CN105863751B - A kind of enclosed low temperature compressed air energy-storage system and method - Google Patents
A kind of enclosed low temperature compressed air energy-storage system and method Download PDFInfo
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- CN105863751B CN105863751B CN201610382016.2A CN201610382016A CN105863751B CN 105863751 B CN105863751 B CN 105863751B CN 201610382016 A CN201610382016 A CN 201610382016A CN 105863751 B CN105863751 B CN 105863751B
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- 238000004146 energy storage Methods 0.000 title claims abstract description 71
- 238000000034 method Methods 0.000 title claims description 15
- 239000000126 substance Substances 0.000 claims abstract description 45
- 238000009825 accumulation Methods 0.000 claims abstract description 44
- 238000001816 cooling Methods 0.000 claims abstract description 28
- 230000001914 calming effect Effects 0.000 claims abstract description 15
- 230000006835 compression Effects 0.000 claims description 13
- 238000007906 compression Methods 0.000 claims description 13
- 230000033228 biological regulation Effects 0.000 claims description 6
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 25
- 230000008569 process Effects 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 5
- 238000010248 power generation Methods 0.000 description 5
- 230000005611 electricity Effects 0.000 description 4
- 230000009467 reduction Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- CUZMQPZYCDIHQL-VCTVXEGHSA-L calcium;(2s)-1-[(2s)-3-[(2r)-2-(cyclohexanecarbonylamino)propanoyl]sulfanyl-2-methylpropanoyl]pyrrolidine-2-carboxylate Chemical compound [Ca+2].N([C@H](C)C(=O)SC[C@@H](C)C(=O)N1[C@@H](CCC1)C([O-])=O)C(=O)C1CCCCC1.N([C@H](C)C(=O)SC[C@@H](C)C(=O)N1[C@@H](CCC1)C([O-])=O)C(=O)C1CCCCC1 CUZMQPZYCDIHQL-VCTVXEGHSA-L 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 238000009421 internal insulation Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
Classifications
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- 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
- F01K7/00—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
- F01K7/02—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating the engines being of multiple-expansion type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01B—MACHINES OR ENGINES, IN GENERAL OR OF POSITIVE-DISPLACEMENT TYPE, e.g. STEAM ENGINES
- F01B23/00—Adaptations of machines or engines for special use; Combinations of engines with devices driven thereby
- F01B23/10—Adaptations for driving, or combinations with, electric generators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B35/00—Piston pumps specially adapted for elastic fluids and characterised by the driving means to their working members, or by combination with, or adaptation to, specific driving engines or motors, not otherwise provided for
- F04B35/04—Piston pumps specially adapted for elastic fluids and characterised by the driving means to their working members, or by combination with, or adaptation to, specific driving engines or motors, not otherwise provided for the means being electric
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B39/00—Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
- F04B39/06—Cooling; Heating; Prevention of freezing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B41/00—Pumping installations or systems specially adapted for elastic fluids
- F04B41/02—Pumping installations or systems specially adapted for elastic fluids having reservoirs
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/16—Mechanical energy storage, e.g. flywheels or pressurised fluids
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
Abstract
A kind of enclosed low temperature compressed air energy-storage system, wherein low-temperature cold accumulation working medium exchange heat in First Heat Exchanger unit to normal temperature air, export normal temperature cold-storage working substance, the air after unit of calming the anger input heat exchange；Normal temperature storage tank is inputted and storage normal temperature cold-storage working substance；The compressed air of unit input storage is expanded, compressed air is in expansion unit to the air after expansion unit acting output expansion cooling；Normal temperature cold-storage working substance exchanges heat in the second heat exchanger unit to the air after expansion cooling, switchs to low-temperature cold accumulation working medium, and the air after expansion cooling switchs to normal temperature air after heat exchange；Low-temperature storage tank input low-temperature cold accumulation working medium is stored, output to First Heat Exchanger unit；And low pressure caisson inputs the normal temperature air and is stored and exported normal temperature air to First Heat Exchanger unit.The energy-storage system uses double loop closed cycle so that occur between compressed-air energy-storage system and environment without mass transfer, increases energy-storage system application, small to environmental factor dependence.
Description
Technical field
The present invention relates to electricity storage technology field, particularly a kind of enclosed low temperature compressed air energy-storage system and energy storage side
Method.
Background technology
In recent years, the peak-to-valley ratio of China's power load is continuously increased, the renewable energy power generation such as wind energy, luminous energy installation amount by
Step increase, adds the growth requirement of distributed energy so that the importance of power energy storage technology progressively shows.At present, electric power is stored up
Can technology include drawing water energy storage, compressed-air energy storage, batteries to store energy, flywheel energy storage, super capacitor etc., and compressed-air energy storage
Can be with energy storage analogy of drawing water in terms of capacity and construction cost so that it turns into one of competitive power energy storage technology.
