Disclosure of Invention
The invention aims to solve the technical problem of improving the operation efficiency of a gas compressor, so as to provide a multistage pressure stabilizing cave type heat-insulating compressed air energy storage power station system.
In order to achieve the above purpose, the invention is realized by the following technical scheme:
A multistage pressure stabilizing cave type adiabatic compressed air energy storage power station system comprises a compression device composed of a low-pressure compressor, a medium-pressure compressor and a high-pressure compressor, wherein the low-pressure compressor is connected with a low-pressure turbine part of an expander, the medium-pressure compressor is connected with the medium-pressure turbine part of the expander, the high-pressure compressor is connected with a high-pressure turbine part of the expander, a first heat-charging and discharging integrated oil-gas heat exchanger is arranged at the front end of the air inlet side of the high-pressure turbine part of the expander, a second heat-charging and discharging integrated oil-gas heat exchanger is arranged between the high-pressure turbine part of the expander and the medium-pressure turbine part of the expander, a third heat-charging and discharging integrated oil-gas heat exchanger is arranged between the medium-pressure turbine part of the expander and the low-pressure turbine part of the expander, and the air storage device comprises a high-pressure air storage chamber, a medium-pressure air storage chamber and a low-pressure air storage chamber, wherein an outlet of the high-pressure air storage chamber is connected with the first heat-charging and discharging integrated oil-gas heat exchanger through a high-pressure air storage chamber inlet/outlet valve, an air inlet end of the medium-pressure compressor is connected with the low-pressure air storage chamber, and an air inlet end of the high-pressure air storage chamber is connected with the medium-pressure air storage chamber.
The preset pressure of the low-pressure air storage chamber is equal to the rated exhaust pressure of the low-pressure air compressor and is also equal to the rated inlet pressure of the medium-pressure air compressor, the preset pressure of the medium-pressure air storage chamber is equal to the rated exhaust pressure of the medium-pressure air compressor and is also equal to the rated inlet pressure of the high-pressure air compressor, and the preset pressure of the high-pressure air storage chamber is equal to the rated exhaust pressure of the high-pressure air compressor.
A medium-pressure compressor bypass valve is arranged on a communicating pipeline between the low-pressure air storage chamber and the medium-pressure air storage chamber, and a high-pressure compressor bypass valve is arranged on a communicating pipeline between the medium-pressure air storage chamber and the high-pressure air storage chamber.
The air inlet side of the low-pressure compressor is provided with a low-pressure compressor air inlet valve, the outlet side of the low-pressure compressor is connected with the low-pressure turbine part of the expander through the arranged low-pressure compressor outlet valve and the low-pressure turbine air inlet valve of the expander, the air inlet side of the medium-pressure compressor is connected with the low-pressure air storage chamber through the arranged medium-pressure compressor air inlet valve and the medium-pressure turbine air inlet valve of the expander, the outlet side of the medium-pressure turbine part of the expander is provided with the medium-pressure turbine outlet valve of the expander, the air inlet side of the high-pressure compressor is connected with the medium-pressure air storage chamber through the arranged high-pressure compressor outlet valve and the high-pressure turbine air inlet valve of the expander, and the outlet side of the high-pressure turbine part of the expander is connected with the high-pressure turbine outlet valve of the expander.
The third heat-charging and releasing integrated oil-gas heat exchanger is connected with the low-pressure air storage chamber through a low-pressure air outlet valve after passing through the heat exchanger, and the second heat-charging and releasing integrated oil-gas heat exchanger is connected with the medium-pressure air storage chamber through a medium-pressure air outlet valve after passing through the heat exchanger.
Still include high-order Chang Yagao warm oil storage tank, low-order ordinary pressure low temperature oil storage room and oil water cooler, wherein, first heat release integral type oil gas heat exchanger that fills, second heat release integral type oil gas heat exchanger that fills and third heat release integral type oil gas heat exchanger all are connected with high-order ordinary pressure high temperature oil storage tank and oil water cooler, and oil water cooler is connected with low-order ordinary pressure low temperature oil storage room.
