the 3rd generator 15 through the 3rd solution pump 18 and the 3rd solution heat exchanger 17, drive thermal medium to flow through the 3rd generator 15, heating enters its interior solution release and provides refrigerant vapour to condenser 4, and the concentrated solution of the 3rd generator 15 enters the 3rd absorber 20 through the 3rd solution heat exchanger 17；The weak solution of the second absorber 3 enters a point steam chest 14 after flowing through absorber 2 and the 3rd absorber 20, heat absorbing part vaporization successively after the second solution pump 9 and the second solution heat exchanger 13, forms Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 16 is achieved in that
1. in structure, in the Branch-cycle first-class absorption type heat pump shown in Fig. 1, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, second solution pump 9 is set up weak solution pipeline and is connected with newly-increased generator A through newly-increased solution heat exchanger C, newly-increased generator A also has concentrated solution pipeline to connect through newly-increased solution heat exchanger C and the second absorber 3, refrigerant steam channel is had connect with the second condenser 5 to be adjusted to after point steam chest 14 has refrigerant steam channel to connect with newly-increased generator A and increase generator A newly and have cryogen liquid pipeline warp to increase choke valve B newly again and the second condenser 5 connects a point steam chest 14, newly-increased generator A also has refrigerant steam channel to connect with the second condenser 5.
2. in flow process, the refrigerant vapour dividing steam chest 14 release is supplied to newly-increased generator A and makees to drive thermal medium, the part weak solution of the second absorber 3 enters newly-increased generator A through the second solution pump 9 and newly-increased solution heat exchanger C, refrigerant vapour flows through newly-increased generator A, heating enters its interior solution release and provides refrigerant vapour to the second condenser 5, the concentrated solution of newly-increased generator A enters the second absorber 3 through newly-increased solution heat exchanger C, the refrigerant vapour heat release flowing through newly-increased generator A becomes warp newly-increased choke valve B throttling entrance the second condenser 5 after cryogen liquid, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 17 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase newly-increased generator、Newly-increased choke valve and newly-increased solution heat exchanger，Second absorber 3 there is weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 and absorber 2 connect with a point steam chest 14 and are adjusted to the second absorber 3 and have weak solution pipeline through the second solution pump 9、Newly-increased solution heat exchanger C、Second solution heat exchanger 13 connects with a point steam chest 14 with absorber 2，Have concentrated solution pipeline to connect with the second absorber 3 through the second solution heat exchanger 13 to be adjusted to point steam chest 14 and have concentrated solution pipeline to connect with newly-increased generator A through the second solution heat exchanger 13 by a point steam chest 14，Newly-increased generator A has concentrated solution pipeline to connect through newly-increased solution heat exchanger C and the second absorber 3 again，Refrigerant steam channel is had connect with the second condenser 5 to be adjusted to after point steam chest 14 has refrigerant steam channel to connect with newly-increased generator A and increase generator A newly and have cryogen liquid pipeline warp to increase choke valve B newly again and the second condenser 5 connects a point steam chest 14，Newly-increased generator A also has refrigerant steam channel to connect with the second condenser 5.
2. in flow process, the refrigerant vapour dividing steam chest 14 release is supplied to newly-increased generator A and makees to drive thermal medium, the weak solution of the second absorber 3 is through the second solution pump 9, absorber 2 is flowed through after newly-increased solution heat exchanger C and the second solution heat exchanger 13, a point steam chest 14 is entered after heat absorbing part vaporization, the concentrated solution dividing steam chest 14 enters newly-increased generator A through the second solution heat exchanger 13, refrigerant vapour flows through newly-increased generator A, heating enters its interior solution release and provides refrigerant vapour to the second condenser 5, the concentrated solution of newly-increased generator A enters the second absorber 3 through newly-increased solution heat exchanger C, the refrigerant vapour heat release flowing through newly-increased generator A becomes warp newly-increased choke valve B throttling entrance the second condenser 5 after cryogen liquid, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 18 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase newly-increased generator、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second absorber 3 there is weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 and absorber 2 connect with a point steam chest 14 and are adjusted to the second absorber 3 and have weak solution pipeline to connect with newly-increased generator A through the second solution pump 9 and the second solution heat exchanger 13，Newly-increased generator A has concentrated solution pipeline again through new solubilization liquid pump D、Newly-increased solution heat exchanger C connects with a point steam chest 14 with absorber 2，Have concentrated solution pipeline connect with the second absorber 3 through the second solution heat exchanger 13 to be adjusted to point steam chest 14 and have concentrated solution pipeline warp to increase solution heat exchanger C newly and the second solution heat exchanger 13 connects with the second absorber 3 by a point steam chest 14，Refrigerant steam channel is had connect with the second condenser 5 to be adjusted to after point steam chest 14 has refrigerant steam channel to connect with newly-increased generator A and increase generator A newly and have cryogen liquid pipeline warp to increase choke valve B newly again and the second condenser 5 connects a point steam chest 14，Newly-increased generator A also has refrigerant steam channel to connect with the second condenser 5.
2. in flow process, the refrigerant vapour dividing steam chest 14 release is supplied to newly-increased generator A and makees to drive thermal medium, the weak solution of the second absorber 3 enters newly-increased generator A through the second solution pump 9 and the second solution heat exchanger 13, refrigerant vapour flows through newly-increased generator A, heating enters its interior solution release and provides refrigerant vapour to the second condenser 5, the concentrated solution of newly-increased generator A flows through absorber 2 after new solubilization liquid pump D and newly-increased solution heat exchanger C, a point steam chest 14 is entered after heat absorbing part gasification, the concentrated solution dividing steam chest 14 enters the second absorber 3 through newly-increased solution heat exchanger C and the second solution heat exchanger 13, the refrigerant vapour heat release flowing through newly-increased generator A becomes warp newly-increased choke valve B throttling entrance the second condenser 5 after cryogen liquid, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 19 is achieved in that
1. in structure, in the Branch-cycle first-class absorption type heat pump shown in Fig. 1, increase newly-increased point of steam chest, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, second vaporizer 7 has refrigerant steam channel connect with the second absorber 3 be adjusted to the second vaporizer 7 and have refrigerant steam channel to connect with newly-increased absorber E, newly-increased absorber E also has weak solution pipeline through new solubilization liquid pump D, newly-increased solution heat exchanger C connects with a newly-increased point steam chest F with absorber 2, a newly-increased point steam chest F also has concentrated solution pipeline to connect with newly-increased absorber E through newly-increased solution heat exchanger C, a newly-increased point steam chest F also has refrigerant steam channel to connect with the second absorber 3, newly-increased absorber E also has heated medium pipeline and ft connection.
2. in flow process, the refrigerant vapour that second vaporizer 7 produces enters newly-increased absorber E, is absorbed also heat release by concentrated solution in heated medium, the weak solution of newly-increased absorber E flows through absorber 2 after new solubilization liquid pump D and newly-increased solution heat exchanger C, heat absorbing part gasification enters newly-increased point of steam chest F, the concentrated solution of newly-increased point of steam chest F enters newly-increased absorber E through newly-increased solution heat exchanger C, the refrigerant vapour of newly-increased point of steam chest F release enters the second absorber 3, forms Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 20 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase newly-increased point of steam chest、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber 3 there is weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 and absorber 2 connect with a point steam chest 14 and are adjusted to the second absorber 3 and have weak solution pipeline to connect with newly-increased absorber E through the second solution pump 9 and newly-increased solution heat exchanger C，Newly-increased absorber E has weak solution pipeline again through new solubilization liquid pump D、Second solution heat exchanger 13 connects with a point steam chest 14 with absorber 2，Have concentrated solution pipeline connect with the second absorber 3 through the second solution heat exchanger 13 to be adjusted to point steam chest 14 and have concentrated solution pipeline to divide a steam chest F to connect through the second solution heat exchanger 13 and absorber 2 with increasing newly by a point steam chest 14，A newly-increased point steam chest F also has concentrated solution pipeline to connect through newly-increased solution heat exchanger C and the second absorber 3，A newly-increased point steam chest F also has refrigerant steam channel to connect with newly-increased absorber E，Newly-increased absorber E also has heated medium pipeline and ft connection.