But existing compressed-air energy-storage system is mostly open-cycle system, it must obtain storing working medium from environment, to environment
Dependence is stronger.
The content of the invention
In view of this, it is an object of the invention to provide a kind of enclosed low temperature compressed air energy-storage system and energy storage method.
To achieve the above object, the present invention provides a kind of enclosed low temperature compressed air energy-storage system, it is characterised in that including：
First Heat Exchanger unit, normal temperature air is exchanged heat in the First Heat Exchanger unit with low-temperature cold accumulation working medium,
Switch to the air after heat exchange after normal temperature air heat exchange, switch to normal temperature cold-storage working substance after the heat exchange of low-temperature cold accumulation working medium；
Calm the anger unit, the air inputted after the heat exchange, the air after output squeezing；
Normal temperature storage tank, is stored for inputting normal temperature cold-storage working substance, is additionally operable to the normal temperature cold-storage working substance output of storage；
High-pressure gas device, is stored for inputting the air after compression, is additionally operable to the compressed air stored by output；
Unit is expanded, the compressed air of storage is inputted, compressed air is swollen to expansion unit acting output in expansion unit
Air after swollen cooling；
Second heat exchanger unit, normal temperature storage tank output normal temperature cold-storage working substance in second heat exchanger unit with it is described
Air after expansion cooling is exchanged heat, and low-temperature cold accumulation working medium, the air after expansion cooling are switched to after the heat exchange of normal temperature cold-storage working substance
Switch to normal temperature air after heat exchange；
Low-temperature storage tank, is stored for inputting the low-temperature cold accumulation working medium, is additionally operable to export the low-temperature cold accumulation working medium
To First Heat Exchanger unit；And
Low pressure caisson, is stored for inputting the normal temperature air, is additionally operable to export the normal temperature air to institute
State First Heat Exchanger unit.
It is preferred that, energy-storage system also includes cryogenic pump, low-temperature cold accumulation working medium pump from low-temperature storage tank by the cryogenic pump
Go out, and enter the First Heat Exchanger unit；It is preferred that also include normal temperature pump, normal temperature cold-storage working substance is by the normal temperature pump from institute
State normal temperature storage storage tank to pump out, and enter second heat exchanger unit.
It is preferred that, the unit of calming the anger includes at least one low-pressure compressor and at least one high-pressure compressor, mutually string
Join or be integrated into overall multistage compressor, the air after each low-pressure compressor entrance input heat exchange exports low-pressure air；
Low-pressure air inputs high-pressure compressor again, the air after high-pressure compressor output squeezing.
It is preferred that, the unit of calming the anger also includes intergrade compressor, and the low-pressure air compresses through intergrade compressor
Afterwards, exchanged heat through First Heat Exchanger unit and low-temperature cold accumulation working medium, then input high-pressure compressor.
It is preferred that, the First Heat Exchanger unit and the second heat exchanger unit include two or more heat exchanger, compressor
Before compressor input air in group with heat exchanger exchange heat or expand unit in expanding machine delivery air after with heat exchange
Device is exchanged heat.
It is preferred that, the expansion unit includes at least one low-pressure expansion machine and at least one high pressure expansion machine, mutually string
Join or be integrated into overall multiple expansion engine, the compressed air of each high pressure expansion machine input storage exports primary expansion air；
Each low-pressure expansion machine inputs primary expansion air, exports final stage expanded air.
It is preferred that, the expansion unit also includes intergrade expanding machine, and the primary expansion air inputs the intergrade
Low-pressure expansion machine is inputted after expanding machine again.
It is preferred that, energy-storage system also includes generator, is connected, is driven when expansion unit is done work with described pair of expansion unit
Electrical power generators.
According to another aspect of the present invention, a kind of enclosed low temperature compressed air energy storage method is also provided, including：
In low power consumption or energy storage：
Normal temperature air and low-temperature cold accumulation working medium are exchanged heat in First Heat Exchanger unit, are converted into and are changed after normal temperature air heat exchange
Air after heat, normal temperature cold-storage working substance is converted into after the heat exchange of low-temperature cold accumulation working medium；
Motor driving calms the anger unit by the air after the air boil down to compression after heat exchange, and press-in high-pressure gas device is deposited
Storage；
Stored by using normal temperature storage tank input normal temperature cold-storage working substance；
In peak of power consumption or when releasing energy：
High-pressure gas device exports stored compressed air, and the interior acting of input expansion unit simultaneously drives electrical power generators,
Air after expansion unit output expansion cooling；
Normal temperature cold-storage working substance in normal temperature storage tank is injected in the second heat exchanger unit, changed with the air after expansion cooling
Heat, switchs to low-temperature cold accumulation working medium after the heat exchange of normal temperature cold-storage working substance, the air after expansion cooling switchs to normal temperature air after heat exchange；
Low-temperature cold accumulation working medium input low-temperature storage tank is stored, low-temperature storage tank is additionally operable in low power consumption or energy storage
The low-temperature cold accumulation working medium is inputted to First Heat Exchanger unit；
Normal temperature air input low pressure caisson is stored, low pressure caisson is additionally operable to export the normal temperature air
To the First Heat Exchanger unit.
