CN213540514U - Liquid air energy storage system with self-absorption of compression heat - Google Patents
Liquid air energy storage system with self-absorption of compression heat Download PDFInfo
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- CN213540514U CN213540514U CN202022333379.1U CN202022333379U CN213540514U CN 213540514 U CN213540514 U CN 213540514U CN 202022333379 U CN202022333379 U CN 202022333379U CN 213540514 U CN213540514 U CN 213540514U
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Abstract
The utility model relates to a liquid air energy storage technical field especially relates to a liquid air energy storage system that compression heat is from dissolving. The system comprises: the input end of a liquid air storage tank of the liquid air energy storage unit is connected with the air compressor set through an energy storage pipeline, and the output end of the liquid air storage tank is connected with the turbine set through an energy release pipeline; the working medium circulation unit comprises a working medium temperature rising pipeline and a working medium temperature lowering pipeline which are connected, the working medium temperature rising pipeline is used for carrying out heat exchange with the output end of the air compressor unit, and the working medium temperature lowering pipeline is used for carrying out heat exchange with the input end of the turbine unit; the absorption refrigerating unit is respectively connected with a first pipeline and a second pipeline, and the first pipeline is used for exchanging heat with the input end of the air compressor unit; and two ends of the second pipeline are respectively connected with the working medium cooling pipelines positioned at two ends of the turbine set in parallel. The system can realize the self-selling and self-accepting of the compression heat in the system, and can solve the problem of energy waste of the existing energy storage system.
Description
Technical Field
The utility model relates to a liquid air energy storage technical field especially relates to a liquid air energy storage system that compression heat is from dissolving.
Background
The accelerated consumption of traditional fossil energy and the increasingly serious environmental problems become the main problems which hinder social progress, and the energy structure is bound to be transformed to green and low carbon. Renewable energy sources are on the move and develop rapidly with the needs of the times, but the incorporation of renewable energy sources into power grids faces great challenges due to their inherent volatility and intermittency, so that the advancement of energy storage technology has become an inevitable requirement for the development of renewable energy sources. Liquid air energy storage has gained wide attention as a large-scale energy storage technology. The reasonable and efficient utilization of the compression heat generated by the liquid air energy storage system in the energy storage process is an important measure for improving the overall efficiency of the system.
At present, most of the compression heat is utilized by coupling an energy storage system and an additional cycle, including an organic rankine cycle, a kalina cycle, an absorption refrigeration cycle and the like, and combining a cold, heat and electricity combined supply flow. In practical engineering, the large-scale energy storage technology focuses on improving the electricity conversion efficiency, and needs of cold energy, heat energy and the like do not exist in many occasions.
However, the existing energy storage system has no technical scheme for reasonably utilizing the compression heat generated in the energy storage process, that is, the existing energy storage system has the condition of energy waste.
SUMMERY OF THE UTILITY MODEL
The utility model discloses aim at solving one of the technical problem that exists among the prior art at least.
Therefore, the utility model provides a liquid air energy storage system that compression heat was from dissolving to solve the extravagant problem of the energy that current energy storage system exists.
According to the utility model discloses liquid air energy storage system of compression heat self-absorption, include:
the liquid air energy storage unit comprises a liquid air storage tank, an air compressor set and a turbine set, wherein the input end of the liquid air storage tank is connected with the air compressor set through an energy storage pipeline, and the output end of the liquid air storage tank is connected with the turbine set through an energy release pipeline;
the working medium circulation unit comprises a working medium temperature rising pipeline and a working medium temperature lowering pipeline which are connected, the working medium temperature rising pipeline is used for carrying out heat exchange with the output end of the air compressor unit, and the working medium temperature lowering pipeline is used for carrying out heat exchange with the input end of the turbine unit;
the absorption refrigeration unit is respectively connected with a first pipeline and a second pipeline, and the first pipeline is used for exchanging heat with the input end of the air compressor unit; and two ends of the second pipeline are respectively connected with the working medium cooling pipelines positioned at two ends of the turbine set in parallel.
