CN106403350A - Combined thermal power supply system - Google Patents

Combined thermal power supply system Download PDF

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Publication number
CN106403350A
CN106403350A CN201610811990.6A CN201610811990A CN106403350A CN 106403350 A CN106403350 A CN 106403350A CN 201610811990 A CN201610811990 A CN 201610811990A CN 106403350 A CN106403350 A CN 106403350A
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China
Prior art keywords
generator
solution
pipeline
absorber
connect
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CN201610811990.6A
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Chinese (zh)
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CN106403350B (en
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李华玉
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K27/00—Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
    • 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
    • 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
    • F25B33/00—Boilers; Analysers; Rectifiers
    • 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
    • F25B37/00—Absorbers; Adsorbers
    • 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
    • F25B41/00—Fluid-circulation arrangements
    • F25B41/30—Expansion means; Dispositions thereof
    • 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
    • Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Power Engineering (AREA)
  • Sorption Type Refrigeration Machines (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

The invention provides a combined thermal power supply system and belongs to the technical field of combined thermoelectric cooling supply and absorption heat pumps. An absorption heat pump circulation system comprises an absorber, a second absorber, a generator, a second generator, a solution pump, a second solution pump, a solution heat exchanger and a second solution heat exchanger; a power machine provides low temperature thermal load via a low-temperature condenser, a heater and a second heater; a circulating pump is communicated with self through a recirculated medium pipeline via the low-temperature condenser, the heater, the second heater, an evaporator and the second generator; and a high-temperature thermal medium channel of the generator, heated medium channels of the absorber and a condenser and a cooling medium channel of the second absorber are communicated with the outside to form the combined thermal power supply system.

Description

The dynamic co-feeding system of heat
Technical field：
The invention belongs to heat-electricity-cold combined supply and absorption type heat pump technical field.
Background technology：
Move in co-feeding system in the conventional thermal with hot fluid sensible heat for thermic load mode of movement, have what many had much room for improvement Place, is mainly reflected in：(1) remote, extensive and graded supply heat is moved in co-feeding system, and first-level pipeline network temperature is high, pressure Power is big, and pipeline is usually in urban population compact district, there is potential safety hazard, and the initial cost of pipe network is big；(2) steam power dress The temperature difference put between the low pressure exhaust steam of discharge and environment is often difficult by；(3) Steam Power Equipment with coal as fuel, combustion gas There is the heat transfer temperature difference being difficult to effectively utilizes and power cycle steam between, lead to the comprehensive energy utilization rate of the dynamic co-feeding system of heat Not high；(4) there is larger heat transfer temperature difference between first-level pipeline network circulatory mediator and secondary network circulatory mediator or heated medium, do not have It is used；(5) to clean energy resource in the dynamic co-feeding system of heat using bringing a definite limitation.
The present invention, premised on heat energy efficient utilization, moves one-level heating network temperature and pressure in co-feeding system to reduce heat For core, take into account increasing pipe network supply backwater temperature difference to reduce corresponding initial cost, take into account lifting power machine job security and heat energy It is converted into the efficiency of mechanical energy, and considers to adapt to the utilization of clean energy resource in the dynamic co-feeding system of heat, propose with engine end row Vapour or low-pressure pumping steam are low-temperature heat source the dynamic co-feeding system of the series of heat combining absorption heat pump technology.
Content of the invention：
Present invention is primarily intended to will provide heat dynamic co-feeding system, concrete content of the invention subitem is described below：
1. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser and Circulating pump is formed；Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has Weak solution pipeline is connected with generator through solution pump and the second solution heat exchanger, and generator also has concentrated solution pipeline molten through second Liquid heat exchanger is connected with the second generator, and the second generator also has concentrated solution pipeline through the second solution pump and solution heat exchanger Connect with absorber, generator also has refrigerant steam channel to connect with condenser, the second generator also have refrigerant steam channel with Second absorber connection, condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer also has refrigerant vapour to lead to Road is connected with absorber, and engine has live steam passage and ft connection, and engine also has exhaust passage to connect with low-temperature condenser Low-temperature condenser has low temperature cold lime set passage and ft connection, engine or also exhaust passage and ft connection more afterwards, follows Ring pump has circulatory mediator pipeline to have circulatory mediator pipeline again through second through the finisher that low-temperature condenser is connected with vaporizer Raw device is connected with circulating pump itself, and absorber and condenser also have heated medium passage and ft connection, the second absorption respectively Device also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and ft connection, forms the dynamic alliance of heat System.
2. the dynamic co-feeding system of heat, is to move in co-feeding system in the 1st described heat, circulating pump is had circulatory mediator pipeline through low The finisher that warm condenser is connected with vaporizer has circulatory mediator pipeline itself to connect through the second generator and circulating pump again, adjusts Whole have circulatory mediator pipeline to connect with the second generator through low-temperature condenser for circulating pump after the second generator again have circulation be situated between Matter pipeline itself connects through vaporizer and circulating pump, forms the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, is to move in co-feeding system in the 1st described heat, circulating pump is had circulatory mediator pipeline through low The finisher that warm condenser is connected with vaporizer has circulatory mediator pipeline itself to connect through the second generator and circulating pump again, adjusts The whole finisher having circulatory mediator pipeline to connect with vaporizer and the second generator respectively through low-temperature condenser for circulating pump and Second generator has circulatory mediator pipeline and circulating pump itself to connect again respectively, forms the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump and heating Device is formed；Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has dilute molten Liquid pipeline is connected with generator through solution pump and the second solution heat exchanger, and generator also has concentrated solution pipeline through the second solution heat Exchanger is connected with the second generator, and the second generator also has concentrated solution pipeline through the second solution pump and solution heat exchanger and suction Receive device connection, generator also has refrigerant steam channel to connect with condenser, and the second generator also has refrigerant steam channel and second Absorber connects, and condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, vaporizer also have refrigerant steam channel and Absorber connects, and engine has live steam passage and ft connection respectively and has exhaust passage and ft connection, and engine also has the The post-heater that one steam channel is connected with heater has the first condensed fluid passage and ft connection again, and circulating pump has circulatory mediator The finisher that the heated device of pipeline is connected with vaporizer has circulatory mediator pipeline through the second generator with circulating pump itself even again Lead to, absorber and condenser also have heated medium passage and ft connection respectively, and the second absorber also has coolant guiding channel With ft connection, generator also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
5. hot dynamic co-feeding system, is to move in co-feeding system in the 4th described heat, circulating pump is had circulatory mediator pipeline through adding The finisher that hot device is connected with vaporizer has circulatory mediator pipeline itself to connect through the second generator and circulating pump again, is adjusted to After circulating pump has the heated device of circulatory mediator pipeline to connect with the second generator, the second generator has circulatory mediator pipeline warp again Vaporizer and circulating pump connect itself, form the dynamic co-feeding system of heat.
6. hot dynamic co-feeding system, is to move in co-feeding system in the 4th described heat, circulating pump is had circulatory mediator pipeline through adding The finisher that hot device is connected with vaporizer has circulatory mediator pipeline itself to connect through the second generator and circulating pump again, is adjusted to Circulating pump has the finisher and second that the heated device of circulatory mediator pipeline is connected with vaporizer and the second generator respectively to occur Device has circulatory mediator pipeline and circulating pump itself to connect again respectively, forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, Circulating pump and heater are formed；Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger, the second suction Receiving device also has weak solution pipeline to connect with generator through solution pump and the second solution heat exchanger, and generator also has concentrated solution pipeline Connect with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline through the second solution pump and solution Heat exchanger is connected with absorber, and generator also has refrigerant steam channel to connect with condenser, and the second generator also has cryogen to steam Vapour passage is connected with the second absorber, and condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer is also cold Agent steam channel is connected with absorber, and engine has live steam passage and ft connection, and engine also has exhaust passage and low temperature cold After condenser connection, low-temperature condenser has low temperature cold lime set passage and ft connection again, and engine also has the first steam channel and adds The post-heater of hot device connection has the first condensed fluid passage and ft connection again, and engine or also exhaust passage and outside connect Logical, circulating pump has circulatory mediator pipeline to have circulatory mediator again through the finisher that low-temperature condenser is connected with vaporizer with heater Pipeline itself connects through the second generator and circulating pump, and absorber and condenser also have heated medium passage and outside to connect respectively Logical, the second absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and ft connection, shape Become the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, is to move in co-feeding system in the 7th described heat, circulating pump is had circulatory mediator pipeline through low The finisher that warm condenser is connected with vaporizer with heater has circulatory mediator pipeline through the second generator with circulating pump certainly again Body connects, and is adjusted to second after circulating pump has circulatory mediator pipeline to connect with the second generator with heater through low-temperature condenser Generator has circulatory mediator pipeline itself to connect through vaporizer and circulating pump again, forms the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, is to move in co-feeding system in the 7th described heat, circulating pump is had circulatory mediator pipeline through low The finisher that warm condenser is connected with vaporizer with heater has circulatory mediator pipeline through the second generator with circulating pump certainly again Body connects, be adjusted to circulating pump have circulatory mediator pipeline through low-temperature condenser and heater respectively with vaporizer and the second generator The finisher of connection and the second generator have circulatory mediator pipeline and circulating pump itself to connect again respectively, form the dynamic alliance system of heat System.
10. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heating Device and secondary heater are formed；Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger, the second suction Receiving device also has weak solution pipeline to connect with generator through solution pump and the second solution heat exchanger, and generator also has concentrated solution pipeline Connect with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline through the second solution pump and solution Heat exchanger is connected with absorber, and generator also has refrigerant steam channel to connect with condenser, and the second generator also has cryogen to steam Vapour passage is connected with the second absorber, and condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer is also cold Agent steam channel is connected with absorber, and engine has live steam passage and ft connection respectively and has exhaust passage and ft connection, Engine also has the post-heater that the first steam channel is connected with heater to have the first condensed fluid passage and ft connection, power again After machine also has the second steam channel to connect with secondary heater, secondary heater has the second condensed fluid passage and ft connection again, Circulating pump has the finisher that the heated device of circulatory mediator pipeline is connected with vaporizer with secondary heater to have circulatory mediator pipe again Road second generator is connected with circulating pump itself, and absorber and condenser also have heated medium passage and outside to connect respectively Logical, the second absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and ft connection, shape Become the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, is to move in co-feeding system in the 10th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that heater is connected with vaporizer with secondary heater has circulatory mediator pipeline again through the second generator and circulating pump Itself connection, is adjusted to after circulating pump has the heated device of circulatory mediator pipeline to connect with the second generator with secondary heater the Two generators have circulatory mediator pipeline itself to connect through vaporizer and circulating pump again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 12. heat, is to move in co-feeding system in the 10th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that heater is connected with vaporizer with secondary heater has circulatory mediator pipeline again through the second generator and circulating pump Itself connection, being adjusted to circulating pump has the heated device of circulatory mediator pipeline and secondary heater to occur with vaporizer and second respectively The finisher of device connection and the second generator have circulatory mediator pipeline and circulating pump itself to connect again respectively, form the dynamic alliance of heat System.
The dynamic co-feeding system of 13. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, Circulating pump, heater and secondary heater are formed；Absorber has weak solution pipeline through solution heat exchanger and the second absorber Connection, the second absorber also has weak solution pipeline to connect with generator through solution pump and the second solution heat exchanger, and generator is also Concentrated solution pipeline is had to connect with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline through second Solution pump is connected with absorber with solution heat exchanger, and generator also has refrigerant steam channel to connect with condenser, the second generation Device also has refrigerant steam channel to connect with the second absorber, and condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, Vaporizer also has refrigerant steam channel to connect with absorber, and engine has live steam passage and ft connection, and engine also has steam discharge After passage is connected with low-temperature condenser, low-temperature condenser has low temperature cold lime set passage and ft connection again, and engine also has first The post-heater that steam channel is connected with heater has the first condensed fluid passage and ft connection again, and engine also has the second steam After passage is connected with secondary heater, secondary heater has the second condensed fluid passage and ft connection, engine or also row again Vapour passage and ft connection, circulating pump has circulatory mediator pipeline through low-temperature condenser, heater and secondary heater and vaporizer The finisher of connection has circulatory mediator pipeline itself to connect through the second generator and circulating pump again, and absorber and condenser also divide There are not heated medium passage and ft connection, the second absorber also has coolant guiding channel and ft connection, and generator also has High temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 14. heat, is to move in co-feeding system in the 13rd described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser, heater are connected with vaporizer with secondary heater has circulatory mediator pipeline again through the second generation Device and circulating pump connect itself, and being adjusted to circulating pump has circulatory mediator pipeline through low-temperature condenser, heater and secondary heater After connecting with the second generator, the second generator has circulatory mediator pipeline itself to connect through vaporizer and circulating pump again, forms heat Dynamic co-feeding system.
The dynamic co-feeding system of 15. heat, is to move in co-feeding system in the 13rd described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser, heater are connected with vaporizer with secondary heater has circulatory mediator pipeline again through the second generation Device and circulating pump connect itself, and being adjusted to circulating pump has circulatory mediator pipeline through low-temperature condenser, heater and secondary heater The finisher connecting with vaporizer and the second generator respectively and the second generator have circulatory mediator pipeline and circulation more respectively Pump itself connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 16. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heating Device, secondary heater and the 3rd heater are formed；Absorber has weak solution pipeline through solution heat exchanger and the second absorber Connection, the second absorber also has weak solution pipeline to connect with generator through solution pump and the second solution heat exchanger, and generator is also Concentrated solution pipeline is had to connect with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline through second Solution pump is connected with absorber with solution heat exchanger, and generator also has refrigerant steam channel to connect with condenser, the second generation Device also has refrigerant steam channel to connect with the second absorber, and condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, Vaporizer also has refrigerant steam channel to connect with absorber, and engine has live steam passage and ft connection respectively and has exhaust passage With ft connection, engine also have the post-heater that the first steam channel is connected with heater have again the first condensed fluid passage with outer Portion connects, and after engine also has the second steam channel to connect with secondary heater, secondary heater has the second condensed fluid passage again With ft connection, after engine also has the 3rd steam channel to connect with the 3rd heater, the 3rd heater has the 3rd condensed fluid again Passage and ft connection, circulating pump has the heated device of circulatory mediator pipeline, secondary heater and the 3rd heater and vaporizer even Logical finisher has circulatory mediator pipeline itself to connect through the second generator and circulating pump again, and absorber and condenser are also distinguished There are heated medium passage and ft connection, the second absorber also has coolant guiding channel and ft connection, generator also has height Warm passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, is to move in co-feeding system in the 16th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that heater, secondary heater and the 3rd heater are connected with vaporizer has circulatory mediator pipeline again through the second generation Device and circulating pump connect itself, and being adjusted to circulating pump has the heated device of circulatory mediator pipeline, secondary heater and the 3rd heater After connecting with the second generator, the second generator has circulatory mediator pipeline itself to connect through vaporizer and circulating pump again, forms heat Dynamic co-feeding system.
The dynamic co-feeding system of 18. heat, is to move in co-feeding system in the 16th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that heater, secondary heater and the 3rd heater are connected with vaporizer has circulatory mediator pipeline again through the second generation Device and circulating pump connect itself, and being adjusted to circulating pump has the heated device of circulatory mediator pipeline, secondary heater and the 3rd heater The finisher connecting with vaporizer and the second generator respectively and the second generator have circulatory mediator pipeline and circulation more respectively Pump itself connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, Circulating pump, heater, secondary heater and the 3rd heater are formed；Absorber have weak solution pipeline through solution heat exchanger with Second absorber connection, the second absorber also has weak solution pipeline to connect with generator through solution pump and the second solution heat exchanger Logical, generator also has concentrated solution pipeline to connect with the second generator through the second solution heat exchanger, and the second generator also has dense molten Liquid pipeline is connected with absorber with solution heat exchanger through the second solution pump, and generator also has refrigerant steam channel with condenser even Logical, the second generator also has refrigerant steam channel to connect with the second absorber, condenser also have cryogen liquid pipeline through choke valve and Vaporizer connects, and vaporizer also has refrigerant steam channel to connect with absorber, and engine has live steam passage and ft connection, power After machine also has exhaust passage to connect with low-temperature condenser, low-temperature condenser has low temperature cold lime set passage and ft connection, power again Machine also has the post-heater that the first steam channel is connected with heater to have the first condensed fluid passage and ft connection again, and engine is also After having the second steam channel to connect with secondary heater, secondary heater has the second condensed fluid passage and ft connection, power again After machine also has the 3rd steam channel to connect with the 3rd heater, the 3rd heater has the 3rd condensed fluid passage and ft connection again, Engine or also exhaust passage and ft connection, circulating pump have circulatory mediator pipeline through low-temperature condenser, heater, second plus The finisher that hot device and the 3rd heater are connected with vaporizer have again circulatory mediator pipeline through the second generator and circulating pump from Body connects, and absorber and condenser also have heated medium passage and ft connection respectively, and the second absorber also has cooling medium Passage and ft connection, generator also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 20. heat, is to move in co-feeding system in the 19th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser, heater, secondary heater and the 3rd heater are connected with vaporizer has circulatory mediator pipe again Road second generator is connected with circulating pump itself, be adjusted to circulating pump have circulatory mediator pipeline through low-temperature condenser, heater, After secondary heater and the 3rd heater are connected with the second generator, the second generator has circulatory mediator pipeline again through vaporizer Connect with circulating pump itself, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, is to move in co-feeding system in the 19th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser, heater, secondary heater and the 3rd heater are connected with vaporizer has circulatory mediator pipe again Road second generator is connected with circulating pump itself, be adjusted to circulating pump have circulatory mediator pipeline through low-temperature condenser, heater, The finisher connecting and the second generator divide again with vaporizer and the second generator respectively for secondary heater and the 3rd heater There are not circulatory mediator pipeline and circulating pump itself to connect, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 22. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, Circulating pump and heater are formed；Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger, the second suction Receiving device also has weak solution pipeline to connect with generator through solution pump and the second solution heat exchanger, and generator also has concentrated solution pipeline Connect with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline through the second solution pump and solution Heat exchanger is connected with absorber, and generator also has refrigerant steam channel to connect with condenser, and the second generator also has cryogen to steam Vapour passage is connected with the second absorber, and condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer is also cold Agent steam channel is connected with absorber, and engine has live steam passage and ft connection, and engine also has exhaust passage and low temperature cold After condenser connection, low-temperature condenser has low temperature cold lime set passage and ft connection, engine or also exhaust passage and outside again Connection, circulating pump has circulatory mediator pipeline to have circulation to be situated between again through the finisher that low-temperature condenser is connected with vaporizer with heater Matter pipeline itself connects through the second generator and circulating pump, and absorber and condenser also have heated medium passage and outside respectively Connection, the second absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and ft connection, Heater also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 23. heat, is to move in co-feeding system in the 22nd described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser is connected with vaporizer with heater has circulatory mediator pipeline again through the second generator and circulating pump Itself connection, is adjusted to after circulating pump has circulatory mediator pipeline to connect with the second generator with heater through low-temperature condenser the Two generators have circulatory mediator pipeline itself to connect through vaporizer and circulating pump again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 24. heat, is to move in co-feeding system in the 22nd described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser is connected with vaporizer with heater has circulatory mediator pipeline again through the second generator and circulating pump Itself connection, being adjusted to circulating pump has circulatory mediator pipeline to occur with vaporizer and second respectively through low-temperature condenser and heater The finisher of device connection and the second generator have circulatory mediator pipeline and circulating pump itself to connect again respectively, form the dynamic alliance of heat System.