The first heat charging and releasing integrated oil-gas heat exchanger is connected with a high-position normal-pressure high-temperature oil storage tank through a first oil-gas heat exchanger hot oil side valve, the first heat charging and releasing integrated oil-gas heat exchanger is connected with an oil-water cooler through a first oil-gas heat exchanger cold oil side valve, the second heat charging and releasing integrated oil-gas heat exchanger is connected with the high-position normal-pressure high-temperature oil storage tank through a second oil-gas heat exchanger hot oil side valve, the second heat charging and releasing integrated oil-gas heat exchanger is connected with the oil-water cooler through a second oil-gas heat exchanger cold oil side valve, the third heat charging and releasing integrated oil-gas heat exchanger is connected with the high-position Chang Yagao-temperature oil storage tank through a third oil-gas heat exchanger hot oil side valve, and the third heat charging and releasing integrated oil-gas heat exchanger is connected with the oil-water cooler through a third oil-gas heat exchanger cold oil side valve.
The inlet side of the high-position Chang Yagao-temperature oil storage tank is provided with a high-temperature oil storage tank inlet valve, the high-temperature oil storage tank inlet valve is arranged on a hot oil main pipe, the outlet side of the high-temperature oil storage tank inlet valve is sequentially provided with a hot oil pump inlet valve, a hot oil pump outlet check valve and a hot oil pump outlet shutoff valve, the inlet side of the low-position normal-pressure low-temperature oil storage chamber is provided with a low-temperature oil storage chamber inlet valve, and the outlet side of the low-position normal-pressure low-temperature oil storage chamber is sequentially provided with a cold oil pump inlet valve, a cold oil pump outlet check valve and a cold oil pump outlet shutoff valve.
Two ends of the oil-water cooler are provided with oil-water cooler bypass valves.
The three heat charging and discharging integrated oil-gas heat exchangers are respectively connected with a hot oil mother pipe and a cold oil mother pipe, and a cold and hot oil communication valve is arranged between the hot oil mother pipe and the cold oil mother pipe.
Compared with the prior art, the multi-stage pressure stabilizing cave type heat-insulating compressed air energy storage power station system has the following beneficial effects that the multi-stage pressure stabilizing cave type heat-insulating compressed air energy storage power station system is provided, and three cave type air storage chambers with high, medium and low pressures are arranged. Firstly, good rock conditions are fully utilized, larger container space is arranged in sections, the investment is reduced, the range of air inlet parameters and back pressure changes of a compressor is reduced, the stable pressure operation of the compression process is partially realized, the efficiency of the energy storage compression process is improved, the electric-electric conversion efficiency of the whole process of the adiabatic compressed air energy storage power station is further improved by at least 5%, secondly, an integrated oil-gas heat exchanger with heat and charge is adopted, the investment is further saved, thirdly, a compressor with low pressure ratio is adopted, the proportion of mechanical energy converted into heat energy in the compression process is effectively controlled, the energy conversion efficiency of equipment body is improved, the temperature of compressed air after being pressurized is controlled to about 250 ℃, the heat recovery quality is improved, the high-grade energy loss in the energy conversion process is reduced, and the electric-electric conversion efficiency is improved.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
In the description of the present invention, it should be understood that the terms "upper," "lower," "front," "rear," "left," "right," "top," "bottom," "inner," "outer," and the like indicate or are based on the orientation or positional relationship shown in the drawings, merely to facilitate description of the present invention and to simplify the description, and do not indicate or imply that the devices or elements referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present invention.
As shown in fig. 1, the multistage pressure stabilizing cave type adiabatic compressed air energy storage power station system comprises a compression device formed by a low-pressure compressor 6, a medium-pressure compressor 7 and a high-pressure compressor 8, wherein the low-pressure compressor 6 is connected with an expander low-pressure turbine part 11, the medium-pressure compressor 7 is connected with an expander medium-pressure turbine part 10, the high-pressure compressor 8 is connected with an expander high-pressure turbine part 9, a first heat charging and discharging integrated oil-gas heat exchanger 12 is arranged at the front end of the air inlet side of the expander high-pressure turbine part 9, a second heat charging and discharging integrated oil-gas heat exchanger 13 is arranged between the expander high-pressure turbine part 9 and the expander medium-pressure turbine part 10, a third heat charging and discharging integrated oil-gas heat exchanger 14 is arranged between the expander medium-pressure turbine part 10 and the expander low-pressure turbine part 11, the air storage device comprises a high-pressure air storage chamber 3, a medium-pressure air storage chamber 2 and a low-pressure air storage chamber 1, an outlet of the high-pressure air storage chamber 3 is connected with the first heat charging and discharging integrated oil-gas heat exchanger 12 through a high-pressure air storage/outlet valve 28, and the air inlet end of the medium-pressure air storage chamber 8 of the high-pressure air storage chamber 1 is connected with the air inlet end of the low-pressure compressor 8. The energy storage system, the energy release system and the heat exchange and heat storage system are formed by the devices, so that the functions of the multistage voltage stabilizing cave type heat insulation compressed air energy storage power station system are realized together.