2. in flow process, the weak solution of the second absorber 3 enters newly-increased absorber E through the second solution pump 9 and newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in heated medium, the weak solution of newly-increased absorber E flows through absorber 2 after new solubilization liquid pump D and the second solution heat exchanger 13, a point steam chest 14 is entered after heat absorbing part gasification, the concentrated solution dividing steam chest 14 flows through absorber 2 after the second solution heat exchanger 13, newly-increased point of steam chest F is entered after heat absorbing part gasification, the concentrated solution of newly-increased point of steam chest F enters the second absorber 3 through newly-increased solution heat exchanger C, the refrigerant vapour of newly-increased point of steam chest F enters newly-increased absorber E, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 21 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve、Newly-increased point of steam chest and newly-increased second point of steam chest，Second absorber 3 there is weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 and absorber 2 connect with a point steam chest 14 and are adjusted to the second absorber 3 and have weak solution pipeline to connect with newly-increased second absorber K through the second solution pump 9 and newly-increased solution heat exchanger C，Newly-increased second absorber K also has weak solution pipeline to connect with newly-increased absorber E with newly-increased second solution heat exchanger H through new solubilization liquid pump D，Newly-increased absorber E has weak solution pipeline again through newly-increased second solution pump G、Second solution heat exchanger 13 connects with a point steam chest 14 with absorber 2，Have concentrated solution pipeline connect with the second absorber 3 through the second solution heat exchanger 13 to be adjusted to point steam chest 14 and have concentrated solution pipeline to divide a steam chest F to connect through the second solution heat exchanger 13 and absorber 2 with increasing newly by a point steam chest 14，A newly-increased point steam chest F also has concentrated solution pipeline to connect with newly-increased second point of steam chest I through new solubilization liquid choke valve J and newly-increased absorber E，Newly-increased second point of steam chest I has concentrated solution pipeline to connect through newly-increased second solution heat exchanger H and newly-increased solution heat exchanger C and the second absorber 3 again，A newly-increased point steam chest F also has refrigerant steam channel to connect with newly-increased absorber E，Newly-increased second point of steam chest I also has refrigerant steam channel to connect with newly-increased second absorber K，Newly-increased absorber E and newly-increased second absorber K has heated medium pipeline and ft connection the most respectively.
null2. in flow process，The weak solution of the second absorber 3 enters newly-increased second absorber K through the second solution pump 9 and newly-increased solution heat exchanger C、Absorb refrigerant vapour heat release in heated medium，The weak solution of newly-increased second absorber K enters newly-increased absorber E through new solubilization liquid pump D and newly-increased second solution heat exchanger H、Absorption refrigerant vapour respectively heat release are in heated medium and flow through its interior solution，The weak solution of newly-increased absorber E flows through absorber 2 after newly-increased second solution pump G and the second solution heat exchanger 13、A point steam chest 14 is entered after heat absorbing part gasification，The concentrated solution dividing steam chest 14 flows through absorber 2 after the second solution heat exchanger 13、Newly-increased point of steam chest F is entered after heat absorbing part gasification，The concentrated solution of newly-increased point of steam chest F flows through newly-increased absorber E after new solubilization liquid choke valve J reducing pressure by regulating flow、Newly-increased second point of steam chest I is entered after heat absorbing part vaporization，The concentrated solution of newly-increased second point of steam chest I enters the second absorber 3 through newly-increased second solution heat exchanger H and newly-increased solution heat exchanger C，The refrigerant vapour of newly-increased point of steam chest F enters newly-increased absorber E，The refrigerant vapour of newly-increased point of steam chest I enters newly-increased second absorber K，Form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 22 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase newly-increased generator、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber 3 there is weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 and absorber 2 connect with a point steam chest 14 and are adjusted to the second absorber 3 and have weak solution pipeline to connect with newly-increased absorber E through the second solution pump 9 and newly-increased solution heat exchanger C，Newly-increased absorber E has weak solution pipeline again through new solubilization liquid pump D、Second solution heat exchanger 13 connects with a point steam chest 14 with absorber 2，Have concentrated solution pipeline to connect with the second absorber 3 through the second solution heat exchanger 13 to be adjusted to point steam chest 14 and have concentrated solution pipeline to connect with newly-increased generator A through the second solution heat exchanger 13 by a point steam chest 14，Newly-increased generator A has concentrated solution pipeline to connect through newly-increased solution heat exchanger C and the second absorber 3 again，Newly-increased generator A also has refrigerant steam channel to connect with newly-increased absorber E，Newly-increased generator A also has driving heat medium pipeline and ft connection，Newly-increased absorber E also has heated medium pipeline and ft connection.
2. in flow process, the weak solution of the second absorber 3 enters newly-increased absorber E through the second solution pump 9 and newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in heated medium, the weak solution of newly-increased absorber E flows through absorber 2 after new solubilization liquid pump D and the second solution heat exchanger 13, a point steam chest 14 is entered after heat absorbing part gasification, the concentrated solution dividing steam chest 14 enters newly-increased generator A through the second solution heat exchanger 13, thermal medium is driven to flow through newly-increased generator A, heating enters its interior solution release and provides refrigerant vapour to newly-increased absorber E, the concentrated solution of newly-increased generator A enters the second absorber 3 through newly-increased solution heat exchanger C, form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 23 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase newly-increased generator、Newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve and newly-increased point of steam chest，Second absorber 3 there is weak solution pipeline through the second solution pump 9、Second solution heat exchanger 13 and absorber 2 connect with a point steam chest 14 and are adjusted to the second absorber 3 and have weak solution pipeline to connect with newly-increased second absorber K through the second solution pump 9 and newly-increased solution heat exchanger C，Newly-increased second absorber K also has weak solution pipeline to connect with newly-increased absorber E with newly-increased second solution heat exchanger H through new solubilization liquid pump D，Newly-increased absorber E has weak solution pipeline again through newly-increased second solution pump G、Second solution heat exchanger 13 connects with a point steam chest 14 with absorber 2，Have concentrated solution pipeline to connect with the second absorber 3 through the second solution heat exchanger 13 to be adjusted to point steam chest 14 and have concentrated solution pipeline to connect with newly-increased generator A through the second solution heat exchanger 13 by a point steam chest 14，Newly-increased generator A also has concentrated solution pipeline to connect with a newly-increased point steam chest F through new solubilization liquid choke valve J and newly-increased absorber E，A newly-increased point steam chest F has concentrated solution pipeline to connect through newly-increased second solution heat exchanger H and newly-increased solution heat exchanger C and the second absorber 3 again，Newly-increased generator A also has refrigerant steam channel to connect with newly-increased absorber E，A newly-increased point steam chest F also has refrigerant steam channel to connect with newly-increased second absorber K，Newly-increased generator A also has driving heat medium pipeline and ft connection，Newly-increased absorber E and newly-increased second absorber K has heated medium pipeline and ft connection the most respectively.
null2. in flow process，The weak solution of the second absorber 3 enters newly-increased second absorber K through the second solution pump 9 and newly-increased solution heat exchanger C、Absorb refrigerant vapour heat release in heated medium，The weak solution of newly-increased second absorber K enters newly-increased absorber E through new solubilization liquid pump D and newly-increased second solution heat exchanger H、Absorption refrigerant vapour respectively heat release are in heated medium and flow through its interior solution，The weak solution of newly-increased absorber E flows through absorber 2 after newly-increased second solution pump G and the second solution heat exchanger 13、A point steam chest 14 is entered after heat absorbing part gasification，The concentrated solution dividing steam chest 14 enters newly-increased generator A through the second solution heat exchanger 13，Thermal medium is driven to flow through newly-increased generator A、Heating enters its interior solution release and provides refrigerant vapour to newly-increased absorber E，The concentrated solution of newly-increased generator A flows through newly-increased absorber E after new solubilization liquid choke valve J reducing pressure by regulating flow、Newly-increased point of steam chest F is entered after heat absorbing part vaporization，The concentrated solution of newly-increased point of steam chest F enters the second absorber 3 through newly-increased second solution heat exchanger H and newly-increased solution heat exchanger C，The refrigerant vapour of newly-increased point of steam chest F enters newly-increased second absorber K，Form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 24 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase newly-increased generator、Newly-increased absorber、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second vaporizer 7 has refrigerant steam channel connect with the second absorber 3 be adjusted to the second vaporizer 7 and have refrigerant steam channel to connect with newly-increased absorber E，Refrigerant steam channel is had connect with the second condenser 5 to be adjusted to after point steam chest 14 has refrigerant steam channel to connect with newly-increased generator A and increase generator A newly and have cryogen liquid pipeline warp to increase choke valve B newly again to connect with newly-increased vaporizer M a point steam chest 14，Newly-increased vaporizer M also has refrigerant steam channel to connect with the second absorber 3，Newly-increased generator A also has concentrated solution pipeline to connect with newly-increased absorber E through newly-increased solution heat exchanger C，Newly-increased absorber E also has weak solution pipeline to connect with newly-increased generator A with newly-increased solution heat exchanger C through new solubilization liquid pump D，Newly-increased generator A also has refrigerant steam channel to connect with the second condenser 5，Newly-increased absorber E also has heated medium pipeline and ft connection，Newly-increased vaporizer M also has surplus heat medium pipeline and ft connection.