The dynamic co-feeding system of 25. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heating Device and heater are formed；Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger, the second absorber Weak solution pipeline is also had to connect with generator through solution pump and the second solution heat exchanger, generator also has concentrated solution pipeline through the Two solution heat exchangers are connected with the second generator, and the second generator also has concentrated solution pipeline to hand over through the second solution pump and solution heat Parallel operation is connected with absorber, and generator also has refrigerant steam channel to connect with condenser, and the second generator also has refrigerant vapour to lead to Road is connected with the second absorber, and condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer also has cryogen to steam Vapour passage is connected with absorber, and engine has live steam passage and ft connection respectively and has exhaust passage and ft connection, power Machine also has the post-heater that the first steam channel is connected with heater to have the first condensed fluid passage and ft connection again, and circulating pump has The finisher that the heated device of circulatory mediator pipeline is connected with vaporizer with heater has circulatory mediator pipeline again through the second generation Device and circulating pump connect itself, and absorber and condenser also have heated medium passage and ft connection, the second absorber respectively Also have coolant guiding channel and ft connection, generator also has high temperature thermal medium passage and ft connection, heater is also added Hot media channel and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 26. heat, is to move in co-feeding system in the 25th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that heater is connected with vaporizer with heater has circulatory mediator pipeline again through the second generator and circulating pump itself Connection, is adjusted to the second generator after circulating pump has the heated device of circulatory mediator pipeline to connect with the second generator with heater There is circulatory mediator pipeline itself to connect through vaporizer and circulating pump again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 27. heat, is to move in co-feeding system in the 25th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that heater is connected with vaporizer with heater has circulatory mediator pipeline again through the second generator and circulating pump itself Connection, being adjusted to circulating pump has the heated device of circulatory mediator pipeline to connect it with vaporizer and the second generator respectively with heater Finisher and the second generator have circulatory mediator pipeline and circulating pump itself to connect again respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 28. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, Circulating pump, heater and heater are formed；Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger, Second absorber also has weak solution pipeline to connect with generator through solution pump and the second solution heat exchanger, and generator also has dense molten Liquid pipeline is connected with the second generator through the second solution heat exchanger, and the second generator also has concentrated solution pipeline through the second solution pump Connect with absorber with solution heat exchanger, generator also has refrigerant steam channel to connect with condenser, the second generator also has Refrigerant steam channel is connected with the second absorber, and condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, vaporizer Also have refrigerant steam channel connect with absorber, engine has live steam passage and ft connection, engine also have exhaust passage and After low-temperature condenser connection, low-temperature condenser has low temperature cold lime set passage and ft connection again, and engine also has the first steam to lead to The post-heater that road is connected with heater has the first condensed fluid passage and ft connection again, and engine or also exhaust passage are with outward Portion connects, and circulating pump has the finisher that circulatory mediator pipeline is connected with vaporizer through low-temperature condenser, heater and heater Circulatory mediator pipeline is had itself to connect through the second generator and circulating pump again, absorber and condenser also have heated medium respectively Passage and ft connection, the second absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage With ft connection, heater also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 29. heat, is to move in co-feeding system in the 28th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser, heater are connected with vaporizer with heater have again circulatory mediator pipeline through the second generator with Circulating pump itself connects, and being adjusted to circulating pump has circulatory mediator pipeline through low-temperature condenser, heater and heater and second After raw device connection, the second generator has circulatory mediator pipeline itself to connect through vaporizer and circulating pump again, forms the dynamic alliance system of heat System.
The dynamic co-feeding system of 30. heat, is to move in co-feeding system in the 28th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser, heater are connected with vaporizer with heater have again circulatory mediator pipeline through the second generator with Circulating pump itself connect, be adjusted to circulating pump have circulatory mediator pipeline through low-temperature condenser, heater and heater respectively with steaming Send out device and the finisher of the second generator connection and the second generator has circulatory mediator pipeline with circulating pump itself even more respectively Logical, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 31. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heating Device, secondary heater and heater are formed；Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger, Second absorber also has weak solution pipeline to connect with generator through solution pump and the second solution heat exchanger, and generator also has dense molten Liquid pipeline is connected with the second generator through the second solution heat exchanger, and the second generator also has concentrated solution pipeline through the second solution pump Connect with absorber with solution heat exchanger, generator also has refrigerant steam channel to connect with condenser, the second generator also has Refrigerant steam channel is connected with the second absorber, and condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, vaporizer Refrigerant steam channel is also had to connect with absorber, engine has live steam passage and ft connection respectively and has exhaust passage and outside Connection, engine also has the post-heater that the first steam channel is connected with heater to have the first condensed fluid passage to connect with outside again Logical, after engine also has the second steam channel to connect with secondary heater, secondary heater has the second condensed fluid passage again with outward Portion connects, and circulating pump has the finisher that the heated device of circulatory mediator pipeline, secondary heater are connected with vaporizer with heater Circulatory mediator pipeline is had itself to connect through the second generator and circulating pump again, absorber and condenser also have heated medium respectively Passage and ft connection, the second absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage With ft connection, heater also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, is to move in co-feeding system in the 31st described heat, circulating pump is had circulatory mediator pipeline warp The finisher that heater, secondary heater are connected with vaporizer with heater have again circulatory mediator pipeline through the second generator with Circulating pump itself connects, and being adjusted to circulating pump has the heated device of circulatory mediator pipeline, secondary heater and heater and second After raw device connection, the second generator has circulatory mediator pipeline itself to connect through vaporizer and circulating pump again, forms the dynamic alliance system of heat System.
The dynamic co-feeding system of 33. heat, is to move in co-feeding system in the 31st described heat, circulating pump is had circulatory mediator pipeline warp The finisher that heater, secondary heater are connected with vaporizer with heater have again circulatory mediator pipeline through the second generator with Circulating pump itself connect, be adjusted to circulating pump have the heated device of circulatory mediator pipeline, secondary heater and heater respectively with steaming Send out device and the finisher of the second generator connection and the second generator has circulatory mediator pipeline with circulating pump itself even more respectively Logical, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 34. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, Circulating pump, heater, secondary heater and heater are formed；Absorber has weak solution pipeline through solution heat exchanger and second Absorber connects, and the second absorber also has weak solution pipeline to connect with generator through solution pump and the second solution heat exchanger, sends out Raw device also has concentrated solution pipeline to connect with the second generator through the second solution heat exchanger, and the second generator also has concentrated solution pipeline Connect with absorber with solution heat exchanger through the second solution pump, generator also has refrigerant steam channel to connect with condenser, the Two generators also have refrigerant steam channel to connect with the second absorber, and condenser also has cryogen liquid pipeline through choke valve and vaporizer Connection, vaporizer also has refrigerant steam channel to connect with absorber, and engine has live steam passage and ft connection, and engine also has After exhaust passage is connected with low-temperature condenser, low-temperature condenser has low temperature cold lime set passage and ft connection again, and engine also has The post-heater that first steam channel is connected with heater has the first condensed fluid passage and ft connection again, and engine also has second After steam channel is connected with secondary heater, secondary heater has the second condensed fluid passage and ft connection again, engine or also There are exhaust passage and ft connection, circulating pump has circulatory mediator pipeline through low-temperature condenser, heater, secondary heater and heat supply The finisher that device is connected with vaporizer has circulatory mediator pipeline itself to connect through the second generator and circulating pump again, absorber and Condenser also has heated medium passage and ft connection respectively, and the second absorber also has coolant guiding channel and ft connection, Generator also has high temperature thermal medium passage and ft connection, and heater also has heated medium passage and ft connection, forms heat Dynamic co-feeding system.
The dynamic co-feeding system of 35. heat, is to move in co-feeding system in the 34th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser, heater, secondary heater are connected with vaporizer with heater has circulatory mediator pipeline warp again Second generator and circulating pump connect itself, be adjusted to circulating pump have circulatory mediator pipeline through low-temperature condenser, heater, second After heater is connected with the second generator with heater, the second generator has circulatory mediator pipeline again through vaporizer and circulating pump Itself connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 36. heat, is to move in co-feeding system in the 34th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser, heater, secondary heater are connected with vaporizer with heater has circulatory mediator pipeline warp again Second generator and circulating pump connect itself, be adjusted to circulating pump have circulatory mediator pipeline through low-temperature condenser, heater, second The finisher that heater is connected with vaporizer and the second generator respectively with heater and the second generator have circulation more respectively Medium pipeline and circulating pump connect itself, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 37. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heating Device, secondary heater, the 3rd heater and heater are formed；Absorber has weak solution pipeline through solution heat exchanger and second Absorber connects, and the second absorber also has weak solution pipeline to connect with generator through solution pump and the second solution heat exchanger, sends out Raw device also has concentrated solution pipeline to connect with the second generator through the second solution heat exchanger, and the second generator also has concentrated solution pipeline Connect with absorber with solution heat exchanger through the second solution pump, generator also has refrigerant steam channel to connect with condenser, the Two generators also have refrigerant steam channel to connect with the second absorber, and condenser also has cryogen liquid pipeline through choke valve and vaporizer Connection, vaporizer also has refrigerant steam channel to connect with absorber, and engine has live steam passage and ft connection respectively and has row Vapour passage and ft connection, engine also has the post-heater that the first steam channel is connected with heater to have the first condensed fluid to lead to again Road and ft connection, after engine also has the second steam channel to connect with secondary heater, secondary heater has the second condensation again Liquid passage and ft connection, after engine also has the 3rd steam channel to connect with the 3rd heater, the 3rd heater has the 3rd again Condensed fluid passage and ft connection, circulating pump has the heated device of circulatory mediator pipeline, secondary heater, the 3rd heater and heat supply The finisher that device is connected with vaporizer has circulatory mediator pipeline itself to connect through the second generator and circulating pump again, absorber and Condenser also has heated medium passage and ft connection respectively, and the second absorber also has coolant guiding channel and ft connection, Generator also has high temperature thermal medium passage and ft connection, and heater also has heated medium passage and ft connection, forms heat Dynamic co-feeding system.
The dynamic co-feeding system of 38. heat, is to move in co-feeding system in the 37th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that heater, secondary heater, the 3rd heater are connected with vaporizer with heater has circulatory mediator pipeline warp again Second generator and circulating pump connect itself, be adjusted to circulating pump have the heated device of circulatory mediator pipeline, secondary heater, the 3rd After heater is connected with the second generator with heater, the second generator has circulatory mediator pipeline again through vaporizer and circulating pump Itself connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 39. heat, is to move in co-feeding system in the 37th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that heater, secondary heater, the 3rd heater are connected with vaporizer with heater has circulatory mediator pipeline warp again Second generator and circulating pump connect itself, be adjusted to circulating pump have the heated device of circulatory mediator pipeline, secondary heater, the 3rd The finisher that heater is connected with vaporizer and the second generator respectively with heater and the second generator have circulation more respectively Medium pipeline and circulating pump connect itself, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 40. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, Circulating pump, heater, secondary heater, the 3rd heater and heater are formed；Absorber has weak solution pipeline through solution heat Exchanger is connected with the second absorber, and the second absorber also has weak solution pipeline through solution pump and the second solution heat exchanger and to send out Raw device connection, generator also has concentrated solution pipeline to connect with the second generator through the second solution heat exchanger, and the second generator is also Have concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution pump, generator also have refrigerant steam channel with cold Condenser connects, and the second generator also has refrigerant steam channel to connect with the second absorber, and condenser also has cryogen liquid pipeline warp knuckle Stream valve is connected with vaporizer, and vaporizer also has refrigerant steam channel to connect with absorber, and engine has live steam passage and outside to connect Logical, after engine also has exhaust passage to connect with low-temperature condenser, low-temperature condenser has low temperature cold lime set passage to connect with outside again Logical, engine also has the post-heater that the first steam channel is connected with heater to have the first condensed fluid passage and ft connection again, After engine also has the second steam channel to connect with secondary heater, secondary heater has the second condensed fluid passage and outside again Connection, engine also have the 3rd steam channel to connect with the 3rd heater after the 3rd heater have again the 3rd condensed fluid passage and Ft connection, engine or also exhaust passage and ft connection, circulating pump has circulatory mediator pipeline through low-temperature condenser, heating The finisher that device, secondary heater, the 3rd heater are connected with vaporizer with heater has circulatory mediator pipeline again through second Generator and circulating pump connect itself, and absorber and condenser also have heated medium passage and ft connection, the second suction respectively Receive device and also have coolant guiding channel and ft connection, generator also has high temperature thermal medium passage and ft connection, and heater also has Heated medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 41. heat, is to move in co-feeding system in the 40th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser, heater, secondary heater, the 3rd heater are connected with vaporizer with heater has circulation again Medium pipeline itself connects through the second generator and circulating pump, be adjusted to circulating pump have circulatory mediator pipeline through low-temperature condenser, After heater, secondary heater, the 3rd heater are connected with the second generator with heater, the second generator has circulation to be situated between again Matter pipeline itself connects through vaporizer and circulating pump, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 42. heat, is to move in co-feeding system in the 40th described heat, circulating pump is had circulatory mediator pipeline warp The finisher that low-temperature condenser, heater, secondary heater, the 3rd heater are connected with vaporizer with heater has circulation again Medium pipeline itself connects through the second generator and circulating pump, be adjusted to circulating pump have circulatory mediator pipeline through low-temperature condenser, Finisher that heater, secondary heater, the 3rd heater are connected with vaporizer and the second generator respectively with heater and Second generator has circulatory mediator pipeline and circulating pump itself to connect again respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 43. heat, is described in the 1st, 4,7,10,13,16,19,22,25,28,31,34,37,40 Any hot moves in co-feeding system, increases preheater, and the second absorber is had weak solution pipeline to hand over through solution pump and the second solution heat Parallel operation is connected with generator and is adjusted to the second absorber and has weak solution pipeline through solution pump, preheater and the second solution heat exchanger Connect with generator, vaporizer is had circulatory mediator pipeline to connect with circulating pump through the second generator and is adjusted to vaporizer and has circulation Medium pipeline is connected with circulating pump with preheater through the second generator, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 44. heat, is described in the 2nd, 5,8,11,14,17,20,23,26,29,32,35,38,41 Any hot moves in co-feeding system, increases preheater, and the second absorber is had weak solution pipeline to hand over through solution pump and the second solution heat Parallel operation is connected with generator and is adjusted to the second absorber and has weak solution pipeline through solution pump, preheater and the second solution heat exchanger Connect with generator, the second generator is had circulatory mediator pipeline to connect with circulating pump through vaporizer and is adjusted to the second generator and has Circulatory mediator pipeline is connected with circulating pump with preheater through vaporizer, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 45. heat, is described in the 3rd, 6,9,12,15,18,21,24,27,30,33,36,39,42 Any hot moves in co-feeding system, increases preheater, and the second absorber is had weak solution pipeline to hand over through solution pump and the second solution heat Parallel operation is connected with generator and is adjusted to the second absorber and has weak solution pipeline through solution pump, preheater and the second solution heat exchanger Connect with generator, by vaporizer and the second generator have respectively circulatory mediator pipeline connect with circulating pump be adjusted to vaporizer and Second generator has the preheated device of circulatory mediator pipeline to connect with circulating pump respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 46. heat, is that any hot described in 1-42 item moves in co-feeding system, increase the 3rd generator, 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber is had weak solution pipeline through solution pump and Two solution heat exchangers connect with generator be adjusted to the second absorber have weak solution pipeline through solution pump and the second solution heat hand over Parallel operation is connected with the 3rd absorber, the 3rd absorber have again weak solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger with Generator connects, and generator is had concentrated solution pipeline to connect with the second generator through the second solution heat exchanger and is adjusted to generator Concentrated solution pipeline is had to connect with the 3rd generator through the 3rd solution heat exchanger, the 3rd generator has concentrated solution pipeline again through second Solution heat exchanger is connected with the second generator, and the 3rd generator also has refrigerant steam channel to connect with the 3rd absorber, and the 3rd Generator also has high temperature thermal medium passage and ft connection, and the 3rd absorber also has heated medium passage and ft connection, shape Become the dynamic co-feeding system of heat.