According to the utility model discloses an embodiment, liquid air energy storage unit still includes the precooling unit, the air compressor unit establish ties in on the energy storage pipeline, the gaseous heat transfer side of precooling unit establish ties in the air compressor unit input the energy storage pipeline is on the road, the liquid heat transfer side of precooling unit passes through first pipeline with absorption refrigeration unit connects.
According to the utility model discloses an embodiment, air compressor unit includes a plurality of grades of air compressor, precooler unit includes a plurality of grades of air precoolers, a plurality of grades of air compressor according to the preface establish ties in on the energy-storage pipeline, at different levels the gaseous heat exchange side of air precooler is established ties respectively at different levels the air compressor input the energy-storage pipeline is on the way, at different levels the liquid heat exchange side of air precooler connect in parallel in on the first pipeline.
According to the utility model discloses an embodiment, liquid air energy storage unit still includes the cooling unit, the gaseous heat transfer side of cooling unit establish ties in the air compressor unit output the energy storage pipeline is last, the working medium heat transfer side of cooling unit connect in on the working medium intensification pipeline.
According to the utility model discloses an embodiment, the cooling unit includes a plurality of grades of air cooler, and is all levels air cooler's gaseous heat transfer side is established ties respectively at all levels the air compressor output the energy storage pipeline is last, and is all levels air cooler's working medium heat transfer side connect in parallel in on the working medium intensification pipeline.
According to the utility model discloses an embodiment, liquid air energy storage unit still includes the heating unit, the gaseous heat exchange side of heating unit establish ties in the turbine unit input the energy release pipeline is last, the working medium heat exchange side of heating unit connect in working medium cooling pipeline is last, the second pipeline with be located the working medium heat exchange side both ends of heating unit the working medium cooling pipeline is parallelly connected.
According to an embodiment of the present invention, the turbine set includes a plurality of stages of turbines, the heating set includes a plurality of stages of air heaters, the plurality of stages of turbines are sequentially connected in series to the energy releasing pipeline, the gas heat exchanging sides of the air heaters are respectively connected in series to the energy releasing pipeline at the input end of the turbines at each stage, and the working medium heat exchanging sides of the air heaters at each stage are connected in parallel to the working medium cooling pipeline; the input end of the second pipeline is communicated with the working medium cooling pipeline at the working medium heat exchange side input end of the last-stage air heater, and the output end of the second pipeline is communicated with the working medium cooling pipeline at the working medium heat exchange side output end of the first-stage air heater.
According to the utility model discloses an embodiment, working medium circulation unit still includes low temperature storage tank and high temperature storage tank, the output of low temperature storage tank passes through working medium intensification pipeline with the input of high temperature storage tank is connected, the output of high temperature storage tank passes through working medium cooling pipeline with the input of low temperature storage tank is connected.
According to an embodiment of the present invention, the liquid air energy storage unit further includes a cold storage subsystem, the cold storage subsystem includes a first heat exchange side, a second heat exchange side and a third heat exchange side, the first heat exchange side is connected in series to the energy storage pipeline, and the second heat exchange side is connected in series to the energy release pipeline; the liquid air storage tank further comprises an exhaust pipeline, and the third heat exchange side is connected in series to the exhaust pipeline.
According to the utility model discloses an embodiment, liquid air energy storage unit still includes choke valve and cryopump, the choke valve establish ties in liquid air storage tank with between the cold-storage subsystem on the energy storage pipeline, the cryopump establish ties in liquid air storage tank with between the cold-storage subsystem on the energy release pipeline.
