CN203159267U - High-efficiency energy-storing cold/heat/electricity/water multi-energy coproduction system - Google Patents
High-efficiency energy-storing cold/heat/electricity/water multi-energy coproduction system Download PDFInfo
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- CN203159267U CN203159267U CN2013201426002U CN201320142600U CN203159267U CN 203159267 U CN203159267 U CN 203159267U CN 2013201426002 U CN2013201426002 U CN 2013201426002U CN 201320142600 U CN201320142600 U CN 201320142600U CN 203159267 U CN203159267 U CN 203159267U
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- 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
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
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- 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
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/138—Water desalination using renewable energy
- Y02A20/141—Wind power
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/70—Wind energy
- Y02E10/72—Wind turbines with rotation axis in wind direction
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Abstract
The utility model provides a system for realizing cold/heat/electricity/water multi-energy coproduction by comprehensively using wind energy and seawater heat energy, which comprises a wind turbine device, a compressed air energy-storing device, a seawater desalting device and a ground source heat pump device. The cold/heat/electricity/water four-energy coproduction is realized by directly using abundant wind energy and seawater heat energy on islands and in remote coastal areas. Thus, in case of isolating from the land, self-sufficiency can be completely realized; and meanwhile, the system does not need the combustion of fossil fuel, and no greenhouse gas or pollution gas (such as sulfide, nitride and the like) is generated. According to the cold/heat/electricity/water multi-energy coproduction system provided by the utility model, mechanical energy obtained from wind by the wind turbine is converted into air internal energy through a compressor, and the energy is converted from mechanical energy into internal energy, which is similar to electrically-driven compressed air energy storage based on wind power generation; and meanwhile, equipment for power generation is omitted, thus having the characteristics of high energy conversion efficiency, simple structure, low investment, simple maintenance process and the like.
Description
Technical field
The utility model belongs to the comprehensive utilization field of renewable energy source, specifically relate to a kind of independent system at island and coastal remote districts comprehensive utilization wind energy and sea water heat energy realization cool and thermal power water tetrad product, to overcome the problem that island are difficult to concentrate energy supply, satisfy the basic life requirement that reaches remote coastland on the island.
Background technology
Along with human and social development, human step has been stepped on everywhere each corner on the ball, has entered since 21 century, economic development and the standard of living that continues constantly improves, and be human to water,, cold, the demand of heat is increasing, especially for some remote districts and island, can't obtain resource in this area, again since with the distance in continent, be difficult to rely on the continent obtain living in required water,, heat, the cold indispensable resource of life that waits.Simultaneously, the energy supply problem on island also affects the soldiers' that garrison on the island, national defence borderland quality of life always.Therefore, have only the new forms of energy that utilize each department fundamentally to overcome the above problems, and for island, generally have abundant wind energy resources and sea water heat energy resource.
Being subjected to the influence of global energy crisis and environmental degradation, is that the new energy development utilization of representative is subjected to the attention of most countries with the wind energy, and has worked out relevant incentive policy and measure one after another.Influenced by this, global wind energy development utilization obtains fast development.At present, the wind-power electricity generation rate of growth in the whole world is surprising, shows that according to the BTM statistic data global wind-powered electricity generation accumulative total in 2010 installed capacity reaches 199.5GW.China continues to keep wind power equipment production and the fast-developing vigorous pace of wind energy turbine set exploitation.Statistics according to Chinese renewable energy source wind energy Professional Committee of association (CWEA), China other areas except Taiwan Province increased 12904 of wind-powered electricity generation installations altogether newly in 2010, installed capacity reaches 18.93GW, continues to keep the rank of global adding new capacity first after 2009.
Yet there are instable characteristics in wind energy resources: wind speed changes often, the energy supply is unstable, has intermittence, fluctuation, also there is the problem of being incorporated into the power networks in wind power generation simultaneously, limited the development of wind-power electricity generation to a certain extent, therefore, unsettled wind energy and accumulator system need have been joined together effectively to utilize wind-resources.