The dynamic co-feeding system of 47. heat, is that any hot described in 43-45 item moves in co-feeding system, increase the 3rd generator, 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber is had weak solution pipeline through solution pump, preheating Device and the second solution heat exchanger connect with generator be adjusted to the second absorber have weak solution pipeline through solution pump, preheater and Second solution heat exchanger is connected with the 3rd absorber, and the 3rd absorber has weak solution pipeline molten through the 3rd solution pump and the 3rd again Liquid heat exchanger is connected with generator, and generator is had concentrated solution pipeline to connect with the second generator through the second solution heat exchanger Being adjusted to generator has concentrated solution pipeline to connect with the 3rd generator through the 3rd solution heat exchanger, and the 3rd generator has dense molten again Liquid pipeline is connected with the second generator through the second solution heat exchanger, and the 3rd generator also has refrigerant steam channel and the 3rd absorption Device connects, and the 3rd generator also has high temperature thermal medium passage and ft connection, the 3rd absorber also have heated medium passage with Ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 48. heat, is that any hot described in 1-42 item moves in co-feeding system, increase the 3rd generator, 3rd solution pump, the 3rd solution heat exchanger and second throttle, the second absorber sets up weak solution pipeline through the 3rd solution pump Connect with the 3rd generator with the 3rd solution heat exchanger, the 3rd generator also has concentrated solution pipeline through the 3rd solution heat exchanger Connect with the second generator, generator is had refrigerant steam channel to connect with condenser and is adjusted to generator and has refrigerant steam channel After connecting with the 3rd generator, the 3rd generator has cryogen liquid pipeline to connect with condenser through second throttle again, the 3rd generation Device also has refrigerant steam channel to connect with condenser, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 49. heat, is that any hot described in 1-42 item moves in co-feeding system, increase the 3rd generator, 3rd solution heat exchanger and second throttle, the second absorber is had weak solution pipeline through solution pump and the second solution heat exchange Device is connected with generator and is adjusted to the second absorber and has weak solution pipeline through solution pump, the second solution heat exchanger and the 3rd solution Heat exchanger is connected with generator, and generator is had concentrated solution pipeline to connect tune through the second solution heat exchanger with the second generator Whole have concentrated solution pipeline to connect with the 3rd generator through the 3rd solution heat exchanger for generator, and the 3rd generator has concentrated solution again Pipeline is connected with the second generator through the second solution heat exchanger, and generator is had refrigerant steam channel to connect adjustment with condenser After having refrigerant steam channel to connect with the 3rd generator for generator, the 3rd generator has cryogen liquid pipeline again through the second throttling Valve is connected with condenser, and the 3rd generator also has refrigerant steam channel to connect with condenser, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 50. heat, is that any hot described in 1-42 item moves in co-feeding system, increase the 3rd generator, 3rd solution pump, the 3rd solution heat exchanger and second throttle, the second absorber is had weak solution pipeline through solution pump and Two solution heat exchangers connect with generator be adjusted to the second absorber have weak solution pipeline through solution pump and the second solution heat hand over Parallel operation is connected with the 3rd generator, the 3rd generator have again concentrated solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger with Generator connects, and generator is had concentrated solution pipeline to connect with the second generator through the second solution heat exchanger and is adjusted to generator There is concentrated solution pipeline to connect with the second generator through the 3rd solution heat exchanger and the second solution heat exchanger, generator is had cold Agent steam channel is connected with condenser and is adjusted to the 3rd generation after generator has refrigerant steam channel to connect with the 3rd generator Device has cryogen liquid pipeline to connect with condenser through second throttle again, and the 3rd generator also has refrigerant steam channel with condenser even Logical, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 51. heat, is that any hot described in 43-45 item moves in co-feeding system, increase the 3rd generator, 3rd solution pump, the 3rd solution heat exchanger and second throttle, the second absorber set up weak solution pipeline through the 3rd solution pump, Preheater and the 3rd solution heat exchanger are connected with the 3rd generator, and the 3rd generator also has concentrated solution pipeline through the 3rd solution heat Exchanger is connected with the second generator, by generator have refrigerant steam channel connect with condenser be adjusted to generator have cryogen steam After vapour passage is connected with the 3rd generator, the 3rd generator has cryogen liquid pipeline to connect with condenser through second throttle again, the Three generators also have refrigerant steam channel to connect with condenser, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 52. heat, is that any hot described in 43-45 item moves in co-feeding system, increase the 3rd generator, 3rd solution heat exchanger and second throttle, the second absorber is had weak solution pipeline molten through solution pump, preheater and second Liquid heat exchanger connect with generator be adjusted to the second absorber have weak solution pipeline through solution pump, preheater, second solution heat Exchanger and the 3rd solution heat exchanger are connected with generator, by generator have concentrated solution pipeline through the second solution heat exchanger with Second generator connection is adjusted to generator has concentrated solution pipeline to connect with the 3rd generator through the 3rd solution heat exchanger, and the 3rd Generator has concentrated solution pipeline to connect with the second generator through the second solution heat exchanger again, and generator is had refrigerant steam channel Connect with condenser and be adjusted to the 3rd generator after generator has refrigerant steam channel to connect with the 3rd generator and have cryogen again Liquid pipeline is connected with condenser through second throttle, and the 3rd generator also has refrigerant steam channel to connect with condenser, forms heat Dynamic co-feeding system.
The dynamic co-feeding system of 53. heat, is that any hot described in 43-45 item moves in co-feeding system, increase the 3rd generator, 3rd solution pump, the 3rd solution heat exchanger and second throttle, the second absorber is had weak solution pipeline through solution pump, preheating Device and the second solution heat exchanger connect with generator be adjusted to the second absorber have weak solution pipeline through solution pump, preheater and Second solution heat exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline molten through the 3rd solution pump and the 3rd again Liquid heat exchanger is connected with generator, and generator is had concentrated solution pipeline to connect with the second generator through the second solution heat exchanger Being adjusted to generator has concentrated solution pipeline to connect with the second generator through the 3rd solution heat exchanger and the second solution heat exchanger, Generator there is is refrigerant steam channel to connect with condenser be adjusted to generator and have refrigerant steam channel to connect with the 3rd generator 3rd generator has cryogen liquid pipeline to connect with condenser through second throttle more afterwards, and the 3rd generator also has refrigerant vapour to lead to Road is connected with condenser, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 54. heat, is that any hot described in 47-52 item moves in co-feeding system, the 3rd generator is set up High temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 55. heat, is that any hot described in 1-45 item moves in co-feeding system, increase the 3rd generator, 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, generator is had refrigerant steam channel to connect tune with condenser Whole have refrigerant steam channel to connect with the 3rd absorber for generator, and the 3rd absorber also has weak solution pipeline through the 3rd solution pump Connect with the 3rd generator with the 3rd solution heat exchanger, the 3rd generator also has concentrated solution pipeline through the 3rd solution heat exchanger Connect with the 3rd absorber, the 3rd generator also has refrigerant steam channel to connect with condenser, the 3rd generator also has high warm Medium channel and ft connection, the 3rd absorber also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 56. heat, is described in the 1st, 4,7,10,13,16,19,22,25,28,31,34,37,40 Any hot moves in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, will Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger to be adjusted to absorber and have weak solution pipeline through Three solution heat exchangers are connected with the 3rd absorber, and the 3rd absorber has weak solution pipeline to hand over through the 3rd solution pump and solution heat again Parallel operation is connected with the second absorber, and the second generator is had concentrated solution pipeline through the second solution pump and solution heat exchanger and absorption Device connection is adjusted to the second generator has concentrated solution pipeline to connect with the 3rd generator through solution heat exchanger, and the 3rd generator is again There is concentrated solution pipeline to connect with absorber through the second solution pump and the 3rd solution heat exchanger, vaporizer is had circulatory mediator pipeline Connect with circulating pump through the second generator be adjusted to vaporizer have circulatory mediator pipeline through the second generator and the 3rd generator with Circulating pump connects, and the 3rd generator also has refrigerant steam channel to connect with the 3rd absorber, and the 3rd absorber also has cooling medium Passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 57. heat, is described in the 2nd, 5,8,11,14,17,20,23,26,29,32,35,38,41 Any hot moves in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, will Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger to be adjusted to absorber and have weak solution pipeline through Three solution heat exchangers are connected with the 3rd absorber, and the 3rd absorber has weak solution pipeline to hand over through the 3rd solution pump and solution heat again Parallel operation is connected with the second absorber, and the second generator is had concentrated solution pipeline through the second solution pump and solution heat exchanger and absorption Device connection is adjusted to the second generator has concentrated solution pipeline to connect with the 3rd generator through solution heat exchanger, and the 3rd generator is again There is concentrated solution pipeline to connect with absorber through the second solution pump and the 3rd solution heat exchanger, the second generator is had circulatory mediator Pipeline connect with circulating pump through vaporizer be adjusted to the second generator have circulatory mediator pipeline through vaporizer and the 3rd generator with Circulating pump connects, and the 3rd generator also has refrigerant steam channel to connect with the 3rd absorber, and the 3rd absorber also has cooling medium Passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 58. heat, is described in the 3rd, 6,9,12,15,18,21,24,27,30,33,36,39,42 Any hot moves in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, will Absorber has weak solution pipeline to connect with the second absorber through solution heat exchanger to be adjusted to absorber and have weak solution pipeline through Three solution heat exchangers are connected with the 3rd absorber, and the 3rd absorber has weak solution pipeline to hand over through the 3rd solution pump and solution heat again Parallel operation is connected with the second absorber, and the second generator is had concentrated solution pipeline through the second solution pump and solution heat exchanger and absorption Device connection is adjusted to the second generator has concentrated solution pipeline to connect with the 3rd generator through solution heat exchanger, and the 3rd generator is again There is concentrated solution pipeline to connect with absorber through the second solution pump and the 3rd solution heat exchanger, vaporizer and the second generator are divided There is not circulatory mediator pipeline to connect with circulating pump and be adjusted to vaporizer and the second generator has circulatory mediator pipeline respectively through the 3rd Generator is connected with circulating pump, and the 3rd generator also has refrigerant steam channel to connect with the 3rd absorber, and the 3rd absorber also has Coolant guiding channel and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 59. heat, is that any hot described at the 56th moves in co-feeding system, increases preheater, by second Absorber have weak solution pipeline connect with generator through solution pump and the second solution heat exchanger be adjusted to the second absorber have dilute Solution line is connected with generator through solution pump, preheater and the second solution heat exchanger, and vaporizer is had circulatory mediator pipeline Connect with circulating pump through the second generator and the 3rd generator be adjusted to vaporizer have circulatory mediator pipeline through the second generator, Three generators are connected with circulating pump with preheater, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 60. heat, is that any hot described at the 57th moves in co-feeding system, increases preheater, by second Absorber have weak solution pipeline connect with generator through solution pump and the second solution heat exchanger be adjusted to the second absorber have dilute Solution line is connected with generator through solution pump, preheater and the second solution heat exchanger, and the second generator is had circulatory mediator Pipeline connect with circulating pump through vaporizer and the 3rd generator be adjusted to the second generator have circulatory mediator pipeline through vaporizer, Three generators are connected with circulating pump with preheater, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 61. heat, is that any hot described at the 58th moves in co-feeding system, increases preheater, by second Absorber have weak solution pipeline connect with generator through solution pump and the second solution heat exchanger be adjusted to the second absorber have dilute Solution line is connected with generator through solution pump, preheater and the second solution heat exchanger, and vaporizer and the second generator are divided There is not circulatory mediator pipeline to connect with circulating pump through the 3rd generator to be adjusted to vaporizer and the second generator and have circulation to be situated between respectively Matter pipeline is connected with circulating pump with preheater through the 3rd generator, forms the dynamic co-feeding system of heat.
Brief description：
Fig. 1 is according to heat provided by the present invention dynamic co-feeding system the 1st kind of structure and schematic flow sheet.
Fig. 2 is according to heat provided by the present invention dynamic co-feeding system the 2nd kind of structure and schematic flow sheet.
Fig. 3 is according to heat provided by the present invention dynamic co-feeding system the 3rd kind of structure and schematic flow sheet.
Fig. 4 is according to heat provided by the present invention dynamic co-feeding system the 4th kind of structure and schematic flow sheet.
Fig. 5 is according to heat provided by the present invention dynamic co-feeding system the 5th kind of structure and schematic flow sheet.
Fig. 6 is according to heat provided by the present invention dynamic co-feeding system the 6th kind of structure and schematic flow sheet.
Fig. 7 is according to heat provided by the present invention dynamic co-feeding system the 7th kind of structure and schematic flow sheet.
Fig. 8 is according to heat provided by the present invention dynamic co-feeding system the 8th kind of structure and schematic flow sheet.
Fig. 9 is according to heat provided by the present invention dynamic co-feeding system the 9th kind of structure and schematic flow sheet.
Figure 10 is according to heat provided by the present invention dynamic co-feeding system the 10th kind of structure and schematic flow sheet.
Figure 11 is according to heat provided by the present invention dynamic co-feeding system the 11st kind of structure and schematic flow sheet.
Figure 12 is according to heat provided by the present invention dynamic co-feeding system the 12nd kind of structure and schematic flow sheet.
Figure 13 is according to heat provided by the present invention dynamic co-feeding system the 13rd kind of structure and schematic flow sheet.
Figure 14 is according to heat provided by the present invention dynamic co-feeding system the 14th kind of structure and schematic flow sheet.
Figure 15 is according to heat provided by the present invention dynamic co-feeding system the 15th kind of structure and schematic flow sheet.
Figure 16 is according to heat provided by the present invention dynamic co-feeding system the 16th kind of structure and schematic flow sheet.
Figure 17 is according to heat provided by the present invention dynamic co-feeding system the 17th kind of structure and schematic flow sheet.
In figure, 1- absorber, 2- second absorber, 3- generator, 4- second generator, 5- condenser, 6- vaporizer, 7- Choke valve, 8- solution pump, 9- the second solution pump, 10- solution heat exchanger, 11- second solution heat exchanger, 12- engine, 13- low-temperature condenser, 14- circulating pump, 15- heater, 16- secondary heater, 17- the 3rd heater, 18- heater, 19- Three generators, 20- the 3rd absorber, 21- the 3rd solution pump, 22- the 3rd solution heat exchanger, 23- second throttle, 24- is pre- Hot device.
Specific embodiment：
First it is noted that in the statement of structure and flow process, inessential in the case of do not repeat；To apparent Flow process do not state.To describe the present invention with example in detail below in conjunction with the accompanying drawings.
Heat shown in Fig. 1 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser and follow Ring pump is formed；Absorber 1 has weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 10, and the second absorber 2 is also Weak solution pipeline is had to connect with generator 3 with the second solution heat exchanger 11 through solution pump 8, generator 3 also has concentrated solution pipeline Connect with the second generator 4 through the second solution heat exchanger 11, the second generator 4 also has concentrated solution pipeline through the second solution pump 9 Connect with absorber 1 with solution heat exchanger 10, generator 3 also has refrigerant steam channel to connect with condenser 5, the second generator 4 also have refrigerant steam channel to connect with the second absorber 2, and condenser 5 also has cryogen liquid pipeline through choke valve 7 with vaporizer 6 even Logical, vaporizer 6 also has refrigerant steam channel to connect with absorber 1, and engine 12 has live steam passage and ft connection, engine 12 After also having exhaust passage to connect with low-temperature condenser 13, low-temperature condenser 13 has low temperature cold lime set passage and ft connection again, follows Ring pump 14 has circulatory mediator pipeline to have circulatory mediator pipeline warp again through the finisher 6 that low-temperature condenser 13 is connected with vaporizer 6 Second generator 4 itself is connected with circulating pump 14, and absorber 1 and condenser 5 also have heated medium passage and outside to connect respectively Logical, the second absorber 2 also has coolant guiding channel and ft connection, and generator 3 also has high temperature thermal medium passage and ft connection.
(2) in flow process, live steam enters engine 12 blood pressure lowering work done, and the steam discharge of engine 12 flows through low-temperature condenser 13 heat release And condense, externally discharge afterwards；The circulatory mediator that circulating pump 14 is discharged flows through low-temperature condenser 13 and absorbs heat, and flows through vaporizer 6 With the second generator 4 and progressively heat release, it is supplied to circulating pump 14 afterwards；The weak solution of absorber 1 is entered through solution heat exchanger 10 Enter the second absorber 2, absorb refrigerant vapour and heat release is in cooling medium, the weak solution of the second absorber 2 is through solution pump 8 and second Solution heat exchanger 11 enters generator 3, and high temperature thermal medium flows through generator 3, heating enters its interior solution release cryogen and steams Vapour simultaneously provides to condenser 5, and the concentrated solution of generator 3 enters the second generator 4, heat absorption release through the second solution heat exchanger 11 Refrigerant vapour simultaneously provides to the second absorber 2, and the concentrated solution of the second generator 4 is through the second solution pump 9 and solution heat exchanger 10 Enter absorber 1, absorb refrigerant vapour and heat release is in heated medium；The refrigerant vapour heat release of condenser 5 is in heated medium And condense, the cryogen liquid of condenser 5 enters vaporizer 6, absorbs heat into refrigerant vapour and to absorber 1 through choke valve 7 reducing pressure by regulating flow There is provided, form the dynamic co-feeding system of heat.
