CN106352590A - Combined heating and power system - Google Patents

Combined heating and power system Download PDF

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Publication number
CN106352590A
CN106352590A CN201610822142.5A CN201610822142A CN106352590A CN 106352590 A CN106352590 A CN 106352590A CN 201610822142 A CN201610822142 A CN 201610822142A CN 106352590 A CN106352590 A CN 106352590A
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China
Prior art keywords
generator
solution
heat exchanger
pipeline
connect
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CN201610822142.5A
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Chinese (zh)
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CN106352590B (en
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李华玉
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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/02—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
    • 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
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00—Climate change mitigation technologies for sector-wide applications
    • Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
    • Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply

Abstract

The invention provides a combined heating and power system and belongs to the technical field of CCHP (combined cooling, heating and power) and heat pumps. An absorption heat pump cycling system comprises a generator, a second generator, an absorber, a condenser, a second condenser, an evaporator, a throttle valve, a refrigerant liquid pump, a solution pump, a solution heat exchanger and a second solution heat exchanger, wherein a power machine provides low-temperature heat load for the generator through an exhaust steam channel and provides low-temperature heat load for the evaporator through a first steam channel, the second generator communicates with the outside through a high-temperature heat medium channel, the absorber and the second condenser communicate with the outside through heated medium channels, the condenser communicates with the outside through a cooling medium channel, and the combined heating and power system is formed.

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:
In Steam Power Equipment, though the temperature difference is little between engine steam discharge and environment, heat is huge, winter season more so, The temperature difference between the low pressure exhaust steam of Steam Power Equipment discharge and environment is often difficult by；Steam power dress with coal as fuel Put, between combustion gas and power cycle steam, there is the heat transfer temperature difference being difficult to effectively utilizes, lead to the comprehensive energy of the dynamic co-feeding system of heat Source utilization rate is not high, and to clean energy resource in the dynamic co-feeding system of heat using bringing a definite limitation.
The present invention is premised on heat energy efficient utilization, warm between engine steam discharge or low-pressure steam and environment to make full use of Difference is core, takes into account lifting power machine job security and heat energy is converted into the efficiency of mechanical energy, and considers to adapt to the dynamic alliance of heat The utilization of clean energy resource in system, proposes as low-temperature heat source and to combine absorption heat pump with engine end steam discharge or low-pressure pumping steam The series of heat of technology moves co-feeding system.
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 generator, the second generator, absorber, condenser, the second condenser, evaporation Device, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator Concentrated solution pipeline is had to connect with the second generator through solution pump, solution heat exchanger and the second solution heat exchanger, the second generation Device also has concentrated solution pipeline to connect with absorber through the second solution heat exchanger, and absorber also has weak solution pipeline to hand over through solution heat Parallel operation is connected with generator, 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 condenser, and condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, and the second condenser also has After cryogen liquid pipeline is connected with generator, generator has cryogen liquid pipeline to connect with vaporizer through choke valve again, and vaporizer also has Refrigerant steam channel is connected with absorber, and engine has live steam passage and ft connection, and engine or also exhaust passage are with outward Portion connects, and after engine also has exhaust passage to be sequentially communicated vaporizer and generator, generator has condensed fluid passage and outside again Connection, it is heated that the second generator also has high temperature thermal medium passage and ft connection, absorber and the second condenser also to have respectively Medium channel and ft connection, condenser also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, condenser, the second condenser, evaporation Device, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator Concentrated solution pipeline is had to connect with the second generator through solution pump, solution heat exchanger and the second solution heat exchanger, the second generation Device also has concentrated solution pipeline to connect with absorber through the second solution heat exchanger, and absorber also has weak solution pipeline to hand over through solution heat Parallel operation is connected with generator, 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 condenser, and condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, and the second condenser also has After cryogen liquid pipeline is connected with generator, generator has cryogen liquid pipeline to connect with vaporizer through choke valve again, and vaporizer also has Refrigerant steam channel is connected with absorber, and engine is had live steam passage and ft connection respectively and has exhaust passage to be connected with outside Logical, engine also have the first steam channel to be sequentially communicated vaporizer and generator after generator have again the first condensed fluid passage with Ft connection, the second generator also have high temperature thermal medium passage and ft connection, absorber and the second condenser also have respectively by Heating medium passage and ft connection, condenser also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, condenser, the second condenser, evaporation Device, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator Concentrated solution pipeline is had to connect with the second generator through solution pump, solution heat exchanger and the second solution heat exchanger, the second generation Device also has concentrated solution pipeline to connect with absorber through the second solution heat exchanger, and absorber also has weak solution pipeline to hand over through solution heat Parallel operation is connected with generator, 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 condenser, and condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, and the second condenser also has After cryogen liquid pipeline is connected with generator, generator has cryogen liquid pipeline to connect with vaporizer through choke valve again, and vaporizer also has Refrigerant steam channel is connected with absorber, and engine has live steam passage and ft connection, and engine or also exhaust passage are with outward Portion connects, and after engine also has exhaust passage to connect with generator, generator has condensed fluid passage and ft connection, power again Machine also has the finisher that the first steam channel is connected with vaporizer to have the first condensed fluid passage and ft connection, the second generation again Device also has high temperature thermal medium passage and ft connection, absorber and the second condenser also to have heated medium passage and outside respectively Connection, condenser also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, condenser, the second condenser, evaporation Device, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator Concentrated solution pipeline is had to connect with the second generator through solution pump, solution heat exchanger and the second solution heat exchanger, the second generation Device also has concentrated solution pipeline to connect with absorber through the second solution heat exchanger, and absorber also has weak solution pipeline to hand over through solution heat Parallel operation is connected with generator, 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 condenser, and condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, and the second condenser also has After cryogen liquid pipeline is connected with generator, generator has cryogen liquid pipeline to connect with vaporizer through choke valve again, and vaporizer also has Refrigerant steam channel is connected with absorber, and engine is had live steam passage and ft connection respectively and has exhaust passage to be connected with outside Logical, after engine also has the first steam channel to connect with generator, generator has the first condensed fluid passage and ft connection again, Engine also has the finisher that the second steam channel is connected with vaporizer to have the second condensed fluid passage and ft connection again, and second Generator also have high temperature thermal medium passage and ft connection, absorber and the second condenser also have respectively heated medium passage with Ft connection, condenser also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, is that any hot described in 1-4 item moves in co-feeding system, increase the 3rd generator, the Two absorbers, the second solution pump and the 3rd solution heat exchanger, generator is had concentrated solution pipeline through solution pump, solution heat exchange Device and the second solution heat exchanger are connected with the second generator and are adjusted to generator and have concentrated solution pipeline to hand over through solution pump, solution heat Parallel operation and the second solution heat exchanger are connected with the second absorber, the second absorber have weak solution pipeline through the second solution pump again and 3rd solution heat exchanger is connected with the second generator, by the second generator have concentrated solution pipeline through the second solution heat exchanger with Absorber connection is adjusted to the second 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 absorber through the second solution heat exchanger again, and the 3rd generator also has refrigerant steam channel Connect with the second absorber, the 3rd generator also has high temperature thermal medium passage and ft connection, the second absorber also has heated Medium channel and ft connection, form the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, is that any hot described in 1-4 item moves in co-feeding system, increase the 3rd generator, the Two absorbers, the second solution pump and the 3rd solution heat exchanger, the second generator is had refrigerant steam channel and the second condenser Connection is adjusted to the second generator has refrigerant steam channel to connect with the second absorber, and the second absorber also has weak solution pipeline warp Second solution pump and the 3rd solution heat exchanger are connected with the 3rd generator, and the 3rd generator also has concentrated solution pipeline molten through the 3rd Liquid heat exchanger is connected with the second absorber, and the 3rd generator also has refrigerant steam channel to connect with the second condenser, the 3rd Raw device also has high temperature thermal medium passage and ft connection, and the second absorber also has heated medium passage and ft connection, is formed The dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, is that any hot described in 1-6 item moves in co-feeding system, cancels choke valve, will occur Device has cryogen liquid pipeline to connect with vaporizer through choke valve to be adjusted to generator and have cryogen liquid pipeline to connect with vaporizer, form heat Dynamic co-feeding system.
