CN101749206B - Low-temperature liquefied energy recovery power supply system - Google Patents
Low-temperature liquefied energy recovery power supply system Download PDFInfo
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- CN101749206B CN101749206B CN2008102312892A CN200810231289A CN101749206B CN 101749206 B CN101749206 B CN 101749206B CN 2008102312892 A CN2008102312892 A CN 2008102312892A CN 200810231289 A CN200810231289 A CN 200810231289A CN 101749206 B CN101749206 B CN 101749206B
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Abstract
The invention provides a low-temperature liquefied energy recovery power supply system which is convenient to install and use, small in occupying area and free of environmental pollution, can absorb heat from a low-temperature heat source, and enable the heat to be converted into power completely without remaining any changes. The low-temperature liquefied energy recovery power supply system comprises a circular liquefied medium heat exchanger, a compressor, a fluid energy recovery heat exchanger, a turbine expander, a flash drum and medium pipelines for communicating all parts; wherein the medium inlet pipeline and the medium outlet pipeline are arranged between the compressor and the flash drum and used for enabling the compressor to be communicated with the flash drum, a pressure-reducing valve is arranged on the medium outlet pipeline between the compressor and the flash drum, a liquefied liquid output pipeline is arranged between the flash drum and a liquid booster pump and used for enabling the flash drum to be communicated with the liquid booster pump, and the output pipeline is communicated with the turbine expander; and a control cabinet connected with a power wire is connected with the compressor, a flash valve, the liquid booster pump, the turbine expander and the fluid energy recovery heat exchanger through a control wire and a power wiring harness.
Description
Technical field
The invention belongs to heat recovery and utilize system again; Relate in particular to the recycling system of cryogenic energy.
Background technique
Contain huge tow taste heat in the water of atmosphere, rivers,lakes and seas; Can produce a large amount of low-temperature waste heats in the industrial process, association great amount of carbon dioxide again when industrial processes produce above-mentioned used heat, the generation of aggravation greenhouse effect raises atmospheric temperature year by year.At present, in order to reclaim these low-grade heats, people have invented wind source heat pump and have been used for heating, but the utilization ratio of low-grade energy is still very low.Number of patent application is to have disclosed a kind of method and device that utilizes a plurality of dispersion waste heats, thermal source, the generating of multiple waste heat mounting medium in 200710050627.8 the patent application; This method can make multiple waste heat obtain the part utilization; Not enough below but this method exists: can only the higher waste heat of recovered temperature, to temperature about 50 ℃ and following waste heat or used heat can't utilize; Condensation effect required in the system must be assisted realization by air cooling, water-cooled or other modes, consume extra energy, waste great lot of water resources etc.; The advances of its Economy when this technology is used for recovery waste heat, the feature of environmental protection, technology etc. are compared with present technique and are had big gap.How to develop these inexhaustible, nexhaustible low-grade energies and be the contemporary science man and make great efforts the problem that solves always.The inventor also once disclosed several kinds of systems that heat recovery utilizes again in number of patent application is 200810140773.4,200820148143.7,200820148144.1,200820148145.6 document, but the opening of research that heat recovery utilizes again and equipment still has very big scope.
Summary of the invention
The objective of the invention is to: provide a kind of be convenient to easy to install, floor space is little, free from environmental pollution, can absorb heat from low-temperature heat source, make it all to be converted into merit, and do not stay the low-temperature liquefied energy recovery power supply system of other any variations.