Heat shown in Fig. 2 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump and heater Formed；Absorber 1 has weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 10, and the second absorber 2 is also dilute Solution line is connected with generator 3 with the second solution heat exchanger 11 through solution pump 8, and generator 3 also has concentrated solution pipeline through the Two solution heat exchangers 11 are connected with the second generator 4, and the second generator 4 also has concentrated solution pipeline through the second solution pump 9 and molten Liquid heat exchanger 10 is connected with absorber 1, and generator 3 also has refrigerant steam channel to connect with condenser 5, and the second generator 4 is also Refrigerant steam channel is had to connect with the second absorber 2, condenser 5 also has cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7, Vaporizer 6 also has refrigerant steam channel to connect with absorber 1, and engine 12 has live steam passage and ft connection respectively and has steam discharge Passage and ft connection, engine 12 also has the post-heater 15 that the first steam channel is connected with heater 15 to have the first condensation again Liquid passage and ft connection, circulating pump 14 has the finisher 6 that the heated device of circulatory mediator pipeline 15 is connected with vaporizer 6 to have again Circulatory mediator pipeline itself is connected with circulating pump 14 through the second generator 4, and absorber 1 and condenser 5 also have heated Jie respectively Matter passage and ft connection, the second absorber 2 also has coolant guiding channel and ft connection, and generator 3 also has high temperature thermal medium Passage and ft connection.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing Live steam is divided into two-way after entering engine 12 blood pressure lowering work done, and the first via is supplied to heater 15 heat release by the first steam channel Externally discharge after condensation, the second tunnel is continued blood pressure lowering work done and externally discharged, circulatory mediator carries after flowing through heater 15 heat absorption Supply vaporizer 6, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 3 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, circulation Pump and heater are formed；Absorber 1 has weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 10, the second suction Receiving device 2 also has weak solution pipeline to connect with generator 3 with the second solution heat exchanger 11 through solution pump 8, and generator 3 also has dense molten Liquid pipeline is connected with the second generator 4 through the second solution heat exchanger 11, and the second generator 4 also has concentrated solution pipeline molten through second Liquid pump 9 is connected with absorber 1 with solution heat exchanger 10, and generator 3 also has refrigerant steam channel to connect with condenser 5, and second Generator 4 also has refrigerant steam channel to connect with the second absorber 2, and condenser 5 also has cryogen liquid pipeline through choke valve 7 and evaporation Device 6 connects, and vaporizer 6 also has refrigerant steam channel to connect with absorber 1, and engine 12 has live steam passage and ft connection, moves After power machine 12 also has exhaust passage to connect with low-temperature condenser 13, low-temperature condenser 13 has low temperature cold lime set passage and outside again Connection, engine 12 also has the post-heater 15 that the first steam channel is connected with heater 15 to have the first condensed fluid passage again with outward Portion connects, and circulating pump 14 has the finisher 6 that circulatory mediator pipeline is connected with vaporizer 6 with heater 15 through low-temperature condenser 13 Circulatory mediator pipeline is had itself to connect with circulating pump 14 through the second generator 4 again, absorber 1 and condenser 5 also have respectively and added Hot media channel and ft connection, the second absorber 2 also has coolant guiding channel and ft connection, and generator 3 also has high warm Medium channel and ft connection.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing Live steam is divided into two-way after entering engine 12 blood pressure lowering work done, and the steam for relative outlet with elevated pressures passes through the first steaming Vapour passage is externally discharged after being supplied to heater 15 exothermic condensation, and the steam discharge after completing blood pressure lowering work done flows through low-temperature condenser 13 exothermic condensation are simultaneously externally discharged, and circulatory mediator flows through low-temperature condenser 13 and heater 15 and is supplied to steaming after progressively absorbing heat Send out device 6, form the dynamic co-feeding system of heat.
Heat shown in Fig. 4 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heater and Secondary heater is formed；Absorber 1 has weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 10, the second suction Receiving device 2 also has weak solution pipeline to connect with generator 3 with the second solution heat exchanger 11 through solution pump 8, and generator 3 also has dense molten Liquid pipeline is connected with the second generator 4 through the second solution heat exchanger 11, and the second generator 4 also has concentrated solution pipeline molten through second Liquid pump 9 is connected with absorber 1 with solution heat exchanger 10, and generator 3 also has refrigerant steam channel to connect with condenser 5, and second Generator 4 also has refrigerant steam channel to connect with the second absorber 2, and condenser 5 also has cryogen liquid pipeline through choke valve 7 and evaporation Device 6 connects, and vaporizer 6 also has refrigerant steam channel to connect with absorber 1, and engine 12 has live steam passage and ft connection respectively And have exhaust passage and ft connection, engine 12 also has the post-heater 15 that connects with heater 15 of the first steam channel to have again First condensed fluid passage and ft connection, after engine 12 also has the second steam channel to connect with secondary heater 16, second adds Hot device 16 has the second condensed fluid passage and ft connection again, and circulating pump 14 has the heated device of circulatory mediator pipeline 15 and the second heating The finisher 6 that device 16 is connected with vaporizer 6 has circulatory mediator pipeline itself to connect with circulating pump 14 through the second generator 4 again, Absorber 1 and condenser 5 also have heated medium passage and ft connection respectively, and the second absorber 2 also has coolant guiding channel With ft connection, generator 3 also high temperature thermal medium passage and ft connection.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing After live steam enters engine 12 blood pressure lowering work done, it is supplied to secondary heater 16 and through the first steam through the second steam channel respectively Passage is supplied to heater 15, and remaining steam continues to complete work done and externally discharges；Heated device 15 heat releases of first steam stream are cold Externally discharge after solidifying, the second steam flows through secondary heater 16 exothermic condensation and externally discharges, and circulatory mediator flows through heater 15 and secondary heater 16 be supplied to vaporizer 6 after progressively absorbing heat, form the dynamic co-feeding system of heat.
Heat shown in Fig. 5 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, circulation Pump, heater and secondary heater are formed；Absorber 1 has weak solution pipeline through solution heat exchanger 10 and the second absorber 2 Connection, the second absorber 2 also has weak solution pipeline to connect with generator 3 with the second solution heat exchanger 11 through solution pump 8, occurs Device 3 also has concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 11, and the second generator 4 also has concentrated solution Pipeline is connected with absorber 1 with solution heat exchanger 10 through the second solution pump 9, and generator 3 also has refrigerant steam channel and condensation Device 5 connects, and the second generator 4 also has refrigerant steam channel to connect with the second absorber 2, and condenser 5 also has cryogen liquid pipeline warp Choke valve 7 is connected with vaporizer 6, and vaporizer 6 also has refrigerant steam channel to connect with absorber 1, and engine 12 has live steam passage With ft connection, after engine 12 also has exhaust passage to connect with low-temperature condenser 13, low-temperature condenser 13 has condensation at low temperature again Liquid passage and ft connection, it is first cold that engine 12 also has the post-heater 15 that connects with heater 15 of the first steam channel to have again Lime set passage and ft connection, engine 12 also have the second steam channel connect with secondary heater 16 after secondary heater 16 There are the second condensed fluid passage and ft connection again, engine 12 also has exhaust passage and ft connection, circulating pump 14 has circulation to be situated between Matter pipeline has circulation to be situated between through the finisher 6 that low-temperature condenser 13, heater 15 are connected with vaporizer 6 with secondary heater 16 again Matter pipeline itself is connected with circulating pump 14 through the second generator 4, and absorber 1 and condenser 5 also have heated medium passage respectively With ft connection, the second absorber 2 also has coolant guiding channel and ft connection, generator 3 also have high temperature thermal medium passage with Ft connection.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing After live steam enters engine 12 blood pressure lowering work done, it is supplied to secondary heater 16 through the second steam channel respectively, through the first steam Passage is supplied to heater 15, is supplied to low-temperature condenser 13 through exhaust passage and externally discharges through exhaust passage；First steam Externally discharge after flowing through heater 15 exothermic condensation, the second steam flows through secondary heater 16 exothermic condensation and externally discharges, Circulatory mediator flows through low-temperature condenser 13, heater 15 and secondary heater 16 and is supplied to vaporizer 6, shape after progressively absorbing heat Become the dynamic co-feeding system of heat.
Heat shown in Fig. 6 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heater, Secondary heater and the 3rd heater are formed；Absorber 1 has weak solution pipeline through solution heat exchanger 10 and the second absorber 2 Connection, the second absorber 2 also has weak solution pipeline to connect with generator 3 with the second solution heat exchanger 11 through solution pump 8, occurs Device 3 also has concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 11, and the second generator 4 also has concentrated solution Pipeline is connected with absorber 1 with solution heat exchanger 10 through the second solution pump 9, and generator 3 also has refrigerant steam channel and condensation Device 5 connects, and the second generator 4 also has refrigerant steam channel to connect with the second absorber 2, and condenser 5 also has cryogen liquid pipeline warp Choke valve 7 is connected with vaporizer 6, and vaporizer 6 also has refrigerant steam channel to connect with absorber 1, and engine 12 has live steam respectively Passage and ft connection and have exhaust passage and ft connection, also the first steam channel connects it with heater 15 to engine 12 Post-heater 15 has the first condensed fluid passage and ft connection again, and engine 12 also has the second steam channel and secondary heater 16 After connection, secondary heater 16 has the second condensed fluid passage and ft connection again, and engine 12 also has the 3rd steam channel and the After three heater 17 connection, the 3rd heater 17 has the 3rd condensed fluid passage and ft connection again, and circulating pump 14 has circulatory mediator The finisher 6 that the heated device of pipeline 15, secondary heater 16 are connected with vaporizer 6 with the 3rd heater 17 has circulatory mediator again Pipeline itself is connected with circulating pump 14 through the second generator 4, absorber 1 and condenser 5 also have respectively heated medium passage with Ft connection, the second absorber 2 also has coolant guiding channel and ft connection, and generator 3 also has high temperature thermal medium passage with outward Portion connects.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing After live steam enters engine 12 blood pressure lowering work done, it is supplied to the 3rd heater 17 through the 3rd steam channel respectively, through the second steam Passage is supplied to secondary heater 16 and is supplied to heater 15 through the first steam channel, and remaining steam continues to complete work done right Outer discharge；Externally discharge after the heated device of first steam stream 15 exothermic condensation, the second steam flows through secondary heater 16 heat release Condensation is simultaneously externally discharged, and the 3rd steam flows through the 3rd heater 17 exothermic condensation and externally discharges, and circulatory mediator flows through heater 15th, secondary heater 16 and the 3rd heater 17 be supplied to vaporizer 6 after progressively absorbing heat, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 7 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, circulation Pump, heater, secondary heater and the 3rd heater are formed；Absorber 1 have weak solution pipeline through solution heat exchanger 10 with Second absorber 2 connects, and the second absorber 2 also has weak solution pipeline through solution pump 8 and the second solution heat exchanger 11 and generation Device 3 connects, and generator 3 also has concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 11, the second generator 4 also have concentrated solution pipeline to connect with absorber 1 with solution heat exchanger 10 through the second solution pump 9, and generator 3 also has refrigerant vapour Passage is connected with condenser 5, and the second generator 4 also has refrigerant steam channel to connect with the second absorber 2, and condenser 5 is also cold Agent liquid pipeline is connected with vaporizer 6 through choke valve 7, and vaporizer 6 also has refrigerant steam channel to connect with absorber 1, engine 12 Have live steam passage and ft connection, engine 12 also have exhaust passage connect with low-temperature condenser 13 after low-temperature condenser 13 again There are low temperature cold lime set passage and ft connection, engine 12 also has the post-heater 15 that the first steam channel is connected with heater 15 Have the first condensed fluid passage and ft connection again, engine 12 also have the second steam channel to connect with secondary heater 16 after the Two heaters 16 have the second condensed fluid passage and ft connection again, and engine 12 also has the 3rd steam channel and the 3rd heater 17 After connection, the 3rd heater 17 has the 3rd condensed fluid passage and ft connection again, and circulating pump 14 has circulatory mediator pipeline through low temperature The finisher 6 that condenser 13, heater 15, secondary heater 16 are connected with vaporizer 6 with the 3rd heater 17 has circulation again Medium pipeline itself is connected with circulating pump 14 through the second generator 4, and absorber 1 and condenser 5 also have heated medium to lead to respectively Road and ft connection, the second absorber 2 also has coolant guiding channel and ft connection, and generator 3 also has high temperature thermal medium passage With ft connection.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing After live steam enters engine 12 blood pressure lowering work done, it is supplied to the 3rd heater 17 through the 3rd steam channel respectively, through the second steam Passage is supplied to secondary heater 16, is supplied to heater 15 through the first steam channel and is supplied to condensation at low temperature through exhaust passage Device 13；Externally discharge after the heated device of first steam stream 15 exothermic condensation, it is cold that the second steam flows through secondary heater 16 heat release Coalescence is externally discharged, and the 3rd steam flows through the 3rd heater 17 exothermic condensation and externally discharges, and circulatory mediator flows through condensation at low temperature It is supplied to vaporizer 6 after device 13, heater 15, secondary heater 16 and the 3rd heater 17 progressively heat absorption, form heat dynamic Co-feeding system.
Heat shown in Fig. 8 moves what co-feeding system was realized in：
Heat shown in Fig. 6 is moved in co-feeding system, increases heater, circulating pump 14 is had the heated device of circulatory mediator pipeline 15th, the finisher 6 that secondary heater 16 is connected with vaporizer 6 with the 3rd heater 17 has circulatory mediator pipeline again through second Raw device 4 itself is connected with circulating pump 14, be adjusted to circulating pump 14 have the heated device of circulatory mediator pipeline 15, secondary heater 16, The finisher 6 that 3rd heater 17 is connected with vaporizer 6 with heater 18 have again circulatory mediator pipeline through the second generator 4 with Circulating pump 14 itself connects, and heater 18 also has heated medium passage and ft connection；Circulatory mediator flow through heater 15, Two heaters 16 and the 3rd heater 17 simultaneously progressively absorb heat, flow through afterwards heater 18, vaporizer 6 and the second generator 4 and by Step heat release, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 9 moves what co-feeding system was realized in：
Heat shown in Fig. 5 is moved in co-feeding system, and circulating pump 14 is had circulatory mediator pipeline through low-temperature condenser 13, heating The finisher 6 that device 15 is connected with vaporizer 6 with secondary heater 16 has circulatory mediator pipeline again through the second generator 4 and circulation Pump 14 itself connects, and being adjusted to circulating pump 14 has circulatory mediator pipeline through low-temperature condenser 13, heater 15 and secondary heater 16 connect with the second generator 4 after the second generator 4 have circulatory mediator pipeline again through vaporizer 6 with circulating pump 14 itself even Logical；The circulatory mediator of circulating pump 14 discharge flows through low-temperature condenser 13, heater 15 and secondary heater 16 and progressively absorbs heat, stream Through the second generator 4 and vaporizer 6 progressively heat release, return to circulating pump 14 afterwards, form the dynamic co-feeding system of heat.
Heat shown in Figure 10 moves what co-feeding system was realized in：
Heat shown in Fig. 5 is moved in co-feeding system, and circulating pump 14 is had circulatory mediator pipeline through low-temperature condenser 13, heating The finisher 6 that device 15 is connected with vaporizer 6 with secondary heater 16 has circulatory mediator pipeline again through the second generator 4 and circulation Pump 14 itself connects, and being adjusted to circulating pump 14 has circulatory mediator pipeline through low-temperature condenser 13, heater 15 and secondary heater 16 the finisher 6 connecting and the second generator 4 have circulatory mediator pipeline more respectively with vaporizer 6 and the second generator 4 respectively Itself connect with circulating pump 14；The circulatory mediator of circulating pump 14 discharge flows through low-temperature condenser 13, heater 15 and the second heating Device 16 simultaneously progressively absorbs heat, and flows separately through vaporizer 6 and the second generator 4 heat release respectively, returns to circulating pump 14 afterwards, forms heat Dynamic co-feeding system.
Heat shown in Figure 11 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 5 is moved in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd molten Liquid pump and the 3rd solution heat exchanger, the second absorber 2 is had weak solution pipeline through solution pump 8 and the second solution heat exchanger 11 Connect with generator 3 and be adjusted to the second absorber 2 and have weak solution pipeline through solution pump 8 and the second solution heat exchanger 11 and the 3rd Absorber 20 connects, and the 3rd absorber 20 has weak solution pipeline through the 3rd solution pump 21 and the 3rd solution heat exchanger 22 and to send out again Raw device 3 connects, and generator 3 is had concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 11 and is adjusted to Raw device 3 has concentrated solution pipeline to connect with the 3rd generator 19 through the 3rd solution heat exchanger 22, and the 3rd generator 19 has dense molten again Liquid pipeline is connected with the second generator 4 through the second solution heat exchanger 11, and the 3rd generator 19 also has refrigerant steam channel and the Three absorbers 20 connect, and the 3rd generator 19 also has high temperature thermal medium passage and ft connection, and the 3rd absorber 20 is also added Hot media channel and ft connection.