The embodiment of the utility model provides an in above-mentioned one or more technical scheme, one of following technological effect has at least:
the utility model discloses liquid air energy storage system of compression heat self-absorption, including liquid air energy storage unit, working medium circulation unit and absorption refrigeration unit. The liquid air energy storage unit comprises a liquid air storage tank, an air compressor unit and a turbine unit, wherein the input end of the liquid air storage tank is connected with the air compressor unit through an energy storage pipeline, and the output end of the liquid air storage tank is connected with the turbine unit through an energy release pipeline so as to execute energy storage and energy release of the liquid air energy storage unit. The working medium circulation unit comprises a working medium warming pipeline and a working medium cooling pipeline which are connected, the working medium warming pipeline is used for heat exchange with the output end of the air compressor unit, and the working medium cooling pipeline is used for heat exchange with the input end of the turbine unit, so that on one hand, the air compression process on the energy storage pipeline of the liquid air energy storage unit is recooled by the working medium warming pipeline, and on the other hand, the air working process on the energy release pipeline of the liquid air energy storage unit is preheated by the working medium cooling pipeline. The absorption refrigerating unit is respectively connected with a first pipeline and a second pipeline, and the first pipeline is used for exchanging heat with the input end of the air compressor unit; and two ends of the second pipeline are respectively connected with the working medium cooling pipelines positioned at two ends of the turbine set in parallel. The absorption refrigeration unit carries out heat exchange in the absorption refrigeration unit by utilizing the first pipeline and the second pipeline, so that the waste heat of the high-temperature heat exchange medium in the working medium circulating unit is recycled for precooling in the air compression process of the air compressor unit. Therefore, the system can realize the self-selling and self-storing of the compression heat in the system, can solve the problem of energy waste of the existing energy storage system, improves the recycling of energy, can avoid energy overflow, and can realize energy conservation and environmental protection.
Additional aspects and advantages of the invention will be set forth in part in the description which follows and, in part, will be obvious from the description, or may be learned by practice of the invention.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
Fig. 1 is a schematic structural diagram of a liquid air energy storage system with self-absorption of compression heat according to an embodiment of the present invention.
Reference numerals:
1: an air compressor; 2: an air precooler; 3: an air cooler; 4: a cold storage subsystem; 5: a throttle valve; 6: a liquid air storage tank; 7: a cryopump; 8: a turbine; 9: an air heater; 10: a low-temperature storage tank; 11: a high-temperature storage tank; 12: an absorption chiller unit; 13: an energy storage pipeline; 14: an energy release pipeline; 15: a working medium temperature rising pipeline; 16: a working medium cooling pipeline; 17: a first pipeline; 18: a second pipeline; 19: an exhaust line; g: a generator; m: an electric motor.
Detailed Description
The following describes embodiments of the present invention in further detail with reference to the accompanying drawings and examples. The following examples are intended to illustrate the invention, but are not intended to limit the scope of the invention.
As shown in fig. 1, an embodiment of the present invention provides a liquid air energy storage system (in the embodiment of the present invention, referred to as "energy storage system" for short) with self-absorption of compression heat. The energy storage system comprises a liquid air energy storage unit, a working medium circulation unit and an absorption refrigerating unit 12.
The liquid air energy storage unit comprises a liquid air storage tank 6, an air compressor set and a turbine set so as to perform energy storage and energy release of the liquid air energy storage unit. The input end of the liquid air storage tank 6 is connected with the air compressor set through an energy storage pipeline 13 to form an energy storage part of the liquid air energy storage unit. The output of the liquid air storage tank 6 is connected to the turbine group via an energy release line 14 to form the energy release part of the liquid air energy storage unit.
The working medium circulating unit comprises a working medium temperature rising pipeline 15 and a working medium temperature reducing pipeline 16 which are connected. The working medium temperature rising pipeline 15 is used for carrying out heat exchange with the output end of the air compressor unit. The working medium cooling line 16 is used for heat exchange with the input of the turbomachine. On one hand, the working medium temperature rising pipeline 15 is used for recooling the air compression process on the energy storage pipeline 13 of the liquid air energy storage unit, so that the compression efficiency of the air compression process is improved; on the other hand, the working medium temperature-reducing pipeline 16 is used for preheating the air working process on the energy-releasing pipeline 14 of the liquid air energy storage unit, so that the working efficiency of the air working process is improved.
The absorption chiller unit 12 is connected to a first line 17 and a second line 18, respectively. The first pipeline 17 is used for exchanging heat with the input end of the air compressor unit; the two ends of the second pipeline 18 are respectively connected in parallel with the working medium cooling pipelines 16 positioned at the two ends of the turbine set. The absorption refrigeration unit 12 performs heat exchange in the absorption refrigeration unit 12 by using the first pipeline 17 and the second pipeline 18, so that waste heat of the high-temperature heat exchange medium in the working medium circulation unit is recycled for precooling in the air compression process of the air compression unit, the waste heat of the high-temperature heat exchange medium in the working medium circulation unit is recycled, and the recycled waste heat is used for precooling in the air compression process, thereby reducing compression power consumption and simultaneously realizing complete utilization of compression heat, namely the compression heat of the energy storage system in the energy storage process and the energy release process is self-consumed, no waste of compression heat is caused, the electric conversion efficiency of the system is effectively improved, and the compression efficiency of the air compression process can also be improved.