8. the dynamic co-feeding system of heat, is that any hot described in 1-4 item moves in co-feeding system, increase the 3rd generator, the Two solution pumps, the 3rd solution heat exchanger, second throttle and heater, generator sets up concentrated solution pipeline through the second solution Pump, solution heat exchanger and the 3rd solution heat exchanger are connected with the 3rd generator, and the 3rd generator also has concentrated solution pipeline warp 3rd solution heat exchanger is connected with absorber, the second generator is had refrigerant steam channel to connect with the second condenser and is adjusted to Second generator have refrigerant steam channel to connect with the 3rd generator after the 3rd generator have again cryogen liquid pipeline through heater, Generator is connected with vaporizer with second throttle, and the 3rd generator also has refrigerant steam channel to connect with the second condenser, supplies Hot device also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, is that any hot described in 1-4 item moves in co-feeding system, increase the 3rd generator, the Three solution heat exchangers, second throttle and heater, by generator have concentrated solution pipeline through solution pump, solution heat exchanger and Second solution heat exchanger is connected with the second generator and is adjusted to generator and has concentrated solution pipeline through solution pump, solution heat exchange Device, the second solution heat exchanger and the 3rd solution heat exchanger are connected with the second generator, and the second generator is had concentrated solution pipe Road second solution heat exchanger is connected with absorber and is adjusted to the second generator and has concentrated solution pipeline through the 3rd solution heat exchange Device is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline to connect with absorber through the second solution heat exchanger again, will Second generator has refrigerant steam channel to connect with the second condenser to be adjusted to the second generator and have refrigerant steam channel and the 3rd After generator connection, the 3rd generator has cryogen liquid pipeline to connect through heater, generator and second throttle and vaporizer again Logical, the 3rd generator also has refrigerant steam channel to connect with the second condenser, and heater also has heated medium passage and outside Connection, forms the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, is that any hot described in 1-4 item moves in co-feeding system, increase the 3rd generator, the Two solution pumps, the 3rd solution heat exchanger, second throttle and heater, generator is had concentrated solution pipeline through solution pump, molten Liquid heat exchanger and the second solution heat exchanger connect with the second generator be adjusted to generator have concentrated solution pipeline through solution pump, Solution heat exchanger and the second solution heat exchanger are connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline again through second Solution pump and the 3rd solution heat exchanger are connected with the second generator, and the second generator is had concentrated solution pipeline through the second solution heat Exchanger connect with absorber be adjusted to the second generator have concentrated solution pipeline through the 3rd solution heat exchanger and the second solution heat Exchanger is connected with absorber, the second generator is had refrigerant steam channel to connect with the second condenser and is adjusted to the second generator After having refrigerant steam channel to connect with the 3rd generator, the 3rd generator has cryogen liquid pipeline again through heater, generator and Two choke valves are connected with vaporizer, and the 3rd generator also has refrigerant steam channel to connect with the second condenser, and heater also has quilt Heating medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, is that any hot described in 8-10 item moves in co-feeding system, height set up by the 3rd generator Warm passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 12. heat, is that any hot described in 8-11 item moves in co-feeding system, cancels choke valve and second Choke valve, generator is had cryogen liquid pipeline to connect with vaporizer through choke valve and is adjusted to generator and has cryogen liquid pipeline and evaporation Device connect, by generator have cryogen liquid pipeline connect with vaporizer through second throttle be adjusted to generator have cryogen liquid pipeline and Vaporizer connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 13. heat, is that the heat described at the 1st is moved in co-feeding system, increases the 3rd generator, the second absorption Device, the second solution pump and the 3rd solution heat exchanger, generator is had concentrated solution pipeline through solution pump, solution heat exchanger and Two solution heat exchangers connect with the second generator be adjusted to generator have concentrated solution pipeline through solution heat exchanger and second suction Receive device connection, the second absorber has weak solution pipeline to connect with the second generator through solution pump and the second solution heat exchanger again, By the second generator have concentrated solution pipeline connect with absorber through the second solution heat exchanger be adjusted to the second generator have dense molten Liquid pipeline is connected with the 3rd generator through the second solution heat exchanger, and the 3rd generator has concentrated solution pipeline again through the second solution pump Connect with absorber with the 3rd solution heat exchanger, absorber is had weak solution pipeline to connect with generator through solution heat exchanger Being adjusted to absorber has weak solution pipeline to connect with generator with solution heat exchanger through the 3rd solution heat exchanger, cold by second After condenser has cryogen liquid pipeline to connect with generator, generator has cryogen liquid pipeline to connect adjustment with vaporizer through choke valve again After having cryogen liquid pipeline to connect with the 3rd generator through generator for the second condenser, the 3rd generator has cryogen liquid pipeline again Connect with vaporizer through choke valve, after engine is had exhaust passage to be sequentially communicated vaporizer and generator generator have again cold Lime set passage and ft connection are adjusted to after engine has exhaust passage to be sequentially communicated vaporizer, generator and the 3rd generator 3rd generator has condensed fluid passage and ft connection again, and the 3rd generator also has refrigerant steam channel with the second absorber even Logical, the second absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 14. heat, is that the heat described at the 2nd is moved in co-feeding system, increases the 3rd generator, the second absorption Device, the second solution pump and the 3rd solution heat exchanger, generator is had concentrated solution pipeline through solution pump, solution heat exchanger and Two solution heat exchangers connect with the second generator be adjusted to generator have concentrated solution pipeline through solution heat exchanger and second suction Receive device connection, the second absorber has weak solution pipeline to connect with the second generator through solution pump and the second solution heat exchanger again, By the second generator have concentrated solution pipeline connect with absorber through the second solution heat exchanger be adjusted to the second generator have dense molten Liquid pipeline is connected with the 3rd generator through the second solution heat exchanger, and the 3rd generator has concentrated solution pipeline again through the second solution pump Connect with absorber with the 3rd solution heat exchanger, absorber is had weak solution pipeline to connect with generator through solution heat exchanger Being adjusted to absorber has weak solution pipeline to connect with generator with solution heat exchanger through the 3rd solution heat exchanger, cold by second After condenser has cryogen liquid pipeline to connect with generator, generator has cryogen liquid pipeline to connect adjustment with vaporizer through choke valve again After having cryogen liquid pipeline to connect with the 3rd generator through generator for the second condenser, the 3rd generator has cryogen liquid pipeline again Connect with vaporizer through choke valve, after engine is had the first steam channel to be sequentially communicated vaporizer and generator, generator is again Having the first condensed fluid passage and ft connection to be adjusted to engine has the first steam channel to be sequentially communicated vaporizer, generator and the After three generators, the 3rd generator has the first condensed fluid passage and ft connection again, and the 3rd generator also has refrigerant steam channel Connect with the second absorber, the second absorber also has coolant guiding channel and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, is that the heat described at the 3rd is moved in co-feeding system, increases the 3rd generator, the second absorption Device, the second solution pump and the 3rd solution heat exchanger, generator is had concentrated solution pipeline through solution pump, solution heat exchanger and Two solution heat exchangers connect with the second generator be adjusted to generator have concentrated solution pipeline through solution heat exchanger and second suction Receive device connection, the second absorber has weak solution pipeline to connect with the second generator through solution pump and the second solution heat exchanger again, By the second generator have concentrated solution pipeline connect with absorber through the second solution heat exchanger be adjusted to the second generator have dense molten Liquid pipeline is connected with the 3rd generator through the second solution heat exchanger, and the 3rd generator has concentrated solution pipeline again through the second solution pump Connect with absorber with the 3rd solution heat exchanger, absorber is had weak solution pipeline to connect with generator through solution heat exchanger Being adjusted to absorber has weak solution pipeline to connect with generator with solution heat exchanger through the 3rd solution heat exchanger, cold by second After condenser has cryogen liquid pipeline to connect with generator, generator has cryogen liquid pipeline to connect adjustment with vaporizer through choke valve again After having cryogen liquid pipeline to connect with the 3rd generator through generator for the second condenser, the 3rd generator has cryogen liquid pipeline again Connect with vaporizer through choke valve, after engine is had exhaust passage to connect with generator generator have again condensed fluid passage with Ft connection is adjusted to the 3rd generator after engine has exhaust passage to connect with the 3rd generator through generator condensation again Liquid passage and ft connection, the 3rd generator also has refrigerant steam channel to connect with the second absorber, and the second absorber is also cold But medium channel and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 16. heat, is that the heat described at the 4th is moved in co-feeding system, increases the 3rd generator, the second