In the long run/term, the development sea water desaltination, no matter it is from economically, still all more feasible from the environment.Stable, the cleaning in sea water desaltination water source is produced the water cost and is reduced gradually, has been subjected to more and more national, especially the attention of drought and water shortage country.In fact, worldwide general lack of water has made desalination technology desert area from middle-east expand to the main coastal cities in the whole world, and has formed production and sales and the sea water desalting equipment manufacturing two big industries of sea water desaltination water.Therefore, sea water desaltination has become global inexorable trend as a kind of technology at the new water source of exploitation beyond the question.Yet, the sea water desaltination big energy-consuming, greatly developing cheap renewable energy source and be used for sea water desaltination will be to solve the expensive important channel of sea water desaltination.
Method for desalting seawater is classified according to sepn process, can be divided into thermal process and membrane process two classes.Thermal process is to utilize heat energy to make evaporation of seawater, and the condensation by water vapor obtains fresh water again.Thermal process have multistage flash evaporation ((Multi Stage Flash, MSF), multi-effect distilling ((Multi Effect Distillation, ME), vapour compression (vapor Compression, VC) etc.; Membrane process then is to utilize separatory membrane to the selection perviousness of water and salt, and salinity is held back or removed, and obtains the method for fresh water.Membrane process have reverse osmosis method ((Reverse Osmosis, RO) and electrodialysis ((Electro DialysisED) etc.Method for desalting seawater relatively more commonly used at present mainly contains multistage flash evaporation (Multi-Stage Flash, MSF), low temperature multiple-effect distillation (Multiple Effect Distillation, MED) and reverse osmosis method (Reverse Osmosis, RO) etc. 3 kinds, wherein the multiple-effect distillation operational load can change from 40 one 110%, elasticity is bigger, can well combine with wind energy.
The present invention is directed to this problem, abundant wind energy and sea water heat energy on the comprehensive utilization island realizes that the tetrad of cool and thermal power water produces.
Summary of the invention
For overcoming the shortcoming and defect of prior art, the utility model provides a kind of cool and thermal power water polygenerations systeme that fully utilizes wind energy and sea water heat energy, directly utilize on the island and wind energy is enriched in remote coastland and sea water heat energy is realized tetrad product hot and cold, electric, water, be under the situation of land isolation, realized fully satisfying certainly, simultaneity factor does not need combustion of fossil fuels, does not produce dusty gass such as greenhouse gases and sulfide nitride.
The utility model is that the technical scheme that its technical problem of solution is taked is:
A kind of cool and thermal power water polygenerations systeme of high-efficiency energy-storage, wind energy and sea water heat energy on the comprehensive utilization island comprise wind energy conversion system device, compression air energy-storing apparatus, sea water desalinating plant, earth source heat pump device, it is characterized in that:
Described compression air energy-storing apparatus comprises stage compression unit, air storage chamber, multistage expansion unit, the generator that connects successively; Described sea water desalinating plant comprises seawater water fetching device, pretreating device, multistage well heater, multi-step evaporator, multi-stage condensing device, described multi-step evaporator comprises multistage central evaporator and finisher, and described multi-stage condensing device comprises multistage intermediate condenser and aftercondenser; Wherein:
Described wind energy conversion system device drives described stage compression unit;
Described earth source heat pump device is arranged between described seawater water fetching device and the pretreating device;
Described stage compression unit comprises some stage compressors, connect a central evaporator behind every stage compressor, the progression of central evaporator and the progression of compressor are complementary, and connect the last step central evaporator behind the first step compressor, connect first step central evaporator behind the last step compressor; The hot side of every grade of central evaporator feeds the pressurized gas that the respective stages compressor produces, and cold side imports the seawater that the upper level central evaporator is discharged, and the cold side of first step central evaporator imports the seawater of crossing through heater heats at different levels; The cold side connecting the sea water of last step well heater, hot side feeds the pressurized gas that first step central evaporator is discharged, and pressurized gas imports air storage chamber behind the last step well heater; The steam that central evaporator at different levels produce confluxes and enters the hot side of finisher, and the seawater that the last step central evaporator is discharged enters the cold side of finisher;
Described multistage expansion unit comprises some grades of decompressors, connect an intermediate condenser before every grade of decompressor, the progression of intermediate condenser and the progression of decompressor are complementary, and connect first step intermediate condenser before the first step decompressor, connect the last step intermediate condenser before the last step decompressor; The cold side of intermediate condensers at different levels leads to pressurized gas, the carbonated drink gas mixture that the logical condensation fresh water of hot side and water vapor are formed; Pressurized gas in the described air storage chamber enters first step decompressor behind the cold side of first step intermediate condenser, the hot side of last step intermediate condenser feeds the carbonated drink gas mixture of being derived by finisher; Described carbonated drink gas mixture enters first step intermediate condenser by the last step intermediate condenser successively, imports aftercondenser afterwards.