(2), in flow process, the weak solution of the second absorber 2 enters the 3rd suction through solution pump 8 and the second solution heat exchanger 11 Receive device 20, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 20 is through the 3rd solution pump 21 and the Three solution heat exchanger 22 enters generator 3, and the concentrated solution of generator 3 enters the 3rd generator through the 3rd solution heat exchanger 22 19, high temperature thermal medium flows through the 3rd generator 19, heating enters its interior solution and discharges refrigerant vapour and to the 3rd absorber 20 There is provided, the concentrated solution of the 3rd generator 19 enters the second generator 4 through the second solution heat exchanger 11, form the dynamic alliance system of heat System.
Heat shown in Figure 12 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 5 is moved in co-feeding system, increases the 3rd generator, the 3rd solution pump, the 3rd molten Liquid heat exchanger and second throttle, the second absorber 2 is set up weak solution pipeline and is handed over through the 3rd solution pump 21 and the 3rd solution heat Parallel operation 22 is connected with the 3rd generator 19, and the 3rd generator 19 also has concentrated solution pipeline through the 3rd solution heat exchanger 22 and second Generator 4 connects, by generator 3 have refrigerant steam channel connect with condenser 5 be adjusted to generator 3 have refrigerant steam channel with After 3rd generator 19 connection, the 3rd generator 19 has cryogen liquid pipeline to connect with condenser 5 through second throttle 23 again, the Three generators 19 also have refrigerant steam channel to connect with condenser 5.
(2), in flow process, the refrigerant vapour that generator 3 produces is supplied to the 3rd generator 19 and makees to drive thermal medium, the second suction The part weak solution receiving device 2 enters the 3rd generator 19, refrigerant vapour through the 3rd solution pump 21 and the 3rd solution heat exchanger 22 Flow through the 3rd generator 19, heating enters its interior solution release refrigerant vapour and provides to condenser 5, the 3rd generator 19 Concentrated solution enters the second generator 4 through the 3rd solution heat exchanger 22；Flow through the refrigerant vapour heat release Cheng Leng of the 3rd generator 19 Agent liquid, cryogen liquor stream, through entering condenser 5 after second throttle 23 reducing pressure by regulating flow, forms the dynamic co-feeding system of heat.
Heat shown in Figure 13 moves what co-feeding system was realized in：
(1), in structure, heat shown in Fig. 5 is moved in co-feeding system, increase the 3rd generator, the 3rd solution heat exchanger and Second throttle, the second absorber 2 is had weak solution pipeline to connect with generator 3 through solution pump 8 and the second solution heat exchanger 11 Logical it is adjusted to the second absorber 2 and has weak solution pipeline through solution pump 8, the second solution heat exchanger 11 and the 3rd solution heat exchanger 22 are connected with generator 3, and generator 3 is had concentrated solution pipeline to connect tune through the second solution heat exchanger 11 with the second generator 4 Whole have concentrated solution pipeline to connect with the 3rd generator 19 through the 3rd solution heat exchanger 22 for generator 3, and the 3rd generator 19 is again Have concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 11, by generator 3 have refrigerant steam channel with cold Condenser 5 connection be adjusted to the 3rd generator 19 after generator 3 has refrigerant steam channel to connect with the 3rd generator 19 have again cold Agent liquid pipeline is connected with condenser 5 through second throttle 23, and the 3rd generator 19 also has refrigerant steam channel with condenser 5 even Logical, the 3rd generator 19 also has high temperature thermal medium passage and ft connection.
(2), in flow process, the refrigerant vapour of high temperature thermal medium and generator 3 generation is supplied to the 3rd generator 19 and makees to drive heat Medium, the weak solution of the second absorber 2 enters through solution pump 8, the second solution heat exchanger 11 and the 3rd solution heat exchanger 22 Generator 3, the concentrated solution of generator 3 enters the 3rd generator 19, refrigerant vapour and high warm through the 3rd solution heat exchanger 22 Medium flows separately through the 3rd generator 19, heating enters its interior solution release refrigerant vapour and provides to condenser 5, the 3rd The concentrated solution of raw device 19 enters the second generator 4 through the second solution heat exchanger 11；Flow through the refrigerant vapour of the 3rd generator 19 Heat release becomes cryogen liquid, and cryogen liquor stream, through entering condenser 5 after second throttle 22 reducing pressure by regulating flow, forms the dynamic co-feeding system of heat.
Heat shown in Figure 14 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 5 is moved in co-feeding system, increases the 3rd generator, the 3rd solution pump, the 3rd molten Liquid heat exchanger and second throttle, the second absorber 2 is had weak solution pipeline through solution pump 8 and the second solution heat exchanger 11 Connect with generator 3 and be adjusted to the second absorber 2 and have weak solution pipeline through solution pump 8 and the second solution heat exchanger 11 and the 3rd Generator 19 connects, and the 3rd generator 19 has concentrated solution pipeline through the 3rd solution pump 21 and the 3rd solution heat exchanger 22 and to send out again Raw device 3 connects, and generator 3 is had concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 11 and is adjusted to Raw device 3 has concentrated solution pipeline to connect with the second generator 4 with the second solution heat exchanger 11 through the 3rd solution heat exchanger 22, will Generator 3 has refrigerant steam channel to connect with condenser 5 to be adjusted to generator 3 and have refrigerant steam channel and the 3rd generator 19 even After logical, the 3rd generator 19 has cryogen liquid pipeline to connect with condenser 5 through second throttle 23 again, and the 3rd generator 19 also has Refrigerant steam channel is connected with condenser 5.
(2), in flow process, the refrigerant vapour that generator 3 produces is supplied to the 3rd generator 19 and makees to drive thermal medium, the second suction The weak solution receiving device 2 enters the 3rd generator 19 through solution pump 8 and the second solution heat exchanger 11, and refrigerant vapour flows through the 3rd Raw device 19, heating enter its interior solution release refrigerant vapour and simultaneously provide to condenser 5, and the concentrated solution of the 3rd generator 19 is through the Three solution pumps 21 and the 3rd solution heat exchanger 22 enter generator 3, and the concentrated solution of generator 3 is through the 3rd solution heat exchanger 22 Enter the second generator 4 with the second solution heat exchanger 11；The refrigerant vapour heat release flowing through the 3rd generator 19 becomes cryogen liquid, cold Agent liquor stream, through entering condenser 5 after second throttle 22 reducing pressure by regulating flow, forms the dynamic co-feeding system of heat.
Heat shown in Figure 15 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 5 is moved in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd molten Liquid pump and the 3rd solution heat exchanger, by generator 3 have refrigerant steam channel connect with condenser 5 be adjusted to generator 3 have cold Agent steam channel is connected with the 3rd absorber 20, and the 3rd absorber 20 also has weak solution pipeline molten through the 3rd solution pump 21 and the 3rd Liquid heat exchanger 22 is connected with the 3rd generator 19, and the 3rd generator 19 also has concentrated solution pipeline through the 3rd solution heat exchanger 22 Connect with the 3rd absorber 20, the 3rd generator 19 also has refrigerant steam channel to connect with condenser 5, and the 3rd generator 19 also has High temperature thermal medium passage and ft connection, the 3rd absorber 20 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 3 produces enters the 3rd absorber 20, the weak solution of the 3rd absorber 20 Enter the 3rd generator 19 through the 3rd solution pump 21 and the 3rd solution heat exchanger 22, high temperature thermal medium flows through the 3rd generator 19th, heating enters its interior solution release refrigerant vapour and provides to condenser 5, and the concentrated solution of the 3rd generator 19 is molten through the 3rd Liquid heat exchanger 22 enters the 3rd absorber 20, absorbs refrigerant vapour and heat release is in heated medium, forms the dynamic co-feeding system of heat.
Heat shown in Figure 16 moves what co-feeding system was realized in：
(1), in structure, the heat shown in Fig. 5 is moved in co-feeding system, increases preheater, the second absorber 2 is had weak solution Pipeline is connected with generator 3 through solution pump 8 and the second solution heat exchanger 11 and is adjusted to the second absorber 2 and has weak solution pipeline warp Solution pump 8, preheater 24 are connected with generator 3 with the second solution heat exchanger 11, and vaporizer 6 is had circulatory mediator pipeline through Two generators 4 connect with circulating pump 14 be adjusted to vaporizer 6 have circulatory mediator pipeline through the second generator 4 and preheater 24 with follow Ring pump 14 connects.
(2) in flow process, the weak solution of the second absorber 2 is boosted through solution pump 8, flows through preheater 24 and the second solution heat is handed over Parallel operation 11 simultaneously progressively absorbs heat, and enters generator 3 afterwards；The circulatory mediator of circulating pump 14 discharge flows through low-temperature condenser 13, heating Device 15 and secondary heater 16 simultaneously progressively absorb heat, and flow through vaporizer 6, the second generator 4 and preheater 24 progressively heat release, afterwards It is supplied to circulating pump 14, form the dynamic co-feeding system of heat.
Heat shown in Figure 16 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 5 is moved in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd molten Liquid pump and the 3rd solution heat exchanger, absorber 1 is had weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 10 Being adjusted to absorber 1 has weak solution pipeline to connect with the 3rd absorber 20 through the 3rd solution heat exchanger 22, the 3rd absorber 20 There is weak solution pipeline to connect with the second absorber 2 with solution heat exchanger 10 through the 3rd solution pump 21 again, the second generator 4 is had Concentrated solution pipeline is connected with absorber 1 through the second solution pump 9 and solution heat exchanger 10 and is adjusted to the second generator 4 and has concentrated solution Pipeline is connected with the 3rd generator 19 through solution heat exchanger 10, and the 3rd generator 19 has concentrated solution pipeline again through the second solution pump 9 are connected with absorber 1 with the 3rd solution heat exchanger 22, and vaporizer 6 is had circulatory mediator pipeline through the second generator 4 and circulation Pump 14 connection is adjusted to vaporizer 6 has circulatory mediator pipeline to connect with circulating pump 14 with the 3rd generator 19 through the second generator 4, 3rd generator 19 also has refrigerant steam channel to connect with the 3rd absorber 20, the 3rd absorber 20 also have coolant guiding channel and Ft connection.
(2), in flow process, the weak solution of absorber 1 is cold through the 3rd solution heat exchanger 22 entrance the 3rd absorber 20, absorption Agent steam heat release is in cooling medium, the weak solution of the 3rd absorber 20 enters through the 3rd solution pump 21 and solution heat exchanger 10 Second absorber 2；The concentrated solution of the second generator 4 enters the 3rd generator 19, heat absorption release cryogen through solution heat exchanger 10 Steam simultaneously provides to the 3rd absorber 20, and the concentrated solution of the 3rd generator 19 is through the second solution pump 9 and the 3rd solution heat exchanger 22 entrance absorbers 1；The circulatory mediator of circulating pump 14 discharge flows through low-temperature condenser 13, heater 15 and secondary heater 16 simultaneously Progressively absorb heat, flow through vaporizer 6, the second generator 4 and the 3rd generator 19 progressively heat release afterwards, form the dynamic alliance system of heat System.
Heat shown in Figure 17 moves what co-feeding system was realized in：
Heat shown in Fig. 5 is moved in co-feeding system, increases preheater, the second absorber 2 is had weak solution pipeline through solution Pump 8 is connected with generator 3 with the second solution heat exchanger 11 and is adjusted to the second absorber 2 and has weak solution pipeline through solution pump 8, pre- Hot device 24 is connected with generator 3 with the second solution heat exchanger 11, and vaporizer 6 is had circulatory mediator pipeline through the second generator 4 Connect with circulating pump 14 and be adjusted to vaporizer 6 and have circulatory mediator pipeline through the second generator 4 and preheater 24 with circulating pump 14 even Logical；The weak solution of the second absorber 2 flows through solution pump 8, preheater 24 and the second solution heat exchanger 11 and enters generator 3；Follow The circulatory mediator of ring pump 14 discharge flows through low-temperature condenser 13, heater 15 and secondary heater 16 and progressively absorbs heat, and flows through steaming Send out device 6, the second generator 4 and preheater 24 progressively heat release, return to circulating pump 14 afterwards, form the dynamic co-feeding system of heat.
Effect that the technology of the present invention can be realized heat proposed by the invention moves co-feeding system, have the effect that and Advantage：
(1) high-grade steam elder generation work done, low-grade steam is used for heat supply, meets heat energy efficient utilization principle.
(2) by low-temperature condenser, heater, secondary heater and the 3rd heater, carry out heat alone or in combination and step by step Load gathers, and in conjunction with the second generator and the second absorber, realizes Steam Power Equipment end steam discharge or low-pressure pumping steam and cold ring The effectively utilizes of the temperature difference between border.
(3) realize the big temperature difference and the conveying of low-pressure thermic load in first-level pipeline network, and reduce conveying thermic load scale, significantly Degree improves one-level heating network safety, and one-level heating network parameter can be adjusted flexibly as the case may be.
(4) release cleaning or high efficient energy sources and move the application restriction in co-feeding system in conventional thermal.
(5) realize effective profit of the temperature difference between first-level pipeline network circulatory mediator and secondary network circulatory mediator or heated medium With.
(6) with engine end steam for the dynamic alliance thermal source of heat, be conducive to improving the thermal efficiency of engine and equipment runs Safety.
(7) enrich the type of thermal and power system, extend the range of application of absorption heat pump, be conducive to preferably using suction Receipts formula heat pump techniques are improving heat utilization rate.

Claims (61)

1. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, section Stream valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser and circulation Pump is formed；Absorber (1) has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (10), the second absorption Device (2) also has weak solution pipeline to connect with generator (3) with the second solution heat exchanger (11) through solution pump (8), generator (3) Concentrated solution pipeline is also had to connect with the second generator (4) through the second solution heat exchanger (11), the second generator (4) also has dense molten Liquid pipeline is connected with absorber (1) with solution heat exchanger (10) through the second solution pump (9), and generator (3) also has refrigerant vapour Passage is connected with condenser (5), and the second generator (4) also has refrigerant steam channel to connect with the second absorber (2), condenser (5) cryogen liquid pipeline is also had to connect with vaporizer (6) through choke valve (7), vaporizer (6) also has refrigerant steam channel and absorber (1) connect, engine (12) has live steam passage and ft connection, engine (12) also has exhaust passage and low-temperature condenser (13) After connection, low-temperature condenser (13) has low temperature cold lime set passage and ft connection again, engine (12) or also exhaust passage with Ft connection, circulating pump (14) has the finisher (6) that circulatory mediator pipeline is connected with vaporizer (6) through low-temperature condenser (13) Circulatory mediator pipeline is had itself to connect with circulating pump (14) through the second generator (4) again, absorber (1) and condenser (5) also divide There are not heated medium passage and ft connection, the second absorber (2) also has coolant guiding channel and ft connection, generator (3) also have high temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in claim 1, circulating pump (14) is had circulatory mediator pipeline Through the finisher (6) that low-temperature condenser (13) is connected with vaporizer (6) have again circulatory mediator pipeline through the second generator (4) with Circulating pump (14) itself connects, and being adjusted to circulating pump (14) has circulatory mediator pipeline through low-temperature condenser (13) and the second generator (4) after connecting, the second generator (4) has circulatory mediator pipeline itself to connect with circulating pump (14) through vaporizer (6) again, is formed The dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in claim 1, circulating pump (14) is had circulatory mediator pipeline Through the finisher (6) that low-temperature condenser (13) is connected with vaporizer (6) have again circulatory mediator pipeline through the second generator (4) with Circulating pump (14) itself connect, be adjusted to circulating pump (14) have circulatory mediator pipeline through low-temperature condenser (13) respectively with vaporizer (6) finisher (6) that with the second generator (4) connects and the second generator (4) have circulatory mediator pipeline and circulation more respectively Pump (14) itself connects, and forms the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, section Stream valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump and heater institute Composition；Absorber (1) has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (10), the second absorber (2) Weak solution pipeline is also had to connect with generator (3) with the second solution heat exchanger (11) through solution pump (8), generator (3) also has Concentrated solution pipeline is connected with the second generator (4) through the second solution heat exchanger (11), and the second generator (4) also has concentrated solution pipe Road the second solution pump (9) is connected with absorber (1) with solution heat exchanger (10), and generator (3) also has refrigerant steam channel Connect with condenser (5), the second generator (4) also has refrigerant steam channel to connect with the second absorber (2), condenser (5) is also Cryogen liquid pipeline is had to connect with vaporizer (6) through choke valve (7), vaporizer (6) also has refrigerant steam channel with absorber (1) even Logical, engine (12) has live steam passage and ft connection respectively and has exhaust passage and ft connection, engine (12) also the The post-heater (15) that one steam channel is connected with heater (15) has the first condensed fluid passage and ft connection, circulating pump again (14) finisher (6) that the heated device of circulatory mediator pipeline (15) is connected with vaporizer (6) is had to have circulatory mediator pipeline warp again Second generator (4) itself is connected with circulating pump (14), and absorber (1) and condenser (5) also have heated medium passage respectively With ft connection, the second absorber (2) also coolant guiding channel and ft connection, generator (3) also has high temperature thermal medium to lead to Road and ft connection, form the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in claim 4, circulating pump (14) is had circulatory mediator pipeline The finisher (6) that heated device (15) is connected with vaporizer (6) has circulatory mediator pipeline again through the second generator (4) and circulation Pump (14) itself connects, and being adjusted to circulating pump (14) has the heated device of circulatory mediator pipeline (15) to connect with the second generator (4) Second generator (4) has circulatory mediator pipeline itself to connect with circulating pump (14) through vaporizer (6) more afterwards, forms the dynamic alliance of heat System.
6. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in claim 4, circulating pump (14) is had circulatory mediator pipeline The finisher (6) that heated device (15) is connected with vaporizer (6) has circulatory mediator pipeline again through the second generator (4) and circulation Pump (14) itself connects, be adjusted to circulating pump (14) have the heated device of circulatory mediator pipeline (15) respectively with vaporizer (6) and the The finisher (6) of two generators (4) connection and the second generator (4) have circulatory mediator pipeline with circulating pump (14) certainly more respectively Body connects, and forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, section Stream valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, circulating pump Formed with heater；Absorber (1) has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (10), the Two absorbers (2) also have weak solution pipeline to connect with generator (3) with the second solution heat exchanger (11) through solution pump (8), send out Raw device (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11), the second generator (4) Concentrated solution pipeline is also had to connect with absorber (1) with solution heat exchanger (10) through the second solution pump (9), generator (3) also has Refrigerant steam channel is connected with condenser (5), and the second generator (4) also has refrigerant steam channel to connect with the second absorber (2), Condenser (5) also has cryogen liquid pipeline connect with vaporizer (6) through choke valve (7), vaporizer (6) also refrigerant steam channel and Absorber (1) connects, and engine (12) has live steam passage and ft connection, and engine (12) also has exhaust passage and condensation at low temperature After device (13) connection, low-temperature condenser (13) has low temperature cold lime set passage and ft connection again, and engine (12) also has the first steaming The post-heater (15) that vapour passage is connected with heater (15) has the first condensed fluid passage and ft connection again, engine (12) or Also have exhaust passage and ft connection, circulating pump (14) have circulatory mediator pipeline through low-temperature condenser (13) and heater (15) and The finisher (6) of vaporizer (6) connection has circulatory mediator pipeline through the second generator (4) with circulating pump (14) itself even again Lead to, absorber (1) and condenser (5) also have heated medium passage and ft connection respectively, the second absorber (2) also has cooling Medium channel and ft connection, generator (3) also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in claim 7, circulating pump (14) is had circulatory mediator pipeline There is circulatory mediator pipeline through the finisher (6) that low-temperature condenser (13) is connected with vaporizer (6) with heater (15) again through Two generators (4) itself are connected with circulating pump (14), and being adjusted to circulating pump (14) has circulatory mediator pipeline through low-temperature condenser (13) after connecting with the second generator (4) with heater (15), the second generator (4) has circulatory mediator pipeline again through vaporizer (6) itself connect with circulating pump (14), form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in claim 7, circulating pump (14) is had circulatory mediator pipeline There is circulatory mediator pipeline through the finisher (6) that low-temperature condenser (13) is connected with vaporizer (6) with heater (15) again through Two generators (4) itself are connected with circulating pump (14), and being adjusted to circulating pump (14) has circulatory mediator pipeline through low-temperature condenser (13) finisher (6) connecting with vaporizer (6) and the second generator (4) respectively with heater (15) and the second generator (4) there is circulatory mediator pipeline itself to connect with circulating pump (14) more respectively, form the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heater and Secondary heater is formed；Absorber (1) has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (10), Second absorber (2) also has weak solution pipeline to connect with generator (3) with the second solution heat exchanger (11) through solution pump (8), Generator (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11), the second generator (4) concentrated solution pipeline is also had to connect with absorber (1) with solution heat exchanger (10) through the second solution pump (9), generator (3) is also Refrigerant steam channel is had to connect with condenser (5), the second generator (4) also has refrigerant steam channel with the second absorber (2) even Logical, condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7), and vaporizer (6) also has refrigerant vapour to lead to Road is connected with absorber (1), and engine (12) has live steam passage and ft connection respectively and has exhaust passage and ft connection, moves Power machine (12) also has the post-heater (15) that the first steam channel is connected with heater (15) to have the first condensed fluid passage again with outward Portion connects, and after engine (12) also has the second steam channel to connect with secondary heater (16), secondary heater (16) has the again Two condensed fluid passages and ft connection, circulating pump (14) have the heated device of circulatory mediator pipeline (15) and secondary heater (16) with The finisher (6) of vaporizer (6) connection has circulatory mediator pipeline through the second generator (4) with circulating pump (14) itself even again Lead to, absorber (1) and condenser (5) also have heated medium passage and ft connection respectively, the second absorber (2) also has cooling Medium channel and ft connection, generator (3) also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, is in the dynamic co-feeding system of heat described in claim 10, circulating pump (14) is had circulatory mediator pipe The finisher (6) that the heated device in road (15) is connected with vaporizer (6) with secondary heater (16) has circulatory mediator pipeline warp again Second generator (4) itself is connected with circulating pump (14), and being adjusted to circulating pump (14) has the heated device of circulatory mediator pipeline (15) After connecting with the second generator (4) with secondary heater (16), the second generator (4) has circulatory mediator pipeline again through vaporizer (6) itself connect with circulating pump (14), form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 12. heat, is in the dynamic co-feeding system of heat described in claim 10, circulating pump (14) is had circulatory mediator pipe The finisher (6) that the heated device in road (15) is connected with vaporizer (6) with secondary heater (16) has circulatory mediator pipeline warp again Second generator (4) itself is connected with circulating pump (14), and being adjusted to circulating pump (14) has the heated device of circulatory mediator pipeline (15) The finisher (6) connecting with vaporizer (6) and the second generator (4) respectively with secondary heater (16) and the second generator (4) there is circulatory mediator pipeline itself to connect with circulating pump (14) more respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 13. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, circulation Pump, heater and secondary heater are formed；Absorber (1) has weak solution pipeline through solution heat exchanger (10) and the second absorption Device (2) connects, and the second absorber (2) also has weak solution pipeline through solution pump (8) and the second solution heat exchanger (11) and generation Device (3) connects, and generator (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11), the Two generators (4) also have concentrated solution pipeline to connect with absorber (1) with solution heat exchanger (10) through the second solution pump (9), send out Raw device (3) also has refrigerant steam channel to connect with condenser (5), and the second generator (4) also has refrigerant steam channel and the second suction Receive device (2) connection, condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7), and vaporizer (6) is also cold Agent steam channel is connected with absorber (1), and engine (12) has live steam passage and ft connection, and engine (12) also has steam discharge to lead to After road is connected with low-temperature condenser (13), low-temperature condenser (13) has low temperature cold lime set passage and ft connection, engine again (12) post-heater (15) that the first steam channel is connected with heater (15) is also had to have the first condensed fluid passage to connect with outside again Logical, engine (12) also have the second steam channel to connect with secondary heater (16) after secondary heater (16) have again second cold Lime set passage and ft connection, engine (12) or also exhaust passage and ft connection, circulating pump (14) has circulatory mediator pipe Road has through the finisher (6) that low-temperature condenser (13), heater (15) are connected with vaporizer (6) with secondary heater (16) again Circulatory mediator pipeline itself is connected with circulating pump (14) through the second generator (4), and absorber (1) and condenser (5) also have respectively Heated medium passage and ft connection, the second absorber (2) also has coolant guiding channel and ft connection, and generator (3) is also There are high temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 14. heat, is in the dynamic co-feeding system of heat described in claim 13, circulating pump (14) is had circulatory mediator pipe Road has through the finisher (6) that low-temperature condenser (13), heater (15) are connected with vaporizer (6) with secondary heater (16) again Circulatory mediator pipeline itself is connected with circulating pump (14) through the second generator (4), and being adjusted to circulating pump (14) has circulatory mediator pipe After road is connected with the second generator (4) with secondary heater (16) through low-temperature condenser (13), heater (15), second occurs Device (4) has circulatory mediator pipeline itself to connect with circulating pump (14) through vaporizer (6) again, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, is in the dynamic co-feeding system of heat described in claim 13, circulating pump (14) is had circulatory mediator pipe Road has through the finisher (6) that low-temperature condenser (13), heater (15) are connected with vaporizer (6) with secondary heater (16) again Circulatory mediator pipeline itself is connected with circulating pump (14) through the second generator (4), and being adjusted to circulating pump (14) has circulatory mediator pipe Road is connected with vaporizer (6) and the second generator (4) respectively through low-temperature condenser (13), heater (15) and secondary heater (16) Logical finisher (6) has circulatory mediator pipeline itself to connect with circulating pump (14) with the second generator (4) more respectively, forms heat Dynamic co-feeding system.
The dynamic co-feeding systems of 16. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heater, Secondary heater and the 3rd heater are formed；Absorber (1) has weak solution pipeline through solution heat exchanger (10) and the second suction Receive device (2) connection, the second absorber (2) also has weak solution pipeline through solution pump (8) and the second solution heat exchanger (11) and to send out Raw device (3) connection, generator (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11), Second generator (4) also has concentrated solution pipeline to connect with absorber (1) with solution heat exchanger (10) through the second solution pump (9), Generator (3) also has refrigerant steam channel to connect with condenser (5), and the second generator (4) also has refrigerant steam channel and second Absorber (2) connects, and condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7), and vaporizer (6) also has Refrigerant steam channel is connected with absorber (1), engine (12) have respectively live steam passage and ft connection and have exhaust passage and Ft connection, engine (12) also has the post-heater (15) that the first steam channel is connected with heater (15) to have the first condensation again Liquid passage and ft connection, engine (12) also have the second steam channel connect with secondary heater (16) after secondary heater (16) there are the second condensed fluid passage and ft connection again, engine (12) also has the 3rd steam channel and the 3rd heater (17) even After logical, the 3rd heater (17) has the 3rd condensed fluid passage and ft connection again, and circulating pump (14) has circulatory mediator pipeline through adding The finisher (6) that hot device (15), secondary heater (16) are connected with vaporizer (6) with the 3rd heater (17) has circulation to be situated between again Matter pipeline itself is connected with circulating pump (14) through the second generator (4), and absorber (1) and condenser (5) also have heated respectively Medium channel and ft connection, the second absorber (2) also has coolant guiding channel and ft connection, and generator (3) also has high temperature Hot media channel and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, is in the dynamic co-feeding system of heat described in claim 16, circulating pump (14) is had circulatory mediator pipe The finisher (6) that the heated device in road (15), secondary heater (16) are connected with vaporizer (6) with the 3rd heater (17) has again Circulatory mediator pipeline itself is connected with circulating pump (14) through the second generator (4), and being adjusted to circulating pump (14) has circulatory mediator pipe After the heated device in road (15), secondary heater (16) are connected with the second generator (4) with the 3rd heater (17), second occurs Device (4) has circulatory mediator pipeline itself to connect with circulating pump (14) through vaporizer (6) again, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 18. heat, is in the dynamic co-feeding system of heat described in claim 16, circulating pump (14) is had circulatory mediator pipe The finisher (6) that the heated device in road (15), secondary heater (16) are connected with vaporizer (6) with the 3rd heater (17) has again Circulatory mediator pipeline itself is connected with circulating pump (14) through the second generator (4), and being adjusted to circulating pump (14) has circulatory mediator pipe The heated device in road (15), secondary heater (16) and the 3rd heater (17) are connected with vaporizer (6) and the second generator (4) respectively Logical finisher (6) has circulatory mediator pipeline itself to connect with circulating pump (14) with the second generator (4) more respectively, forms heat Dynamic co-feeding system.
The dynamic co-feeding systems of 19. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, circulation Pump, heater, secondary heater and the 3rd heater are formed；Absorber (1) has weak solution pipeline through solution heat exchanger (10) connect with the second absorber (2), the second absorber (2) also has weak solution pipeline to hand over through solution pump (8) and the second solution heat Parallel operation (11) is connected with generator (3), and generator (3) also has concentrated solution pipeline through the second solution heat exchanger (11) and second Raw device (4) connection, the second generator (4) also has concentrated solution pipeline through the second solution pump (9) and solution heat exchanger (10) and suction Receive device (1) connection, generator (3) also has refrigerant steam channel to connect with condenser (5), the second generator (4) also has cryogen to steam Vapour passage is connected with the second absorber (2), and condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7), Vaporizer (6) also has refrigerant steam channel to connect with absorber (1), and engine (12) has live steam passage and ft connection, power Machine (12) also have exhaust passage connect with low-temperature condenser (13) after low-temperature condenser (13) have again low temperature cold lime set passage and Ft connection, engine (12) also has the post-heater (15) that the first steam channel is connected with heater (15) to have the first condensation again Liquid passage and ft connection, engine (12) also have the second steam channel connect with secondary heater (16) after secondary heater (16) there are the second condensed fluid passage and ft connection again, engine (12) also has the 3rd steam channel and the 3rd heater (17) even After logical, the 3rd heater (17) has the 3rd condensed fluid passage and ft connection again, and engine (12) or also exhaust passage are with outward Portion connects, and circulating pump (14) has circulatory mediator pipeline through low-temperature condenser (13), heater (15), secondary heater (16) and the The finisher (6) that three heaters (17) are connected with vaporizer (6) has circulatory mediator pipeline again through the second generator (4) and circulation Pump (14) itself connects, and absorber (1) and condenser (5) also have heated medium passage and ft connection, the second absorption respectively Device (2) also has coolant guiding channel and ft connection, and generator (3) also has high temperature thermal medium passage and ft connection, forms heat Dynamic co-feeding system.
The dynamic co-feeding system of 20. heat, is in the dynamic co-feeding system of heat described in claim 19, circulating pump (14) is had circulatory mediator pipe Road connects it with the 3rd heater (17) with vaporizer (6) through low-temperature condenser (13), heater (15), secondary heater (16) Finisher (6) has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, is adjusted to circulating pump (14) there is circulatory mediator pipeline through low-temperature condenser (13), heater (15), secondary heater (16) and the 3rd heater (17) After connecting with the second generator (4), the second generator (4) has circulatory mediator pipeline through vaporizer (6) with circulating pump (14) certainly again Body connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, is in the dynamic co-feeding system of heat described in claim 19, circulating pump (14) is had circulatory mediator pipe Road connects it with the 3rd heater (17) with vaporizer (6) through low-temperature condenser (13), heater (15), secondary heater (16) Finisher (6) has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, is adjusted to circulating pump (14) there is circulatory mediator pipeline through low-temperature condenser (13), heater (15), secondary heater (16) and the 3rd heater (17) The finisher (6) connecting with vaporizer (6) and the second generator (4) respectively and the second generator (4) have circulation to be situated between again respectively Matter pipeline itself is connected with circulating pump (14), forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 22. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, circulation Pump and heater are formed；Absorber (1) has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (10), Second absorber (2) also has weak solution pipeline to connect with generator (3) with the second solution heat exchanger (11) through solution pump (8), Generator (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11), the second generator (4) concentrated solution pipeline is also had to connect with absorber (1) with solution heat exchanger (10) through the second solution pump (9), generator (3) is also Refrigerant steam channel is had to connect with condenser (5), the second generator (4) also has refrigerant steam channel with the second absorber (2) even Logical, condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7), and vaporizer (6) also has refrigerant vapour to lead to Road is connected with absorber (1), and engine (12) has live steam passage and ft connection, and engine (12) also has exhaust passage and low temperature After condenser (13) connection, low-temperature condenser (13) has low temperature cold lime set passage and ft connection again, engine (12) or also have Exhaust passage and ft connection, circulating pump (14) has circulatory mediator pipeline through low-temperature condenser (13) and heater (18) and evaporation The finisher (6) of device (6) connection has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, inhales Receive device (1) and condenser (5) also has heated medium passage and ft connection respectively, the second absorber (2) also has cooling medium Passage and ft connection, generator (3) also has high temperature thermal medium passage and ft connection, and heater (18) also has heated medium Passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 23. heat, is in the dynamic co-feeding system of heat described in claim 22, circulating pump (14) is had circulatory mediator pipe There is circulatory mediator pipeline warp on road again through the finisher (6) that low-temperature condenser (13) is connected with vaporizer (6) with heater (18) Second generator (4) itself is connected with circulating pump (14), and being adjusted to circulating pump (14) has circulatory mediator pipeline through low-temperature condenser (13) after connecting with the second generator (4) with heater (18), the second generator (4) has circulatory mediator pipeline again through vaporizer (6) itself connect with circulating pump (14), form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 24. heat, is in the dynamic co-feeding system of heat described in claim 22, circulating pump (14) is had circulatory mediator pipe There is circulatory mediator pipeline warp on road again through the finisher (6) that low-temperature condenser (13) is connected with vaporizer (6) with heater (18) Second generator (4) itself is connected with circulating pump (14), and being adjusted to circulating pump (14) has circulatory mediator pipeline through low-temperature condenser (13) finisher (6) connecting with vaporizer (6) and the second generator (4) respectively with heater (18) and the second generator (4) there is circulatory mediator pipeline itself to connect with circulating pump (14) more respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 25. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heater and Heater is formed；Absorber (1) has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (10), and second Absorber (2) also has weak solution pipeline to connect with generator (3) with the second solution heat exchanger (11) through solution pump (8), occurs Device (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11), and the second generator (4) is also Concentrated solution pipeline is had to connect with absorber (1) with solution heat exchanger (10) through the second solution pump (9), generator (3) is also cold Agent steam channel is connected with condenser (5), and the second generator (4) also has refrigerant steam channel to connect with the second absorber (2), cold Condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7), and vaporizer (6) also has refrigerant steam channel and suction Receive device (1) connection, engine (12) has live steam passage and ft connection respectively and has exhaust passage and ft connection, engine (12) post-heater (15) that the first steam channel is connected with heater (15) is also had to have the first condensed fluid passage to connect with outside again Logical, circulating pump (14) has the finisher that the heated device of circulatory mediator pipeline (15) is connected with vaporizer (6) with heater (18) (6) circulatory mediator pipeline is had itself to connect with circulating pump (14) through the second generator (4) again, absorber (1) and condenser (5) are also There are heated medium passage and ft connection respectively, the second absorber (2) also has coolant guiding channel and ft connection, generator (3) also have high temperature thermal medium passage and ft connection, heater (18) also has heated medium passage and ft connection, forms heat Dynamic co-feeding system.