The present invention seeks to realize through following technological scheme: a kind of low-temperature liquefied energy recovery power supply system, reclaim heat exchanger, turbo-expander, liquid booster pump, flash drum and the connection medium pipeline between them by circulation liquefaction medium heat exchanger, compressor, flash valve, fluid energy and form; Be equipped with between compressor and the flash drum and make they are communicated with advance medium pipeline and go out medium pipeline; Going out between compressor and the flash drum is equipped with reduction valve on the medium pipeline; Between flash drum and the liquid booster pump liquefied liquid output pipeline that is communicated with them is arranged; Be communicated with heat exchanger and fluid energy on this output pipeline and reclaim heat exchanger, this output pipeline also is communicated with turbo-expander; Discharge medium pipeline with heat exchanger or advance medium pipeline and be connected with the exhaust steam that turbo-expander is communicated with, and be connected with the gas inlet of compressor; The control cabinet that links to each other with power line reclaims heat exchanger through guide line and power supply wire harness with compressor, flash valve, liquid booster pump, turbo-expander, fluid energy and is connected; On the pipeline between compressor and the flash drum heat exchanger is housed; One side of a heat exchanger is communicated with the medium pipeline that advances between flash drum and the compressor; One end of another side with go out medium pipeline and link to each other; Its other end is communicated with medium pipeline on being contained in another heat exchanger, and this medium pipeline is connected with the medium pipeline that reduction valve is housed through this heat exchanger, and links to each other with flash drum; One end of another heat exchanger links to each other with the feed liquor medium pipeline that the liquid booster pump outlet is connected, and the other end is connected with the heat exchanger that the feed liquor medium pipeline that is connected by the liquid booster pump outlet is communicated with.
The parallel connection or at least two group circulation liquefaction medium heat exchanger package of connecting on the pipeline between turbo-expander and the flash drum.
Have at least two compressors parallelly connected with the tank connected compressor of flash distillation, at least two group circulation liquefaction medium heat exchanger package parallel connection or connect between turbo-expander and the flash drum.
Turbo-expander in the system and compressor are directly formed as a whole.
The energy recovery heat exchanger is that wind energy reclaims the combination that heat exchanger or fluid heat exchanger or wind energy reclaim heat exchanger and fluid heat exchanger.
This low-temperature liquefied energy recovery power supply system; Replenishing pipeline by circulation liquefaction medium heat exchanger, compressor, reduction valve, flash drum, liquid booster pump, fluid energy recovery heat exchanger, turbo-expander and their medium pipeline of connection and medium solution forms; The whole system structure is very simple; Therefore be convenient to install, floor space is also very little, uses easily; Provide the fluid of energy to get into the energy recovery heat exchanger among the present invention; Low boiling point working medium gets into turbo-expander through energy recovery heat exchanger heating back; The exhaust steam that the turbo-expander of low-temperature liquefied energy recovery power supply system is discharged directly gets into the heat exchanger of exhaust steam energy-recuperation system, and the liquid of carrying with liquid booster pump carries out heat exchange in heat exchanger, progressively become cryogenic gas; After boosting, the process compressor gets into reduction valve; A part of flash distillation is a liquid in flash drum, and another part machine of being compressed is inhaled back compression chamber and continued compression, also gets into compressor by heat exchanger through the cryogenic gas of discharging from turbo-expander of cryogenic liquide cooling simultaneously; And be pressurized, be collapsed into cryogenic gas and get into reduction valve with certain pressure at this; The flash distillation that circulates liquefaction is constantly supplied low-temperature liquefaction liquid and is given the liquid suction booster, realizes the continuous circulation of heat absorption vaporization → entering turbo-expander expansion acting → entering compressor compresses supercharging → flash distillation liquefaction from the energy recovery heat exchanger; Reach constantly and absorb energy, externally the purpose of acting from low temperature environment or cryogen.
Therefore this system can be with the gas that contains in the water of atmosphere, rivers,lakes and seas and various industrial process produces, the tow taste heat recycling in the flow body; Be converted into useful kinetic energy; For various processes provide power, as: can be used as the power of automobile power, train power, wheel ship power, industrial processes, the power of driving generator ....Simultaneously, can be the various spaces of cooling that need provides the equipment of chilled water, needs cooling cooling medium to be provided, for various cryogenic freezing processes the low temperature cold to be provided ....This has not only reduced environmental pollution, to cold space of need and medium cold is provided, and has saved the energy, can fundamentally reduce energy cost, solve energy crisis.
From this system of theory analysis is reasonably, and the Kano of the second law of thermodynamics is explained and told us: can not absorb heat from single source, make it all to be converted into merit and the heat engine that do not stay other any variations.
Thermomechanics also has definition to perpetuum mobile of the second kind: heat absorption constantly obtains mechanical work in ambient air or the seawater, and this single source power engine of acting down is called perpetuum mobile of the second kind.Though it does not violate the first law of thermodynamics and energy conservation, but run counter to the second law of thermodynamics, the second law of thermodynamics also can be expressed as: perpetuum mobile of the second kind is non-existent.