absorption Device, the second solution pump and the 3rd solution heat exchanger, generator is had concentrated solution pipeline through solution pump, solution heat exchanger and Two solution heat exchangers connect with the second generator be adjusted to generator have concentrated solution pipeline through solution heat exchanger and second suction Receive device connection, the second absorber has weak solution pipeline to connect with the second generator through solution pump and the second solution heat exchanger again, By the second generator have concentrated solution pipeline connect with absorber through the second solution heat exchanger be adjusted to the second generator have dense molten Liquid pipeline is connected with the 3rd generator through the second solution heat exchanger, and the 3rd generator has concentrated solution pipeline again through the second solution pump Connect with absorber with the 3rd solution heat exchanger, absorber is had weak solution pipeline to connect with generator through solution heat exchanger Being adjusted to absorber has weak solution pipeline to connect with generator with solution heat exchanger through the 3rd solution heat exchanger, cold by second After condenser has cryogen liquid pipeline to connect with generator, generator has cryogen liquid pipeline to connect adjustment with vaporizer through choke valve again After having cryogen liquid pipeline to connect with the 3rd generator through generator for the second condenser, the 3rd generator has cryogen liquid pipeline again Connect with vaporizer through choke valve, after engine is had the first steam channel to connect with generator, generator has the first condensation again Liquid passage is adjusted to the 3rd after engine has the first steam channel to connect with the 3rd generator through generator with ft connection Raw device has the first condensed fluid passage and ft connection again, and the 3rd generator also has refrigerant steam channel to connect with the second absorber, Second absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, is that the heat described at the 4th is moved in co-feeding system, increases the 3rd generator, the second absorption Device, the second solution pump and the 3rd solution heat exchanger, generator is had concentrated solution pipeline through solution pump, solution heat exchanger and Two solution heat exchangers connect with the second generator be adjusted to generator have concentrated solution pipeline through solution heat exchanger and second suction Receive device connection, the second absorber has weak solution pipeline to connect with the second generator through solution pump and the second solution heat exchanger again, By the second generator have concentrated solution pipeline connect with absorber through the second solution heat exchanger be adjusted to the second generator have dense molten Liquid pipeline is connected with the 3rd generator through the second solution heat exchanger, and the 3rd generator has concentrated solution pipeline again through the second solution pump Connect with absorber with the 3rd solution heat exchanger, absorber is had weak solution pipeline to connect with generator through solution heat exchanger Being adjusted to absorber has weak solution pipeline to connect with generator with solution heat exchanger through the 3rd solution heat exchanger, cold by second After condenser has cryogen liquid pipeline to connect with generator, generator has cryogen liquid pipeline to connect adjustment with vaporizer through choke valve again After having cryogen liquid pipeline to connect with the 3rd generator through generator for the second condenser, the 3rd generator has cryogen liquid pipeline again Connect with vaporizer through choke valve, engine is had exhaust passage and ft connection to be adjusted to engine exhaust passage and the 3rd Generator connection after the 3rd generator have condensed fluid passage and ft connection again, the 3rd generator also have refrigerant steam channel with Second absorber connection, the second absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or The 3rd generator after exhaust passage is connected set up with the 3rd generator by engine condensed fluid passage and ft connection again.
The dynamic co-feeding systems of 18. heat, are that any hot described in 12-17 item moves in co-feeding system, cancel choke valve, by the Three generators have cryogen liquid pipeline to connect with vaporizer through choke valve to be adjusted to the 3rd generator and have cryogen liquid pipeline and vaporizer Connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, is that the heat described at the 3rd is moved in co-feeding system, increases preheater, condenser is had cold Agent liquid pipeline is connected with vaporizer through cryogen liquid pump and is adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and preheater and steaming Send out device connection, generator is had condensed fluid passage and ft connection to be adjusted to generator the preheated device of condensed fluid passage and outside Connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 20. heat, are that any hot described in 1-19 item moves in co-feeding system, cancel the second generator with The high temperature thermal medium passage of connection, the second generator after high-temperature steam passage is connected set up with the second generator by engine has again High temperature condensed fluid passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 21. heat, are that any hot described in 5-6 item moves in co-feeding system, cancel the second generator and The 3rd generator high temperature thermal medium passage with ft connection respectively, engine is set up high-temperature steam passage and is sequentially communicated second After raw device and the 3rd generator, the 3rd generator has high temperature condensed fluid passage and ft connection again, 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.
In figure, 1- generator, 2- second generator, 3- absorber, 4- condenser, 5- second condenser, 6- vaporizer, 7- Choke valve, 8- cryogen liquid pump, 9- solution pump, 10- solution heat exchanger, 11- second solution heat exchanger, 12- engine, 13- 3rd generator, 14- second absorber, 15- the second solution pump, 16- the 3rd solution heat exchanger, 17- second throttle, 18- Heater, 19- preheater.
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 is moved co-feeding system and is achieved in that
(1) in structure, it mainly by generator, the second generator, absorber, condenser, the second condenser, vaporizer, Choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator 1 has Concentrated solution pipeline is connected with the second generator 2 with the second solution heat exchanger 11 through solution pump 9, solution heat exchanger 10, and second Generator 2 also has concentrated solution pipeline to connect with absorber 3 through the second solution heat exchanger 11, and absorber 3 also has weak solution pipeline Connect with generator 1 through solution heat exchanger 10, generator 1 also has refrigerant steam channel to connect with condenser 4, the second generator 2 also have refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 8 and vaporizer 6 Connection, after the second condenser 5 also has cryogen liquid pipeline to connect with generator 1, generator 1 has cryogen liquid pipeline again through choke valve 7 Connect with vaporizer 6, vaporizer 6 also has refrigerant steam channel to connect with absorber 3, and engine 12 has live steam passage and outside to connect Logical, after engine 12 also has exhaust passage to be sequentially communicated vaporizer 6 and generator 1, generator 1 has condensed fluid passage again with outward Portion connects, the second generator 2 also have high temperature thermal medium passage and ft connection, absorber 3 and the second condenser 5 also have respectively by Heating medium passage and ft connection, condenser 4 also has coolant guiding channel 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 vaporizer 6 and generator 1 Progressively heat release condensing, externally discharges afterwards；The concentrated solution of generator 1 is through solution pump 9, solution heat exchanger 10 and the second solution Heat exchanger 11 enters the second generator 2, and it is cold that high temperature thermal medium flows through the second generator 2, heating enters its interior solution release Agent steam simultaneously provides to the second condenser 5, the concentrated solution of the second generator 2 through the second solution heat exchanger 11 enter absorber 3, Absorb refrigerant vapour and heat release is in heated medium, the weak solution of absorber 3 enters generator 1, inhales through solution heat exchanger 10 Heat release refrigerant vapour simultaneously provides to condenser 4；The refrigerant vapour heat release of condenser 4 becomes cryogen liquid, condenser 4 in cooling medium Cryogen liquid pressurize through cryogen liquid pump 8 and enter vaporizer 6, absorb heat into refrigerant vapour and provide to absorber 3；Second condenser 5 Refrigerant vapour heat release become cryogen liquid in heated medium, the cryogen liquor stream of the second condenser 5 through generator 1 and heat release, afterwards Enter vaporizer 6, absorb heat into refrigerant vapour and provide to absorber 3 through choke valve 7 reducing pressure by regulating flow, form the dynamic co-feeding system of heat.
Heat shown in Fig. 2 is moved co-feeding system and is achieved in that
(1) in structure, it mainly by generator, the second generator, absorber, condenser, the second condenser, vaporizer, Choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator 1 has Concentrated solution pipeline is connected with the second generator 2 with the second solution heat exchanger 11 through solution pump 9, solution heat exchanger 10, and second Generator 2 also has concentrated solution pipeline to connect with absorber 3 through the second solution heat exchanger 11, and absorber 3 also has weak solution pipeline Connect with generator 1 through solution heat exchanger 10, generator 1 also has refrigerant steam channel to connect with condenser 4, the second generator 2 also have refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 8 and vaporizer 6 Connection, after the second condenser 5 also has cryogen liquid pipeline to connect with generator 1, generator 1 has cryogen liquid pipeline again through choke valve 7 Connect with vaporizer 6, vaporizer 6 also has refrigerant steam channel to connect with absorber 3, engine 12 has live steam passage respectively with outward Portion connects and has exhaust passage and ft connection, and engine 12 also has the first steam channel to be sequentially communicated vaporizer 6 and generator 1 Generator 1 has the first condensed fluid passage and ft connection more afterwards, and the second generator 2 also has high temperature thermal medium passage to connect with outside Lead to, absorber 3 and the second condenser 5 also have heated medium passage and ft connection respectively, condenser 4 also has cooling medium to lead to Road 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 vaporizer 6 by the first steam channel and sends out Externally discharge after raw device 1 exothermic condensation, the second road is externally discharged after completing blood pressure lowering work done, form the dynamic co-feeding system of heat.