null2. in flow process，The refrigerant vapour dividing steam chest 14 to produce is supplied to newly-increased generator A and makees to drive thermal medium，The weak solution of newly-increased absorber E enters newly-increased generator A through new solubilization liquid pump D and newly-increased solution heat exchanger C，Refrigerant vapour flows through newly-increased generator A、Heating enters its interior solution release and provides refrigerant vapour to the second condenser 5，The concentrated solution of newly-increased generator A enters newly-increased absorber E through newly-increased solution heat exchanger C，The refrigerant vapour heat release flowing through newly-increased generator A becomes the warp newly-increased choke valve B reducing pressure by regulating flow newly-increased vaporizer M of entrance after cryogen liquid、Absorb waste heat become refrigerant vapour and provide to the second absorber 3，The cryogen liquid of the second condenser 5 enters the second vaporizer 7 through second throttle 11 reducing pressure by regulating flow、Absorb waste heat become refrigerant vapour and provide to newly-increased absorber E，Form Branch-cycle first-class absorption type heat pump.
Branch-cycle first-class absorption type heat pump shown in Figure 25 is achieved in that
null1. in structure，In the Branch-cycle first-class absorption type heat pump shown in Fig. 1，Increase newly-increased choke valve、Newly-increased solution heat exchanger、New solubilization liquid pump、Newly-increased absorber、Newly-increased point of steam chest、Newly-increased condenser and newly-increased vaporizer，Cancel the heated medium pipeline of the second absorber 3 and ft connection，Newly-increased absorber E has weak solution pipeline through new solubilization liquid pump D、Newly-increased solution heat exchanger C and the second absorber 3 connect with a newly-increased point steam chest F，A newly-increased point steam chest F also has concentrated solution to connect with newly-increased absorber E through newly-increased solution heat exchanger C，A newly-increased point steam chest F also has refrigerant steam channel to connect with newly-increased condenser L，Newly-increased condenser L also has cryogen liquid pipeline to connect with newly-increased vaporizer M through newly-increased choke valve B，Newly-increased vaporizer M also has refrigerant steam channel to connect with newly-increased absorber E，Newly-increased absorber E and newly-increased condenser L has heated medium pipeline and ft connection the most respectively，Newly-increased vaporizer M also has surplus heat medium pipeline and ft connection.
2. in flow process, second vaporizer 7 produces refrigerant vapour and enters the second absorber 3, absorbed by concentrated solution and heat release is in flowing through its interior solution, the weak solution of newly-increased absorber E flows through the second absorber 3 after new solubilization liquid pump D and newly-increased solution heat exchanger C, newly-increased point of steam chest F is entered after heat absorbing part gasification, the concentrated solution of newly-increased point of steam chest F enters newly-increased absorber E through newly-increased solution heat exchanger C, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour of newly-increased point of steam chest F enters newly-increased condenser L, heat release becomes cryogen liquid in heated medium, the cryogen liquid of newly-increased condenser L enters newly-increased vaporizer M through newly-increased choke valve B reducing pressure by regulating flow, absorb waste heat become refrigerant vapour and provide to newly-increased absorber E, form Branch-cycle first-class absorption type heat pump.
Effect that the technology of the present invention can realize Branch-cycle first-class absorption type heat pump proposed by the invention has following effect and an advantage:
(1) two-way or the circulation of multichannel solution, waste heat is used for the generating process of other circulation solution, is conducive to driving the selection between thermal medium, circulation solution and flow process and coupling, overcomes the restriction of single working media, improves the temperature difference and utilize level after promoting temperature.
(2) multiterminal heat supply, it is possible to preferably adapt to the operating mode that the range of temperature of heated medium is wider, obtains rational thermodynamics consummating degree.
(3) there is the flow process of backheat heat supply end, thermodynamic parameter smooth change, heating parameter scalable, it is possible to preferably adaptation condition change, obtain higher thermodynamics consummating degree.
(4) there is the flow process of backheat heat supply end, it is possible to realize the deep exploitation of driving heat source or the lifting amplitude of waste heat supply temperature can be increased, improve heat utilization rate.
(5) comprising single-action supplies thermal flow process, substep to realize temperature difference utilization for thermal flow process and economic benefits and social benefits, is conducive to improving the performance index circulated and thermodynamics consummating degree.
(6) there is single-action-economic benefits and social benefits backheat or there is the flow process of economic benefits and social benefits backheat, thermodynamic parameter smooth change, heating parameter scalable, it is possible to preferably adaptation condition change, obtaining higher performance index and thermodynamics consummating degree.
(7) enrich the type of first-class absorption type heat pump, extend the range of application of first-class absorption type heat pump, be conducive to preferably using first-class absorption type heat pump to realize the temperature difference and utilize, improve utilization efficiency of heat energy.

Claims (48)

1. Branch-cycle first-class absorption type heat pump, is mainly made up of generator, absorber, the second absorber, condenser, the second condenser, vaporizer, the second vaporizer, solution pump, the second solution pump, choke valve, second throttle, solution heat exchanger, the second solution heat exchanger and a point steam chest；Absorber (2) has weak solution pipeline to connect with generator (1) with solution heat exchanger (12) through solution pump (8), generator (1) also has concentrated solution pipeline to connect with absorber (2) through solution heat exchanger (12), generator (1) also has refrigerant steam channel to connect with condenser (4), condenser (4) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (10), and vaporizer (6) also has refrigerant steam channel to connect with absorber (2)；Second absorber (3) has weak solution pipeline through the second solution pump (9), second solution heat exchanger (13) connects with a point steam chest (14) with absorber (2), steam chest (14) is divided to also have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13), steam chest (14) is divided to also have refrigerant steam channel to connect with the second condenser (5), second condenser (5) also has cryogen liquid pipeline to connect with the second vaporizer (7) through second throttle (11), second vaporizer (7) also has refrigerant steam channel to connect with the second absorber (3)；Generator (1) also has driving heat medium pipeline and ft connection, second absorber (3), condenser (4) and the second condenser (5) have heated medium pipeline and ft connection the most respectively, vaporizer (6) and the second vaporizer (7) have surplus heat medium pipeline and ft connection the most respectively, form Branch-cycle first-class absorption type heat pump.
null2. Branch-cycle first-class absorption type heat pump，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd choke valve and the 3rd solution heat exchanger，Solution pump (8) is set up weak solution pipeline and is connected with the 3rd generator (15) through the 3rd solution heat exchanger (17)，3rd generator (15) also has concentrated solution pipeline to connect with absorber (2) through the 3rd solution heat exchanger (17)，Generator (1) has refrigerant steam channel connect with condenser (4) be adjusted to the 3rd generator (15) after generator (1) has refrigerant steam channel to connect with the 3rd generator (15) and have cryogen liquid pipeline to connect with condenser (4) through the 3rd choke valve (16) again，3rd generator (15) also has refrigerant steam channel to connect with condenser (4)，Form Branch-cycle first-class absorption type heat pump.