Therefore, the system can realize the self-selling and self-storing of the compression heat in the system, can solve the problem of energy waste of the existing energy storage system, improves the recycling of energy, can avoid energy overflow, and can realize energy conservation and environmental protection.
In one embodiment, the liquid air energy storage unit further comprises a pre-chiller. The air compressor unit is connected in series on the energy storage pipeline 13, the gas heat exchange side of the precooler unit is connected in series on the energy storage pipeline 13 at the input end of the air compressor unit, the liquid heat exchange side of the precooler unit is connected with the absorption type refrigerating unit 12 through the first pipeline 17, and the waste heat recovered in the first pipeline 17 exchanges heat with the air in the energy storage pipeline 13 in the precooler unit, so that precooling in the air compression process is realized.
In one embodiment, the liquid air energy storage unit further comprises a cooling unit. The gas heat exchange side of the cooling unit is connected in series to the energy storage pipeline 13 at the output end of the air compressor unit, the working medium heat exchange side of the cooling unit is connected to the working medium warming pipeline 15, and low-temperature heat exchange media in the working medium warming pipeline 15 exchange heat with high-pressure air in the energy storage pipeline 13 in the cooling unit, so that recooling of the air compression process is achieved.
It will be appreciated that the air compressor package comprises a number of stages of air compressors 1 and the pre-chiller package comprises a number of stages of air pre-coolers 2. The air compressors 1 of a plurality of stages are sequentially connected in series on the energy storage pipeline 13, the gas heat exchange sides of the air precoolers 2 of each stage are respectively connected in series on the energy storage pipeline 13 at the input end of the air compressor 1 of each stage, and the liquid heat exchange sides of the air precoolers 2 of each stage are connected in parallel on the first pipeline 17. This structure can realize the multistage air compression process on the energy storage pipeline 13 and correspond to the multistage precooling process of multistage air compression process to further improve air compression efficiency.
It will be appreciated that the cooling package comprises several stages of air coolers 3. The gas heat exchange sides of the air coolers 3 are respectively connected in series on the energy storage pipeline 13 at the output end of the air compressor 1, and the working medium heat exchange sides of the air coolers 3 are connected in parallel on the working medium temperature rising pipeline 15. This structure can realize corresponding to above-mentioned multistage air compression process's multistage sub-cooling process to further improve air compression efficiency.
In one embodiment, the liquid air energy storage unit further comprises a heating unit. The gas heat exchange side of the heating unit is connected in series with the energy release pipeline 14 at the input end of the turbine unit, the working medium heat exchange side of the heating unit is connected to the working medium cooling pipeline 16, and the second pipeline 18 is connected in parallel with the working medium cooling pipelines 16 at the two ends of the working medium heat exchange side of the heating unit. A part of high-temperature heat exchange medium in the working medium cooling pipeline 16 enters the heating unit to exchange heat with air in the energy release pipeline 14, so that the air is preheated in the working process; another part of the high-temperature heat exchange medium enters the absorption refrigeration unit 12 through the second pipeline 18 so as to facilitate waste heat recovery.
Understandably, the turbine set comprises a plurality of stages of turbines 8, the heating set comprises a plurality of stages of air heaters 9, the plurality of stages of turbines 8 are sequentially connected in series on the energy release pipeline 14, the gas heat exchange sides of the air heaters 9 are respectively connected in series on the energy release pipeline 14 at the input end of the turbines 8, and the working medium heat exchange sides of the air heaters 9 are connected in parallel on the working medium cooling pipeline 16; the input end of the second pipeline 18 is communicated with the working medium cooling pipeline 16 at the working medium heat exchange side input end of the final-stage air heater 9, and the output end of the second pipeline 18 is communicated with the working medium cooling pipeline 16 at the working medium heat exchange side output end of the primary-stage air heater 9. The structure can realize the multi-stage air work-doing process on the energy-releasing pipeline 14 and the multi-stage preheating process corresponding to the multi-stage air work-doing process, thereby further improving the air work-doing efficiency; and a part of heat energy of the high-temperature heat exchange medium can be recovered in advance, so that the self-selling of the compression heat in the system is realized.