Heat shown in Fig. 3 is moved co-feeding system and is achieved in that
(1) in structure, it mainly by generator, the second generator, absorber, condenser, the second condenser, vaporizer, Choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator 1 has Concentrated solution pipeline is connected with the second generator 2 with the second solution heat exchanger 11 through solution pump 9, solution heat exchanger 10, and second Generator 2 also has concentrated solution pipeline to connect with absorber 3 through the second solution heat exchanger 11, and absorber 3 also has weak solution pipeline Connect with generator 1 through solution heat exchanger 10, generator 1 also has refrigerant steam channel to connect with condenser 4, the second generator 2 also have refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 8 and vaporizer 6 Connection, after the second condenser 5 also has cryogen liquid pipeline to connect with generator 1, generator 1 has cryogen liquid pipeline again through choke valve 7 Connect with vaporizer 6, vaporizer 6 also has refrigerant steam channel to connect with absorber 3, and engine 12 has live steam passage and outside to connect Logical, engine 12 also has exhaust passage and ft connection, engine 12 also have exhaust passage to connect with generator 1 after generator 1 has condensed fluid passage and ft connection again, and engine 12 finisher 6 that also the first steam channel is connected with vaporizer 6 is again There are the first condensed fluid passage and ft connection, the second generator 2 also has high temperature thermal medium passage and ft connection, absorber 3 He Second condenser 5 also has heated medium passage and ft connection respectively, and condenser 4 also has coolant guiding channel to connect with outside Logical.
(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 three tunnels 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 vaporizer 6 exothermic condensation, complete a part of steam discharge after blood pressure lowering work done be supplied to send out Raw device 1 exothermic condensation is simultaneously externally discharged, and completes another part steam discharge after blood pressure lowering work done and externally discharges, and forms the dynamic alliance system of heat System.
Heat shown in Fig. 4 is moved co-feeding system and is achieved in that
(1) in structure, it mainly by generator, the second generator, absorber, condenser, the second condenser, vaporizer, Choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator 1 has Concentrated solution pipeline is connected with the second generator 2 with the second solution heat exchanger 11 through solution pump 9, solution heat exchanger 10, and second Generator 2 also has concentrated solution pipeline to connect with absorber 3 through the second solution heat exchanger 11, and absorber 3 also has weak solution pipeline Connect with generator 1 through solution heat exchanger 10, generator 1 also has refrigerant steam channel to connect with condenser 4, the second generator 2 also have refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 8 and vaporizer 6 Connection, after the second condenser 5 also has cryogen liquid pipeline to connect with generator 1, generator 1 has cryogen liquid pipeline again through choke valve 7 Connect with vaporizer 6, vaporizer 6 also has refrigerant steam channel to connect with absorber 3, engine 12 has live steam passage respectively with outward Portion connect and have exhaust passage and ft connection, engine 12 also have the first steam channel connect with generator 1 after generator 1 There are the first condensed fluid passage and ft connection again, engine 12 also has the finisher 6 that the second steam channel is connected with vaporizer 6 There are the second condensed fluid passage and ft connection again, the second generator 2 also has high temperature thermal medium passage and ft connection, absorber 3 Also there are heated medium passage and ft connection with the second condenser 5 respectively, condenser 4 also has coolant guiding channel to connect with outside Logical.
(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 vaporizer 6 and through the first steam channel through the second steam channel respectively It is supplied to generator 1, remaining steam continues to complete work done and externally discharges；After first steam flows through generator 1 exothermic condensation Externally discharge, the second steam is externally discharged after flowing through vaporizer 6 exothermic condensation, form the dynamic co-feeding system of heat.
Heat shown in Fig. 5 is moved co-feeding system and is achieved in that
(1) in structure, heat shown in Fig. 3 is moved in co-feeding system, increases the 3rd generator, the second absorber, second molten Liquid pump and the 3rd solution heat exchanger, generator 1 is had concentrated solution pipeline molten through solution pump 9, solution heat exchanger 10 and second Liquid heat exchanger 11 is connected with the second generator 2 and is adjusted to generator 1 and has concentrated solution pipeline through solution pump 9, solution heat exchanger 10 are connected with the second absorber 14 with the second solution heat exchanger 11, and the second absorber 14 has weak solution pipeline again through the second solution Pump 15 is connected with the second generator 2 with the 3rd solution heat exchanger 16, and the second generator 2 is had concentrated solution pipeline through the second solution Heat exchanger 11 is connected with absorber 3 and is adjusted to the second generator 2 and has concentrated solution pipeline through the 3rd solution heat exchanger 16 and Three generators 13 connect, and the 3rd generator 13 has concentrated solution pipeline to connect with absorber 3 through the second solution heat exchanger 11 again, the Three generators 13 also have refrigerant steam channel to connect with the second absorber 14, the 3rd generator 13 also have high temperature thermal medium passage and Ft connection, the second absorber 14 also has heated medium passage and ft connection.
(2), in flow process, the concentrated solution of generator 1 is through solution pump 9, solution heat exchanger 10 and the second solution heat exchanger 11 Enter the second absorber 14, absorb refrigerant vapour and heat release is in heated medium, the weak solution of the second absorber 14 is molten through second Liquid pump 15 and the 3rd solution heat exchanger 16 enter the second generator 2, and the concentrated solution of the second generator 2 is through the 3rd solution heat exchange Device 16 enters the 3rd generator 13, and high temperature thermal medium flows through the 3rd generator 13, heating enters its interior solution release cryogen and steams Vapour simultaneously provides to the second absorber 14, and the concentrated solution of the 3rd generator 13 enters absorber 3, shape through the second solution heat exchanger 11 Become the dynamic co-feeding system of heat.
Heat shown in Fig. 6 is moved co-feeding system and is achieved in that
(1) in structure, heat shown in Fig. 3 is moved in co-feeding system, increases the 3rd generator, the second absorber, second molten Liquid pump and the 3rd solution heat exchanger, the second generator 2 are had refrigerant steam channel to connect with the second condenser 5 and are adjusted to second Generator 2 has refrigerant steam channel to connect with the second absorber 14, and the second absorber 14 also has weak solution pipeline through the second solution Pump 15 is connected with the 3rd generator 13 with the 3rd solution heat exchanger 16, and the 3rd generator 13 also has concentrated solution pipeline molten through the 3rd Liquid heat exchanger 16 is connected with the second absorber 14, and the 3rd generator 13 also has refrigerant steam channel to connect with the second condenser 5, 3rd generator 13 also has high temperature thermal medium passage and ft connection, and the second absorber 14 also has heated medium passage and outside Connection.
(2) in flow process, the second generator 2 produce refrigerant vapour enter the second absorber 14, the second absorber 14 dilute Solution enters the 3rd generator 13 through the second solution pump 15 and the 3rd solution heat exchanger 16, and high temperature thermal medium flows through the 3rd generation Device 13, heating enter its interior solution release refrigerant vapour and provide to the second condenser 5, the concentrated solution warp of the 3rd generator 13 3rd solution heat exchanger 16 enters the second absorber 14, absorbs refrigerant vapour and heat release is in heated medium, forms the dynamic connection of heat For system.