null3. Branch-cycle first-class absorption type heat pump，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd choke valve and the 3rd solution heat exchanger，Absorber (2) has weak solution pipeline connect with generator (1) through solution pump (8) and solution heat exchanger (12) be adjusted to absorber (2) and have weak solution pipeline through solution pump (8)、3rd solution heat exchanger (17) connects with generator (1) with solution heat exchanger (12)，Generator (1) has concentrated solution pipeline connect with absorber (2) through solution heat exchanger (12) be adjusted to generator (1) and have concentrated solution pipeline to connect with the 3rd generator (15) through solution heat exchanger (12)，3rd generator (15) has concentrated solution pipeline to connect with absorber (2) through the 3rd solution heat exchanger (17) again，Generator (1) has refrigerant steam channel connect with condenser (4) be adjusted to the 3rd generator (15) after generator (1) has refrigerant steam channel to connect with the 3rd generator (15) and have cryogen liquid pipeline to connect with condenser (4) through the 3rd choke valve (16) again，3rd generator (15) also has refrigerant steam channel to connect with condenser (4)，Form Branch-cycle first-class absorption type heat pump.
null4. Branch-cycle first-class absorption type heat pump，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd choke valve、3rd solution heat exchanger and the 3rd solution pump，Absorber (2) has weak solution pipeline connect with generator (1) through solution pump (8) and solution heat exchanger (12) be adjusted to absorber (2) and have weak solution pipeline to connect with the 3rd generator (15) through solution pump (8) and the second solution heat exchanger (12)，3rd generator (15) has concentrated solution pipeline to connect with generator (1) with the 3rd solution heat exchanger (17) through the 3rd solution pump (18) again，Generator (1) has concentrated solution pipeline connect with absorber (2) through solution heat exchanger (12) be adjusted to generator (1) and have concentrated solution pipeline to connect with absorber (2) through the 3rd solution heat exchanger (17) and solution heat exchanger (12)，Generator (1) has refrigerant steam channel connect with condenser (4) be adjusted to the 3rd generator (15) after generator (1) has refrigerant steam channel to connect with the 3rd generator (15) and have cryogen liquid pipeline to connect with condenser (4) through the 3rd choke valve (16) again，3rd generator (15) also has refrigerant steam channel to connect with condenser (4)，Form Branch-cycle first-class absorption type heat pump.
null5. Branch-cycle first-class absorption type heat pump，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd choke valve、3rd solution heat exchanger and the 3rd condenser，Absorber (2) has weak solution pipeline connect with generator (1) through solution pump (8) and solution heat exchanger (12) be adjusted to absorber (2) and have weak solution pipeline through solution pump (8)、3rd solution heat exchanger (17) connects with generator (1) with solution heat exchanger (12)，Generator (1) has concentrated solution pipeline connect with absorber (2) through solution heat exchanger (12) be adjusted to generator (1) and have concentrated solution pipeline to connect with the 3rd generator (15) through solution heat exchanger (12)，3rd generator (15) has concentrated solution pipeline to connect with absorber (2) through the 3rd solution heat exchanger (17) again，3rd generator (15) also has refrigerant steam channel to connect with the 3rd condenser (19)，3rd condenser (19) also has cryogen liquid pipeline to connect with vaporizer (6) through the 3rd choke valve (16)，3rd generator (15) also has driving heat medium pipeline and ft connection，3rd condenser (19) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump；Wherein, or by condenser (4) have cryogen liquid pipeline to connect with vaporizer (6) through choke valve (10) to be adjusted to condenser (4) and have cryogen liquid pipeline to connect with the 3rd condenser (19) through choke valve (10).
null6. Branch-cycle first-class absorption type heat pump，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Absorber (2) has weak solution pipeline connect with generator (1) through solution pump (8) and solution heat exchanger (12) be adjusted to absorber (2) and have weak solution pipeline to connect with the 3rd absorber (20) through solution pump (8) and the 3rd solution heat exchanger (17)，3rd absorber (20) has weak solution pipeline to connect with generator (1) with solution heat exchanger (12) through the 3rd solution pump (18) again，Generator (1) has concentrated solution pipeline connect with absorber (2) through solution heat exchanger (12) be adjusted to generator (1) and have concentrated solution pipeline to connect with the 3rd generator (15) through solution heat exchanger (12)，3rd generator (15) has concentrated solution pipeline to connect with absorber (2) through the 3rd solution heat exchanger (17) again，3rd generator (15) also has refrigerant steam channel to connect with the 3rd absorber (20)，3rd generator (15) also has driving heat medium pipeline and ft connection，3rd absorber (20) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null7. Branch-cycle first-class absorption type heat pump，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Absorber (2) has weak solution pipeline connect with generator (1) through solution pump (8) and solution heat exchanger (12) be adjusted to absorber (2) and have weak solution pipeline to connect with the 3rd absorber (20) through solution pump (8) and the 3rd solution heat exchanger (17)，3rd absorber (20) has weak solution pipeline to connect with generator (1) with solution heat exchanger (12) through the 3rd solution pump (18) again，Generator (1) has concentrated solution pipeline connect with absorber (2) through solution heat exchanger (12) be adjusted to generator (1) and have concentrated solution pipeline to connect with the 3rd generator (15) through solution heat exchanger (12)，3rd generator (15) has concentrated solution pipeline to connect with absorber (2) through the 3rd solution heat exchanger (17) again，3rd generator (15) also has refrigerant steam channel to connect with the 3rd absorber (20)，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and absorber (2) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) connects with a point steam chest (14) with the 3rd absorber (20)，3rd generator (15) also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null8. Branch-cycle first-class absorption type heat pump，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd absorber、3rd solution pump、Second point of steam chest、Solution choke valve and the second solution choke valve，Absorber (2) has weak solution pipeline connect with generator (1) through solution pump (8) and solution heat exchanger (12) be adjusted to absorber (2) and have weak solution pipeline to connect with the 3rd absorber (20) through solution pump (8) and solution heat exchanger (12)，3rd absorber (20) has weak solution pipeline to connect with generator (1) through the second solution choke valve (22) again，Generator (1) has concentrated solution pipeline connect with absorber (2) through solution heat exchanger (12) be adjusted to generator (1) and have concentrated solution pipeline to connect with the 3rd generator (15) through the 3rd solution pump (18)，3rd generator (15) also has concentrated solution pipeline to connect with second point of steam chest (23) with the 3rd absorber (20) through solution choke valve (21)，Second point of steam chest (23) has concentrated solution pipeline to connect with absorber (2) through solution heat exchanger (12) again，3rd generator (15) also has refrigerant steam channel to connect with the 3rd absorber (20)，Second point of steam chest (23) also has refrigerant steam channel to connect with condenser (4)，3rd generator (15) also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null9. Branch-cycle first-class absorption type heat pump，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd absorber、Second point of steam chest and solution choke valve，Absorber (2) has weak solution pipeline connect with generator (1) through solution pump (8) and solution heat exchanger (12) be adjusted to absorber (2) and have weak solution pipeline to connect with the 3rd absorber (20) through solution pump (8) and solution heat exchanger (12)，3rd absorber (20) also has weak solution pipeline and the connection of the 3rd generator (15)，3rd generator (15) has concentrated solution pipeline to connect with generator (1) through solution choke valve (21) again，Generator (1) has concentrated solution pipeline connect with absorber (2) through solution heat exchanger (12) be adjusted to generator (1) and have concentrated solution pipeline to connect with second point of steam chest (23) through the 3rd absorber (20)，Second point of steam chest (23) has concentrated solution pipeline to connect with absorber (2) through solution heat exchanger (12) again，3rd generator (15) also has refrigerant steam channel to connect with the 3rd absorber (20)，Second point of steam chest (23) also has refrigerant steam channel to connect with condenser (4)，3rd generator (15) also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump；Wherein, arrange for convenience of parts, or increase by the 3rd solution pump, the 3rd absorber (20) have weak solution pipeline and the connection of the 3rd generator (15) are adjusted to the 3rd absorber (20) and have weak solution pipeline to connect with the 3rd generator (15) through the 3rd solution pump (18).