It is preferred that, the part compressor or regulation rotating speed of gas compressor control compressor flow of unit of being calmed the anger by start-stop, from
And adjust energy storage capacity；And/or the expanding machine or regulation expanding machine rotating speed control expanding machine by start-stop demi-inflation unit are done
Function power, so as to adjust generating capacity.
By above-mentioned technical proposal, the beneficial effect that the present invention is realized is：
(1) using double closed cycle loops so that energy-storage system does not enter in thermal energy storage process and exoergic process with environment
Row working medium is exchanged, and heat exchange is only existed, so as to reduce compressed-air energy-storage system to environmental factor dependence；
(2) storage of high temperature heat source is not present in system, reduces system heat dissipation in storing process, improves system stored energy effect
Rate, and the cold energy of expander outlet is reclaimed, as the wasted work of the low-temperature receiver of the cascade EDFA of compressor, further reduction compressor,
So as to improve system effectiveness；
(3) compressed-air energy-storage system also has the energy storage cycle unrestricted, it is adaptable to various types of power supplys, to environment
Friendly the advantages of, with wide prospect of the application.
Brief description of the drawings
Fig. 1 is the structural representation of enclosed low temperature compressed air energy-storage system embodiment 1 of the invention；
Fig. 2 is the structural representation of enclosed low temperature compressed air energy-storage system embodiment 2 of the invention.
Embodiment
In the present invention, " low temperature " refers to the temperature less than normal temperature；" low-temperature storage tank " refers to for storing less than normal temperature
The tank arrangement of working medium；" cryogenic pump " refers to the pump less than the working medium of normal temperature for pumping.
According to present invention inventive concept generally, a kind of enclosed low temperature compressed air energy-storage system, including：First heat exchange
Device unit, normal temperature air is exchanged heat in the First Heat Exchanger unit with low-temperature cold accumulation working medium, is turned after normal temperature air heat exchange
For the air after heat exchange, switch to normal temperature cold-storage working substance after the heat exchange of low-temperature cold accumulation working medium；Calm the anger unit, the sky inputted after the heat exchange
Air after gas, output squeezing；Normal temperature storage tank, is stored for inputting normal temperature cold-storage working substance, is additionally operable to the normal temperature of storage
Cold-storage working substance is exported；High-pressure gas device, is stored for inputting the air after compression, is additionally operable to the compression stored by output
Air；Unit is expanded, the compressed air of storage is inputted, compressed air is in expansion unit to expansion unit acting output expansion drop
Air after temperature；Second heat exchanger unit, normal temperature storage tank output normal temperature cold-storage working substance in second heat exchanger unit with
Air after the expansion cooling is exchanged heat, and low-temperature cold accumulation working medium is switched to after the heat exchange of normal temperature cold-storage working substance, after expansion cooling
Air switchs to normal temperature air after heat exchange；Low-temperature storage tank, is stored for inputting the low-temperature cold accumulation working medium, is additionally operable to output
The low-temperature cold accumulation working medium is to First Heat Exchanger unit；And low pressure caisson, stored up for inputting the normal temperature air
Deposit, be additionally operable to export the normal temperature air to the First Heat Exchanger unit.
By using double loop closed circulation system, cold energy storage and compressed air storage are combined, reduction compression is empty
The heat dissipation of gas energy storage system and the dependence to environment.
The enclosed low temperature compressed air energy-storage system of the present invention, it is filled low pressure gas storage by unit of calming the anger in low power consumption
Put hollow air pressure and enter the storage of high-pressure gas device, the interior energy for converting electrical energy into air is stored, while will by cryogenic pump
Low-temperature cold accumulation working medium is used for cooling down every grade of compressor inlet air, reduces power input to compressor；In peak of power consumption, high-pressure gas device
Mesohigh air drives electrical power generators by expanding machine, while the normal temperature cold-storage working substance in normal temperature storage tank passes through heater between level
Air is heated to environment temperature there is provided the power output of the unit working medium of expanding machine, while reclaiming every grade of expander outlet sky
The cold energy of gas, the low-temperature receiver for compressor cascade EDFA in next thermal energy storage process.The present invention is using double closed cycle loops so that
Energy-storage system does not carry out working medium with environment in thermal energy storage process and exoergic process and exchanged, and heat exchange is only existed, so as to reduce
Compressed-air energy-storage system reclaims the cold energy of expander outlet air to environmental factor dependence, is used as the cascade EDFA of compressor
Low-temperature receiver, reduce compressor wasted work, so as to improve system effectiveness.Meanwhile, the compressed-air energy-storage system also has the energy storage cycle
It is unrestricted, it is adaptable to various types of power supplys, it is environmentally friendly.