" cycle engine that only cools off a thermal source is unsuccessful ", " spontaneous process is irreversible ", " in irreversible adiabatic process, entropy increases, but can not reduce ".Above-mentioned theory is correct.Therefore adopt the low-temperature liquefaction technology, create low temperature environment, under the relatively low ambient temperature and under the medium temperature; Obtain cryogenic liquide through flash distillation; The cryogenic liquide of selecting possesses the rerum natura of low-temperature vaporization; Through sending into heat exchanger after the compression pump supercharging, the atmosphere and the heat in other fluid that absorb normal temperature or lower temperature are vaporizated into temperature and the higher relatively steam of pressure, promote the turbo-expander acting; The cold that utilizes the different transfer of heat principle that cryogenic liquide evaporation is produced simultaneously is applied to the higher relatively cryogen of temperature that condensation is discharged from turbo-expander again, and with sending into flash distillation after the compressor compresses behind its greenhouse cooling, circulation obtains cryogenic liquide.Just can realize: absorb heat from low-temperature heat source, make it all to be converted into merit and the heat engine that do not stay other any variations.Such system is feasible; It does not run counter to the law of thermodynamics; With the wind energy power generating system is example: when having cooled off two thermals source: 1. 2. exhaust steam of air (helium of discharging from turbine engine, nitrogen, carbon dioxide gas etc.), and also these processes all are enforceable.Selected under very environmental protection, the low temperature thermal performance compressed media preferably again in the system: helium, nitrogen, carbon dioxide etc., can be from low-temperature heat source heat removal.
Through this invention; Can draw: system itself is as creating the relatively low environment of temperature; Realize the two alternate mutual conversions of circulatory mediator vapour-liquid; This system just can be from the higher relatively thermal source of temperature heat removal, such system just can realize making it all to be converted into from the low-temperature heat source heat absorption heat engine of merit.
Description of drawings
Fig. 1 is embodiment 1 a structural representation;
Fig. 2 is the schematic representation of embodiment's 1 another kind of structural type;
Fig. 3 is embodiment 2 a structural representation;
Fig. 4 is embodiment 3 a structural representation;
Fig. 5 is the schematic representation of embodiment's 3 another kind of structural types;
Fig. 6 is embodiment 4 a structural representation;
Fig. 7 is the schematic representation of embodiment's 4 another kind of structural types;
Fig. 8 is embodiment 5 a structural representation;
Fig. 9 is the turbo-expander in the system and compressor is as a whole, the structural representation when fluid energy reclaims heat exchanger and adopts fluid heat exchanger;
Figure 10 is for having many turbo-expander parallel connections, multiple compressors parallel connection, the system architecture schematic representation of many energy recovery heat exchanger parallel connections;
Figure 11 is the system architecture schematic representation of many turbo-expanders and compressor parallel;
Figure 12 is a turbo-expander and compressor is as a whole and the system architecture schematic representation of many parallel connections.
Figure 13 is parallel with the structural representation of two groups of circulation liquefaction medium heat exchanger package on the pipeline between turbo-expander and the flash drum;
Figure 14 is embodiment 6 a structural representation;
Figure 15 is another kind of structural representation of the embodiment 6.
Embodiment
Embodiment 1: a kind of low-temperature liquefied energy recovery power supply system comprises that compressor 15, reduction valve 14, flash drum (also can be described as liquid container) 12, first heat exchanger 5, second heat exchanger 7, the 3rd heat exchanger 9, fluid energy reclaim heat exchanger 3, turbo-expander (also can be described as motor) 1, electrical power control cabinet 23, liquid booster pump 11 and the connecting tube between them and control wire harness.
