Disclosure of Invention
The invention aims to provide a photo-thermal power generation energy supply system for an agricultural industrial park, which can supply electric energy to the agricultural industrial park and external facilities all the year round, can also utilize the generated waste heat, realize the function of energy storage of the waste heat in a non-heating season in a crossing season, meet the refrigeration requirement in summer, meet the heating requirement in a heating season, realize the cascade utilization of energy from high temperature to low temperature and improve the economic benefit of the agricultural industrial park.
In order to achieve the above purpose, the invention provides a photo-thermal power generation energy supply system for an agricultural industrial park, which comprises an agricultural facility unit, a solar heat collection energy storage unit, a power generation unit, a low-temperature energy supply unit and a cross-season heat storage unit, wherein the agricultural facility unit and a heat collector array of the solar heat collection energy storage unit are arranged side by side at intervals, and the low-temperature energy supply unit is connected with the cross-season heat storage unit;
The solar energy heat collection energy storage unit with be provided with steam generator, superheater and reheater between the power generation unit, the power generation unit with low temperature energy supply unit passes through the condenser and is connected.
Preferably, the solar heat collection and energy storage unit comprises a second electric three-way valve, an oil-gas separator, a heat conduction oil pump, a first electric three-way valve, a groove type heat collector, an oil salt heat exchanger and a third electric three-way valve which are sequentially connected, and the first electric three-way valve is also communicated with an oil inlet of the oil salt heat exchanger.
Preferably, one end of the oil salt heat exchanger is connected with a low-temperature molten salt tank, the other end of the oil salt heat exchanger is connected with a high-temperature molten salt tank, a low-temperature molten salt pump is arranged on the outlet side of the low-temperature molten salt tank, a high-temperature molten salt pump is arranged on the outlet side of the high-temperature molten salt tank, and anti-condensation electric heaters are arranged inside the high-temperature molten salt tank and the low-temperature molten salt tank.
Preferably, one side of the oil-gas separator is provided with a high-low level groove device connected with the nitrogen sealing device.
Preferably, a pipeline at one end of the third electric three-way valve penetrates through the reheater and then is communicated with the second electric three-way valve, and a pipeline at the other end of the third electric three-way valve penetrates through the superheater and the steam generator in sequence and then is communicated with the second electric three-way valve.
Preferably, the power generation unit comprises a steam turbine, a condenser, a condensate pump, a low-pressure heater, a deaerator, a high-pressure heater, a fourth electric three-way valve and a biomass boiler which are sequentially connected, wherein a pipeline of the fourth electric three-way valve sequentially penetrates through the steam generator, the superheater is communicated with a high-pressure cylinder of the steam turbine, a high-pressure cylinder outlet pipe of the steam turbine penetrates through the reheater and then is connected with a low-pressure cylinder of the steam turbine, the biomass boiler is communicated with the high-pressure cylinder of the steam turbine, a turbine generator is arranged at one end of the low-pressure cylinder of the steam turbine, and the low-pressure cylinder of the steam turbine is connected with the low-pressure heater, the deaerator, the high-pressure heater and the lithium bromide unit through air extraction pipelines respectively.
Preferably, the low-temperature energy supply unit comprises a heat exchange coil, a cooling water circulating pump, a fifth electric three-way valve, a sixth electric three-way valve, a high-temperature ground source heat pump unit and a seventh electric three-way valve which are sequentially closed and connected, the fifth electric three-way valve is further communicated with a water inlet of the heat exchange coil of the condenser through a cooling tower and an electric two-way valve, and a water outlet of the lithium bromide unit is further communicated with the water inlet of the cooling tower.
Preferably, the lithium bromide unit is connected with a refrigerating mechanism of the agricultural facility unit, and a water outlet of the refrigerating mechanism of the agricultural facility unit is communicated with a water inlet of the lithium bromide unit through a refrigerating circulating pump;
preferably, the condensation end of the high-temperature ground source heat pump unit is connected with a heating mechanism of the agricultural facility unit, and the water outlet of the heating mechanism of the agricultural facility unit is communicated with the water inlet of the condensation end of the high-temperature ground source heat pump unit through a heating circulating pump.
Preferably, the sixth electric three-way valve is further communicated with an inlet of the cross-season heat storage unit, the seventh electric three-way valve is further communicated with a water outlet of the cross-season heat storage unit, and the cross-season heat storage unit is composed of a vertical buried pipe array arranged in soil;
the agricultural facility unit further comprises a greenhouse and a culture room.
Therefore, the photo-thermal power generation energy supply system for the agricultural industrial park has the beneficial effects that:
(1) According to the invention, the greenhouse and the solar trough type heat collectors are arranged alternately and side by side, and crops can be planted normally below the solar trough type heat collectors, so that the planar use of the traditional agriculture to the land is changed, the land utilization rate of the agriculture industrial park is improved, the effective combination of modern agriculture and clean energy is realized, and the problems of remote places, behind infrastructure construction and insufficient energy supply facilities of the agriculture industrial park are solved.