Wherein, system can also include generator, be connected with described pair of expansion unit, expansion unit is driven hair when doing work
Electric power generation.
Wherein, system can also include cryogenic pump, and low-temperature cold accumulation working medium is pumped out by the cryogenic pump from low-temperature storage tank,
And enter the First Heat Exchanger unit.It is preferred that also include normal temperature pump, normal temperature cold-storage working substance is by the normal temperature pump from described
Normal temperature storage storage tank is pumped out, and enters second heat exchanger unit.
For cryogenic pump or normal temperature pump, preferably impeller pump or positive displacement pump.Described enclosed low temperature compressed air
Energy-storage system, its described impeller pump is axial-flow type, mixed-flow or centrifugal pump one or more combination therein；Volume
Formula pump, is gear pump, screw pump, lobe pump or sliding-vane pump one or more combination therein.
For unit of calming the anger, the unit of calming the anger includes at least one low-pressure compressor and at least one high-pressure compressor,
Overall multistage compressor is serially connected or is integrated into, the air after each low-pressure compressor entrance input heat exchange is exported low
Press air；Low-pressure air inputs high-pressure compressor again, the air after high-pressure compressor output squeezing.
It is preferred that, the unit of calming the anger also includes intergrade compressor, and the low-pressure air compresses through intergrade compressor
Afterwards, exchanged heat through First Heat Exchanger unit and low-temperature cold accumulation working medium, then input high-pressure compressor.
For First Heat Exchanger unit and the second heat exchanger unit, it is preferred that the First Heat Exchanger unit and second is changed
Hot device unit includes exchanging heat or swollen with heat exchanger before the compressor input air in two or more heat exchanger, unit of calming the anger
Exchanged heat after expanding machine delivery air in swollen unit with heat exchanger.
It is preferred that, can be plate-fin, bushing type, shell-and-tube, fin-tube type or jacket type for heat exchanger.
For expansion unit, the expansion unit includes at least one low-pressure expansion machine and at least one high pressure expansion machine,
Overall multiple expansion engine is serially connected or is integrated into, the compressed air of each high pressure expansion machine input storage, output is primary swollen
Swollen air；Each low-pressure expansion machine inputs primary expansion air, exports final stage expanded air.
It is preferred that, the expansion unit also includes intergrade expanding machine, and the primary expansion air inputs the intergrade
Low-pressure expansion machine is inputted after expanding machine again.
It is preferred that, for unit or the expansion unit of calming the anger, when more than for two-stage, be coaxial cascade or split axle simultaneously
Connection form；In parallel form, each split axle is moved with main drive shaft and is connected.Compressor or expanding machine, are piston type, axial-flow type, oblique flow
The one or more combination therein of formula, centrifugal, screw.
It is preferred that, the driving power supply of motor is conventional power plant trough-electricity, nuclear power, wind-powered electricity generation, solar power generation, water power or tide
Nighttide generating one or more combination therein.
For the high-pressure gas device, it is preferred that be cave or artificial pressure container.The low pressure caisson, it is excellent
Choosing is pressure vessel, its variable volume, and can carry out heat exchange with environment so that internal temperature is identical with environment temperature.
For normal temperature storage tank, it can be man-made vessel, heat exchange can be carried out with outside so that the cold-storage working substance temperature of storage
It is identical with environment temperature.It is interlayer vacuum-pumping structure, internal insulation structure or external thermal insulation structure for the low-temperature storage tank.
For the air, preferably also replace as carbon dioxide or nitrogen；It is oil, alcohol for the cold-storage working substance
One or two kinds of combinations of the class aqueous solution.