The expansion unit comprises a coaxial multistage air turbine expander and a generator, and comprises an expander low-pressure turbine part 11, an expander medium-pressure turbine part 10 and an expander high-pressure turbine part 9. The air inlet pressure of the expansion unit is the pressure of the high-pressure air storage chamber, and the air outlet pressure is the atmospheric pressure. The multistage air turbine expander can be divided into 3 small-capacity different-shaft units according to the power grid requirement, so that the operation flexibility and the low-electric-load power generation efficiency are further improved.
The gas storage device comprises a low-pressure gas storage chamber 1, a medium-pressure gas storage chamber 2 and a high-pressure gas storage chamber 3. The preset pressure of the low-pressure air storage chamber 1 is equal to the rated exhaust pressure of the low-pressure air compressor 6 and is also equal to the rated inlet pressure of the medium-pressure air compressor 7, and is about 0.45-0.5 MPa, the preset pressure of the medium-pressure air storage chamber 2 is equal to the rated exhaust pressure of the medium-pressure air compressor 7 and is also equal to the rated inlet pressure of the high-pressure air compressor 8, and is about 2.0-2.5 MPa, and the preset pressure of the high-pressure air storage chamber 3 is equal to the rated exhaust pressure of the high-pressure air compressor 8, and is about 9.0-12.5 MPa.
Further, a medium-pressure compressor bypass valve 21 is arranged on a communication pipeline between the low-pressure air storage chamber 1 and the medium-pressure air storage chamber 2, and a high-pressure compressor bypass valve 22 is arranged on a communication pipeline between the medium-pressure air storage chamber 2 and the high-pressure air storage chamber 3.
The inlet side of the low-pressure compressor 6 is provided with a low-pressure compressor inlet valve 18, and the outlet side of the low-pressure compressor is connected with the low-pressure turbine part 11 of the expander through a low-pressure compressor outlet valve 19 and an expander low-pressure turbine inlet valve 33. The air inlet side of the medium-pressure compressor 7 is connected with the low-pressure air storage chamber 1 through a medium-pressure compressor air inlet valve 23, the outlet side of the medium-pressure compressor 7 is connected with the medium-pressure turbine part 10 of the expander through a medium-pressure compressor outlet valve 24 and an expander medium-pressure turbine air inlet valve 31 which are arranged, and the outlet side of the expander medium-pressure turbine part 10 is provided with an expander medium-pressure turbine outlet valve 32. The air inlet side of the high-pressure compressor 8 is connected with the medium-pressure air storage chamber 2 through a high-pressure compressor air inlet valve 26, the outlet side of the high-pressure compressor 8 is connected with the high-pressure turbine part 9 of the expander through a high-pressure compressor outlet valve 27 and an expander high-pressure turbine air inlet valve 29 which are arranged, and the outlet side of the high-pressure turbine part 9 of the expander is connected with an expander high-pressure turbine outlet valve 30.
Further, the low-pressure compressor 6, the medium-pressure compressor 7 and the high-pressure compressor 8 are each provided with an independent driving motor.
Further, the pressure ratios of the high, medium and low pressure compressors are basically the same, and the pressure ratio is 4.5-5.0.
Further, the third heat-charging and releasing integrated oil-gas heat exchanger 14 is connected with the low-pressure air storage chamber 1 through a low-pressure air through a heat exchanger rear outlet valve 20, and the second heat-charging and releasing integrated oil-gas heat exchanger 13 is connected with the medium-pressure air storage chamber 2 through a medium-pressure air through a heat exchanger rear outlet valve 25.