Heat shown in Fig. 7 is moved co-feeding system and is achieved in that
(1), in structure, the heat shown in Fig. 3 is moved in co-feeding system, cancels choke valve, the second condenser 5 is had cryogen liquid Pipeline connect with generator 1 after generator 1 have cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7 again to be adjusted to second cold After condenser 5 has cryogen liquid pipeline to connect with generator 1, generator 1 has cryogen liquid pipeline to connect with vaporizer 6 again；Increase the 3rd Generator, the second solution pump, the 3rd solution heat exchanger and heater, generator 1 sets up concentrated solution pipeline through the second solution pump 15th, solution heat exchanger 10 is connected with the 3rd generator 13 with the 3rd solution heat exchanger 16, and the 3rd generator 13 also has dense molten Liquid pipeline is connected with absorber 3 through the 3rd solution heat exchanger 16, and the second generator 2 is had refrigerant steam channel and the second condensation Device 5 connection is adjusted to the 3rd generator 13 after the second generator 2 has refrigerant steam channel to connect with the 3rd generator 13 to be had again Cryogen liquid pipeline is connected with vaporizer 6 with generator 1 through heater 18, and the 3rd generator 13 also has refrigerant steam channel and second Condenser 5 connects, and heater 18 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that the second generator 2 produces is supplied to the 3rd generator 13 and makees to drive thermal medium, sends out The part concentrated solution of raw device 1 enters the 3rd through the second solution pump 15, solution heat exchanger 10 and the 3rd solution heat exchanger 16 Raw device 13, refrigerant vapour flows through the 3rd generator 13, heating enters its interior solution and discharges refrigerant vapour and to the second condenser 5 There is provided, the concentrated solution of the 3rd generator 13 enters absorber 3 through the 3rd solution heat exchanger 16；Flow through the cold of the 3rd generator 13 Agent steam heat release becomes cryogen liquid, and cryogen liquor stream through heater 18 and generator 1 and progressively enters vaporizer 6 after heat release, and second The cryogen liquor stream of condenser 5 enters vaporizer 6 through generator 1 heat release and after blood pressure lowering, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 8 is moved co-feeding system and is achieved in that
(1), in structure, the heat shown in Fig. 3 is moved in co-feeding system, and the heat shown in Fig. 8 is moved co-feeding system and is realized in :
(1), in structure, heat shown in Fig. 3 is moved in co-feeding system, increase the 3rd generator, the 3rd solution heat exchanger, Second throttle and heater, generator 1 is had concentrated solution pipeline through solution pump 9, solution heat exchanger 10 and the second solution heat Exchanger 11 connect with the second generator 2 be adjusted to generator 1 have concentrated solution pipeline through solution pump 9, solution heat exchanger 10, Two solution heat exchangers 11 are connected with the second generator 2 with the 3rd solution heat exchanger 16, and the second generator 2 is had concentrated solution pipe Road the second solution heat exchanger 11 connect with absorber 3 be adjusted to the second generator 2 have concentrated solution pipeline through the 3rd solution heat Exchanger 16 is connected with the 3rd generator 13, and the 3rd generator 13 has concentrated solution pipeline again through the second solution heat exchanger 11 and suction Receive device 3 to connect, the second generator 2 is had refrigerant steam channel to connect with the second condenser 5 and is adjusted to the second generator 2 and has cryogen Steam channel connect with the 3rd generator 13 after the 3rd generator 13 have again cryogen liquid pipeline through heater 18, generator 1 and Second throttle 17 is connected with vaporizer 6, and the 3rd generator 13 also has refrigerant steam channel to connect with the second condenser 5, heat supply Device 18 also has heated medium passage and ft connection, and the 3rd generator 13 also has high temperature thermal medium passage and ft connection.
(2), in flow process, the refrigerant vapour of high temperature thermal medium and the second generator 2 generation is supplied to the 3rd generator 13 and drives Dynamic thermal medium, the concentrated solution of generator 1 is through solution pump 9, solution heat exchanger 10, the second solution heat exchanger 11 and the 3rd solution Heat exchanger 16 enters the second generator 2, and the concentrated solution of the second generator 2 enters the 3rd generation through the 3rd solution heat exchanger 16 Device 13, high temperature thermal medium and refrigerant vapour stream enter its interior solution release refrigerant vapour through the 3rd generator 13, heating respectively And provide to the second condenser 5, the concentrated solution of the 3rd generator 13 enters absorber 3 through the second solution heat exchanger 11；Flow through The refrigerant vapour heat release of the 3rd generator 13 becomes cryogen liquid, cryogen liquor stream through heater 18 and generator 1 and progressively heat release, afterwards Enter vaporizer 6 through second throttle 17 reducing pressure by regulating flow, form the dynamic co-feeding system of heat.
Heat shown in Fig. 9 is moved co-feeding system and is achieved in that
(1) in structure, heat shown in Fig. 3 is moved in co-feeding system, increases the 3rd generator, the second solution pump, the 3rd molten Liquid heat exchanger, second throttle and heater, generator 1 is had concentrated solution pipeline through solution pump 9, solution heat exchanger 10 and Second solution heat exchanger 11 connect with the second generator 2 be adjusted to generator 1 have concentrated solution pipeline through solution pump 9, solution heat Exchanger 10 is connected with the 3rd generator 13 with the second solution heat exchanger 11, and the 3rd generator 13 has concentrated solution pipeline again through Two solution pumps 15 are connected with the second generator 2 with the 3rd solution heat exchanger 16, and the second generator 2 is had concentrated solution pipeline through Two solution heat exchangers 11 are connected with absorber 3 and are adjusted to the second generator 2 and have concentrated solution pipeline through the 3rd solution heat exchanger 16 are connected with absorber 3 with the second solution heat exchanger 11, and the second generator 2 is had refrigerant steam channel and the second condenser 5 Connection is adjusted to the 3rd generator 13 after the second generator 2 has refrigerant steam channel to connect with the 3rd generator 13 cryogen again Liquid pipeline is connected with vaporizer 6 with second throttle 17 through heater 18, generator 1, and the 3rd generator 13 also has refrigerant vapour Passage is connected with the second condenser 5, and heater 18 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that the second generator 2 produces is supplied to the 3rd generator 13 and makees to drive thermal medium, sends out The concentrated solution of raw device 1 enters the 3rd generator 13 through solution pump 9, solution heat exchanger 10 and the second solution heat exchanger 11, cold Agent steam flows through the 3rd generator 13, heating enters its interior solution release refrigerant vapour and provides to the second condenser 5, the 3rd The concentrated solution of generator 13 enters the second generator 2, the second generator 2 through the second solution pump 15 and the 3rd solution heat exchanger 16 Concentrated solution enter absorber 3 through the 3rd solution heat exchanger 16 and the second solution heat exchanger 11；Flow through the 3rd generator 13 Refrigerant vapour heat release become cryogen liquid, cryogen liquor stream through heater 18 and generator 1 and progressively heat release, after through second throttle 17 reducing pressure by regulating flows enter vaporizer 6, form the dynamic co-feeding system of heat.
Heat shown in Figure 10 is moved co-feeding system and is achieved in that
(1) in structure, heat shown in Fig. 3 is moved in co-feeding system, increases the 3rd generator, the second absorber, second molten Liquid pump and the 3rd solution heat exchanger, generator 1 is had concentrated solution pipeline molten through solution pump 9, solution heat exchanger 10 and second Liquid heat exchanger 11 is connected with the second generator 2 and is adjusted to generator 1 and has concentrated solution pipeline through solution heat exchanger 10 and second Absorber 14 connects, and the second absorber 14 has weak solution pipeline again through solution pump 9 and the second solution heat exchanger 11 and second Raw device 2 connects, and the second generator 2 is had concentrated solution pipeline to connect with absorber 3 through the second solution heat exchanger 11 and is adjusted to the Two generators 2 have concentrated solution pipeline to connect with the 3rd generator 13 through the second solution heat exchanger 11, and the 3rd generator 13 has again Concentrated solution pipeline is connected with absorber 3 with the 3rd solution heat exchanger 16 through the second solution pump 15, and absorber 3 is had weak solution pipe Road is connected with generator 1 through solution heat exchanger 10 and is adjusted to absorber 3 and has weak solution pipeline through the 3rd solution heat exchanger 16 Connect with generator 1 with solution heat exchanger 10, occur after the second condenser 5 is had cryogen liquid pipeline to connect with generator 1 Device 1 has cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7 to be adjusted to the second condenser 5 and have cryogen liquid pipeline through generator 1 again After connecting with the 3rd generator 13, the 3rd generator 13 has cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7 again, by power After machine 12 has exhaust passage to connect with generator 1, generator 1 has condensed fluid passage and ft connection to be adjusted to engine 12 again After having exhaust passage to connect with the 3rd generator 13 through generator 1, the 3rd generator 13 has condensed fluid passage and outside to connect again Logical, the 3rd generator 13 also has refrigerant steam channel to connect with the second absorber 14, and the second absorber 14 also has cooling medium to lead to Road and ft connection.