As can be seen from the above, the structures of the multi-stage air compressor 1 and the multi-stage turbine 8 can be flexibly adjusted according to the difference of parameters such as the outlet pressure and temperature of each stage of compressor 1 and the inlet pressure and temperature of each stage of turbine 8, and some or all of the compressors 1 or turbines 8 are used to achieve the complete recovery of the compression heat on the basis of meeting the required working conditions.
It will be appreciated that the working fluid circulation unit also comprises a low temperature storage tank 10 and a high temperature storage tank 11. The output end of the low-temperature storage tank 10 is connected with the input end of the high-temperature storage tank 11 through a working medium temperature rising pipeline 15, and the output end of the high-temperature storage tank 11 is connected with the input end of the low-temperature storage tank 10 through a working medium temperature lowering pipeline 16. Based on the air compression process and the air work applying process, in the energy storage part, a low-temperature heat exchange medium flows through the working medium temperature rising pipeline 15 between the low-temperature storage tank 10 and each level of air cooler 3, and a high-temperature heat exchange medium flows through the working medium temperature rising pipeline 15 between each level of air cooler 3 and the high-temperature storage tank 11; in the energy release part, a high-temperature heat exchange medium flows through the working medium cooling pipeline 16 between the high-temperature storage tank 11 and each level of air heater 9, and a low-temperature heat exchange medium flows through the working medium cooling pipeline 16 between each level of air heater 9 and the low-temperature storage tank 10.
It can be understood that, in the process of recovering and utilizing the compression heat, the heat exchange medium flowing through the air cooler 3 and the air heater 9 can adopt fluids such as water, heat transfer oil and the like, or adopt a solid-phase packed bed, a phase-change material packed bed and the like to store heat, thereby completing the recovery and storage of the compression heat.
Understandably, the liquid air energy storage unit further comprises a cold accumulation subsystem 4, and the cold accumulation subsystem 4 comprises a first heat exchange side, a second heat exchange side and a third heat exchange side. The first heat exchange side is connected in series to the energy storage pipeline 13, and the second heat exchange side is connected in series to the energy release pipeline 14; the liquid air storage tank 6 further includes an exhaust line 19, and the third heat exchange side is connected in series to the exhaust line 19. In the energy storage stage: the high-pressure air after completing the air compression process is cooled through the first heat exchange side, and then is converted into liquid air to be stored in the liquid air storage tank 6; the original gas in the liquid air storage tank 6 is discharged by the liquid air entering the liquid air storage tank 6, and the discharged gas enters the third heat exchange side through the exhaust pipeline 19 to participate in the internal heat exchange of the cold accumulation subsystem 4, so that the heat exchange efficiency is further improved. In the energy release stage, the liquid air pumped out of the liquid air storage tank 6 enters the second heat exchange side to absorb heat and raise the temperature, so that the liquid air is converted into gaseous air again.
It will be appreciated that the cold storage medium of the cold storage subsystem 4 is preferably at least one of a liquid phase refrigerant (e.g., at least one of methanol, propane, and R123 refrigerants), a solid phase refrigerant (e.g., at least one of metals, rocks, and glass), and a refrigerant made of a phase change cold storage material. In the cold accumulation subsystem 4, the liquid or gaseous air and the cold accumulation medium directly or indirectly contact for heat exchange. Preferably, the cold accumulation subsystems 4 are in one stage or multiple stages, and the cold accumulation subsystems 4 of all stages are preferably connected in series or in parallel or in a structure of corresponding combination of series connection and parallel connection.
It will be appreciated that the liquid air energy storage unit also includes a throttle valve 5 and a cryogenic pump 7. The throttle valve 5 is connected in series on the energy storage pipeline 13 between the liquid air storage tank 6 and the cold accumulation subsystem 4, and is used for decompressing and expanding the low-temperature air flowing through and converting the low-temperature air into liquid air. Cryopump 7 is connected in series with a discharge line 14 between liquid air storage tank 6 and cold storage subsystem 4 for faster pumping of liquid air from liquid air storage tank 6.