The heat exchange device comprises a first heat charging and discharging integrated oil-gas heat exchanger 12, a second heat charging and discharging integrated oil-gas heat exchanger 13 and a third heat charging and discharging integrated oil-gas heat exchanger 14. Wherein, the three oil-gas heat exchangers all adopt high-temperature synthetic heat conduction oil as heat exchange and heat storage media. In the expansion process, the high-temperature heat conduction oil heats the high-pressure air through the oil-gas heat exchanger for expansion work, and the heat conduction oil is further cooled by the oil-water cooler before entering the low-temperature oil storage chamber. The heat-charging and discharging integrated oil-gas heat exchanger is adopted, so that the heat exchanger is shared by the compression process and the expansion process, and the equipment cost of a heat exchange system is saved.
The heat exchange device further comprises a high-level normal pressure high-temperature oil storage tank 5, a low-level normal pressure low-temperature oil storage chamber 4 and an oil-water cooler 15, wherein the first heat charging and discharging integrated oil-gas heat exchanger 12, the second heat charging and discharging integrated oil-gas heat exchanger 13 and the third heat charging and discharging integrated oil-gas heat exchanger 14 are connected with the high-level normal pressure high-temperature oil storage tank 5 and the oil-water cooler 15, and the oil-water cooler 15 is connected with the low-level normal pressure low-temperature oil storage chamber 4. The invention fully utilizes rock conditions, the low-level normal-pressure low-temperature oil storage chamber 4 is used for storing low-temperature heat conduction oil, and the high-level normal-pressure high-temperature oil storage tank 5 is used for storing high-temperature heat conduction oil. In the engineering implementation process, the high-position normal-pressure low-temperature oil storage tank can be used for replacing the function of the low-position normal-pressure low-temperature oil storage chamber 4 according to actual conditions, and the realization of the overall function of the system is not affected.
Further, the first heat-charging and discharging integrated oil-gas heat exchanger 12 is connected with the high-level normal-pressure high-temperature oil storage tank 5 through a first oil-gas heat exchanger hot oil side valve 43, the first heat-charging and discharging integrated oil-gas heat exchanger 12 is connected with the oil-water cooler 15 through a first oil-gas heat exchanger cold oil side valve 40, the second heat-charging and discharging integrated oil-gas heat exchanger 13 is connected with the high-level normal-pressure high-temperature oil storage tank 5 through a second oil-gas heat exchanger hot oil side valve 42, the second heat-charging and discharging integrated oil-gas heat exchanger 13 is connected with the oil-water cooler 15 through a second oil-gas heat exchanger cold oil side valve 39, the third heat-charging and discharging integrated oil-gas heat exchanger 14 is connected with the high-level normal-pressure high-temperature oil storage tank 5 through a third oil-gas heat exchanger hot oil side valve 41, and the third heat-charging and discharging integrated oil-gas heat exchanger 14 is connected with the oil-water cooler 15 through a third oil-gas heat exchanger cold oil side valve 38.
Further, a high-temperature oil storage tank inlet valve 44 is arranged on the inlet side of the high-level normal-pressure high-temperature oil storage tank 5, the high-temperature oil storage tank inlet valve 44 is arranged on the hot oil mother pipe, a hot oil pump inlet valve 45, a hot oil pump 17, a hot oil pump outlet check valve 46 and a hot oil pump outlet shutoff valve 47 are sequentially arranged on the outlet side, a low-temperature oil storage chamber inlet valve 48 is arranged on the inlet side of the low-level normal-pressure low-temperature oil storage chamber 4, and a cold oil pump inlet valve 34, a cold oil pump 16, a cold oil pump outlet check valve 35 and a cold oil pump outlet shutoff valve 36 are sequentially arranged on the outlet side.
Further, both ends of the oil-water cooler 15 are provided with an oil-water cooler bypass valve 37.
Further, the three heat charging and discharging integrated oil-gas heat exchangers are respectively connected with a hot oil main pipe and a cold oil main pipe, and a cold-hot oil communication valve 49 is arranged between the hot oil main pipe and the cold oil main pipe.
The invention constructs a multistage pressure stabilizing cave type heat-insulating compressed air energy storage power station system by utilizing three air storage chambers with high, medium and low pressure, and a compressor, an expander and a heat exchange and heat storage system, thereby realizing the mutual transmission and conversion of energy among electric energy, heat energy, mechanical energy and pressure potential energy. The invention is suitable for popularization and application in areas with good rock conditions and can build cave air storage chambers.