(2), in flow process, live steam is divided into three tunnels after entering engine 12 blood pressure lowering work done, and the steam with elevated pressures passes through First steam channel is externally discharged after being supplied to vaporizer 6 exothermic condensation, completes a part of steam discharge after blood pressure lowering work done and carries Supply generator 1 and the 3rd generator 13 exothermic condensation and externally discharge, complete another part steam discharge pair after blood pressure lowering work done Outer discharge；The cryogen liquor stream of the second condenser 5, through generator 1 and the 3rd generator 13 progressively heat release, saves through choke valve 7 afterwards Stream blood pressure lowering enters vaporizer 6；The concentrated solution of generator 1 enters the second absorber 14, absorbs cryogen steaming through solution heat exchanger 10 Vapour heat release enter second in cooling medium, the weak solution of the second absorber 14 through solution pump 9 and the second solution heat exchanger 11 Generator 2；The concentrated solution of the second generator 2 enters the 3rd generator 13, heat absorption release cryogen through the second solution heat exchanger 11 Steam simultaneously provides to the second absorber 14, and the concentrated solution of the 3rd generator 13 is through the second solution pump 15 and the 3rd solution heat exchanger 16 entrance absorbers 3, the weak solution of absorber 3 enters generator 1 through the 3rd solution heat exchanger 16 and solution heat exchanger 10, Form the dynamic co-feeding system of heat.
Heat shown in Figure 11 is moved co-feeding system and is achieved in that
(1), in structure, the heat shown in Fig. 3 is moved in co-feeding system, increases preheater, condenser 4 is had cryogen liquid pipeline Connect with vaporizer 6 through cryogen liquid pump 8 and be adjusted to condenser 4 and have cryogen liquid pipeline through cryogen liquid pump 8 and preheater 19 and evaporation Device 6 connects, by generator 1 have condensed fluid passage and ft connection be adjusted to generator 1 have the preheated device of condensed fluid passage 19 with Ft connection.
(2), in flow process, the cryogen liquor stream of condenser 4 is boosted through cryogen liquid pump 8, flows through preheater 19 and absorbs heat, laggard Enter vaporizer 6；The part steam discharge of engine 12 flows through generator 1 heat release and condenses, and condensed fluid flows through preheater 19 heat release, it Externally discharge afterwards, form the dynamic co-feeding system of heat.
Heat shown in Figure 12 is moved co-feeding system and is achieved in that
Heat shown in Fig. 3 is moved in co-feeding system, cancels the second generator 2 and the high temperature thermal medium passage connecting, power The second generator 2 after high-temperature steam passage is connected set up with the second generator 2 by machine 12 high temperature condensed fluid passage and outside again Connection；Engine 12 passes through high-temperature steam passage respectively to be provided high temperature driven thermic load, passes through the first steam to the second generator 2 Passage provides low temperature thermic load and by exhaust passage to generator 1 offer low temperature thermic load to vaporizer 6, forms the dynamic alliance of heat System.
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 engine steam discharge, the first steam and the second steam channel, individually or respectively to vaporizer and generator provide Low temperature thermic load, and combine generator and condenser, realize Steam Power Equipment end steam discharge or low-pressure pumping steam and cold environment it Between the temperature difference effectively utilizes.
(3) release cleaning or high efficient energy sources and move the application restriction in co-feeding system in conventional thermal.
(4) with engine end steam for the dynamic alliance low-temperature heat source of heat, be conducive to improving the thermal efficiency and the equipment of engine The safety running.
(5) enrich the type of the dynamic co-feeding system of heat, extend the range of application of absorption heat pump, be conducive to preferably adopting Improve heat utilization rate with absorption heat pump technology.

Claims (21)

1. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, condenser, the second condenser, vaporizer, section Stream valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator (1) has Concentrated solution pipeline is through solution pump (9), solution heat exchanger (10) and the second solution heat exchanger (11) with the second generator (2) even Logical, the second generator (2) also has concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (11), absorber (3) Also have weak solution pipeline to connect with generator (1) through solution heat exchanger (10), generator (1) also refrigerant steam channel with cold Condenser (4) connects, and the second generator (2) also has refrigerant steam channel to connect with the second condenser (5), and condenser (4) is also cold Agent liquid pipeline is connected with vaporizer (6) through cryogen liquid pump (8), and the second condenser (5) also has cryogen liquid pipeline with generator (1) even After logical, generator (1) has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) again, and vaporizer (6) also has refrigerant vapour Passage is connected with absorber (3), and engine (12) has live steam passage and a ft connection, engine (12) or also exhaust passage with Ft connection, after engine (12) also has exhaust passage to be sequentially communicated vaporizer (6) and generator (1), generator (1) has again Condensed fluid passage and ft connection, the second generator (2) also has high temperature thermal medium passage and ft connection, absorber (3) and the Two condensers (5) also have heated medium passage and ft connection respectively, and condenser (4) also has coolant guiding channel to connect with outside Logical, form the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, condenser, the second condenser, vaporizer, section Stream valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator (1) has Concentrated solution pipeline is through solution pump (9), solution heat exchanger (10) and the second solution heat exchanger (11) with the second generator (2) even Logical, the second generator (2) also has concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (11), absorber (3) Also have weak solution pipeline to connect with generator (1) through solution heat exchanger (10), generator (1) also refrigerant steam channel with cold Condenser (4) connects, and the second generator (2) also has refrigerant steam channel to connect with the second condenser (5), and condenser (4) is also cold Agent liquid pipeline is connected with vaporizer (6) through cryogen liquid pump (8), and the second condenser (5) also has cryogen liquid pipeline with generator (1) even After logical, generator (1) has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) again, and vaporizer (6) also has refrigerant vapour Passage is connected with absorber (3), and engine (12) has live steam passage and ft connection respectively and has exhaust passage and ft connection, Engine (12) also have the first steam channel be sequentially communicated vaporizer (6) and generator (1) afterwards generator (1) have again first cold Lime set passage and ft connection, the second generator (2) also has high temperature thermal medium passage and ft connection, absorber (3) and second Condenser (5) also has heated medium passage and ft connection respectively, and condenser (4) also has coolant guiding channel to connect with outside Logical, form the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, condenser, the second condenser, vaporizer, section Stream valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator (1) has Concentrated solution pipeline is through solution pump (9), solution heat exchanger (10) and the second solution heat exchanger (11) with the second generator (2) even Logical, the second generator (2) also has concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (11), absorber (3) Also have weak solution pipeline to connect with generator (1) through solution heat exchanger (10), generator (1) also refrigerant steam channel with cold Condenser (4) connects, and the second generator (2) also has refrigerant steam channel to connect with the second condenser (5), and condenser (4) is also cold Agent liquid pipeline is connected with vaporizer (6) through cryogen liquid pump (8), and the second condenser (5) also has cryogen liquid pipeline with generator (1) even After logical, generator (1) has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) again, and vaporizer (6) also has refrigerant vapour Passage is connected with absorber (3), and engine (12) has live steam passage and a ft connection, engine (12) or also exhaust passage with Ft connection, after engine (12) also has exhaust passage to connect with generator (1), generator (1) has condensed fluid passage again with outward Portion connects, and engine (12) also has the finisher (6) that the first steam channel is connected with vaporizer (6) to have the first condensed fluid to lead to again Road and ft connection, the second generator (2) also has high temperature thermal medium passage and ft connection, absorber (3) and the second condenser (5) also there are heated medium passage and ft connection respectively, condenser (4) also has coolant guiding channel and ft connection, formed The dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, condenser, the second condenser, vaporizer, section Stream valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator (1) has Concentrated solution pipeline is through solution pump (9), solution heat exchanger (10) and the second solution heat exchanger (11) with the second generator (2) even Logical, the second generator (2) also has concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (11), absorber (3) Also have weak solution pipeline to connect with generator (1) through solution heat exchanger (10), generator (1) also refrigerant steam channel with cold Condenser (4) connects, and the second generator (2) also has refrigerant steam channel to connect with the second condenser (5), and condenser (4) is also cold Agent liquid pipeline is connected with vaporizer (6) through cryogen liquid pump (8), and the second condenser (5) also has cryogen liquid pipeline with generator (1) even After logical, generator (1) has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) again, and vaporizer (6) also has refrigerant