In the energy storage stage, the air at normal temperature and normal pressure is pre-cooled by each stage of air pre-cooler 2 and then enters the corresponding air compressor 1, and the air is compressed into high-pressure air and then enters the cold accumulation subsystem 4. In the air compression process, the outlet of each stage of air compressor 1 is connected with the corresponding air cooler 3 through the energy storage pipeline 13, the high-temperature exhaust gas of the air compressor 1 exchanges heat with the low-temperature heat exchange medium from the low-temperature storage tank 10 in the air cooler 3, and the heat exchange medium absorbing the compression heat is heated to form the high-temperature heat exchange medium and enters the high-temperature storage tank 11 for storage. Part of the heat generated in the air compression process returns from the air pre-cooler 2 to the absorption refrigerating unit 12 through the first pipeline 17, while the low-temperature heat storage medium generated by the absorption refrigerating unit 12 reenters the inlet gas of the pre-cooling air compressor 1 in the air pre-cooler 2 through the first pipeline 17, and the other part of the heat is stored in the high-temperature storage tank 11 from the air cooler 3 through the working medium temperature-increasing pipeline 15. The compressed air which completes the air compression process enters the cold accumulation subsystem 4 to absorb cold energy to realize cooling liquefaction. The low-temperature air is throttled by the throttle valve 5 and then is further cooled and depressurized to be converted into low-pressure liquid air which is stored in the liquid air storage tank 6.
In the energy release stage, the liquid air flows out of the liquid air storage tank 6, passes through the cryogenic pump 7 and is pressurized to a certain pressure. The high-pressure liquid air enters the cold accumulation subsystem 4 to release cold energy to the cold accumulation medium, and then the temperature recovery is completed. The air after being reheated enters the turbine set after being preheated by the air heaters 9 at all stages, and is expanded in the turbine set to output work. The high-temperature heat exchange medium in the air heater 9 is the residual high-temperature heat exchange medium from the high-temperature storage tank 11, the air heater 9 is arranged in front of the inlet of each stage of turbine 8, and the air heaters 9 and the turbines 8 are connected through energy release pipelines 14. One part of the high-temperature heat exchange medium flowing out of the high-temperature storage tank 11 enters the air heaters 9 at all stages to complete heat exchange, and the other part of the high-temperature heat exchange medium enters the absorption refrigerating unit 12 to complete waste heat recovery. The low-temperature heat exchange medium after heat exchange flows back to the low-temperature storage tank 10 to be circulated for the next time.
The embodiment of the utility model provides a liquid air energy storage method of heat of compression self-absorption (the utility model discloses in the embodiment for short "energy storage method"), by foretell liquid air energy storage system execution of heat of compression self-absorption. The liquid air energy storage method with self-absorption of compression heat executes an energy storage stage and an energy release stage.
The energy storage stage comprises:
compressing the air into high-pressure air by using an air compressor unit; in the compression process, the air input into the air compressor unit exchanges heat with the heat storage medium in the first pipeline 17 of the absorption refrigeration unit 12 in advance to realize a precooling process, and the high-pressure air output from the air compressor unit exchanges heat with the heat exchange medium in the working medium heating pipeline 15 of the working medium circulation unit to realize a recooling process;
the recooled high-pressure air is converted into liquid air in the energy storage pipeline 13, and the liquid air is stored in the liquid air storage tank 6.
The energy release stage comprises:
the liquid air pumped out of the liquid air storage tank 6 is converted into air in the energy release pipeline 14;
using air to do work in the turbine set; in the working process, a part of the heat exchange medium in the working medium cooling pipeline 16 of the working medium circulation unit exchanges heat with the air input into the turbine unit to realize the preheating process, and the other part of the heat exchange medium enters the absorption refrigerating unit 12 through the second pipeline 18 and exchanges heat with the heat storage medium in the first pipeline 17.