The working process of the invention is as follows:
the technological process of the system is mainly divided into an initial preparation stage, an energy release stage and an energy storage stage.
The solid line in fig. 1 represents an air medium, and the broken line represents a heat conductive oil medium.
Initial preparation stage example:
the low-pressure compressor inlet valve 18, the low-pressure compressor outlet valve 19 and the low-pressure air pass through the heat exchanger back outlet valve 20, the medium-pressure compressor bypass valve 21 and the high-pressure compressor bypass valve 22 are opened, the low-pressure compressor 6 is started, air is sucked from the environment, air injection and pressure boosting are carried out on the low-pressure air storage chamber 1, the medium-pressure air storage chamber 2 and the high-pressure air storage chamber 3, when the pressure of each air storage chamber reaches the preset pressure of the low-pressure air storage chamber, the medium-pressure compressor bypass valve 21 is closed, and the low-pressure preset is completed at the moment.
The medium-pressure compressor inlet valve 23, the medium-pressure compressor outlet valve 24 and the medium-pressure air are opened, the medium-pressure compressor 7 is started through the heat exchanger rear outlet valve 25, the medium-pressure compressor and the low-pressure compressor simultaneously perform gas injection and pressure boosting for the medium-pressure gas storage chamber 2 and the high-pressure gas storage chamber 3, the low-pressure gas storage chamber 1 plays a role in stabilizing pressure in the process, and when the pressures in the medium-pressure gas storage chamber 2 and the high-pressure gas storage chamber 3 reach the preset pressure of the medium-pressure gas storage chamber, the high-pressure compressor bypass valve 22 is closed, and the medium-pressure presetting is completed at the moment.
The high-pressure compressor inlet valve 26, the high-pressure compressor outlet valve 27 and the high-pressure air storage chamber inlet/outlet valve 28 are opened, the high-pressure compressor 8 is started, the high-pressure air, the middle-pressure air and the low-pressure air are used for injecting air and boosting the pressure of the high-pressure air storage chamber 3, the low-pressure air storage chamber 1 and the middle-pressure air storage chamber 2 perform a pressure stabilizing function in the process, when the pressure in the high-pressure air storage chamber 3 reaches the preset pressure of the high-pressure air storage chamber, the low-pressure compressor 6, the middle-pressure air compressor 7 and the high-pressure air storage chamber 8 stop working, the low-pressure compressor outlet valve 19 and the low-pressure air are closed, and the low-pressure air passes through the heat exchanger back outlet valve 20, the middle-pressure air compressor outlet valve 24 and the middle-pressure air passes through the heat exchanger back outlet valve 25, the high-pressure compressor outlet valve 27 and the high-pressure air storage chamber inlet/outlet valve 28, and the high-pressure air storage chamber is finished at the moment.
At the beginning of the initial preparation phase, the cold oil pump inlet valve 34, the cold oil pump outlet shutoff valve 36, the oil-water cooler bypass valve 37, the third oil-gas heat exchanger cold oil side valve 38, the second oil-gas heat exchanger cold oil side valve 39, the first oil-gas heat exchanger cold oil side valve 40, the third oil-gas heat exchanger hot oil side valve 41, the second oil-gas heat exchanger hot oil side valve 42, the first oil-gas heat exchanger hot oil side valve 43, the high-temperature oil storage tank inlet valve 44 are kept open, and the cold oil pump 16 is started while the low-pressure compressor is started. The heat conducting oil flows out from the low-level normal pressure low-temperature oil storage chamber 4, passes through the oil-water cooler bypass valve 37, absorbs heat generated in the compression process of the air compressor by the third heat charging and discharging integrated oil-gas heat exchanger 14, the second heat charging and discharging integrated oil-gas heat exchanger 13 and the first heat charging and discharging integrated oil-gas heat exchanger 12, and is stored in the high-level normal pressure high-temperature oil storage tank 5.
Through the process, the conversion of electric energy into pressure potential energy and compression heat energy is realized. At this time, the pressure potential energy is stored in the air storage chamber in the form of high-pressure air, and the compression heat energy is stored in the high-temperature oil tank in the form of high-temperature heat conduction oil.