Further, the seawater to make heat exchange of the steam of the hot side of a finisher part and finisher cold side, a part imports the hot side of all the other well heaters at different levels except the last step well heater, with the seawater to make heat exchange of corresponding well heater cold side.
Further, the cold side of aftercondenser feeds the seawater through pre-treatment that pretreating device N discharges, hot side feeds water of condensation and the non-condensable gas that first step intermediate condenser is discharged, and the seawater part of intensification is returned pretreating device N, and a part enters well heaters at different levels.
Further, the strong brine of described sea water desalinating plant generation is discharged by finisher.
Further, the carbonated drink gas mixture of the condensation fresh water of described sea water desalinating plant generation and water vapor composition is discharged by aftercondenser.
Further, after the pressurized gas that air storage chamber stores reaches default pressure, high-pressure air is sent into the cold side of first step intermediate condenser.
Further, described wind energy conversion system device is by the described stage compression unit of an actuator drives, and described transmission mechanism is preferably wheel box.
Further, described wind energy conversion system device comprises at least one wind energy conversion system, and described wind energy conversion system is transverse axis or vertical axis windmill.
Further, described system also comprises store battery, and described generator is respectively to store battery and user's power supply.The principle of described store battery reduces discharging and recharging number of times under the prerequisite that satisfies system's operation demand, act as to regulate contradiction between compressed-air energy storage generating and the customer need.
Further, described sea water desalinating plant also comprises some water pumps that are arranged on the seawater pipeline, with thinking that pipeline fluid provides power.
Further, described earth source heat pump device comprises outdoor sea water heat energy heat-exchange system, earth source heat pump unit and indoor heating air conditioning terminal system, wherein: the seawater water intake conduit coupled arrangement of described outdoor sea water heat energy heat-exchange system and described seawater water fetching device, adopt ground configuration and seabed to arrange dual mode; Described indoor heating air conditioning terminal system need satisfy indoor heating, food, the oven dry effect of storings such as clothing.
Advantage of the present utility model and beneficial effect are:
1, the utility model adopts the direct utilization of wind energy, the mechanical energy that wind energy conversion system is obtained from wind is converted to air internal energy by compressor, conversion process of energy is that mechanical energy-Nei can, with respect to the driven by power compressed-air energy storage based on wind-power electricity generation, simultaneously owing to save power generation part equipment, have characteristics such as effciency of energy transfer height, simple in structure, reduced investment, maintenance are simple.Total system does not produce the material of any contaminate environment in the running engineering, be genuine environmental protection, energy conserving system.
2, the utility model adopts store battery and compressed-air energy storage generating coupling power supply, successfully solves the instability of wind energy and the contradiction of user power utilization.Compressed-air energy storage itself has the effect in certain peak clipping Pinggu, and store battery further cooperates with the compressed-air energy storage generating, further strengthens the effect in peak clipping Pinggu.
3, the utility model adopts the thought of earth source heat pump to combine with the sea water desaltination water fetching device, takes full advantage of the sea water heat energy resource, has simplified device simultaneously, saves cost.
4, compressed-air energy storage and desalting seawater through multi-effect evaporation coupled arrangement, isothermal compression and isothermal expansion process have been realized, optimized compressed-air energy-storage system, to compress simultaneously and expansion process in heat absorption and heat release and desalting seawater through multi-effect evaporation system evaporate and condensation combines cleverly, utilized low-grade heat energy to make fresh water.
5, the utility model has really been realized cold on the isolated island, heat, and electricity, water, Poly-generation is to have realized fully satisfying certainly under the situation that land isolates, and simultaneity factor does not need combustion of fossil fuels, do not produce dusty gass such as greenhouse gases and sulfide nitride.
6, the utility model is combined applied widelyly with wind energy conversion system, both can combine with wind energy turbine set, also can independently build production; Can unit group wind energy conversion system design also can the multimachine unitized design; Be suitable for wind resource than island and other coastlands of horn of plenty.
Description of drawings
Fig. 1 is the cool and thermal power water polygenerations systeme synoptic diagram of high-efficiency energy-storage of the present utility model.