(2) The biomass boiler auxiliary equipment is provided with the high-temperature molten salt energy storage device, so that power generation can be stably performed all the year round, power generation waste heat is utilized for cross-season energy storage and summer refrigeration in non-heating seasons, and power generation waste heat and cross-season heat storage units are utilized for heating in heating seasons, so that full utilization of high-grade heat energy to low-grade heat energy is realized through cascade utilization of energy sources, the energy-saving effect is remarkable, and better economic benefits can be brought to an agricultural industrial park.
(3) The invention couples two renewable energy sources of solar energy and biomass energy, and the biomass energy can use waste straws, waste fungus sticks or other agricultural wastes of the agricultural industry as sources, so that the closed cycle of agricultural production can be realized, and the agricultural wastes are converted into wastes for power generation, thereby further increasing the economic benefit. The solar energy and biomass energy belong to clean energy, can replace the existing coal-fired boiler used in the agricultural heat field, is beneficial to reducing the emission of atmospheric pollutants, and has stronger popularization and demonstration significance in winning blue sky guard war.
The technical scheme of the invention is further described in detail through the drawings and the embodiments.
Detailed Description
Embodiments of the present invention will be further described with reference to the accompanying drawings.
Fig. 1 is a schematic structural view of a photo-thermal power generation and supply system for an agricultural industrial park according to the present invention, fig. 2 is a schematic structural view of a photo-thermal power generation and supply system for an agricultural industrial park according to the present invention, and fig. 3 is an energy utilization schematic view of a photo-thermal power generation and supply system for an agricultural industrial park according to the present invention, as shown in the drawings, a photo-thermal power generation and supply system for an agricultural industrial park comprises an agricultural facility unit 100, a solar heat collection and storage unit 200, a power generation unit 300, a low Wen Gongneng unit 400 and a cross-season heat storage unit 500, the agricultural facility unit 100 further comprises a greenhouse and a cultivation room, and the agricultural facility unit 100 and a trough collector 201 array of the solar heat collection and storage unit 200 are arranged side by side at intervals, thereby improving land utilization rate of the agricultural industrial park and realizing effective combination of modern agriculture and clean energy.
The solar heat collection and energy storage unit 200 comprises a second electric three-way valve 210, an oil-gas separator 212, a heat conduction oil pump 208, a first electric three-way valve 209, a groove type heat collector 201, an oil salt heat exchanger 202 and a third electric three-way valve 211 which are sequentially connected, wherein heat collected by the groove type heat collector 201 is introduced into the oil salt heat exchanger 202 under the action of the heat conduction oil pump 208 and flows out through the third electric three-way valve 211. One side of the oil-gas separator 212 is provided with a high-low level groove device 213 connected with a nitrogen sealing device 214, and has a liquid level early warning function.
The pipeline at one end of the third electric three-way valve 211 penetrates through the reheater 304 and then is communicated with the second electric three-way valve 210, and the medium oil is cooled in the reheater 304 and then returns to the trough type heat collector through the second electric three-way valve 210. The pipeline at the other end of the third electric three-way valve 211 sequentially penetrates through the superheater 303 and the steam generator 302 and then is communicated with the second electric three-way valve 210, and medium oil sequentially passes through the superheater 303 and the steam generator 302 to dissipate heat and then enters the pipeline of the second electric three-way valve 210. That is, a steam generator 302, a superheater 303, and a reheater 304 are provided between the solar heat collection and energy storage unit 200 and the power generation unit 300, and heat absorbed by the solar heat collection and energy storage unit 300 is exchanged by the reheater 304, the superheater 303, and the steam generator 302.
One end of the oil salt heat exchanger 202 is connected with a low-temperature molten salt tank 203, the outlet side of the low-temperature molten salt tank 203 is provided with a low-temperature molten salt pump 205, the other end of the oil salt heat exchanger is connected with a high-temperature molten salt tank 204, the outlet side of the high-temperature molten salt tank 204 is provided with a high-temperature molten salt pump 206, the low-temperature molten salt tank 203 is pumped in under the action of the low-temperature molten salt pump 205, absorbs heat in the oil salt heat exchanger 202 and becomes high-temperature molten salt, and the high-temperature molten salt is stored in the high-temperature molten salt tank 204. In the process, the medium oil in the oil salt heat exchanger 202 releases heat, and energy is stored in the molten salt. Or the high-temperature molten salt in the high-temperature molten salt tank 204 enters the oil salt heat exchanger 202 to release heat under the action of the high-temperature molten salt pump 206, and returns to the low-temperature molten salt tank 203 after being changed into low-temperature molten salt. In the process, medium oil in the oil-salt heat exchanger 202 absorbs heat, so that release of molten salt energy storage is realized. The high-temperature molten salt tank 204 and the low-temperature molten salt tank 203 are both internally provided with an anti-condensation electric heater 207 to prevent molten salt condensation.
When the solar energy is insufficient due to the fact that the first electric three-way valve 209 is communicated with the oil inlet of the oil-salt heat exchanger 202, the first electric three-way valve 209 is connected with the oil-salt heat exchanger 202, and medium oil directly enters the oil-salt heat exchanger 202 through the first electric three-way valve 209 to absorb heat.