Energy release power generation phase embodiment:
In the external power utilization peak period, a high-pressure air storage chamber inlet/outlet valve 28, an expander high-pressure turbine inlet valve 29, an expander high-pressure turbine outlet valve 30, an expander medium-pressure turbine inlet valve 31, an expander medium-pressure turbine outlet valve 32 and an expander low-pressure turbine inlet valve 33 are opened, a coaxial multistage air turbine expansion unit is opened, and high-pressure air in the high-pressure air storage chamber 3 is discharged into the atmosphere after power generation through power generation of an expander.
At the beginning of the energy release stage, the hot oil pump inlet valve 45, the hot oil pump outlet shutoff valve 47 and the low-temperature oil storage chamber inlet valve 48 are kept open, the hot oil pump 17 is started, high-temperature heat conduction oil exchanges heat with air through the first heat charging and discharging integrated oil-gas heat exchanger 12, the second heat charging and discharging integrated oil-gas heat exchanger 13 and the third heat charging and discharging integrated oil-gas heat exchanger 14, and the heat conduction oil is cooled again through the oil-water cooler 15 after heat release and temperature reduction, and then is stored in the low-level normal-pressure low-temperature oil storage chamber 4.
Through the process, the conversion of pressure potential energy and compression heat energy into electric energy is realized.
Energy storage phase examples:
when the electricity of the external power grid is rich and electricity is needed to be stored, the low-pressure air compressor 6, the medium-pressure air compressor 7, the high-pressure air compressor 8 and the cold oil pump 16 are started. The low-pressure compressor sucks air from the environment and compresses, the air enters the medium-pressure compressor 7 for compression after being stabilized by the low-pressure air storage chamber 1, and the air enters the medium-pressure air storage chamber 2 for stabilization again and is compressed to the high-pressure air storage chamber 3 for storage by the high-pressure air compressor 8.
Meanwhile, the compressed high-temperature high-pressure air respectively enters the third heat charging and discharging integrated oil-gas heat exchanger 14, the second heat charging and discharging integrated oil-gas heat exchanger 13 and the first heat charging and discharging integrated oil-gas heat exchanger 12 to exchange heat with heat conduction oil, and the heat conduction oil absorbs heat and heats up and then enters the high-position normal-pressure high-temperature oil storage tank 5.
Through the process, the conversion of electric energy into pressure potential energy and compression heat energy is realized. And after the energy storage phase is finished, waiting for the next energy release power generation phase, and finishing the whole energy storage-power generation cycle.
The compression device comprises three air compressors with independent driving motors, namely a high-pressure compressor, a medium-pressure compressor and a low-pressure compressor, wherein the pressure ratios of the high-pressure compressor, the medium-pressure compressor and the low-pressure compressor are basically the same. Each set of air compressor can be a single high-power compressor or a plurality of low-power compressors which are operated in parallel. And the inlet and the outlet of the air compressor are respectively provided with a shutoff valve, so that flexible scheduling of an initial preparation stage and an energy storage stage is realized.
The expansion device comprises a coaxial multistage air turbine expansion unit, and the expansion unit comprises a high-pressure turbine section, a medium-pressure turbine section, a low-pressure turbine section and a generator, and is used for realizing the energy release process of a system together with a turbine inlet and outlet valve. The multistage air turbine expander can be divided into 3 small-capacity different-shaft units according to the power grid requirement, so that the operation flexibility and the low-electric-load power generation efficiency are further improved.
The gas storage device comprises three cave type gas storage chambers with high, medium and low pressure, and the inlet and outlet of the gas storage chambers are provided with shutoff valves, so that the pressure potential energy is stored. In the initial preparation stage, a compressor is started to compress air, so that the pressure presettings of the high, medium and low pressure air storage chambers are realized. And in the energy release stage, releasing high-pressure air in the high-pressure air storage chamber to the expander to perform expansion work. In the energy storage stage, the high-pressure, medium-pressure and low-pressure compressors are simultaneously started to compress air in the environment to high pressure and store the compressed air in the high-pressure air storage chamber, and in the process, the low-pressure air storage chamber and the medium-pressure air storage chamber can play a role in stabilizing pressure.