The dynamic co-feeding system of 26. heat, is in the dynamic co-feeding system of heat described in claim 25, circulating pump (14) is had circulatory mediator pipe The finisher (6) that the heated device in road (15) is connected with vaporizer (6) with heater (18) has circulatory mediator pipeline again through second Generator (4) itself is connected with circulating pump (14), and being adjusted to circulating pump (14) has the heated device of circulatory mediator pipeline (15) and supply After hot device (18) is connected with the second generator (4), the second generator (4) has circulatory mediator pipeline again through vaporizer (6) and circulation Pump (14) itself connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 27. heat, is in the dynamic co-feeding system of heat described in claim 25, circulating pump (14) is had circulatory mediator pipe The finisher (6) that the heated device in road (15) is connected with vaporizer (6) with heater (18) has circulatory mediator pipeline again through second Generator (4) itself is connected with circulating pump (14), and being adjusted to circulating pump (14) has the heated device of circulatory mediator pipeline (15) and supply With vaporizer (6) and second generator (4) distinguish again respectively by the finisher (6) connecting and the second generator (4) for hot device (18) There is circulatory mediator pipeline itself to connect with circulating pump (14), form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 28. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, circulation Pump, heater and heater are formed；Absorber (1) has weak solution pipeline through solution heat exchanger (10) and the second absorber (2) connect, the second absorber (2) also has weak solution pipeline through solution pump (8) and the second solution heat exchanger (11) and generator (3) connect, generator (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11), second Generator (4) also has concentrated solution pipeline to connect with absorber (1) with solution heat exchanger (10) through the second solution pump (9), occurs Device (3) also has refrigerant steam channel to connect with condenser (5), and the second generator (4) also has refrigerant steam channel and the second absorption Device (2) connects, and condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7), and vaporizer (6) also has cryogen Steam channel is connected with absorber (1), and engine (12) has live steam passage and ft connection, and engine (12) also has exhaust passage After connecting with low-temperature condenser (13), low-temperature condenser (13) has low temperature cold lime set passage and ft connection, engine (12) again Also have the post-heater (15) that the first steam channel is connected with heater (15) to have the first condensed fluid passage and ft connection again, move Power machine (12) or also exhaust passage and ft connection, circulating pump (14) has circulatory mediator pipeline through low-temperature condenser (13), adds The finisher (6) that hot device (15) is connected with vaporizer (6) with heater (18) has circulatory mediator pipeline again through the second generator (4) itself connect with circulating pump (14), absorber (1) and condenser (5) also have heated medium passage and ft connection respectively, Second absorber (2) also has coolant guiding channel and ft connection, and generator (3) also has high temperature thermal medium passage to connect with outside Logical, heater (18) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 29. heat, is in the dynamic co-feeding system of heat described in claim 28, circulating pump (14) is had circulatory mediator pipe There is circulation on road again through the finisher (6) that low-temperature condenser (13), heater (15) are connected with vaporizer (6) with heater (18) Medium pipeline itself is connected with circulating pump (14) through the second generator (4), and being adjusted to circulating pump (14) has circulatory mediator pipeline warp After low-temperature condenser (13), heater (15) are connected with the second generator (4) with heater (18), the second generator (4) has again Circulatory mediator pipeline itself is connected with circulating pump (14) through vaporizer (6), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 30. heat, is in the dynamic co-feeding system of heat described in claim 28, circulating pump (14) is had circulatory mediator pipe There is circulation on road again through the finisher (6) that low-temperature condenser (13), heater (15) are connected with vaporizer (6) with heater (18) Medium pipeline itself is connected with circulating pump (14) through the second generator (4), and being adjusted to circulating pump (14) has circulatory mediator pipeline warp Low-temperature condenser (13), heater (15) are steamed after being connected with vaporizer (6) and the second generator (4) respectively with heater (18) Sending out device (6) has circulatory mediator pipeline itself to connect with circulating pump (14) with the second generator (4) more respectively, forms the dynamic alliance system of heat System.
The dynamic co-feeding systems of 31. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heater, Secondary heater and heater are formed；Absorber (1) has weak solution pipeline through solution heat exchanger (10) and the second absorber (2) connect, the second absorber (2) also has weak solution pipeline through solution pump (8) and the second solution heat exchanger (11) and generator (3) connect, generator (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11), second Generator (4) also has concentrated solution pipeline to connect with absorber (1) with solution heat exchanger (10) through the second solution pump (9), occurs Device (3) also has refrigerant steam channel to connect with condenser (5), and the second generator (4) also has refrigerant steam channel and the second absorption Device (2) connects, and condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7), and vaporizer (6) also has cryogen Steam channel is connected with absorber (1), and engine (12) has live steam passage and ft connection respectively and has exhaust passage and outside Connection, engine (12) also has the post-heater (15) that the first steam channel is connected with heater (15) to have the first condensed fluid to lead to again Road and ft connection, engine (12) also have the second steam channel connect with secondary heater (16) after secondary heater (16) There are the second condensed fluid passage and ft connection again, circulating pump (14) has the heated device of circulatory mediator pipeline (15), secondary heater (16) finisher (6) connecting with vaporizer (6) with heater (18) have again circulatory mediator pipeline through the second generator (4) with Circulating pump (14) itself connects, and absorber (1) and condenser (5) also have heated medium passage and ft connection respectively, and second Absorber (2) also has coolant guiding channel and ft connection, and generator (3) also has high temperature thermal medium passage and ft connection, supplies Hot device (18) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, is in the dynamic co-feeding system of heat described in claim 31, circulating pump (14) is had circulatory mediator pipe The finisher (6) that the heated device in road (15), secondary heater (16) are connected with vaporizer (6) with heater (18) has circulation again Medium pipeline itself is connected with circulating pump (14) through the second generator (4), and being adjusted to circulating pump (14) has circulatory mediator pipeline warp After heater (15), secondary heater (16) are connected with the second generator (4) with heater (18), the second generator (4) has again Circulatory mediator pipeline itself is connected with circulating pump (14) through vaporizer (6), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 33. heat, is in the dynamic co-feeding system of heat described in claim 31, circulating pump (14) is had circulatory mediator pipe The finisher (6) that the heated device in road (15), secondary heater (16) are connected with vaporizer (6) with heater (18) has circulation again Medium pipeline itself is connected with circulating pump (14) through the second generator (4), and being adjusted to circulating pump (14) has circulatory mediator pipeline warp Heater (15), secondary heater (16) are steamed after being connected with vaporizer (6) and the second generator (4) respectively with heater (18) Sending out device (6) has circulatory mediator pipeline itself to connect with circulating pump (14) with the second generator (4) more respectively, forms the dynamic alliance system of heat System.
The dynamic co-feeding systems of 34. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, circulation Pump, heater, secondary heater and heater are formed；Absorber (1) have weak solution pipeline through solution heat exchanger (10) with Second absorber (2) connects, and the second absorber (2) also has weak solution pipeline through solution pump (8) and the second solution heat exchanger (11) connect with generator (3), generator (3) also has concentrated solution pipeline through the second solution heat exchanger (11) and the second generator (4) connect, the second generator (4) also has concentrated solution pipeline through the second solution pump (9) and solution heat exchanger (10) and absorber (1) connect, generator (3) also has refrigerant steam channel to connect with condenser (5), the second generator (4) also has refrigerant vapour to lead to Road is connected with the second absorber (2), and condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7), evaporation Device (6) also has refrigerant steam channel to connect with absorber (1), and engine (12) has live steam passage and ft connection, engine (12) after also having exhaust passage to connect with low-temperature condenser (13), low-temperature condenser (13) has low temperature cold lime set passage again with outward Portion connects, and engine (12) also has the post-heater (15) that the first steam channel is connected with heater (15) to have the first condensed fluid again Passage and ft connection, engine (12) also have the second steam channel connect with secondary heater (16) after secondary heater (16) there are the second condensed fluid passage and ft connection, engine (12) or also exhaust passage and ft connection, circulating pump again (14) there is circulatory mediator pipeline through low-temperature condenser (13), heater (15), secondary heater (16) and heater (18) and steaming The finisher (6) sending out device (6) connection has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, Absorber (1) and condenser (5) also have heated medium passage and ft connection respectively, and the second absorber (2) also has cooling to be situated between Matter passage and ft connection, generator (3) also has high temperature thermal medium passage and ft connection, and heater (18) also has heated Jie Matter passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 35. heat, is in the dynamic co-feeding system of heat described in claim 34, circulating pump (14) is had circulatory mediator pipe Road is steamed after being connected with vaporizer (6) with heater (18) through low-temperature condenser (13), heater (15), secondary heater (16) Sending out device (6) has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, and being adjusted to circulating pump (14) has Circulatory mediator pipeline is through low-temperature condenser (13), heater (15), secondary heater (16) and heater (18) and the second generation After device (4) connection, the second generator (4) has circulatory mediator pipeline itself to connect with circulating pump (14) through vaporizer (6) again, shape Become the dynamic co-feeding system of heat.
The dynamic co-feeding system of 36. heat, is in the dynamic co-feeding system of heat described in claim 34, circulating pump (14) is had circulatory mediator pipe Road is steamed after being connected with vaporizer (6) with heater (18) through low-temperature condenser (13), heater (15), secondary heater (16) Sending out device (6) has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, and being adjusted to circulating pump (14) has Circulatory mediator pipeline through low-temperature condenser (13), heater (15), secondary heater (16) and heater (18) respectively with evaporation The finisher (6) that device (6) connects with the second generator (4) and the second generator (4) have circulatory mediator pipeline respectively and follow again Ring pump (14) itself connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 37. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, circulating pump, heater, Secondary heater, the 3rd heater and heater are formed；Absorber (1) have weak solution pipeline through solution heat exchanger (10) with Second absorber (2) connects, and the second absorber (2) also has weak solution pipeline through solution pump (8) and the second solution heat exchanger (11) connect with generator (3), generator (3) also has concentrated solution pipeline through the second solution heat exchanger (11) and the second generator (4) connect, the second generator (4) also has concentrated solution pipeline through the second solution pump (9) and solution heat exchanger (10) and absorber (1) connect, generator (3) also has refrigerant steam channel to connect with condenser (5), the second generator (4) also has refrigerant vapour to lead to Road is connected with the second absorber (2), and condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7), evaporation Device (6) also has refrigerant steam channel to connect with absorber (1), and engine (12) has live steam passage and ft connection respectively and has row Vapour passage and ft connection, engine (12) also has the post-heater (15) that the first steam channel is connected with heater (15) to have again First condensed fluid passage and ft connection, engine (12) also have the second steam channel to connect with secondary heater (16) after the Two heaters (16) have the second condensed fluid passage and ft connection again, and engine (12) also has the 3rd steam channel and the 3rd heating After device (17) connection, the 3rd heater (17) has the 3rd condensed fluid passage and ft connection again, and circulating pump (14) has circulatory mediator After the heated device of pipeline (15), secondary heater (16), the 3rd heater (17) are connected with vaporizer (6) with heater (18) Vaporizer (6) has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, absorber (1) and condensation Device (5) also has heated medium passage and ft connection respectively, and the second absorber (2) also has coolant guiding channel to connect with outside Logical, generator (3) also has high temperature thermal medium passage and ft connection, and heater (18) also has heated medium passage to connect with outside Logical, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 38. heat, is in the dynamic co-feeding system of heat described in claim 37, circulating pump (14) is had circulatory mediator pipe The heated device in road (15), secondary heater (16), the 3rd heater (17) are steamed after being connected with vaporizer (6) with heater (18) Sending out device (6) has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, and being adjusted to circulating pump (14) has The heated device of circulatory mediator pipeline (15), secondary heater (16), the 3rd heater (17) and heater (18) and the second generation After device (4) connection, the second generator (4) has circulatory mediator pipeline itself to connect with circulating pump (14) through vaporizer (6) again, shape Become the dynamic co-feeding system of heat.
The dynamic co-feeding system of 39. heat, is in the dynamic co-feeding system of heat described in claim 37, circulating pump (14) is had circulatory mediator pipe The heated device in road (15), secondary heater (16), the 3rd heater (17) are steamed after being connected with vaporizer (6) with heater (18) Sending out device (6) has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, and being adjusted to circulating pump (14) has The heated device of circulatory mediator pipeline (15), secondary heater (16), the 3rd heater (17) and heater (18) respectively with evaporation The finisher (6) that device (6) connects with the second generator (4) and the second generator (4) have circulatory mediator pipeline respectively and follow again Ring pump (14) itself connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 40. heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, engine, low-temperature condenser, circulation Pump, heater, secondary heater, the 3rd heater and heater are formed；Absorber (1) has weak solution pipeline to hand over through solution heat Parallel operation (10) is connected with the second absorber (2), and the second absorber (2) also has weak solution pipeline through solution pump (8) and the second solution Heat exchanger (11) is connected with generator (3), and generator (3) also has concentrated solution pipeline through the second solution heat exchanger (11) and the Two generators (4) connect, and the second generator (4) also has concentrated solution pipeline through the second solution pump (9) and solution heat exchanger (10) Connect with absorber (1), generator (3) also has refrigerant steam channel to connect with condenser (5), and the second generator (4) is also cold Agent steam channel is connected with the second absorber (2), and condenser (5) also has cryogen liquid pipeline through choke valve (7) with vaporizer (6) even Logical, vaporizer (6) also has refrigerant steam channel to connect with absorber (1), and engine (12) has live steam passage and ft connection, moves After power machine (12) also has exhaust passage to connect with low-temperature condenser (13), low-temperature condenser (13) has low temperature cold lime set passage again With ft connection, it is first cold that engine (12) also has the post-heater (15) that connects with heater (15) of the first steam channel to have again Lime set passage and ft connection, after engine (12) also has the second steam channel to connect with secondary heater (16), second heats Device (16) has the second condensed fluid passage and ft connection again, and engine (12) also has the 3rd steam channel and the 3rd heater (17) After connection, the 3rd heater (17) has the 3rd condensed fluid passage and ft connection again, engine (12) or also exhaust passage with Ft connection, circulating pump (14) have circulatory mediator pipeline through low-temperature condenser (13), heater (15), secondary heater (16), The finisher (6) that 3rd heater (17) is connected with vaporizer (6) with heater (18) has circulatory mediator pipeline again through second Generator (4) itself is connected with circulating pump (14), and absorber (1) and condenser (5) also have heated medium passage respectively with outward Portion connect, the second absorber (2) also have coolant guiding channel and ft connection, generator (3) also have high temperature thermal medium passage with Ft connection, heater (18) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 41. heat, is in the dynamic co-feeding system of heat described in claim 40, circulating pump (14) is had circulatory mediator pipe Road is through low-temperature condenser (13), heater (15), secondary heater (16), the 3rd heater (17) and heater (18) and evaporation The finisher (6) of device (6) connection has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, adjusts Whole have circulatory mediator pipeline through low-temperature condenser (13), heater (15), secondary heater (16), Acanthopanan trifoliatus (L.) Merr. for circulating pump (14) After hot device (17) is connected with the second generator (4) with heater (18), the second generator (4) has circulatory mediator pipeline again through steaming Send out device (6) itself to connect with circulating pump (14), form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 42. heat, is in the dynamic co-feeding system of heat described in claim 40, circulating pump (14) is had circulatory mediator pipe Road is through low-temperature condenser (13), heater (15), secondary heater (16), the 3rd heater (17) and heater (18) and evaporation The finisher (6) of device (6) connection has circulatory mediator pipeline itself to connect with circulating pump (14) through the second generator (4) again, adjusts Whole have circulatory mediator pipeline through low-temperature condenser (13), heater (15), secondary heater (16), Acanthopanan trifoliatus (L.) Merr. for circulating pump (14) Finisher (6) and the second generation that hot device (17) is connected with vaporizer (6) and the second generator (4) respectively with heater (18) Device (4) has circulatory mediator pipeline itself to connect with circulating pump (14) more respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 43. heat, is described in claim 1,4,7,10,13,16,19,22,25,28,31,34,37,40 Any hot moves in co-feeding system, increases preheater, the second absorber (2) is had weak solution pipeline molten through solution pump (8) and second Liquid heat exchanger (11) connect with generator (3) be adjusted to the second absorber (2) have weak solution pipeline through solution pump (8), preheating Device (24) is connected with generator (3) with the second solution heat exchanger (11), and vaporizer (6) is had circulatory mediator pipeline through second Raw device (4) is connected with circulating pump (14) and is adjusted to vaporizer (6) and has circulatory mediator pipeline through the second generator (4) and preheater (24) connect with circulating pump (14), form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 44. heat, is described in claim 2,5,8,11,14,17,20,23,26,29,32,35,38,41 Any hot moves in co-feeding system, increases preheater, the second absorber (2) is had weak solution pipeline molten through solution pump (8) and second Liquid heat exchanger (11) connect with generator (3) be adjusted to the second absorber (2) have weak solution pipeline through solution pump (8), preheating Device (24) is connected with generator (3) with the second solution heat exchanger (11), and the second generator (4) is had circulatory mediator pipeline through steaming Send out device (6) and connect with circulating pump (14) and be adjusted to the second generator (4) and have circulatory mediator pipeline through vaporizer (6) and preheater (24) connect with circulating pump (14), form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 45. heat, is described in claim 3,6,9,12,15,18,21,24,27,30,33,36,39,42 Any hot moves in co-feeding system, increases preheater, the second absorber (2) is had weak solution pipeline molten through solution pump (8) and second Liquid heat exchanger (11) connect with generator (3) be adjusted to the second absorber (2) have weak solution pipeline through solution pump (8), preheating Device (24) is connected with generator (3) with the second solution heat exchanger (11), and vaporizer (6) and the second generator (4) are had respectively Circulatory mediator pipeline is connected with circulating pump (14) and is adjusted to vaporizer (6) and the second generator (4) has circulatory mediator pipeline respectively Preheated device (24) is connected with circulating pump (14), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 46. heat, is that any hot described in claim 1-42 moves in co-feeding system, increase the 3rd generator, 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber (2) is had weak solution pipeline through solution pump (8) with the second solution heat exchanger (11) is connected with generator (3) and is adjusted to the second absorber (2) and has weak solution pipeline through solution Pump (8) is connected with the 3rd absorber (20) with the second solution heat exchanger (11), and the 3rd absorber (20) has weak solution pipeline again Connect with generator (3) with the 3rd solution heat exchanger (22) through the 3rd solution pump (21), generator (3) is had concentrated solution pipeline Connect with the second generator (4) through the second solution heat exchanger (11) and be adjusted to generator (3) and have concentrated solution pipeline molten through the 3rd Liquid heat exchanger (22) is connected with the 3rd generator (19), and the 3rd generator (19) has concentrated solution pipeline to hand over through the second solution heat again Parallel operation (11) is connected with the second generator (4), and the 3rd generator (19) also has refrigerant steam channel with the 3rd absorber (20) even Logical, the 3rd generator (19) also has high temperature thermal medium passage and ft connection, and the 3rd absorber (20) also has heated medium to lead to Road and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 47. heat, is that any hot described in claim 43-45 moves in co-feeding system, increase the 3rd generator, 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber (2) is had weak solution pipeline through solution pump (8), preheater (24) connect with generator (3) with the second solution heat exchanger (11) be adjusted to the second absorber (2) have dilute molten Liquid pipeline is connected with the 3rd absorber (20) with the second solution heat exchanger (11) through solution pump (8), preheater (24), the 3rd suction Receiving device (20) has weak solution pipeline to connect with generator (3) with the 3rd solution heat exchanger (22) through the 3rd solution pump (21) again, Generator (3) there is is concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11) and is adjusted to generator (3) concentrated solution pipeline is had to connect with the 3rd generator (19) through the 3rd solution heat exchanger (22), the 3rd generator (19) has again Concentrated solution pipeline is connected with the second generator (4) through the second solution heat exchanger (11), and the 3rd generator (19) also has cryogen to steam Vapour passage is connected with the 3rd absorber (20), and the 3rd generator (19) also has high temperature thermal medium passage and ft connection, the 3rd suction Receive device (20) and also have heated medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 48. heat, is that any hot described in claim 1-42 moves in co-feeding system, increase the 3rd generator, 3rd solution pump, the 3rd solution heat exchanger and second throttle, the second absorber (2) sets up weak solution pipeline through the 3rd solution Pump (21) is connected with the 3rd generator (19) with the 3rd solution heat exchanger (22), and the 3rd generator (19) also has concentrated solution pipeline Connect with the second generator (4) through the 3rd solution heat exchanger (22), generator (3) is had refrigerant steam channel and condenser (5) connection is adjusted to after generator (3) has refrigerant steam channel to connect the 3rd generator (19) with the 3rd generator (19) again Have cryogen liquid pipeline to connect with condenser (5) through second throttle (23), the 3rd generator (19) also have refrigerant steam channel with Condenser (5) connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 49. heat, is that any hot described in claim 1-42 moves in co-feeding system, increase the 3rd generator, 3rd solution heat exchanger and second throttle, the second absorber (2) is had weak solution pipeline through solution pump (8) and the second solution Heat exchanger (11) is connected with generator (3) and is adjusted to the second absorber (2) and has weak solution pipeline through solution pump (8), second molten Liquid heat exchanger (11) is connected with generator (3) with the 3rd solution heat exchanger (22), and generator (3) is had concentrated solution pipeline warp Second solution heat exchanger (11) is connected with the second generator (4) and is adjusted to generator (3) and has concentrated solution pipeline through the 3rd solution Heat exchanger (22) is connected with the 3rd generator (19), and the 3rd generator (19) has concentrated solution pipeline again through the second solution heat exchange Device (11) is connected with the second generator (4), generator (3) is had refrigerant steam channel to connect with condenser (5) and is adjusted to generation After device (3) has refrigerant steam channel to connect with the 3rd generator (19), the 3rd generator (19) has cryogen liquid pipeline again through second Choke valve (23) is connected with condenser (5), and the 3rd generator (19) also has refrigerant steam channel to connect with condenser (5), is formed The dynamic co-feeding system of heat.