Among the figure: A wind energy conversion system device, B transmission mechanism, C1～C3 compressor, D air storage chamber, E1～E3 decompressor, the F generator, G store battery, H1～H5 vaporizer, I1～I3 well heater, J1～J4 condenser, K1～K7 water pump, L earth source heat pump unit, M seawater water fetching device, N pretreating device.
Embodiment
For making the purpose of this utility model, technical scheme and advantage clearer, below with reference to the accompanying drawing embodiment that develops simultaneously, the utility model is further described.
For convenience described below, illustrate in advance at vaporizer, well heater all has heat transfer process in the condenser, heat exchange can adopt following current to arrange, counter-flow arrangement, cross-stream arranges that satisfying under the situation of works better, three kinds of modes all can adopt, will be not in the present embodiment heat exchanging mode carry out set forth in detail, all be reduced to " heat exchange ".
As shown in Figure 1, the cool and thermal power water polygenerations systeme of high-efficiency energy-storage of the present utility model, by A wind energy conversion system device, the B transmission mechanism, C1～C3 compressor, the D air storage chamber, E1～E3 decompressor, the F generator, the G store battery, H1～H5 vaporizer, I1～I3 well heater, J1～J4 condenser, K1～K7 water pump, L earth source heat pump unit, M seawater water fetching device, formations such as N pretreating device, compressor C1 is connected to horizontal-shaft wind turbine A by transmission mechanism B, air is through compressor C1 increasing temperature and pressure, enter vaporizer H3 and seawater and carry out heat exchange, return compressor C2 behind the air cooling-down, through entering vaporizer H2 after the compressor C2 increasing temperature and pressure, after lowering the temperature again, air returns compressor C3, continue increasing temperature and pressure through compressor C3, entering vaporizer H1 and seawater exchanges, then being fed through air storage chamber D by well heater I1 and seawater to make heat exchange stores, after air storage chamber D reaches certain pressure intensity, high-pressure air is sent into condenser J1 and water vapor carries out heat exchange, enter decompressor E1 expansion acting after the heating, decrease temperature and pressure enters condenser J2 and water vapor carries out heat exchange, the decompressor E2 acting of expanding of entering again after the heating, enter after the decrease temperature and pressure again condenser J3 and water vapor carries out heat exchange, enter decompressor E3 expansion acting after the heating again, enter atmosphere.Decompressor E1～E3 acting drives generator F generating, and the electricity that generator F sends is for customer need, and the surplus generation that while generator F sends is stored by store battery G, and when generator F generated energy was not enough, store battery G can replenish to the user and power.Earth source heat pump device L comprises outdoor ground energy heat-exchange system, earth source heat pump unit and indoor heating air conditioning terminal system, the seawater water fetching device M coupled arrangement of outdoor ground energy heat-exchange system and sea water desalinating plant, can adopt two kinds of decoration forms, a kind of employing ground configuration, the seawater water intaking is at first carried out heat exchange through outdoor ground energy heat-exchange system reach the earth source heat pump effect, the another kind of seabed decoration form that adopts, outdoor ground can heat-exchange system be combined with the seawater water intake conduit be arranged into the seabed, the indoor heating air conditioning terminal is can satisfy multiple user to the demand of cold and heat.Such as the indoor heating cooling, food, the oven dry effect of storings such as clothing.Earth source heat pump and seawater water intaking coupled arrangement simplify the structure, and have saved cost.Seawater enters pre-treatment N through earth source heat pump, after pressurizeing by water pump K7, the seawater of process pre-treatment enters condenser J4 and water vapor through the row heat exchange, a seawater part that heats up is returned pre-treatment N, a part enters well heater I1 through water pump K6 and water vapor carries out heat exchange, the seawater that heats up enters well heater I2 again and water vapor carries out heat exchange, the seawater that heats up continues to enter well heater I3 and high-pressure air carries out heat exchange, after raising again, seawater temperature enters vaporizer H1 and high-pressure air heat exchange, a seawater part is vaporizated into steam, a part enters vaporizer H2 through water pump K1 and continues and the high-pressure air heat exchange, a seawater part is vaporizated into steam, a part through water pump K2 enter vaporizer H3 again with the high-pressure air heat exchange, a seawater part is vaporizated into steam, a part enters vaporizer H4 and is that steam carries out heat exchange from vaporizer H1～H3 through water pump K3, a seawater part is vaporizated into steam, a part enters vaporizer H5 through water pump K4 and carries out heat exchange with the steam that comes from vaporizer H4, a seawater part is vaporizated into