According to the same design of the present invention, a kind of enclosed low temperature compressed air energy storage method is also provided,
Including：
In low power consumption or energy storage：
Normal temperature air and low-temperature cold accumulation working medium are exchanged heat in First Heat Exchanger unit, are converted into and are changed after normal temperature air heat exchange
Air after heat, normal temperature cold-storage working substance is converted into after the heat exchange of low-temperature cold accumulation working medium；
Motor driving calms the anger unit by the air after the air boil down to compression after heat exchange, and press-in high-pressure gas device is deposited
Storage；
Stored by using normal temperature storage tank input normal temperature cold-storage working substance；
In peak of power consumption or when releasing energy：
High-pressure gas device exports stored compressed air, and the interior acting of input expansion unit simultaneously drives electrical power generators,
Air after expansion unit output expansion cooling；
By in normal temperature cold-storage working substance injection heat exchanger in normal temperature storage tank, exchanged heat with the air after expansion cooling, normal temperature
Switch to low-temperature cold accumulation working medium after cold-storage working substance heat exchange, the air after expansion cooling switchs to normal temperature air after heat exchange；
Low-temperature cold accumulation working medium input low-temperature storage tank is stored, low-temperature storage tank is additionally operable in low power consumption or energy storage
The low-temperature cold accumulation working medium is exported to First Heat Exchanger unit；
Normal temperature air input low pressure caisson is stored, low pressure caisson is additionally operable to export the normal temperature air
To the First Heat Exchanger unit.
It is preferred that, its described energy storage is enabled in electric power low ebb, renewable energy power generation redundancy；Release can peak of power consumption,
Electric power accident, renewable energy power generation are enabled when undesirable.
It is preferred that, the part compressor or regulation rotating speed of gas compressor control compressor flow of unit of being calmed the anger by start-stop, from
And adjust energy storage capacity；And/or the expanding machine or regulation expanding machine rotating speed control expanding machine by start-stop demi-inflation unit are done
Function power, so as to adjust generating capacity.
For the object, technical solutions and advantages of the present invention are more clearly understood, below in conjunction with specific embodiment, and reference
Accompanying drawing, the present invention is described in further detail.Following explanations referring to the drawings to embodiment of the present invention are intended to this hair
Bright present general inventive concept is explained, and is not construed as a kind of limitation to the present invention.
Embodiment 1：
Fig. 1 show the enclosed low temperature compressed air energy-storage system embodiment 1 of the present invention, and it is used between two stages of compression, level
Heated between cooling and double expansion, level.Wherein, reference has following meanings in Fig. 1：
Motor 1, low-pressure compressor 2, high-pressure compressor 6, high pressure expansion machine 14, low-pressure expansion machine 18, heat exchanger 4,16,
21st, 29, valve 8,12,23,27,33,40,44,51, pipeline 3,5,7,9,11,13,15,17,20,22,24,26,28,30,
32nd, 34,36,37,38,39,41,43,45,47,48,49,50,52, high-pressure gas device 10, low pressure caisson 25 generates electricity
Machine 19, normal temperature storage tank 31, low-temperature storage tank 42, cryogenic pump 46, normal temperature pump 35, cold-storage working substance and air.
The shared propeller shaft couplings of motor 1 and unit of calming the anger, the shared propeller shaft couplings of generator 19 and expansion unit.
Low-pressure compressor 2 is connected with heat exchanger 29 respectively through pipeline 30, low pressure caisson 25 through pipeline 26,28, valve 27；Low pressure
Compressor 2 interlinks with heat exchanger 4 respectively through pipeline 3, high-pressure compressor 6 through pipeline 5；High-pressure compressor 6 through pipeline 7,9 with and
Valve 8 is connected with high-pressure gas device 10；High pressure expansion machine 14 is through pipeline 11,13 and valve 12 and the phase of high-pressure gas device 10
Lead to；High pressure expansion machine 14 interlinks with heat exchanger 16 respectively through pipeline 15, low-pressure expansion machine 18 through pipeline 17；Low pressure gas storage is filled
25 are put through pipeline 20,22,24, valve 23, heat exchanger 21 with low-pressure expansion machine 18 to be connected；Cryogenic pump 46 is through pipeline 43,45, valve
Door 44 is connected with low-temperature storage tank 42；Heat exchanger 29 and heat exchanger 4 are connected through pipeline 47 and pipeline 49 with cryogenic pump 46 respectively；
Heat exchanger 29 and heat exchanger 4 are connected through pipeline 48 and pipeline 50 with valve 51 respectively；Valve 51 is passed through through pipeline 52, normal temperature pump 35
Pipeline 32,34, valve 33 are connected with normal temperature storage tank 31 respectively；Heat exchanger 16 and heat exchanger 21 are respectively through pipeline 36 and pipeline 38
It is connected with normal temperature pump 35；Hot device 16 and heat exchanger 21 are connected through pipeline 37 and pipeline 39 with valve 40 respectively；Valve 40 is passed through
Pipeline 41 is connected with low-temperature storage tank 42.