vapour Passage is connected with absorber (3), and engine (12) has live steam passage and ft connection respectively and has exhaust passage and ft connection, After engine (12) also has the first steam channel to connect with generator (1), generator (1) has the first condensed fluid passage again with outward Portion connects, and engine (12) also has the finisher (6) that the second steam channel is connected with vaporizer (6) to have the second condensed fluid to lead to again Road and ft connection, the second generator (2) also has high temperature thermal medium passage and ft connection, absorber (3) and the second condenser (5) also there are heated medium passage and ft connection respectively, condenser (4) also has coolant guiding channel and ft connection, formed The dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Two absorbers, the second solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline through solution pump (9), solution Heat exchanger (10) is connected with the second generator (2) with the second solution heat exchanger (11) and is adjusted to generator (1) and has concentrated solution Pipeline is connected with the second absorber (14) with the second solution heat exchanger (11) through solution pump (9), solution heat exchanger (10), the Two absorbers (14) have weak solution pipeline again through the second solution pump (15) and the 3rd solution heat exchanger (16) and the second generator (2) connect, the second generator (2) is had concentrated solution pipeline to connect adjustment through the second solution heat exchanger (11) with absorber (3) Concentrated solution pipeline is had to connect with the 3rd generator (13) through the 3rd solution heat exchanger (16) for the second generator (2), the 3rd Raw device (13) has concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (11) again, and the 3rd generator (13) is also Refrigerant steam channel is had to connect with the second absorber (14), the 3rd generator (13) also has high temperature thermal medium passage to connect with outside Logical, the second absorber (14) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Two absorbers, the second solution pump and the 3rd solution heat exchanger, the second generator (2) is had refrigerant steam channel and the second condensation Device (5) connection is adjusted to the second generator (2) has refrigerant steam channel to connect with the second absorber (14), the second absorber (14) Weak solution pipeline is also had to connect with the 3rd generator (13) with the 3rd solution heat exchanger (16) through the second solution pump (15), the 3rd Generator (13) also has concentrated solution pipeline to connect with the second absorber (14) through the 3rd solution heat exchanger (16), the 3rd generator (13) refrigerant steam channel is also had to connect with the second condenser (5), the 3rd generator (13) also has high temperature thermal medium passage with outward Portion connects, and the second absorber (14) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, is that any hot described in claim 1-6 moves in co-feeding system, cancels choke valve, will occur Device (1) has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) to be adjusted to generator (1) and have cryogen liquid pipeline and evaporation Device (6) connects, and forms the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Two solution pumps, the 3rd solution heat exchanger, second throttle and heater, it is molten through second that concentrated solution pipeline set up by generator (1) Liquid pump (15), solution heat exchanger (10) are connected with the 3rd generator (13) with the 3rd solution heat exchanger (16), the 3rd generation Device (13) also has concentrated solution pipeline to connect with absorber (3) through the 3rd solution heat exchanger (16), the second generator (2) is had cold Agent steam channel is connected with the second condenser (5) and is adjusted to the second generator (2) and has refrigerant steam channel and the 3rd generator (13) after connecting, the 3rd generator (13) has cryogen liquid pipeline again through heater (18), generator (1) and second throttle (17) connect with vaporizer (6), the 3rd generator (13) also has refrigerant steam channel to connect with the second condenser (5), heater (18) also have heated medium passage and ft connection, form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three solution heat exchangers, second throttle and heater, generator (1) is had concentrated solution pipeline to hand over through solution pump (9), solution heat Parallel operation (10) is connected with the second generator (2) with the second solution heat exchanger (11) and is adjusted to generator (1) and has concentrated solution pipeline Through solution pump (9), solution heat exchanger (10), the second solution heat exchanger (11) and the 3rd solution heat exchanger (16) and second Generator (2) connects, and the second generator (2) is had concentrated solution pipeline through the second solution heat exchanger (11) with absorber (3) even Logical be adjusted to the second generator (2) and have concentrated solution pipeline to connect with the 3rd generator (13) through the 3rd solution heat exchanger (16), 3rd generator (13) has concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (11) again, and second is occurred Device (2) has refrigerant steam channel to connect with the second condenser (5) to be adjusted to the second generator (2) and have refrigerant steam channel and the 3rd After generator (13) connection, the 3rd generator (13) has cryogen liquid pipeline again through heater (18), generator (1) and second section Stream valve (17) is connected with vaporizer (6), and the 3rd generator (13) also has refrigerant steam channel to connect with the second condenser (5), supplies Hot device (18) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Two solution pumps, the 3rd solution heat exchanger, second throttle and heater, generator (1) is had concentrated solution pipeline through solution pump (9), solution heat exchanger (10) is connected with the second generator (2) with the second solution heat exchanger (11) and is adjusted to generator (1) There is concentrated solution pipeline through solution pump (9), solution heat exchanger (10) and the second solution heat exchanger (11) and the 3rd generator (13) connect, the 3rd generator (13) have concentrated solution pipeline through the second solution pump (15) and the 3rd solution heat exchanger (16) again and Second generator (2) connects, and the second generator (2) is had concentrated solution pipeline through the second solution heat exchanger (11) and absorber (3) connection is adjusted to the second generator (2) has concentrated solution pipeline through the 3rd solution heat exchanger (16) and the second solution heat exchange Device (11) is connected with absorber (3), the second generator (2) is had refrigerant steam channel to connect with the second condenser (5) and is adjusted to After second generator (2) has refrigerant steam channel to connect with the 3rd generator (13), the 3rd generator (13) has cryogen liquid pipe again Road is connected with vaporizer (6) with second throttle (17) through heater (18), generator (1), and the 3rd generator (13) is also cold Agent steam channel is connected with the second condenser (5), and heater (18) also has heated medium passage and ft connection, forms heat dynamic Co-feeding system.
The dynamic co-feeding system of 11. heat, is that any hot described in claim 8-10 moves in co-feeding system, the 3rd generator (13) increases If high temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 12. heat, is that any hot described in claim 8-11 moves in co-feeding system, cancels choke valve and second Choke valve, generator (1) is had cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) and is adjusted to generator (1) and has cryogen Liquid pipeline is connected with vaporizer (6), and generator (1) is had cryogen liquid pipeline to connect with vaporizer (6) through second throttle (17) Being adjusted to generator (1) has cryogen liquid pipeline to connect with vaporizer (6), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 13. heat, is that the heat described in claim 1 is moved in co-feeding system, increases the 3rd generator, the second absorption Device, the second solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline through solution pump (9), solution heat exchange Device (10) is connected with the second generator (2) with the second solution heat exchanger (11) and is adjusted to generator (1) and has concentrated solution pipeline warp Solution heat exchanger (10) is connected with the second absorber (14), and the second absorber (14) has weak solution pipeline again through solution pump (9) Connect with the second generator (2) with the second solution heat exchanger (11), the second generator (2) is had concentrated solution pipeline molten through second Liquid heat exchanger (11) is connected with absorber (3) and is adjusted to the second generator (2) and has concentrated solution pipeline through the second solution heat exchange Device (11) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline again through the second solution pump (15) and the 3rd Solution heat exchanger (16) is connected with absorber (3), and absorber (3) is had weak solution pipeline through solution heat exchanger (10) and to send out Raw device (1) connection is adjusted to absorber (3) has weak solution pipeline through the 3rd solution heat exchanger (16) and solution heat exchanger (10) connect with generator (1), after the second condenser (5) is had cryogen liquid pipeline to connect with generator (1), generator (1) is again There is cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) to be adjusted to the second condenser (5) and have cryogen liquid pipeline through generator (1) after connecting with the 3rd generator (13), the 3rd generator (13) has cryogen liquid pipeline again through choke valve (7) and vaporizer (6) Connection, after engine (12) is had exhaust passage to be sequentially communicated vaporizer (6) and generator (1), generator (1) has condensation again Liquid passage and ft connection are adjusted to engine (12) has exhaust passage to be sequentially communicated vaporizer (6), generator (1) and the 3rd After raw device (13), the 3rd generator (13) has condensed fluid passage and ft connection again, and the 3rd generator (13) also has refrigerant vapour Passage is connected with the second absorber (14), and the second absorber (14) also has coolant guiding channel and ft connection, forms the dynamic connection of heat For system.