In the invention, heat conduction oil is used as a heat exchange and storage medium. The heat exchange device comprises three groups of charge and discharge integrated oil-gas heat exchangers and one group of oil-water coolers. In the initial preparation stage and the energy storage stage, high-temperature air generated by the operation of the low, medium and high-pressure compressors respectively enters corresponding oil-gas heat exchangers to exchange heat with heat conduction oil, and the heat conduction oil after heat absorption and temperature rise enters a high-temperature oil storage tank to be stored. In the energy release stage, air is heated by high-temperature heat conduction oil through a corresponding oil-gas heat exchanger before entering each section of turbine, then enters the turbine to expand and do work, and the heat conduction oil after heat release and temperature reduction is cooled again through an oil-water cooler and then enters a low-temperature oil storage chamber for storage.
In the invention, heat conduction oil is used as a heat exchange and storage medium. The heat storage device comprises a high-level Chang Yagao-temperature oil storage tank and a low-level normal-pressure low Wen Dongxue-type oil storage chamber (the low-level normal-pressure low Wen Dongxue-type oil storage chamber can be replaced by the high-level normal-pressure low-temperature oil storage tank according to practical situations, and the repeated explanation is omitted hereinafter), and a hot oil pump and a cold oil pump which are connected with the heat storage system and the heat exchange system. In the initial preparation stage and the energy storage stage, the low-temperature heat conduction oil in the low-temperature oil storage chamber is conveyed to the heat exchange system through the cold oil pump to absorb heat and then returns to the high-temperature oil storage tank to store heat. In the energy release stage, the high-temperature heat conduction oil in the high-temperature oil storage tank is conveyed to the heat exchanger system through the hot oil pump to release heat and then returns to the low-temperature oil storage chamber for storage. Meanwhile, in the necessary stages of system maintenance and the like, the circulating flow of the heat conduction oil in the high-temperature oil storage tank can be realized by opening the hot oil pump, the front valve, the rear valve and the inlet valve of the high-temperature oil storage tank so as to avoid solidification, the circulating flow of the heat conduction oil in the low-temperature oil storage tank can be realized by opening the cold oil pump, the front valve, the rear valve and the inlet valve of the low-temperature oil storage chamber so as to avoid solidification, and the circulating flow of the heat conduction oil in a system pipeline can be realized by opening the communicating valve of the hot oil main pipe and the cold oil main pipe.
The middle-high, middle-low pressure air storage chambers and the low-position normal-pressure low-temperature air storage chambers realize functions by constructing artificial cave. Other devices such as a compression device, an expansion device, a heat exchange device and a high-level normal-pressure high-temperature oil storage tank are uniformly distributed in the ground area.
The beneficial effects of the invention are:
in the existing adiabatic compressed air energy storage system, a coaxial multistage air compressor set is adopted, and only one high-pressure air storage chamber is arranged. In the actual operation process, the working performance and efficiency of the air compressor can be affected due to the continuous change of the pressure of the air storage chamber.
The invention is provided with a low-pressure compressor, a medium-pressure compressor and a high-pressure compressor which have basically the same pressure ratio and are provided with three air storage chambers with high, medium and low pressures respectively. In the energy storage stage, the low-pressure air storage chamber provides stable back pressure for the operation of the low-pressure air compressor, the operation efficiency of the low-pressure air compressor is guaranteed, the low-pressure air storage chamber and the medium-pressure air storage chamber provide stable air inlet parameters and back pressure for the operation of the medium-pressure air compressor, the operation efficiency of the medium-pressure air compressor is guaranteed, and the medium-pressure air storage chamber and the high-pressure air storage chamber provide stable air inlet parameters and back pressure for the operation of the high-pressure air compressor, and the operation efficiency of the high-pressure air compressor is guaranteed.
In conclusion, the invention improves the problem of efficiency reduction of variable working condition operation in the existing adiabatic compressed air energy storage system to a certain extent, establishes a novel multistage voltage stabilizing cave type adiabatic compressed air energy storage power station system and improves the overall efficiency of the adiabatic compressed air energy storage power station.
Meanwhile, the invention adopts the charge and discharge integrated oil-gas heat exchanger, so that the compression process and the expansion process share the heat exchanger, thereby saving the equipment cost of a heat exchange system and having economic advantages.
The foregoing is merely a preferred embodiment of the present invention, and it should be noted that it will be apparent to those skilled in the art that several changes and modifications can be made without departing from the general inventive concept, and these should also be regarded as the scope of the invention.