Have between flash drum (also can be described as liquid container) 12 and the compressor 15 to make they are communicated with advance medium pipeline 16 and go out medium pipeline 17, going out between compressor 15 and the flash drum 12 places reduction valve 14 on the medium pipeline 17; Be connected by liquefaction cycle medium pipeline 25 between flash drum 12 and the liquid booster pump 11, the feed liquor medium pipeline 10 that is connected with liquid booster pump 11 outlets is communicated with first heat exchanger 9.The fed sheet of a media pipeline 8 and discharge medium pipeline 19 that connect them are housed between first heat exchanger 9 and second heat exchanger 7; The fed sheet of a media pipeline 6 and discharge medium pipeline 20 that connect them are arranged between second heat exchanger 7 and the 3rd heat exchanger 5; The 3rd heat exchanger 5 and fluid energy reclaim between the heat exchanger 3 and are connected by fed sheet of a media pipeline 4, and fluid energy reclaims between heat exchanger 3 and the turbo-expander 1 and connected by gas delivery medium pipeline 2.Discharging medium pipeline 21 by exhaust steam between turbo-expander 1 and the heat exchanger 5 is connected.Discharge medium pipeline 18 and be connected, advance medium pipeline 16 and be connected with the gas inlet of compressor with the medium pipeline 16 that advances between flash drum 12 and the compressor 15.
And the feed liquor medium pipeline 10 that is connected with liquid booster pump 11 outlet be with first heat exchanger 9 and second heat exchanger 7 between fed sheet of a media pipeline 4 and the gas delivery medium pipeline 2 between fluid energy recovery heat exchanger 3 and the turbo-expander 1 between the fed sheet of a media pipeline 6, the 3rd heat exchanger 5 and the fluid energy recovery heat exchanger 3 that link to each other between the fed sheet of a media pipeline 8, second heat exchanger 7 and the 3rd heat exchanger 5 that link to each other be connected.And discharge medium pipeline 19, the discharge medium pipeline 18 that links to each other with first heat exchanger 9 and the medium pipeline 16 that advances between flash drum 12 and the compressor 15 that the exhaust steam between turbo-expander 1 and the heat exchanger 5 is discharged between discharge medium pipeline 20, first heat exchanger 9 and second heat exchanger 7 between medium pipeline 21 and second heat exchanger 7 and the 3rd heat exchanger 5 are connected, and are connected with the gas inlet of compressor again.
The control cabinet 23 that links to each other with power line 22 reclaims heat exchanger 3 with compressor 15, reduction valve 14, turbo-expander 1, fluid energy respectively through guide line and power supply wire harness 24 and is connected with suction booster 11.It is other that control cabinet 23 can be installed on turbo-expander 1, also can select suitable mounting point.Be filled with an amount of helium or nitrogen or other compressed media in the medium pipeline.
Be to drive air through blower fan to send in this system fluid energy recovery heat exchanger 3 in the present embodiment; Be delivered in the heat exchanger after through the liquid after the flash distillation by the liquid booster pump supercharging; Carry out heat exchange with the exhaust steam of discharging from turbo-expander; The loop compression medium progressively is heated into gas or partly is heated into gas (being heterogeneous fluid this moment); Sending into then in the inherent energy recovery heat exchanger of energy recovery heat exchanger is made it be vaporized into the pressurized gas with uniform temperature fully by the further heating of air; Externally do work through gas delivery medium pipeline 2 entering turbo-expanders 1, driving turbo-expander 1, the exhaust steam after the acting is discharged medium pipeline 21 by exhaust steam and is got into heat exchangers.In heat exchanger, to then progressively becoming cryogenic gas by the liquid heat through after the flash distillation of carrying after the suction booster supercharging, get into reduction valve after boosting through compressor, a part of flash distillation is a liquid in flash drum.Said flash drum is liquefaction medium flash drum.
Heat exchanger in the present embodiment not only can adopt three, can adopt one, two, four or other quantity as required.
In the present embodiment, be called one group of circulation liquefaction medium heat exchanger package by a feed liquor medium pipeline connection heat exchanger and an energy recovery heat exchanger that is connected with liquid booster pump 11 outlets.As required can the parallel connection or at least two group circulation liquefaction medium heat exchanger package of connecting on the pipeline between turbo-expander and the flash drum.Shown in figure 13.
Embodiment 2: the structure of present embodiment is close with embodiment 1; Just on the liquefaction cycle medium pipeline 25 between flash drum (also can be described as liquid container) 12 and the liquid booster pump 11, be communicated with one again and increase liquid pipe 26; Increase liquid pipe 26 and be positioned at liquid booster pump 11 imports one side, other structure is identical with embodiment 1.