During energy storage, valve 8,27,44,51 is opened, valve 12,23,33,40 is closed, motor 1 utilizes trough-electricity band dynamic pressure
Normal temperature air in mechanism of qi group, low pressure energy storage device enters heat exchanger 29 by pipeline 26,28, valve 27, while low-temperature storage tank
Low-temperature cold accumulation working medium enters the cooling normal temperature air of heat exchanger 29 through pipeline 43,45,47, valve 44, cryogenic pump 46 in 42, air
Enter low-pressure compressor 2 after temperature reduction and compress increasing temperature and pressure, the air after compression continues low through pipeline 3 into heat exchanger 4
Warm cold-storage working substance cooling, the air after cooling enters high-pressure compressor 6 through pipeline 5 to be continued to compress and increasing temperature and pressure, and it exports empty
Gas enters high-pressure gas device 10 through valve 8 and pipeline 7,9 and stored, while into the low-temperature cold accumulation in heat exchanger 29, heat exchanger 4
While working medium cooling air, after low-temperature cold accumulation working medium is heated by the air, enters normal temperature storage tank 31 through valve 51, pipeline 52 and carry out
Storage, energy storage terminates, and closes valve 8,27,44,51.Release can when, close valve 8,27,44,51, open valve 12,23,33,
40, pressure-air in high-pressure gas device 10, which enters high pressure expansion machine 14 through pipeline 11,13 and valve 12 and expanded, to cool, and it goes out
The normal temperature cold-storage working substance that mouthful air enters in heat exchanger 16, normal temperature storage tank 31 through pipeline 15 is through pipeline 32,34,36, valve 33, often
Warm pump 35 enters heat exchanger 16 and heats air, and after heat exchanger 16, normal temperature cold-storage working substance is cold by high pressure expansion machine outlet air
But to low temperature, air is heated to environment temperature, enters the continuation expansion work of low-pressure expansion machine 18 through pipeline 17 and drives generating
Machine 19 generates electricity, and the air that low-pressure expansion machine 18 is exported is heated to environment temperature by normal temperature cold-storage working substance again and filled into low pressure gas storage
Stored in putting 25, the cold-storage working substance after the cooling of heat exchanger 16,21 enters through valve 40, pipeline 41 into low-temperature storage tank 42
Row storage.Releasing to terminate, and valve 12,23,33,40 is closed.
Generally, carried out when energy storage is different with exoergic process, during energy storage, valve 8,27,44,51 is opened simultaneously, valve
Door 12,23,33,40 is closed, and the aperture of valve 27,44 is by unit flow control of calming the anger.When releasing energy, valve 12,23,33,40 is same
When open, valve 8,27,44,51 is closed, and the aperture of valve 12,33 is controlled by expansion unit flow.
Embodiment 2：
Fig. 2 show the enclosed low temperature compressed air energy-storage system embodiment 2 of the present invention, its agent structure and embodiment 1
It is identical, but it is using between the two stages of compression in heating replacement embodiment 1 between three stage compression, cascade EDFA and three-level expansion, level, level
Heated between cooling and double expansion, level.Wherein, reference has following meanings in Fig. 2：
Motor 1, low-pressure compressor 55, intermediate pressure compressor 59, high-pressure compressor 63, high pressure expansion machine 64, middle compression swelling
Machine 68, low-pressure expansion machine 72, heat exchanger 53,57,61,66,70,74, high-pressure gas device 10, low pressure caisson 25, normal temperature
Storage tank 31, low-temperature storage tank 42, cryogenic pump 46, normal temperature pump 35, valve 8,12,23,27,33,40,44,51, pipeline 26,28,54,
56、58、60、62、7、9、11、13、65、67、69、71、73、22、24、43、45、81、82、83、84、85、86、52、32、34、
75th, 76,77,78,79,80,41, generator 19, cold-storage working substance and air.
The connection of each part is substantially the same manner as Example 1.
During energy storage, valve 8,27,44,51 is opened, air in valve 12,23,33,40, low pressure caisson 25 is closed and passes through
Cross heat exchanger 53, low-pressure compressor 55, heat exchanger 57, intermediate pressure compressor 59, heat exchanger 61, high-pressure compressor 63, valve 8,27
And pipeline 26,28,54,56,58,60,62,7,9 enters high-pressure gas device 10 and stored, meanwhile, in low-temperature storage tank 42
Low-temperature cold accumulation working medium, which also enters in heat exchanger 53,57,61, cools down every grade of compressor inlet air, and low-temperature cold accumulation working medium is added by air
Enter after heat in normal temperature storage tank 31 and store, energy storage terminates, close valve 8,27,44,51.Release can when, close valve 8,27,44,
51, valve 12,23,33,40 is opened, pressure-air enters the expansion work of high pressure expansion machine 64 by valve 12 and pipeline 11,13,
Then heated, then done work by pipeline 67 into middle-pressure expansion machine 68 into heat exchanger 66 by pipeline 65, then through pipeline 69
Heated into heat exchanger 70, the air after heating does work through pipeline 71 into low-pressure expansion machine 72, while in normal temperature storage tank 31
Cold-storage working substance is entered after every grade of expander outlet air cooling to be stored in low-temperature storage tank 42, is released after terminating, shutoff valve
Door 12,23,33,40.