In the energy storage method, the heat energy of the heat exchange medium is recovered to the absorption refrigeration unit 12 by using the second pipeline 18 in the energy release stage, and is used for precooling in the air compression process of the air compression unit through the first pipeline 17. Therefore, the energy storage method can self-sell the compression heat in the energy storage system in the system, and the energy storage method is executed by the energy storage system, so that the energy storage method has all the advantages of the energy storage system, and is not described herein again.
In the description of the embodiments of the present invention, it should be noted that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of describing the embodiments of the present invention and simplifying the description, but do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus should not be construed as limiting the embodiments of the present invention. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the embodiments of the present invention, it should be noted that, unless explicitly stated or limited otherwise, the terms "connected" and "connected" should be interpreted broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; may be directly connected or indirectly connected through an intermediate. The specific meaning of the above terms in the embodiments of the present invention can be understood in specific cases by those skilled in the art.
In embodiments of the invention, unless expressly stated or limited otherwise, the first feature may be directly on or directly under the second feature or indirectly via intermediate members. Also, a first feature "on," "over," and "above" a second feature may be directly or diagonally above the second feature, or may simply indicate that the first feature is at a higher level than the second feature. A first feature being "under," "below," and "beneath" a second feature may be directly under or obliquely under the first feature, or may simply mean that the first feature is at a lesser elevation than the second feature.
In the description herein, references to the description of the term "one embodiment," "some embodiments," "an example," "a specific example," or "some examples," etc., mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of an embodiment of the invention. In this specification, the schematic representations of the terms used above are not necessarily intended to refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, various embodiments or examples and features of different embodiments or examples described in this specification can be combined and combined by one skilled in the art without contradiction.
The above embodiments are merely illustrative, and not restrictive, of the present invention. Although the present invention has been described in detail with reference to the embodiments, it should be understood by those skilled in the art that various combinations, modifications or equivalent substitutions may be made to the technical solution of the present invention without departing from the spirit and scope of the technical solution of the present invention, and all of the technical solutions should be covered by the scope of the claims of the present invention.
Claims (10)
1. A liquid air energy storage system with self-absorption of compression heat, comprising:
the liquid air energy storage unit comprises a liquid air storage tank (6), an air compressor set and a turbine set, wherein the input end of the liquid air storage tank (6) is connected with the air compressor set through an energy storage pipeline (13), and the output end of the liquid air storage tank (6) is connected with the turbine set through an energy release pipeline (14);
the working medium circulation unit comprises a working medium temperature rising pipeline (15) and a working medium temperature reducing pipeline (16) which are connected, the working medium temperature rising pipeline (15) is used for carrying out heat exchange with the output end of the air compressor unit, and the working medium temperature reducing pipeline (16) is used for carrying out heat exchange with the input end of the turbine unit;
the absorption refrigeration unit (12) is respectively connected with a first pipeline (17) and a second pipeline (18), and the first pipeline (17) is used for exchanging heat with the input end of the air compressor unit; and two ends of the second pipeline (18) are respectively connected with the working medium cooling pipelines (16) positioned at two ends of the turbine set in parallel.
2. The liquid air energy storage system with self-absorption of compression heat according to claim 1, wherein the liquid air energy storage unit further comprises a pre-cooling unit, the air compressor unit is connected in series to the energy storage pipeline (13), a gas heat exchange side of the pre-cooling unit is connected in series to the energy storage pipeline (13) at the input end of the air compressor unit, and a liquid heat exchange side of the pre-cooling unit is connected to the absorption refrigeration unit (12) through the first pipeline (17).
3. The liquid air energy storage system with self-absorption of compression heat as claimed in claim 2, wherein the air compressor set comprises a plurality of stages of air compressors (1), the precooler set comprises a plurality of stages of air precoolers (2), the plurality of stages of air compressors (1) are sequentially connected in series on the energy storage pipeline (13), the gas heat exchange side of each stage of air precooler (2) is respectively connected in series on the energy storage pipeline (13) at the input end of each stage of air compressor (1), and the liquid heat exchange side of each stage of air precooler (2) is connected in parallel on the first pipeline (17).
4. The liquid air energy storage system with self-absorption of compression heat as claimed in claim 3, wherein the liquid air energy storage unit further comprises a cooling unit, the gas heat exchange side of the cooling unit is connected in series with the energy storage pipeline (13) at the output end of the air compressor unit, and the working medium heat exchange side of the cooling unit is connected to the working medium temperature rising pipeline (15).