null10. Branch-cycle first-class absorption type heat pump，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and second point of steam chest，Absorber (2) has weak solution pipeline connect with generator (1) through solution pump (8) and solution heat exchanger (12) be adjusted to absorber (2) and have weak solution pipeline through solution pump (8)、Solution heat exchanger (12) connects with the 3rd absorber (20) with the 3rd solution heat exchanger (17)，3rd absorber (20) also has weak solution pipeline and the connection of the 3rd generator (15)，3rd generator (15) has concentrated solution pipeline to connect with generator (1) through the 3rd solution heat exchanger (17) again，Generator (1) has concentrated solution pipeline connect with absorber (2) through solution heat exchanger (12) be adjusted to generator (1) and have concentrated solution pipeline to connect with second point of steam chest (23) through the 3rd absorber (20)，Second point of steam chest (23) has concentrated solution pipeline to connect with absorber (2) through solution heat exchanger (12) again，3rd generator (15) also has refrigerant steam channel to connect with the 3rd absorber (20)，Second point of steam chest (23) also has refrigerant steam channel to connect with condenser (4)，3rd generator (15) also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump；Wherein, arrange for convenience of parts, or increase by the 3rd solution pump, the 3rd absorber (20) have weak solution pipeline and the connection of the 3rd generator (15) are adjusted to the 3rd absorber (20) and have weak solution pipeline to connect with the 3rd generator (15) through the 3rd solution pump (18).
null11. Branch-cycle first-class absorption type heat pumps，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd absorber、4th absorber、3rd solution pump、4th solution pump、3rd solution heat exchanger、4th solution heat exchanger、Second point of steam chest and solution choke valve，Absorber (2) has weak solution pipeline connect with generator (1) through solution pump (8) and solution heat exchanger (12) be adjusted to absorber (2) and have weak solution pipeline to connect with the 4th absorber (24) through solution pump (8) and the 3rd solution heat exchanger (17)，4th absorber (24) also has weak solution pipeline to connect with the 3rd absorber (20) with the 4th solution heat exchanger (26) through the 3rd solution pump (18)，3rd absorber (20) has weak solution pipeline to connect with generator (1) with solution heat exchanger (12) through the 4th solution pump (25) again，Generator (1) has concentrated solution pipeline connect with absorber (2) through solution heat exchanger (12) be adjusted to generator (1) and have concentrated solution pipeline to connect with the 3rd generator (15) through solution heat exchanger (12)，3rd generator (15) also has concentrated solution pipeline to connect with second point of steam chest (23) with the 3rd absorber (20) through solution choke valve (21)，Second point of steam chest (23) has concentrated solution pipeline to connect with absorber (2) with the 3rd solution heat exchanger (17) through the 4th solution heat exchanger (26) again，3rd generator (15) also has refrigerant steam channel to connect with the 3rd absorber (20)，Second point of steam chest (23) also has refrigerant steam channel to connect with the 4th absorber (24)，3rd generator (15) also has driving heat medium pipeline and ft connection，3rd absorber (20) or also heated medium pipeline and ft connection，4th absorber (24) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null12. Branch-cycle first-class absorption type heat pumps，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd absorber、4th absorber、3rd solution pump、4th solution pump、3rd solution heat exchanger、4th solution heat exchanger、Solution choke valve and second point of steam chest，Absorber (2) has weak solution pipeline connect with generator (1) through solution pump (8) and solution heat exchanger (12) be adjusted to absorber (2) and have weak solution pipeline to connect with the 4th absorber (24) through solution pump (8) and the 3rd solution heat exchanger (17)，4th absorber (24) also has weak solution pipeline to connect with the 3rd absorber (20) with the 4th solution heat exchanger (26) through the 3rd solution pump (18)，3rd absorber (20) has weak solution pipeline to connect with generator (1) with solution heat exchanger (12) through the 4th solution pump (25) again，Generator (1) has concentrated solution pipeline connect with absorber (2) through solution heat exchanger (12) be adjusted to generator (1) and have concentrated solution pipeline to connect with the 3rd generator (15) through solution heat exchanger (12)，3rd generator (15) also has concentrated solution pipeline to connect with second point of steam chest (23) with the 3rd absorber (20) through solution choke valve (21)，Second point of steam chest (23) has concentrated solution pipeline to connect with absorber (2) with the 3rd solution heat exchanger (17) through the 4th solution heat exchanger (26) again，3rd generator (15) also has refrigerant steam channel to connect with the 3rd absorber (20)，Second point of steam chest (23) also has refrigerant steam channel to connect with the 4th absorber (24)，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and absorber (2) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or connect with dividing a steam chest (14) through the 3rd absorber (20)，3rd generator (15) also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null13. Branch-cycle first-class absorption type heat pumps，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Generator (1) has refrigerant steam channel connect with condenser (4) be adjusted to generator (1) and have refrigerant steam channel to connect with the 3rd absorber (20)，3rd absorber (20) also has weak solution pipeline to connect with the 3rd generator (15) with the 3rd solution heat exchanger (17) through the 3rd solution pump (18)，3rd generator (15) also has concentrated solution pipeline to connect with the 3rd absorber (20) through the 3rd solution heat exchanger (17)，3rd generator (15) also has refrigerant steam channel to connect with condenser (4)，3rd generator (15) also has driving heat medium pipeline and ft connection，3rd absorber (20) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null14. Branch-cycle first-class absorption type heat pumps，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Generator (1) has refrigerant steam channel connect with condenser (4) be adjusted to generator (1) and have refrigerant steam channel to connect with the 3rd absorber (20)，3rd absorber (20) also has weak solution pipeline to connect with the 3rd generator (15) with the 3rd solution heat exchanger (17) through the 3rd solution pump (18)，3rd generator (15) also has concentrated solution pipeline to connect with the 3rd absorber (20) through the 3rd solution heat exchanger (17)，3rd generator (15) also has refrigerant steam channel to connect with condenser (4)，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and absorber (2) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) connects with a point steam chest (14) with the 3rd absorber (20)，Absorber (2) sets up heated medium pipeline and ft connection，3rd generator (15) also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null15. Branch-cycle first-class absorption type heat pumps，It is in the Branch-cycle first-class absorption type heat pump described in claim 1，Increase by the 3rd generator、3rd absorber、3rd solution heat exchanger and the 3rd solution pump，Generator (1) has refrigerant steam channel connect with condenser (4) be adjusted to generator (1) and have refrigerant steam channel to connect with the 3rd absorber (20)，3rd absorber (20) also has weak solution pipeline to connect with the 3rd generator (15) with the 3rd solution heat exchanger (17) through the 3rd solution pump (18)，3rd generator (15) also has concentrated solution pipeline to connect with the 3rd absorber (20) through the 3rd solution heat exchanger (17)，3rd generator (15) also has refrigerant steam channel to connect with condenser (4)，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and absorber (2) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) connects with a point steam chest (14) with the 3rd absorber (20)，3rd generator (15) also has driving heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null16. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 1-15，Increase newly-increased generator、Newly-increased choke valve and newly-increased solution heat exchanger，Second solution pump (9) is set up weak solution pipeline and is connected with newly-increased generator (A) through newly-increased solution heat exchanger (C)，Newly-increased generator (A) also has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C)，Refrigerant steam channel is had connect with the second condenser (5) to be adjusted to after a point steam chest (14) has refrigerant steam channel to connect with newly-increased generator (A) and increase generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly again to connect with the second condenser (5) a point steam chest (14)，Newly-increased generator (A) also has refrigerant steam channel to connect with the second condenser (5)，Form Branch-cycle first-class absorption type heat pump.
null17. Branch-cycle first-class absorption type heat pumps，It is in claim 1-6、8-11、In arbitrary Branch-cycle first-class absorption type heat pump described in 13，Increase newly-increased generator、Newly-increased choke valve and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and absorber (2) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline through the second solution pump (9)、Newly-increased solution heat exchanger (C)、Second solution heat exchanger (13) connects with a point steam chest (14) with absorber (2)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C) again，Refrigerant steam channel is had connect with the second condenser (5) to be adjusted to after a point steam chest (14) has refrigerant steam channel to connect with newly-increased generator (A) and increase generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly again to connect with the second condenser (5) a point steam chest (14)，Newly-increased generator (A) also has refrigerant steam channel to connect with the second condenser (5)，Form Branch-cycle first-class absorption type heat pump.