Particular embodiments described above, has been carried out further in detail to the purpose of the present invention, technical scheme and beneficial effect
Describe in detail bright, it should be understood that the foregoing is only the present invention specific embodiment, be not intended to limit the invention, it is all
Within the spirit and principles in the present invention, any modification, equivalent substitution and improvements done etc. should be included in the protection of the present invention
Within the scope of.
Claims (11)
1. a kind of enclosed low temperature compressed air energy-storage system, it is characterised in that including：
First Heat Exchanger unit, normal temperature air is exchanged heat in the First Heat Exchanger unit with low-temperature cold accumulation working medium, normal temperature
Switch to the air after heat exchange after air heat-exchange, switch to normal temperature cold-storage working substance after the heat exchange of low-temperature cold accumulation working medium, wherein low temperature, which refers to, is less than
The temperature of normal temperature；
Calm the anger unit, the air inputted after the heat exchange, the air after output squeezing, the unit of calming the anger to be more than two-stage, and
And be coaxial cascade or split axle parallel form；
Normal temperature storage tank, is stored for inputting normal temperature cold-storage working substance, is additionally operable to the normal temperature cold-storage working substance output of storage；
High-pressure gas device, is stored for inputting the air after compression, is additionally operable to the compressed air stored by output；
Unit is expanded, the compressed air of storage is inputted, compressed air is in expansion unit to expansion unit acting output expansion drop
Air after temperature；
Second heat exchanger unit, normal temperature storage tank output normal temperature cold-storage working substance in second heat exchanger unit with the expansion
Air after cooling is exchanged heat, and low-temperature cold accumulation working medium is switched to after the heat exchange of normal temperature cold-storage working substance, the air after expansion cooling is through changing
Switch to normal temperature air after heat；
Low-temperature storage tank, is stored for inputting the low-temperature cold accumulation working medium, is additionally operable to export the low-temperature cold accumulation working medium to
One heat exchanger unit；And
Low pressure caisson, is stored for inputting the normal temperature air, is additionally operable to export the normal temperature air to described
One heat exchanger unit.
2. enclosed low temperature compressed air energy-storage system according to claim 1, it is characterised in that also including cryogenic pump, low temperature
Cold-storage working substance is pumped out by the cryogenic pump from low-temperature storage tank, and enters the First Heat Exchanger unit.
3. enclosed low temperature compressed air energy-storage system according to claim 1, it is characterised in that also including normal temperature pump, normal temperature
Cold-storage working substance is pumped out by the normal temperature pump from the normal temperature storage tank, and enters second heat exchanger unit.
4. enclosed low temperature compressed air energy-storage system according to claim 3, it is characterised in that the unit of calming the anger includes
At least one low-pressure compressor and at least one high-pressure compressor, are serially connected as overall multistage compressor, from each low pressure
Air after compressor inlet input heat exchange, exports low-pressure air；Low-pressure air inputs high-pressure compressor again, from high-pressure compressor
Air after output squeezing.
5. enclosed low temperature compressed air energy-storage system according to claim 4, it is characterised in that the unit of calming the anger also is wrapped
Intergrade compressor is included, after the low-pressure air compresses through intergrade compressor, through First Heat Exchanger unit and low-temperature cold accumulation work
Matter exchanges heat, then inputs high-pressure compressor.
6. enclosed low temperature compressed air energy-storage system according to claim 1, it is characterised in that the First Heat Exchanger list
Member and the second heat exchanger unit include two or more heat exchanger, before the compressor input air in unit of calming the anger and heat exchanger
Exchanged heat after expanding machine delivery air in heat exchange or expansion unit with heat exchanger.
7. enclosed low temperature compressed air energy-storage system according to claim 1, it is characterised in that the expansion unit includes
At least one low-pressure expansion machine and at least one high pressure expansion machine, are serially connected or are integrated into overall multiple expansion engine, Mei Yitai
The compressed air of high pressure expansion machine input storage, exports primary expansion air；Each low-pressure expansion machine input primary expansion is empty
Gas, exports final stage expanded air.
8. enclosed low temperature compressed air energy-storage system according to claim 7, it is characterised in that the expansion unit is also wrapped
Intergrade expanding machine is included, the primary expansion air inputs low-pressure expansion machine again after inputting the intergrade expanding machine.