steam, part simmer down to strong brine removal system, a part through water pump K5 enter again vaporizer H5 circulation with from vaporizer H4 and the steam that comes through the row heat exchange.The steam that comes from vaporizer H1～H3 enters vaporizer H4 and seawater to make heat exchange carries out condensation, enter well heater I2 and seawater to make heat exchange condensation simultaneously, the water of condensation that obtains and not the carbonated drink gas mixture of condensing enter vaporizer H5, among vaporizer H5, carry out condensation with seawater to make heat exchange with the steam that comes from vaporizer H4, enter well heater I3 and seawater to make heat exchange condensation simultaneously, the water of condensation that obtains and not the carbonated drink gas mixture of condensing enter condenser J3, among condenser J3, carry out condensation with the high-pressure air heat exchange with the steam that comes from vaporizer H5, the water of condensation that obtains and not the carbonated drink gas mixture of condensing enter condenser J2 again and condensation is carried out in the high-pressure air heat exchange, the water of condensation that obtains and not the carbonated drink gas mixture of condensing enter condenser J1 again and condensation is carried out in the high-pressure air heat exchange, the water of condensation that obtains and not the carbonated drink gas mixture of condensing enter condenser J4 at last and carry out heat exchange with the seawater that comes from pre-treatment, finally obtain fresh water and condensing not.
The above only is preferred embodiment of the present utility model, and is in order to limit the utility model, not all within spirit of the present utility model and principle, any modification of making, is equal to replacement, improvement etc., all should be included within the scope of the present utility model.
Claims (10)
1. the cool and thermal power water polygenerations systeme of a high-efficiency energy-storage fully utilizes wind energy and sea water heat energy on the island, comprises wind energy conversion system device (A), compression air energy-storing apparatus, sea water desalinating plant, earth source heat pump device, it is characterized in that:
Described compression air energy-storing apparatus comprises successively the stage compression unit that connects (C1～C3), air storage chamber (D), multistage expansion unit (E1～E3), generator (F); Described sea water desalinating plant comprises seawater water fetching device (M), pretreating device (N), multistage well heater (I1～I3), multi-step evaporator (H1～H5), multi-stage condensing device (J1～J4), described multi-step evaporator (H1～H5) comprise multistage central evaporator (H1～H3) and finisher (and H4～H5), (J1～J4) comprises multistage intermediate condenser (J1～J3) and aftercondenser (J4) to described multi-stage condensing device; Wherein:
Described earth source heat pump device is arranged between seawater water fetching device (M) and the pretreating device (N);
(C1～C3) comprises some stage compressors to described stage compression unit, connect a central evaporator behind every stage compressor, the progression of central evaporator and the progression of compressor are complementary, first step compressor (C1) back connects last step central evaporator (H3), and last step compressor (C3) back connects first step central evaporator (H1); The hot side of every grade of central evaporator feeds the pressurized gas that the respective stages compressor produces, and cold side imports the seawater that the upper level central evaporator is discharged, and the cold side of first step central evaporator (H1) imports through the well heaters at different levels (seawater of I1～I3) heated; The cold side connecting the sea water of last step well heater (I3), hot side feeds the pressurized gas that first step central evaporator (H1) is discharged, and pressurized gas imports air storage chamber (D) behind last step well heater (I3); (steam that H1～H3) produces confluxes and enters finisher (the hot side of H4～H5), the seawater that last step central evaporator (H3) is discharged enter the finisher (cold side of H4～H5) central evaporator at different levels;
(E1～E3) comprises some grades of decompressors to described multistage expansion unit, connect an intermediate condenser before every grade of decompressor, the progression of intermediate condenser and the progression of decompressor are complementary, first step decompressor (E1) preceding connection first step intermediate condenser (J1), last step decompressor (E3) preceding connection last step intermediate condenser (J3); Intermediate condensers at different levels (the logical pressurized gas of the cold side of J1～J3), the carbonated drink gas mixture that the logical condensation fresh water of hot side and water vapor are formed; Pressurized gas in the described air storage chamber (D) enters first step decompressor (E1) behind the cold side of first step intermediate condenser (J1), the hot side of last step intermediate condenser (J3) feeds by finisher (the carbonated drink gas mixture of H4～H5) derive; Described carbonated drink gas mixture enters first step intermediate condenser (J1) by last step intermediate condenser (J3) successively, imports aftercondenser (J4) afterwards.