The dynamic co-feeding system of 50. heat, is that any hot described in claim 1-42 moves in co-feeding system, increase the 3rd generator, 3rd solution pump, the 3rd solution heat exchanger and second throttle, the second absorber (2) is had weak solution pipeline through solution pump (8) with the second solution heat exchanger (11) is connected with generator (3) and is adjusted to the second absorber (2) and has weak solution pipeline through solution Pump (8) is connected with the 3rd generator (19) with the second solution heat exchanger (11), and the 3rd generator (19) has concentrated solution pipeline again Connect with generator (3) with the 3rd solution heat exchanger (22) through the 3rd solution pump (21), generator (3) is had concentrated solution pipeline Connect with the second generator (4) through the second solution heat exchanger (11) and be adjusted to generator (3) and have concentrated solution pipeline molten through the 3rd Liquid heat exchanger (22) is connected with the second generator (4) with the second solution heat exchanger (11), and generator (3) is had refrigerant vapour Passage is connected with condenser (5) and is adjusted to the 3rd after generator (3) has refrigerant steam channel to connect with the 3rd generator (19) Generator (19) has cryogen liquid pipeline to connect with condenser (5) through second throttle (23) again, and the 3rd generator (19) is also cold Agent steam channel is connected with condenser (5), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 51. heat, is that any hot described in claim 43-45 moves in co-feeding system, increase the 3rd generator, 3rd solution pump, the 3rd solution heat exchanger and second throttle, the second absorber (2) sets up weak solution pipeline through the 3rd solution Pump (21), preheater (24) are connected with the 3rd generator (19) with the 3rd solution heat exchanger (22), and the 3rd generator (19) is also There is concentrated solution pipeline to connect with the second generator (4) through the 3rd solution heat exchanger (22), generator (3) is had refrigerant vapour to lead to Road is connected with condenser (5) and is adjusted to the 3rd after generator (3) has refrigerant steam channel to connect with the 3rd generator (19) Raw device (19) has cryogen liquid pipeline to connect with condenser (5) through second throttle (23) again, and the 3rd generator (19) also has cryogen Steam channel is connected with condenser (5), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 52. heat, is that any hot described in claim 43-45 moves in co-feeding system, increase the 3rd generator, 3rd solution heat exchanger and second throttle, the second absorber (2) is had weak solution pipeline through solution pump (8), preheater (24) with the second solution heat exchanger (11) is connected with generator (3) and is adjusted to the second absorber (2) and has weak solution pipeline through molten Liquid pump (8), preheater (24), the second solution heat exchanger (11) are connected with generator (3) with the 3rd solution heat exchanger (22), Generator (3) there is is concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11) and is adjusted to generator (3) concentrated solution pipeline is had to connect with the 3rd generator (19) through the 3rd solution heat exchanger (22), the 3rd generator (19) has again Concentrated solution pipeline is connected with the second generator (4) through the second solution heat exchanger (11), and generator (3) is had refrigerant steam channel Connect with condenser (5) and be adjusted to the 3rd generation after generator (3) has refrigerant steam channel to connect with the 3rd generator (19) Device (19) has cryogen liquid pipeline to connect with condenser (5) through second throttle (23) again, and the 3rd generator (19) also has cryogen to steam Vapour passage is connected with condenser (5), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 53. heat, is that any hot described in claim 43-45 moves in co-feeding system, increase the 3rd generator, 3rd solution pump, the 3rd solution heat exchanger and second throttle, the second absorber (2) is had weak solution pipeline through solution pump (8), preheater (24) connect with generator (3) with the second solution heat exchanger (11) be adjusted to the second absorber (2) have dilute molten Liquid pipeline is connected with the 3rd generator (19) with the second solution heat exchanger (11) through solution pump (8), preheater (24), the 3rd Raw device (19) has concentrated solution pipeline to connect with generator (3) with the 3rd solution heat exchanger (22) through the 3rd solution pump (21) again, Generator (3) there is is concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (11) and is adjusted to generator (3) concentrated solution pipeline is had to connect with the second generator (4) through the 3rd solution heat exchanger (22) and the second solution heat exchanger (11) Logical, generator (3) there is is refrigerant steam channel to connect with condenser (5) and is adjusted to generator (3) and has refrigerant steam channel and the After three generators (19) connection, the 3rd generator (19) has cryogen liquid pipeline through second throttle (23) with condenser (5) even again Logical, the 3rd generator (19) also has refrigerant steam channel to connect with condenser (5), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 54. heat, is that any hot described in claim 47-52 moves in co-feeding system, the 3rd generator (19) Set up high temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 55. heat, is that any hot described in claim 1-45 moves in co-feeding system, increase the 3rd generator, 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, generator (3) is had refrigerant steam channel and condenser (5) Connection is adjusted to generator (3) has refrigerant steam channel to connect with the 3rd absorber (20), and the 3rd absorber (20) also has dilute molten Liquid pipeline is connected with the 3rd generator (19) with the 3rd solution heat exchanger (22) through the 3rd solution pump (21), the 3rd generator (19) concentrated solution pipeline is also had to connect with the 3rd absorber (20) through the 3rd solution heat exchanger (22), the 3rd generator (19) is also Refrigerant steam channel is had to connect with condenser (5), the 3rd generator (19) also high temperature thermal medium passage and ft connection, the 3rd Absorber (20) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 56. heat, is described in claim 1,4,7,10,13,16,19,22,25,28,31,34,37,40 Any hot moves in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, will Absorber (1) have weak solution pipeline connect with the second absorber (2) through solution heat exchanger (10) be adjusted to absorber (1) have dilute Solution line is connected with the 3rd absorber (20) through the 3rd solution heat exchanger (22), and the 3rd absorber (20) has weak solution pipe again Lu Jing tri- solution pump (21) is connected with the second absorber (2) with solution heat exchanger (10), the second generator (4) is had dense molten Liquid pipeline connect with absorber (1) through the second solution pump (9) and solution heat exchanger (10) be adjusted to the second generator (4) have dense Solution line is connected with the 3rd generator (19) through solution heat exchanger (10), and the 3rd generator (19) has concentrated solution pipeline warp again Second solution pump (9) is connected with absorber (1) with the 3rd solution heat exchanger (22), and vaporizer (6) is had circulatory mediator pipeline Connect with circulating pump (14) through the second generator (4) be adjusted to vaporizer (6) have circulatory mediator pipeline through the second generator (4) and 3rd generator (19) is connected with circulating pump (14), and the 3rd generator (19) also has refrigerant steam channel and the 3rd absorber (20) Connection, the 3rd absorber (20) also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 57. heat, is described in claim 2,5,8,11,14,17,20,23,26,29,32,35,38,41 Any hot moves in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, will Absorber (1) have weak solution pipeline connect with the second absorber (2) through solution heat exchanger (10) be adjusted to absorber (1) have dilute Solution line is connected with the 3rd absorber (20) through the 3rd solution heat exchanger (22), and the 3rd absorber (20) has weak solution pipe again Lu Jing tri- solution pump (21) is connected with the second absorber (2) with solution heat exchanger (10), the second generator (4) is had dense molten Liquid pipeline connect with absorber (1) through the second solution pump (9) and solution heat exchanger (10) be adjusted to the second generator (4) have dense Solution line is connected with the 3rd generator (19) through solution heat exchanger (10), and the 3rd generator (19) has concentrated solution pipeline warp again Second solution pump (9) is connected with absorber (1) with the 3rd solution heat exchanger (22), and the second generator (4) is had circulatory mediator Pipeline connect with circulating pump (14) through vaporizer (6) be adjusted to the second generator (4) have circulatory mediator pipeline through vaporizer (6) and 3rd generator (19) is connected with circulating pump (14), and the 3rd generator (19) also has refrigerant steam channel and the 3rd absorber (20) Connection, the 3rd absorber (20) also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 58. heat, is described in claim 3,6,9,12,15,18,21,24,27,30,33,36,39,42 Any hot moves in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, will Absorber (1) have weak solution pipeline connect with the second absorber (2) through solution heat exchanger (10) be adjusted to absorber (1) have dilute Solution line is connected with the 3rd absorber (20) through the 3rd solution heat exchanger (22), and the 3rd absorber (20) has weak solution pipe again Lu Jing tri- solution pump (21) is connected with the second absorber (2) with solution heat exchanger (10), the second generator (4) is had dense molten Liquid pipeline connect with absorber (1) through the second solution pump (9) and solution heat exchanger (10) be adjusted to the second generator (4) have dense Solution line is connected with the 3rd generator (19) through solution heat exchanger (10), and the 3rd generator (19) has concentrated solution pipeline warp again Second solution pump (9) is connected with absorber (1) with the 3rd solution heat exchanger (22), by vaporizer (6) and the second generator (4) There is circulatory mediator pipeline to connect with circulating pump (14) respectively to be adjusted to vaporizer (6) and the second generator (4) and have circulation to be situated between respectively Matter pipeline is connected with circulating pump (14) through the 3rd generator (19), and the 3rd generator (19) also has refrigerant steam channel and the 3rd suction Receive device (20) connection, the 3rd absorber (20) also has coolant guiding channel and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 59. heat, is that any hot described in claim 56 moves in co-feeding system, increases preheater, by second Absorber (2) has weak solution pipeline to connect with generator (3) through solution pump (8) and the second solution heat exchanger (11) to be adjusted to Two absorbers (2) have weak solution pipeline through solution pump (8), preheater (24) and the second solution heat exchanger (11) and generator (3) connect, vaporizer (6) is had circulatory mediator pipeline through the second generator (4) and the 3rd generator (19) and circulating pump (14) Connection be adjusted to vaporizer (6) have circulatory mediator pipeline through the second generator (4), the 3rd generator (19) and preheater (24) and Circulating pump (14) connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 60. heat, is that any hot described in claim 57 moves in co-feeding system, increases preheater, by second Absorber (2) has weak solution pipeline to connect with generator (3) through solution pump (8) and the second solution heat exchanger (11) to be adjusted to Two absorbers (2) have weak solution pipeline through solution pump (8), preheater (24) and the second solution heat exchanger (11) and generator (3) connect, the second generator (4) is had circulatory mediator pipeline through vaporizer (6) and the 3rd generator (19) and circulating pump (14) Connection be adjusted to the second generator (4) have circulatory mediator pipeline through vaporizer (6), the 3rd generator (19) and preheater (24) and Circulating pump (14) connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 61. heat, is that any hot described in claim 58 moves in co-feeding system, increases preheater, by second Absorber (2) has weak solution pipeline to connect with generator (3) through solution pump (8) and the second solution heat exchanger (11) to be adjusted to Two absorbers (2) have weak solution pipeline through solution pump (8), preheater (24) and the second solution heat exchanger (11) and generator (3) connect, vaporizer (6) and the second generator (4) are had circulatory mediator pipeline respectively through the 3rd generator (19) and circulating pump (14) connection is adjusted to vaporizer (6) and the second generator (4) has circulatory mediator pipeline through the 3rd generator (19) and in advance respectively Hot device (24) is connected with circulating pump (14), forms the dynamic co-feeding system of heat.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104006567A (en) * 2013-05-08 2014-08-27 李华玉 Branch circulating first-kind absorption heat pump
CN104165477A (en) * 2013-07-30 2014-11-26 李华玉 Combined heating and power system, combined cooling and power system and dual-purpose combined heat and power and cooling and power system
CN104180557A (en) * 2013-07-30 2014-12-03 李华玉 Combined heat power system, combined cooling power system and combined heat-cooling power dual-purpose system
CN104654658A (en) * 2014-01-27 2015-05-27 李华玉 Combined thermal dynamic system
CN104748434A (en) * 2013-12-26 2015-07-01 李华玉 Second-type absorption heat pump using multi-end heat supplying
CN104864623A (en) * 2014-01-27 2015-08-26 李华玉 Thermodynamic combined supply system

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104006567A (en) * 2013-05-08 2014-08-27 李华玉 Branch circulating first-kind absorption heat pump
CN104165477A (en) * 2013-07-30 2014-11-26 李华玉 Combined heating and power system, combined cooling and power system and dual-purpose combined heat and power and cooling and power system
CN104180557A (en) * 2013-07-30 2014-12-03 李华玉 Combined heat power system, combined cooling power system and combined heat-cooling power dual-purpose system
CN104748434A (en) * 2013-12-26 2015-07-01 李华玉 Second-type absorption heat pump using multi-end heat supplying
CN104654658A (en) * 2014-01-27 2015-05-27 李华玉 Combined thermal dynamic system
CN104864623A (en) * 2014-01-27 2015-08-26 李华玉 Thermodynamic combined supply system

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