Embodiment 3: between the flash drum 12 of present embodiment and the compressor 15 heat exchanger 13 is housed; Heat exchanger 13 respectively with flash drum (also can be described as liquid container) 12 and compressor 15 between advance medium pipeline 16 and go out medium pipeline 17 and be connected, going out reduction valve 14 is housed on the medium pipeline 17; Reduction valve 14 is contained between flash drum 12 and the heat exchanger 13, discharges medium pipeline 18 and advances medium pipeline 16 and be connected.Other structures are identical with embodiment 1.System in the present embodiment sends into reduction valve 14 to pressurized gas after heat exchanger 13 coolings.
Embodiment 4: between the flash drum 12 of present embodiment and the compressor 15 heat exchanger 13 is housed; Heat exchanger 13 on one side with flash drum 12 and compressor 15 between the medium pipeline 16 that advances be communicated with; One end of another side with go out medium pipeline 17 and link to each other; The other end is communicated with medium pipeline 29 on being contained in another heat exchanger 9a, and medium pipeline 29 is connected with the medium pipeline that reduction valve 14 is housed 28 through another heat exchanger 9a; The medium pipeline 28 that reduction valve 14 is housed links to each other with flash drum 12.The end of another heat exchanger 9a links to each other with the feed liquor medium pipeline 10 that liquid booster pump 11 outlets are connected, and the other end is communicated with through second heat exchanger 7 and first heat exchanger 5 that fed sheet of a media pipeline 8 and the feed liquor medium pipeline 10 that is connected by liquid booster pump 11 outlets are communicated with.Other structures are identical with embodiment 1.
Native system is further to send into reduction valve 14 after the cooling with sending into heat exchanger 9a through the pressurized gas of heat exchanger 13 coolings.
Embodiment 5: the structure of present embodiment is close with embodiment 4, but increases a turbo-expander 1a in compressor 17 outlets; Between the heat exchanger 13 and back heat exchanger 13a before being equipped with between the flash drum 12 of present embodiment and the compressor 15, flash drum 12 and compressor 15 advance medium pipeline 16 and preceding heat exchanger 13 and after heat exchanger 13a be communicated with; Going out reduction valve 14 is housed on the medium pipeline 17; Reduction valve 14 is contained between flash drum 12 and the preceding heat exchanger 13a; Discharge tube 17a is equipped with in the outlet of compressor 15, discharge tube 17a with go out medium pipeline 17 and be connected with inlet pipe 26, inlet pipe 26 links to each other with the turbo-expander 1a that increases again; The exhaust steam discharge tube of being adorned on the turbo-expander 1a that increases by 27 with advance medium pipeline 16 and be connected, connection place is at preceding heat exchanger 13 with afterwards between the heat exchanger 13a.The turbo-expander 1a that increases also links to each other with control cabinet 23 through guide line and power supply wire harness 24.
In order to make the more compact structure of system, turbo-expander among the present invention and compressor can be integrated into as a whole device; Like this, embodiment 1 structure then is shown in Figure 2; Embodiment 3 structure then is shown in Figure 5; Embodiment's 4 structures then are shown in Figure 8.
Embodiment 6: shown in figure 14; A heat exchanger 9 is only arranged in the present embodiment; Be equipped with between compressor and the flash drum and make they are communicated with advance medium pipeline 16 and go out medium pipeline 17; Heat exchanger 9 is communicated with the medium pipeline 16 of going out that links to each other with compressor, goes out medium pipeline 17 and is communicated with medium pipeline 30 on being contained in the medium flash drum 12 that liquefies through heat exchanger 9, and reduction valve 14 is housed on the medium pipeline 30; Between liquefaction medium flash drum 12 and the liquid booster pump 11 the liquefied liquid output pipeline 25 that is communicated with them is arranged; Heat exchanger 9 links to each other with the output pipeline 10 that liquid booster pump 11 outlets link to each other, and output pipeline 10 reclaims heat exchanger 3 through heat exchanger 9 and fluid energy and is communicated with output pipeline 2, and this output pipeline 2 is communicated with turbo-expander 1; Discharge medium pipeline 21 and advance medium pipeline 16 and be connected with the exhaust steam that turbo-expander is communicated with.The control cabinet that links to each other with power line reclaims heat exchanger through guide line and power supply wire harness with compressor, flash valve, liquid booster pump, turbo-expander, fluid energy and is connected.