5. The liquid air energy storage system with self-absorption of compression heat as claimed in claim 4, wherein the cooling unit comprises a plurality of stages of air coolers (3), the gas heat exchange side of each stage of air cooler (3) is respectively connected in series with the energy storage pipeline (13) at the output end of each stage of air compressor (1), and the working medium heat exchange side of each stage of air cooler (3) is connected in parallel with the working medium temperature rise pipeline (15).
6. The liquid air energy storage system with self-absorption of compression heat as claimed in claim 1, wherein the liquid air energy storage unit further comprises a heating unit, the gas heat exchange side of the heating unit is connected in series to the energy release pipeline (14) at the input end of the turbine unit, the working medium heat exchange side of the heating unit is connected to the working medium cooling pipeline (16), and the second pipeline (18) is connected in parallel to the working medium cooling pipelines (16) at both ends of the working medium heat exchange side of the heating unit.
7. The liquid air energy storage system with self-absorption of compression heat as claimed in claim 6, wherein the turbine set comprises a plurality of stages of turbines (8), the heating set comprises a plurality of stages of air heaters (9), the plurality of stages of turbines (8) are sequentially connected in series on the energy release pipeline (14), the gas heat exchange side of each stage of air heater (9) is respectively connected in series on the energy release pipeline (14) at the input end of each stage of turbine (8), and the working medium heat exchange side of each stage of air heater (9) is connected in parallel on the working medium cooling pipeline (16); the input end of the second pipeline (18) is communicated with the working medium cooling pipeline (16) at the working medium heat exchange side input end of the last-stage air heater (9), and the output end of the second pipeline (18) is communicated with the working medium cooling pipeline (16) at the working medium heat exchange side output end of the first-stage air heater (9).
8. The compressed heat self-absorption liquid air energy storage system according to any one of claims 1 to 7, wherein the working medium circulation unit further comprises a low temperature storage tank (10) and a high temperature storage tank (11), an output end of the low temperature storage tank (10) is connected with an input end of the high temperature storage tank (11) through the working medium temperature increasing pipeline (15), and an output end of the high temperature storage tank (11) is connected with an input end of the low temperature storage tank (10) through the working medium temperature decreasing pipeline (16).
9. The liquid air energy storage system with self-absorption of compression heat according to any one of claims 1 to 7, characterized in that the liquid air energy storage unit further comprises a cold accumulation subsystem (4), the cold accumulation subsystem (4) comprises a first heat exchange side, a second heat exchange side and a third heat exchange side, the first heat exchange side is connected in series to the energy storage pipeline (13), the second heat exchange side is connected in series to the energy release pipeline (14); the liquid air storage tank (6) further comprises an exhaust pipeline (19), and the third heat exchange side is connected in series with the exhaust pipeline (19).
10. The compressed heat self-dissipating liquid air energy storage system according to claim 9, further comprising a throttle valve (5) and a cryogenic pump (7), the throttle valve (5) being connected in series on the energy storage line (13) between the liquid air storage tank (6) and the cold storage subsystem (4), the cryogenic pump (7) being connected in series on the energy discharge line (14) between the liquid air storage tank (6) and the cold storage subsystem (4).
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112112694A (en) * | 2020-10-19 | 2020-12-22 | 中国科学院理化技术研究所 | Liquid air energy storage system and method for self-absorption of compression heat |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112112694A (en) * | 2020-10-19 | 2020-12-22 | 中国科学院理化技术研究所 | Liquid air energy storage system and method for self-absorption of compression heat |
| CN112112694B (en) * | 2020-10-19 | 2023-10-13 | 中国科学院理化技术研究所 | Liquid air energy storage system and method capable of self-dissipating compression heat |
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Effective date of registration: 20230728 Address after: Building 2, No. 18 Lishi Hutong, Dongcheng District, Beijing 100010 Patentee after: Zhonglv Zhongke energy storage Co.,Ltd. Address before: No. 29 East Zhongguancun Road, Haidian District, Beijing 100190 Patentee before: Technical Institute of Physics and Chemistry Chinese Academy of Sciences |