The dynamic co-feeding system of 14. heat, is that the heat described in claim 2 is moved in co-feeding system, increases the 3rd generator, the second absorption Device, the second solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline through solution pump (9), solution heat exchange Device (10) is connected with the second generator (2) with the second solution heat exchanger (11) and is adjusted to generator (1) and has concentrated solution pipeline warp Solution heat exchanger (10) is connected with the second absorber (14), and the second absorber (14) has weak solution pipeline again through solution pump (9) Connect with the second generator (2) with the second solution heat exchanger (11), the second generator (2) is had concentrated solution pipeline molten through second Liquid heat exchanger (11) is connected with absorber (3) and is adjusted to the second generator (2) and has concentrated solution pipeline through the second solution heat exchange Device (11) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline again through the second solution pump (15) and the 3rd Solution heat exchanger (16) is connected with absorber (3), and absorber (3) is had weak solution pipeline through solution heat exchanger (10) and to send out Raw device (1) connection is adjusted to absorber (3) has weak solution pipeline through the 3rd solution heat exchanger (16) and solution heat exchanger (10) connect with generator (1), after the second condenser (5) is had cryogen liquid pipeline to connect with generator (1), generator (1) is again There is cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) to be adjusted to the second condenser (5) and have cryogen liquid pipeline through generator (1) after connecting with the 3rd generator (13), the 3rd generator (13) has cryogen liquid pipeline again through choke valve (7) and vaporizer (6) Connection, after engine (12) is had the first steam channel to be sequentially communicated vaporizer (6) and generator (1), generator (1) has again First condensed fluid passage and ft connection are adjusted to engine (12) has the first steam channel to be sequentially communicated vaporizer (6), occur After device (1) and the 3rd generator (13), the 3rd generator (13) has the first condensed fluid passage and ft connection again, the 3rd generation Device (13) also has refrigerant steam channel to connect with the second absorber (14), and the second absorber (14) also has coolant guiding channel with outward Portion connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, is that the heat described in claim 3 is moved in co-feeding system, increases the 3rd generator, the second absorption Device, the second solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline through solution pump (9), solution heat exchange Device (10) is connected with the second generator (2) with the second solution heat exchanger (11) and is adjusted to generator (1) and has concentrated solution pipeline warp Solution heat exchanger (10) is connected with the second absorber (14), and the second absorber (14) has weak solution pipeline again through solution pump (9) Connect with the second generator (2) with the second solution heat exchanger (11), the second generator (2) is had concentrated solution pipeline molten through second Liquid heat exchanger (11) is connected with absorber (3) and is adjusted to the second generator (2) and has concentrated solution pipeline through the second solution heat exchange Device (11) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline again through the second solution pump (15) and the 3rd Solution heat exchanger (16) is connected with absorber (3), and absorber (3) is had weak solution pipeline through solution heat exchanger (10) and to send out Raw device (1) connection is adjusted to absorber (3) has weak solution pipeline through the 3rd solution heat exchanger (16) and solution heat exchanger (10) connect with generator (1), after the second condenser (5) is had cryogen liquid pipeline to connect with generator (1), generator (1) is again There is cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) to be adjusted to the second condenser (5) and have cryogen liquid pipeline through generator (1) after connecting with the 3rd generator (13), the 3rd generator (13) has cryogen liquid pipeline again through choke valve (7) and vaporizer (6) Connection, after engine (12) is had exhaust passage to connect with generator (1), generator (1) has condensed fluid passage and outside to connect again Lead to and be adjusted to the 3rd generator (13) after engine (12) has exhaust passage to connect with the 3rd generator (13) through generator (1) There are condensed fluid passage and ft connection again, the 3rd generator (13) also has refrigerant steam channel to connect with the second absorber (14), Second absorber (14) also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 16. heat, is that the heat described in claim 4 is moved in co-feeding system, increases the 3rd generator, the second absorption Device, the second solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline through solution pump (9), solution heat exchange Device (10) is connected with the second generator (2) with the second solution heat exchanger (11) and is adjusted to generator (1) and has concentrated solution pipeline warp Solution heat exchanger (10) is connected with the second absorber (14), and the second absorber (14) has weak solution pipeline again through solution pump (9) Connect with the second generator (2) with the second solution heat exchanger (11), the second generator (2) is had concentrated solution pipeline molten through second Liquid heat exchanger (11) is connected with absorber (3) and is adjusted to the second generator (2) and has concentrated solution pipeline through the second solution heat exchange Device (11) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline again through the second solution pump (15) and the 3rd Solution heat exchanger (16) is connected with absorber (3), and absorber (3) is had weak solution pipeline through solution heat exchanger (10) and to send out Raw device (1) connection is adjusted to absorber (3) has weak solution pipeline through the 3rd solution heat exchanger (16) and solution heat exchanger (10) connect with generator (1), after the second condenser (5) is had cryogen liquid pipeline to connect with generator (1), generator (1) is again There is cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) to be adjusted to the second condenser (5) and have cryogen liquid pipeline through generator (1) after connecting with the 3rd generator (13), the 3rd generator (13) has cryogen liquid pipeline again through choke valve (7) and vaporizer (6) Connection, after engine (12) is had the first steam channel to connect with generator (1), generator (1) has the first condensed fluid passage again It is adjusted to after engine (12) has the first steam channel to connect with the 3rd generator (13) through generator (1) with ft connection Three generators (13) have the first condensed fluid passage and ft connection again, and the 3rd generator (13) also has refrigerant steam channel and second Absorber (14) connects, and the second absorber (14) also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, is that the heat described in claim 4 is moved in co-feeding system, increases the 3rd generator, the second absorption Device, the second solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline through solution pump (9), solution heat exchange Device (10) is connected with the second generator (2) with the second solution heat exchanger (11) and is adjusted to generator (1) and has concentrated solution pipeline warp Solution heat exchanger (10) is connected with the second absorber (14), and the second absorber (14) has weak solution pipeline again through solution pump (9) Connect with the second generator (2) with the second solution heat exchanger (11), the second generator (2) is had concentrated solution pipeline molten through second Liquid heat exchanger (11) is connected with absorber (3) and is adjusted to the second generator (2) and has concentrated solution pipeline through the second solution heat exchange Device (11) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline again through the second solution pump (15) and the 3rd Solution heat exchanger (16) is connected with absorber (3), and absorber (3) is had weak solution pipeline through solution heat exchanger (10) and to send out Raw device (1) connection is adjusted to absorber (3) has weak solution pipeline through the 3rd solution heat exchanger (16) and solution heat exchanger (10) connect with generator (1), after the second condenser (5) is had cryogen liquid pipeline to connect with generator (1), generator (1) is again There is cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) to be adjusted to the second condenser (5) and have cryogen liquid pipeline through generator (1) after connecting with the 3rd generator (13), the 3rd generator (13) has cryogen liquid pipeline again through choke valve (7) and vaporizer (6) Connection, engine (12) is had exhaust passage and ft connection to be adjusted to engine (12) exhaust passage and the 3rd generator (13) after connecting, the 3rd generator (13) has condensed fluid passage and ft connection again, and the 3rd generator (13) also has refrigerant vapour Passage is connected with the second absorber (14), and the second absorber (14) also has coolant guiding channel and ft connection, forms the dynamic connection of heat For system；Wherein, or engine (12) sets up after exhaust passage is connected the 3rd generator (13) with the 3rd generator (13) again There are condensed fluid passage and ft connection.
The dynamic co-feeding systems of 18. heat, are that any hot described in claim 12-17 moves in co-feeding system, cancel choke valve, by the Three generators (13) have cryogen liquid pipeline to connect with vaporizer (6) through choke valve (7) to be adjusted to the 3rd generator (13) and have cryogen Liquid pipeline is connected with vaporizer (6), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, is that the heat described in claim 3 is moved in co-feeding system, increases preheater, by condenser (4) There is cryogen liquid pipeline to connect with vaporizer (6) through cryogen liquid pump (8) to be adjusted to condenser (4) and have cryogen liquid pipeline through cryogen liquid pump (8) connect with vaporizer (6) with preheater (19), generator (1) is had condensed fluid passage and ft connection to be adjusted to generator (1) there are the preheated device of condensed fluid passage (19) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 20. heat, is that any hot described in claim 1-19 moves in co-feeding system, cancels the second generator (2) with the high temperature thermal medium passage connecting, engine (12) is set up after high-temperature steam passage is connected with the second generator (2) Two generators (2) have high temperature condensed fluid passage and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, is that any hot described in claim 5-6 moves in co-feeding system, cancels the second generator (2) With the 3rd generator (13) the high temperature thermal medium passage with ft connection respectively, engine (12) sets up high-temperature steam passage successively After connecting the second generator (2) and the 3rd generator (13), the 3rd generator (13) has high temperature condensed fluid passage to connect with outside again Logical, form the dynamic co-feeding system of heat.
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