In order to make the more compact structure of system, turbo-expander among the present invention and compressor can be integrated into as a whole device; Shown in figure 15.
Turbo-expander and compressor can be integrated into as a whole device, perhaps use the turbo-expander pressure-increasing machine.
Fluid energy recovery heat exchanger in the foregoing description can be wind energy recovery heat exchanger and also can be fluid heat exchanger; When adopting fluid heat exchanger; The liquid that is utilized then should get in the fluid heat exchanger from intake pipe the loop compression medium is further heated, and the equipment that the water of discharging from outlet pipe can be the various spaces that need cooling provides chilled water, needs to cool off provides cooling medium, for various cryogenic freezing processes the low temperature cold is provided ....Fluid energy reclaims heat exchanger and can be the combination that wind energy reclaims heat exchanger and fluid heat exchanger.
Fig. 9 is as a whole for turbo-expander and compressor can be integrated into, the structural representation when fluid energy reclaims heat exchanger employing fluid heat exchanger;
The form that also can adopt at least two group circulation liquefaction medium heat exchanger package parallel connection between the parallel connection of compressor at least, turbo-expander and the flash drum or connect with the tank connected compressor of flash distillation in the system among the present invention as required, shown in figure 10;
Also can adopt many turbo-expander parallel connections, multiple compressors parallel connection, many energy recovery heat exchanger parallel connections or the form of connecting system pipeline afterwards of connecting, shown in figure 11;
Also can adopt the structural type of connecting system behind many turbo-expanders and the compressor parallel; Or integrate turbo-expander and compressor as a whole and many parallel connection back connecting systems, shown in figure 12.
Be communicated with in the foregoing description all can install on the liquefied liquid output pipeline between liquefaction medium flash drum and the liquid booster pump and increase the liquid pipeline, this increases on the pipeline of ingress that the liquid pipeline should be contained in the liquefied liquid suction booster.
According to system design scheme; Also can adopt the form of the energy recovery heat exchanger serial or parallel connection of various ways; So that contain in the exhaust steam that low-grade energy is arranged, the circulating water of refrigeration system etc. one or more to what the steam turbine of the water in air, the rivers,lakes and seas, thermal power plant or nuclear power plant was discharged; Drive or the pressurized delivered of liquid pump through blower fan, import in this system fluid energy recovery heat exchanger and its Btu utilization.
Gas in the native system after the flash distillation is through the flash distillation of compressor boost continued, and the pressure and temperature after compressor boost can not be too high, is beneficial to flash distillation and is advisable.Be controlled at below the 40k like the compressor exit temperature of helium and be advisable, the compressor exit temperature of nitrogen should be controlled at is advisable below the 140k etc.Temperature, the overpressure not only energy consumption of system increase, and the liquefied fraction of flash system will reduce greatly, even can't liquefy.It is low more that the temperature of liquefaction system keeps, the easy more liquefaction of gas, and system energy consumption is low more.
Claims (5)
1. low-temperature liquefied energy recovery power supply system reclaims heat exchanger, turbo-expander, liquid booster pump, flash drum and the connection medium pipeline between them by circulation liquefaction medium heat exchanger, compressor, flash valve, fluid energy and forms; Be equipped with between compressor and the flash drum and make they are communicated with advance medium pipeline and go out medium pipeline; Going out between compressor and the flash drum is equipped with reduction valve on the medium pipeline; Between flash drum and the liquid booster pump liquefied liquid output pipeline that is communicated with them is arranged; Be communicated with heat exchanger and fluid energy on this output pipeline and reclaim heat exchanger, this output pipeline also is communicated with turbo-expander; Discharge medium pipeline with heat exchanger or advance medium pipeline and be connected with the exhaust steam that turbo-expander is communicated with, and be connected with the gas inlet of compressor; The control cabinet that links to each other with power line reclaims heat exchanger through guide line and power supply wire harness with compressor, flash valve, liquid booster pump, turbo-expander, fluid energy and is connected; It is characterized in that: on the pipeline between compressor and the flash drum heat exchanger is housed; One side of a heat exchanger is communicated with the medium pipeline that advances between flash drum and the compressor; One end of another side with go out medium pipeline and link to each other; Its other end is communicated with medium pipeline on being contained in another heat exchanger, and this medium pipeline is connected with the medium pipeline that reduction valve is housed through this heat exchanger, and links to each other with flash drum; One end of another heat exchanger links to each other with the feed liquor medium pipeline that the liquid booster pump outlet is connected, and the other end is connected with the heat exchanger that the feed liquor medium pipeline that is connected by the liquid booster pump outlet is communicated with.