null18. Branch-cycle first-class absorption type heat pumps，It is in claim 7、In arbitrary Branch-cycle first-class absorption type heat pump described in 15，Increase newly-increased generator、Newly-increased choke valve and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline through the second solution pump (9)、Newly-increased solution heat exchanger (C)、Second solution heat exchanger (13)、Absorber (2) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C) again，Refrigerant steam channel is had connect with the second condenser (5) to be adjusted to after a point steam chest (14) has refrigerant steam channel to connect with newly-increased generator (A) and increase generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly again to connect with the second condenser (5) a point steam chest (14)，Newly-increased generator (A) also has refrigerant steam channel to connect with the second condenser (5)，Form Branch-cycle first-class absorption type heat pump.
null19. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 12，Increase newly-increased generator、Newly-increased choke valve and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or have weak solution pipeline through the second solution pump (9) through the 3rd absorber (20) with dividing a steam chest (14) to connect to be adjusted to the second absorber (3) again、Newly-increased solution heat exchanger (C)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or connect with dividing a steam chest (14) through the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C) again，Refrigerant steam channel is had connect with the second condenser (5) to be adjusted to after a point steam chest (14) has refrigerant steam channel to connect with newly-increased generator (A) and increase generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly again to connect with the second condenser (5) a point steam chest (14)，Newly-increased generator (A) also has refrigerant steam channel to connect with the second condenser (5)，Form Branch-cycle first-class absorption type heat pump.
null20. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 14，Increase newly-increased generator、Newly-increased choke valve and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline through the second solution pump (9)、Newly-increased solution heat exchanger (C)、Second solution heat exchanger (13) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C) again，Refrigerant steam channel is had connect with the second condenser (5) to be adjusted to after a point steam chest (14) has refrigerant steam channel to connect with newly-increased generator (A) and increase generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly again to connect with the second condenser (5) a point steam chest (14)，Newly-increased generator (A) also has refrigerant steam channel to connect with the second condenser (5)，Form Branch-cycle first-class absorption type heat pump.
null21. Branch-cycle first-class absorption type heat pumps，It is in claim 1-6、8-11、In arbitrary Branch-cycle first-class absorption type heat pump described in 13，Increase newly-increased generator、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and absorber (2) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased generator (A) through the second solution pump (9) and the second solution heat exchanger (13)，Newly-increased generator (A) has concentrated solution pipeline again through new solubilization liquid pump (D)、Newly-increased solution heat exchanger (C) connects with a point steam chest (14) with absorber (2)，Have concentrated solution pipeline connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline warp to increase solution heat exchanger (C) newly and the second solution heat exchanger (13) connects with the second absorber (3) by a point steam chest (14)，Refrigerant steam channel is had connect with the second condenser (5) to be adjusted to after a point steam chest (14) has refrigerant steam channel to connect with newly-increased generator (A) and increase generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly again to connect with the second condenser (5) a point steam chest (14)，Newly-increased generator (A) also has refrigerant steam channel to connect with the second condenser (5)，Form Branch-cycle first-class absorption type heat pump.
null22. Branch-cycle first-class absorption type heat pumps，It is in claim 7、In arbitrary Branch-cycle first-class absorption type heat pump described in 15，Increase newly-increased generator、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased generator (A) through the second solution pump (9) and the second solution heat exchanger (13)，Newly-increased generator (A) has concentrated solution pipeline again through new solubilization liquid pump (D)、Newly-increased solution heat exchanger (C)、Absorber (2) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline warp to increase solution heat exchanger (C) newly and the second solution heat exchanger (13) connects with the second absorber (3) by a point steam chest (14)，Refrigerant steam channel is had connect with the second condenser (5) to be adjusted to after a point steam chest (14) has refrigerant steam channel to connect with newly-increased generator (A) and increase generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly again to connect with the second condenser (5) a point steam chest (14)，Newly-increased generator (A) also has refrigerant steam channel to connect with the second condenser (5)，Form Branch-cycle first-class absorption type heat pump.
null23. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 12，Increase newly-increased generator、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or have weak solution pipeline to connect with newly-increased generator (A) through the second solution pump (9) and the second solution heat exchanger (13) through the 3rd absorber (20) with dividing a steam chest (14) to connect to be adjusted to the second absorber (3) again，Newly-increased generator (A) has concentrated solution pipeline again through new solubilization liquid pump (D)、Newly-increased solution heat exchanger (C)、Absorber (2) and the 4th absorber (20) connects with a point steam chest (14) or connect with dividing a steam chest (14) through the 3rd absorber (20)，Have concentrated solution pipeline connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline warp to increase solution heat exchanger (C) newly and the second solution heat exchanger (13) connects with the second absorber (3) by a point steam chest (14)，Refrigerant steam channel is had connect with the second condenser (5) to be adjusted to after a point steam chest (14) has refrigerant steam channel to connect with newly-increased generator (A) and increase generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly again to connect with the second condenser (5) a point steam chest (14)，Newly-increased generator (A) also has refrigerant steam channel to connect with the second condenser (5)，Form Branch-cycle first-class absorption type heat pump.
null24. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 14，Increase newly-increased generator、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased generator (A) through the second solution pump (9) and the second solution heat exchanger (13)，Newly-increased generator (A) has concentrated solution pipeline again through new solubilization liquid pump (D)、Newly-increased solution heat exchanger (C) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline warp to increase solution heat exchanger (C) newly and the second solution heat exchanger (13) connects with the second absorber (3) by a point steam chest (14)，Refrigerant steam channel is had connect with the second condenser (5) to be adjusted to after a point steam chest (14) has refrigerant steam channel to connect with newly-increased generator (A) and increase generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly again to connect with the second condenser (5) a point steam chest (14)，Newly-increased generator (A) also has refrigerant steam channel to connect with the second condenser (5)，Form Branch-cycle first-class absorption type heat pump.
null25. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 1-15，Increase newly-increased point of steam chest、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second vaporizer (7) has refrigerant steam channel connect with the second absorber (3) be adjusted to the second vaporizer (7) and have refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased absorber (E) also has weak solution pipeline through new solubilization liquid pump (D)、Newly-increased solution heat exchanger (C) connects with a newly-increased point steam chest (F) with absorber (2)，Newly-increased point of steam chest (F) also has concentrated solution pipeline to connect with newly-increased absorber (E) through newly-increased solution heat exchanger (C)，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with the second absorber (3)，Newly-increased absorber (E) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null26. Branch-cycle first-class absorption type heat pumps，It is in claim 1-6、8-11、In arbitrary Branch-cycle first-class absorption type heat pump described in 13，Increase newly-increased point of steam chest、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and absorber (2) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased absorber (E) has weak solution pipeline again through new solubilization liquid pump (D)、Second solution heat exchanger (13) connects with a point steam chest (14) with absorber (2)，Have concentrated solution pipeline connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to divide a steam chest (F) to connect through the second solution heat exchanger (13) and absorber (2) with increasing newly by a point steam chest (14)，Newly-increased point of steam chest (F) also has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C)，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased absorber (E) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null27. Branch-cycle first-class absorption type heat pumps，It is in claim 7、In arbitrary Branch-cycle first-class absorption type heat pump described in 15，Increase newly-increased point of steam chest、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased absorber (E) has weak solution pipeline again through new solubilization liquid pump (D)、Second solution heat exchanger (13)、Absorber (2) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline through the second solution heat exchanger (13) by a point steam chest (14)、Absorber (2) connects with a newly-increased point steam chest (F) with the 3rd absorber (20)，Newly-increased point of steam chest (F) also has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C)，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased absorber (E) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null28. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 12，Increase newly-increased point of steam chest、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Connect with a point steam chest (14) with absorber (2) and the 4th absorber (24) or have weak solution pipeline to connect with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C) through the 3rd absorber (20) with dividing a steam chest (14) to connect to be adjusted to the second absorber (3) again，Newly-increased absorber (E) has weak solution pipeline again through new solubilization liquid pump (D)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or connect with dividing a steam chest (14) through the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline through the second solution heat exchanger (13) by a point steam chest (14)、Absorber (2) connects with the 4th absorber (24) with increasing a point steam chest (F) newly or connects with a newly-increased point steam chest (F) through the 3rd absorber (20)，Newly-increased point of steam chest (F) also has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C)，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased absorber (E) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null29. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 14，Increase newly-increased point of steam chest、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased absorber (E) has weak solution pipeline again through new solubilization liquid pump (D)、Second solution heat exchanger (13) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to divide a steam chest (F) to connect through the second solution heat exchanger (13) and the 3rd absorber (20) with increasing newly by a point steam chest (14)，Newly-increased point of steam chest (F) also has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C)，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased absorber (E) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null30. Branch-cycle first-class absorption type heat pumps，It is in claim 1-6、8-11、In arbitrary Branch-cycle first-class absorption type heat pump described in 13，Increase newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve、Newly-increased point of steam chest and newly-increased second point of steam chest，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and absorber (2) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased second absorber (K) also has weak solution pipeline to connect with newly-increased absorber (E) with newly-increased second solution heat exchanger (H) through new solubilization liquid pump (D)，Newly-increased absorber (E) has weak solution pipeline again through newly-increased second solution pump (G)、Second solution heat exchanger (13) connects with a point steam chest (14) with absorber (2)，Have concentrated solution pipeline connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to divide a steam chest (F) to connect through the second solution heat exchanger (13) and absorber (2) with increasing newly by a point steam chest (14)，Newly-increased point of steam chest (F) also has concentrated solution pipeline to connect with newly-increased second point of steam chest (I) with newly-increased absorber (E) through new solubilization liquid choke valve (J)，Newly-increased second point of steam chest (I) has concentrated solution pipeline to connect with the second absorber (3) with newly-increased solution heat exchanger (C) through newly-increased second solution heat exchanger (H) again，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased second point of steam chest (I) also has refrigerant steam channel to connect with newly-increased second absorber (K)，Newly-increased absorber (E) or also heated medium pipeline and ft connection，Newly-increased second absorber (K) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null31. Branch-cycle first-class absorption type heat pumps，It is in claim 7、In arbitrary Branch-cycle first-class absorption type heat pump described in 15，Increase newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve、Newly-increased point of steam chest and newly-increased second point of steam chest，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased second absorber (K) also has weak solution pipeline to connect with newly-increased absorber (E) with newly-increased second solution heat exchanger (H) through new solubilization liquid pump (D)，Newly-increased absorber (E) has weak solution pipeline again through newly-increased second solution pump (G)、Second solution heat exchanger (13)、Absorber (2) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline through the second solution heat exchanger (13) by a point steam chest (14)、Absorber (2) connects with a newly-increased point steam chest (F) with the 3rd absorber (20)，Newly-increased point of steam chest (F) also has concentrated solution pipeline to connect with newly-increased second point of steam chest (I) with newly-increased absorber (E) through new solubilization liquid choke valve (J)，Newly-increased second point of steam chest (I) has concentrated solution pipeline to connect with the second absorber (3) with newly-increased solution heat exchanger (C) through newly-increased second solution heat exchanger (H) again，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased second point of steam chest (I) also has refrigerant steam channel to connect with newly-increased second absorber (K)，Newly-increased absorber (E) or also heated medium pipeline and ft connection，Newly-increased second absorber (K) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null32. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 12，Increase newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve、Newly-increased point of steam chest and newly-increased second point of steam chest，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or have weak solution pipeline to connect with newly-increased second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C) through the 3rd absorber (20) with dividing a steam chest (14) to connect to be adjusted to the second absorber (3) again，Newly-increased second absorber (K) also has weak solution pipeline to connect with newly-increased absorber (E) with newly-increased second solution heat exchanger (H) through new solubilization liquid pump (D)，Newly-increased absorber (E) has weak solution pipeline again through newly-increased second solution pump (G)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or connect with dividing a steam chest (14) through the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline through the second solution heat exchanger (13) by a point steam chest (14)、Absorber (2) connects with the 4th absorber (24) with increasing a point steam chest (F) newly or connects with a newly-increased point steam chest (F) through the 3rd absorber (20)，Newly-increased point of steam chest (F) also has concentrated solution pipeline to connect with newly-increased second point of steam chest (I) with newly-increased absorber (E) through new solubilization liquid choke valve (J)，Newly-increased second point of steam chest (I) has concentrated solution pipeline to connect with the second absorber (3) with newly-increased solution heat exchanger (C) through newly-increased second solution heat exchanger (H) again，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased second point of steam chest (I) also has refrigerant steam channel to connect with newly-increased second absorber (K)，Newly-increased absorber (E) or also heated medium pipeline and ft connection，Newly-increased second absorber (K) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null33. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 14，Increase newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve、Newly-increased point of steam chest and newly-increased second point of steam chest，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased second absorber (K) also has weak solution pipeline to connect with newly-increased absorber (E) with newly-increased second solution heat exchanger (H) through new solubilization liquid pump (D)，Newly-increased absorber (E) has weak solution pipeline again through newly-increased second solution pump (G)、Second solution heat exchanger (13) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to divide a steam chest (F) to connect through the second solution heat exchanger (13) and the 3rd absorber (20) with increasing newly by a point steam chest (14)，Newly-increased point of steam chest (F) also has concentrated solution pipeline to connect with newly-increased second point of steam chest (I) with newly-increased absorber (E) through new solubilization liquid choke valve (J)，Newly-increased second point of steam chest (I) has concentrated solution pipeline to connect with the second absorber (3) with newly-increased solution heat exchanger (C) through newly-increased second solution heat exchanger (H) again，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased second point of steam chest (I) also has refrigerant steam channel to connect with newly-increased second absorber (K)，Newly-increased absorber (E) or also heated medium pipeline and ft connection，Newly-increased second absorber (K) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null34. Branch-cycle first-class absorption type heat pumps，It is in claim 1-6、8-11、In arbitrary Branch-cycle first-class absorption type heat pump described in 13，Increase newly-increased generator、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and absorber (2) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased absorber (E) has weak solution pipeline again through new solubilization liquid pump (D)、Second solution heat exchanger (13) connects with a point steam chest (14) with absorber (2)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C) again，Newly-increased generator (A) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased generator (A) also has driving heat medium pipeline and ft connection，Newly-increased absorber (E) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null35. Branch-cycle first-class absorption type heat pumps，It is in claim 7、In arbitrary Branch-cycle first-class absorption type heat pump described in 15，Increase newly-increased generator、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased absorber (E) has weak solution pipeline again through new solubilization liquid pump (D)、Second solution heat exchanger (13)、Absorber (2) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C) again，Newly-increased generator (A) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased generator (A) also has driving heat medium pipeline and ft connection，Newly-increased absorber (E) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null36. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 12，Increase newly-increased generator、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or have weak solution pipeline to connect with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C) through the 3rd absorber (20) with dividing a steam chest (14) to connect to be adjusted to the second absorber (3) again，Newly-increased absorber (E) has weak solution pipeline again through new solubilization liquid pump (D)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or connect with dividing a steam chest (14) through the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C) again，Newly-increased generator (A) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased generator (A) also has driving heat medium pipeline and ft connection，Newly-increased absorber (E) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null37. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 14，Increase newly-increased generator、Newly-increased absorber、New solubilization liquid pump and newly-increased solution heat exchanger，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased absorber (E) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased absorber (E) has weak solution pipeline again through new solubilization liquid pump (D)、Second solution heat exchanger (13) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) has concentrated solution pipeline to connect with the second absorber (3) through newly-increased solution heat exchanger (C) again，Newly-increased generator (A) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased generator (A) also has driving heat medium pipeline and ft connection，Newly-increased absorber (E) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null38. Branch-cycle first-class absorption type heat pumps，It is in claim 1-6、8-11、In arbitrary Branch-cycle first-class absorption type heat pump described in 13，Increase newly-increased generator、Newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve and newly-increased point of steam chest，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and absorber (2) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased second absorber (K) also has weak solution pipeline to connect with newly-increased absorber (E) with newly-increased second solution heat exchanger (H) through new solubilization liquid pump (D)，Newly-increased absorber (E) has weak solution pipeline again through newly-increased second solution pump (G)、Second solution heat exchanger (13) connects with a point steam chest (14) with absorber (2)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) also has concentrated solution pipeline to connect with a newly-increased point steam chest (F) with newly-increased absorber (E) through new solubilization liquid choke valve (J)，A newly-increased point steam chest (F) has concentrated solution pipeline to connect with the second absorber (3) with newly-increased solution heat exchanger (C) through newly-increased second solution heat exchanger (H) again，Newly-increased generator (A) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased second absorber (K)，Newly-increased generator (A) also has driving heat medium pipeline and ft connection，Newly-increased absorber (E) or also heated medium pipeline and ft connection，Newly-increased second absorber (K) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null39. Branch-cycle first-class absorption type heat pumps，It is in claim 7、In arbitrary Branch-cycle first-class absorption type heat pump described in 15，Increase newly-increased generator、Newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve and newly-increased point of steam chest，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased second absorber (K) also has weak solution pipeline to connect with newly-increased absorber (E) with newly-increased second solution heat exchanger (H) through new solubilization liquid pump (D)，Newly-increased absorber (E) has weak solution pipeline again through newly-increased second solution pump (G)、Second solution heat exchanger (13)、Absorber (2) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) also has concentrated solution pipeline to connect with a newly-increased point steam chest (F) with newly-increased absorber (E) through new solubilization liquid choke valve (J)，A newly-increased point steam chest (F) has concentrated solution pipeline to connect with the second absorber (3) with newly-increased solution heat exchanger (C) through newly-increased second solution heat exchanger (H) again，Newly-increased generator (A) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased second absorber (K)，Newly-increased generator (A) also has driving heat medium pipeline and ft connection，Newly-increased absorber (E) or also heated medium pipeline and ft connection，Newly-increased second absorber (K) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null40. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 12，Increase newly-increased generator、Newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve and newly-increased point of steam chest，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or have weak solution pipeline to connect with newly-increased second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C) through the 3rd absorber (20) with dividing a steam chest (14) to connect to be adjusted to the second absorber (3) again，Newly-increased second absorber (K) also has weak solution pipeline to connect with newly-increased absorber (E) with newly-increased second solution heat exchanger (H) through new solubilization liquid pump (D)，Newly-increased absorber (E) has weak solution pipeline again through newly-increased second solution pump (G)、Second solution heat exchanger (13)、Absorber (2) and the 4th absorber (24) connects with a point steam chest (14) or connect with dividing a steam chest (14) through the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) also has concentrated solution pipeline to connect with a newly-increased point steam chest (F) with newly-increased absorber (E) through new solubilization liquid choke valve (J)，A newly-increased point steam chest (F) has concentrated solution pipeline to connect with the second absorber (3) with newly-increased solution heat exchanger (C) through newly-increased second solution heat exchanger (H) again，Newly-increased generator (A) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased second absorber (K)，Newly-increased generator (A) also has driving heat medium pipeline and ft connection，Newly-increased absorber (E) or also heated medium pipeline and ft connection，Newly-increased second absorber (K) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null41. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 14，Increase newly-increased generator、Newly-increased absorber、Newly-increased second absorber、New solubilization liquid pump、Newly-increased second solution pump、Newly-increased solution heat exchanger、Newly-increased second solution heat exchanger、New solubilization liquid choke valve and newly-increased point of steam chest，Second absorber (3) is had weak solution pipeline through the second solution pump (9)、Second solution heat exchanger (13) and the 3rd absorber (20) connect with a point steam chest (14) and are adjusted to the second absorber (3) and have weak solution pipeline to connect with newly-increased second absorber (K) through the second solution pump (9) and newly-increased solution heat exchanger (C)，Newly-increased second absorber (K) also has weak solution pipeline to connect with newly-increased absorber (E) with newly-increased second solution heat exchanger (H) through new solubilization liquid pump (D)，Newly-increased absorber (E) has weak solution pipeline again through newly-increased second solution pump (G)、Second solution heat exchanger (13) connects with a point steam chest (14) with the 3rd absorber (20)，Have concentrated solution pipeline to connect with the second absorber (3) through the second solution heat exchanger (13) to be adjusted to a point steam chest (14) and have concentrated solution pipeline to connect with newly-increased generator (A) through the second solution heat exchanger (13) by a point steam chest (14)，Newly-increased generator (A) also has concentrated solution pipeline to connect with a newly-increased point steam chest (F) with newly-increased absorber (E) through new solubilization liquid choke valve (J)，A newly-increased point steam chest (F) has concentrated solution pipeline to connect with the second absorber (3) with newly-increased solution heat exchanger (C) through newly-increased second solution heat exchanger (H) again，Newly-increased generator (A) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased second absorber (K)，Newly-increased generator (A) also has driving heat medium pipeline and ft connection，Newly-increased absorber (E) or also heated medium pipeline and ft connection，Newly-increased second absorber (K) also has heated medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
42. Branch-cycle first-class absorption type heat pumps, it is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 1-41, vaporizer (6) and the second vaporizer (7) are united two into one, forms Branch-cycle first-class absorption type heat pump.
43. Branch-cycle first-class absorption type heat pumps, it is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 1-42, condenser (5) and the second condenser (6) are united two into one, forms Branch-cycle first-class absorption type heat pump.
null44. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 1-15，Increase newly-increased generator、Newly-increased absorber、Newly-increased choke valve、Newly-increased solution heat exchanger and new solubilization liquid pump，Second vaporizer (7) has refrigerant steam channel connect with the second absorber (3) be adjusted to the second vaporizer (7) and have refrigerant steam channel to connect with newly-increased absorber (E)，Refrigerant steam channel is had connect with the second condenser (5) to be adjusted to after a point steam chest (14) has refrigerant steam channel to connect with newly-increased generator (A) and increase generator (A) newly and have cryogen liquid pipeline warp to increase choke valve (B) newly again to connect with newly-increased vaporizer (M) a point steam chest (14)，Newly-increased vaporizer (M) also has refrigerant steam channel to connect with the second absorber (3)，Newly-increased generator (A) also has concentrated solution pipeline to connect with newly-increased absorber (E) through newly-increased solution heat exchanger (C)，Newly-increased absorber (E) also has weak solution pipeline to connect with newly-increased generator (A) with newly-increased solution heat exchanger (C) through new solubilization liquid pump (D)，Newly-increased generator (A) also has refrigerant steam channel to connect with the second condenser (5)，Newly-increased absorber (E) also has heated medium pipeline and ft connection，Newly-increased vaporizer (M) also has surplus heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
null45. Branch-cycle first-class absorption type heat pumps，It is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 1-15，Increase newly-increased choke valve、Newly-increased solution heat exchanger、New solubilization liquid pump、Newly-increased absorber、Newly-increased point of steam chest、Newly-increased condenser and newly-increased vaporizer，Cancel the heated medium pipeline of the second absorber (3) and ft connection，Newly-increased absorber (E) has weak solution pipeline through new solubilization liquid pump (D)、Newly-increased solution heat exchanger (C) connects with a newly-increased point steam chest (F) with the second absorber (3)，Newly-increased point of steam chest (F) also has concentrated solution to connect with newly-increased absorber (E) through newly-increased solution heat exchanger (C)，Newly-increased point of steam chest (F) also has refrigerant steam channel to connect with newly-increased condenser (L)，Newly-increased condenser (L) also has cryogen liquid pipeline to connect with newly-increased vaporizer (M) through newly-increased choke valve (B)，Newly-increased vaporizer (M) also has refrigerant steam channel to connect with newly-increased absorber (E)，Newly-increased absorber (E) and newly-increased condenser (L) have heated medium pipeline and ft connection the most respectively，Newly-increased vaporizer (M) also has surplus heat medium pipeline and ft connection，Form Branch-cycle first-class absorption type heat pump.
46. Branch-cycle first-class absorption type heat pumps, it is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 44-45, vaporizer (6), the second vaporizer (7) and newly-increased vaporizer (M) are closed three is one, forms Branch-cycle first-class absorption type heat pump.
47. Branch-cycle first-class absorption type heat pumps, it is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 44, condenser (4) and the second condenser (5) are united two into one, forms Branch-cycle first-class absorption type heat pump.
48. Branch-cycle first-class absorption type heat pumps, it is in the arbitrary Branch-cycle first-class absorption type heat pump described in claim 45, condenser (4), the second condenser (5) and newly-increased condenser (L) are closed three is one, forms Branch-cycle first-class absorption type heat pump.
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