9. enclosed low temperature compressed air energy-storage system according to claim 1, it is characterised in that also including generator, with institute
Expansion unit connection is stated, electrical power generators are driven when expansion unit is done work.
10. a kind of enclosed low temperature compressed air energy storage method, it is characterised in that including：
In low power consumption or energy storage：
Normal temperature air and low-temperature cold accumulation working medium are exchanged heat in First Heat Exchanger unit, are converted into after normal temperature air heat exchange after heat exchange
Air, low-temperature cold accumulation working medium heat exchange after be converted into normal temperature cold-storage working substance；
Motor driving calms the anger unit by the air after the air boil down to compression after heat exchange, and press-in high-pressure gas device is stored；
Stored by using normal temperature storage tank input normal temperature cold-storage working substance；
In peak of power consumption or when releasing energy：
Done work in the stored compressed air of high-pressure gas device output, input expansion unit and simultaneously drive electrical power generators, from swollen
Air after swollen unit output expansion cooling；
Normal temperature cold-storage working substance in normal temperature storage tank is injected in the second heat exchanger unit, exchanged heat with the air after expansion cooling,
Switch to low-temperature cold accumulation working medium after the heat exchange of normal temperature cold-storage working substance, the air after expansion cooling switchs to normal temperature air after heat exchange；
Low-temperature cold accumulation working medium input low-temperature storage tank is stored, low-temperature storage tank is additionally operable to input in low power consumption or energy storage
The low-temperature cold accumulation working medium is to First Heat Exchanger unit；
Normal temperature air input low pressure caisson is stored, low pressure caisson is additionally operable to export the normal temperature air to institute
State First Heat Exchanger unit.
11. enclosed low temperature compressed air energy storage method according to claim 10, it is characterised in that pass through start-stop compressor
The part compressor or regulation rotating speed of gas compressor control compressor flow of group, so as to adjust energy storage capacity；And/or pass through start-stop portion
Divide the expanding machine or regulation expanding machine rotating speed control expanding machine acting ability of expansion unit, so as to adjust generating capacity.
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| CN114909196B (en) * | 2022-04-28 | 2023-06-20 | 西安热工研究院有限公司 | Water pumping compression isobaric release air energy storage system and method |
| CN114991896B (en) * | 2022-06-07 | 2023-09-05 | 西安热工研究院有限公司 | Closed circulation energy storage system and method |
| CN115234329A (en) * | 2022-08-24 | 2022-10-25 | 哈电发电设备国家工程研究中心有限公司 | Closed-cycle compression energy storage power generation system and operation method thereof |
| CN115773164B (en) * | 2023-02-13 | 2023-05-16 | 西安热工研究院有限公司 | Isothermal compressed air synergistic energy storage system and method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3869857A (en) * | 1973-02-01 | 1975-03-11 | Atomenergi Ab | Thermal power plant |
| CN103352830A (en) * | 2013-07-25 | 2013-10-16 | 中国科学院理化技术研究所 | Compressed-air energy-storing power generation system adopting unsteady state compression process |
| CN103438612A (en) * | 2013-08-28 | 2013-12-11 | 中国科学院工程热物理研究所 | Compressed gas distributed energy source system using rare gases as working medium |
| CN104696028A (en) * | 2015-03-04 | 2015-06-10 | 中国大唐集团新能源股份有限公司 | Compressed air energy storage power generation system |
| CN205805631U (en) * | 2016-06-01 | 2016-12-14 | 中国科学院工程热物理研究所 | A kind of enclosed low temperature compressed air energy-storage system |
-
2016
- 2016-06-01 CN CN201610382016.2A patent/CN105863751B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3869857A (en) * | 1973-02-01 | 1975-03-11 | Atomenergi Ab | Thermal power plant |
| CN103352830A (en) * | 2013-07-25 | 2013-10-16 | 中国科学院理化技术研究所 | Compressed-air energy-storing power generation system adopting unsteady state compression process |
| CN103438612A (en) * | 2013-08-28 | 2013-12-11 | 中国科学院工程热物理研究所 | Compressed gas distributed energy source system using rare gases as working medium |
| CN104696028A (en) * | 2015-03-04 | 2015-06-10 | 中国大唐集团新能源股份有限公司 | Compressed air energy storage power generation system |
| CN205805631U (en) * | 2016-06-01 | 2016-12-14 | 中国科学院工程热物理研究所 | A kind of enclosed low temperature compressed air energy-storage system |
Non-Patent Citations (1)
| Title |
|---|
| 《一种完全基于风能的供暖系统的基础研究》;彭国勋;《中国优秀硕士学位论文全文数据库 工程科技II辑（月刊）》;20160315(第03期);C038-997 * |
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