2. polygenerations systeme according to claim 1, it is characterized in that: finisher (the steam part of the hot side of H4～H5) and the finisher (seawater to make heat exchange of cold side of H4～H5), a part import all the other well heaters at different levels except last step well heater (I1) (the hot side of I2～I3), with the seawater to make heat exchange of corresponding well heater cold side.
3. polygenerations systeme according to claim 2 is characterized in that: (H4～H5) comprises and all cooperates a well heater to carry out heat exchange by a plurality of finishers behind each finisher described finisher.
4. polygenerations systeme according to claim 3, it is characterized in that: the cold side of aftercondenser (J4) feeds the seawater through pre-treatment that pretreating device (N) is discharged, hot side feeds the condensation fresh water of first step intermediate condenser (J1) discharge and the carbonated drink gas mixture that water vapor is formed, a seawater part that heats up is returned pretreating device (N), and a part enters well heaters at different levels (I1～I3).
5. according to each described polygenerations systeme of claim 1 to 4, it is characterized in that: the strong brine that described sea water desalinating plant produces is by finisher (H4～H5) discharge.
6. according to each described polygenerations systeme of claim 1 to 4, it is characterized in that: fresh water and non-condensable gas that described sea water desalinating plant produces are discharged by aftercondenser (J4).
7. according to each described polygenerations systeme of claim 1 to 4, it is characterized in that: after the pressurized gas that air storage chamber (D) stores reaches default pressure, high-pressure air is sent into the cold side of first step intermediate condenser (J).
8. according to each described polygenerations systeme of claim 1 to 4, it is characterized in that: described wind energy conversion system device (A) drives described stage compression unit by a transmission mechanism (B).
9. according to each described polygenerations systeme of claim 1 to 4, it is characterized in that: described system also comprises store battery (G), and described generator (F) is respectively to store battery (G) and user's power supply.
10. according to each described polygenerations systeme of claim 1 to 4, it is characterized in that: described earth source heat pump device comprises outdoor sea water heat energy heat-exchange system, earth source heat pump unit and indoor heating air conditioning terminal system, wherein, the seawater water intake conduit coupled arrangement of described outdoor sea water heat energy heat-exchange system and described seawater water fetching device adopts ground configuration or seabed to arrange.
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103193283A (en) * | 2013-03-26 | 2013-07-10 | 中国科学院工程热物理研究所 | High-efficiency energy-storing cold, heat, electricity and water poly-generation system |
| CN103776165A (en) * | 2014-02-28 | 2014-05-07 | 无锡同春新能源科技有限公司 | Air-source heat pump water heater powered by wind-solar complementary power generation system |
| WO2014183564A1 (en) * | 2013-05-14 | 2014-11-20 | 国家电网公司 | Cold, heat, electricity and water multi-cogeneration system comprehensively using wind energy and heat energy of seawater |
| CN104806456A (en) * | 2014-03-18 | 2015-07-29 | 摩尔动力(北京)技术股份有限公司 | Wind-energy steady-flow energy supply method and system |
| CN104819111A (en) * | 2014-03-18 | 2015-08-05 | 摩尔动力(北京)技术股份有限公司 | Photovoltaic power generation current-stabilized energy supply method and system |
| US11502323B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11502322B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11855324B1 (en) | 2022-11-15 | 2023-12-26 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell with heat pump |
| US12040517B2 (en) | 2023-05-09 | 2024-07-16 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell and methods of use thereof |
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2013
- 2013-03-26 CN CN2013201426002U patent/CN203159267U/en not_active Withdrawn - After Issue
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103193283A (en) * | 2013-03-26 | 2013-07-10 | 中国科学院工程热物理研究所 | High-efficiency energy-storing cold, heat, electricity and water poly-generation system |
| WO2014183564A1 (en) * | 2013-05-14 | 2014-11-20 | 国家电网公司 | Cold, heat, electricity and water multi-cogeneration system comprehensively using wind energy and heat energy of seawater |
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| US11699803B1 (en) | 2022-05-09 | 2023-07-11 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
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