2. low-temperature liquefied energy recovery power supply system according to claim 1 is characterized in that: the parallel connection or at least two group circulation liquefaction medium heat exchanger package of connecting on the pipeline between turbo-expander and the flash drum.
3. low-temperature liquefied energy recovery power supply system according to claim 1 and 2; It is characterized in that: have at least two compressors parallelly connected with the tank connected compressor of flash distillation, at least two group circulation liquefaction medium heat exchanger package parallel connection or connect between turbo-expander and the flash drum.
4. low-temperature liquefied energy recovery power supply system according to claim 3 is characterized in that: turbo-expander in the system and compressor are directly formed as a whole.
5. low-temperature liquefied energy recovery power supply system according to claim 1 is characterized in that: the energy recovery heat exchanger is that wind energy reclaims the combination that heat exchanger or fluid heat exchanger or wind energy reclaim heat exchanger and fluid heat exchanger.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2008102312892A CN101749206B (en) | 2008-12-10 | 2008-12-10 | Low-temperature liquefied energy recovery power supply system |
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| CN2008102312892A CN101749206B (en) | 2008-12-10 | 2008-12-10 | Low-temperature liquefied energy recovery power supply system |
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| CN101749206A CN101749206A (en) | 2010-06-23 |
| CN101749206B true CN101749206B (en) | 2012-08-22 |
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| CN104976514A (en) * | 2014-04-11 | 2015-10-14 | 杨双来 | Method for carrying out power outputting and gas conveying through low-temperature liquid |
| CN104976833A (en) * | 2014-04-11 | 2015-10-14 | 杨双来 | Refrigeration method utilizing low-temperature liquid refrigeration medium |
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|---|---|---|---|---|
| US4118934A (en) * | 1975-03-21 | 1978-10-10 | Enterprise Industrielle De Chaudronnerie | Process and apparatus for transforming heat at a relatively low temperature into power or energy |
| CN1122413A (en) * | 1994-05-19 | 1996-05-15 | 霍占满 | Power generating method and equipment using low temperature energy |
| US5694772A (en) * | 1994-04-28 | 1997-12-09 | Ormat Industries Ltd. | Method of apparatus for disposing of non-condensable gases present in geo fluid |
| CN1175663A (en) * | 1996-08-29 | 1998-03-11 | 毛元章 | Method for refrigerating and electrically generating using low-temp. medium and refrigerating generating station |
| CN201045334Y (en) * | 2007-06-18 | 2008-04-09 | 葆光（大连）节能技术研究所有限公司 | Thermo-electric generation and heat supply uniset |
| CN201367998Y (en) * | 2008-12-10 | 2009-12-23 | 陈万仁 | Low-temperature liquefied energy recovery power supply system |
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2008
- 2008-12-10 CN CN2008102312892A patent/CN101749206B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4118934A (en) * | 1975-03-21 | 1978-10-10 | Enterprise Industrielle De Chaudronnerie | Process and apparatus for transforming heat at a relatively low temperature into power or energy |
| US5694772A (en) * | 1994-04-28 | 1997-12-09 | Ormat Industries Ltd. | Method of apparatus for disposing of non-condensable gases present in geo fluid |
| CN1122413A (en) * | 1994-05-19 | 1996-05-15 | 霍占满 | Power generating method and equipment using low temperature energy |
| CN1175663A (en) * | 1996-08-29 | 1998-03-11 | 毛元章 | Method for refrigerating and electrically generating using low-temp. medium and refrigerating generating station |
| CN201045334Y (en) * | 2007-06-18 | 2008-04-09 | 葆光（大连）节能技术研究所有限公司 | Thermo-electric generation and heat supply uniset |
| CN201367998Y (en) * | 2008-12-10 | 2009-12-23 | 陈万仁 | Low-temperature liquefied energy recovery power supply system |
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