The power generation unit 300 comprises a steam turbine 305, a condenser 307, a condensate pump 308, a low-pressure heater 309, a deaerator 310, a high-pressure heater 311, a fourth electric three-way valve 312 and a biomass boiler 301 which are sequentially connected, wherein the biomass boiler 301 is communicated with a high-pressure cylinder of the steam turbine 305, condensed water in the steam turbine 305 sequentially enters the low-pressure heater 309, the deaerator 310 and the high-pressure heater 311 under the action of the condensate pump 308 to perform primary heating on the water, and then is changed into steam under the heating action of the biomass boiler 301 to enter the high-pressure cylinder of the steam turbine 305.
The pipeline of the fourth electric three-way valve 312 also sequentially penetrates through the steam generator 302 and the superheater 303 and then is communicated with the steam turbine 305, and the primarily heated water sequentially passes through the steam generator 302 and the superheater 303 to absorb heat again. The high-pressure cylinder outlet pipe of the steam turbine 305 penetrates through the reheater 304 and then is connected with the low-pressure cylinder of the steam turbine 305, and water in the high-pressure cylinder of the steam turbine 305 enters the low-pressure cylinder of the steam turbine 305 after the reheater 304 absorbs heat. One end of the low pressure cylinder on the steam turbine 305 is provided with a steam turbine generator 306, and the steam turbine generator 306 is driven to generate electricity. The low-pressure cylinder of the steam turbine 306 is respectively connected with the low-pressure heater 309, the deaerator 310 and the high-pressure heater 311 through the air extraction pipeline 313, and the steam of the low-pressure cylinder in the steam turbine 305 can also enter the low-pressure heater 309, the deaerator 310 and the high-pressure heater 311.
The low-pressure cylinder of the steam turbine 305 is connected with the lithium bromide unit 403 through an air extraction pipeline, the lithium bromide unit 403 is connected with the refrigerating mechanism of the agricultural facility unit 100, a refrigerating circulation pump 410 is arranged between the refrigerating mechanism of the agricultural facility unit 100 and a water inlet of the lithium bromide unit 403, and water vapor absorbs heat in the lithium bromide unit 410 under the action of the refrigerating circulation pump 410, so that the refrigerating mechanism of the agricultural facility unit realizes refrigeration. The water outlet of the lithium bromide unit 403 is also communicated with the water inlet of the cooling tower 407, and the cooling water can be cooled in the cooling tower 407.
The power generation unit 300 is connected with the low-temperature energy supply unit 400 through the condenser 307, and a heat exchange coil in the condenser 307 on the power generation unit 300 is positioned in the low-temperature energy supply unit 400. The low Wen Gongneng unit 400 comprises a heat exchange coil pipe, a cooling water circulating pump 401, a fifth electric three-way valve 402, a sixth electric three-way valve 405, a high-temperature ground source heat pump unit 404 and a seventh electric three-way valve 406 which are sequentially connected in a closed mode, and condensed water is returned to the heat exchange coil pipe for absorbing heat after the heat of the high-temperature ground source heat pump unit 404 is dissipated.
The condensation end of the high-temperature ground source heat pump unit 404 is connected with a heating mechanism of the agricultural facility unit 100, and the water outlet of the heating mechanism of the agricultural facility unit 100 is communicated with the water inlet of the condensation end of the high-temperature ground source heat pump unit 404 through a heating circulating pump 409, so that cold water in the heating mechanism of the agricultural facility unit 100 continuously absorbs heat under the action of the heating circulating pump 409.
The low Wen Gongneng unit 400 is connected with the cross-season heat storage unit 500, the cross-season heat storage unit 500 is formed by an array of vertical buried pipes 501 arranged in soil, and the low Wen Gongneng unit 400 stores heat in the cross-season heat storage unit 500. The sixth electric three-way valve 406 is communicated with the inlet of the cross-season heat storage unit 400, the seventh electric three-way valve 406 is also communicated with the water outlet of the cross-season heat storage unit 500, and water in the pipeline of the sixth electric three-way valve 406 is returned to the heat exchange coil in the condenser 307 through the seventh electric three-way valve 406 after heat dissipation in the cross-season heat storage unit 500.
The fifth electric three-way valve 402 is also communicated with a water inlet of a heat exchange coil of the condenser 307 through the cooling tower 407 and the electric two-way valve 408, and water flow heat in a pipeline of the fifth electric three-way valve 402 is released by the cooling tower 407 and then returns into the heat exchange coil through the electric two-way valve 408.
When the solar heat-conducting oil pump is used, the heat-conducting oil pump 208 circulates low-temperature heat-conducting oil into a mirror field pipeline of the groove type heat collector 201 through the first electric three-way valve 209, the groove type heat collector 201 collects solar energy, the low-temperature heat-conducting oil is heated to high-temperature heat-conducting oil with the temperature of 393 ℃, the high-temperature heat-conducting oil enters the third electric three-way valve through the oil salt heat exchanger 202, the high-temperature heat-conducting oil respectively enters the superheater 303 and the reheater 304 to heat the steam in the superheater 303 and the reheater 304, the temperature of the heat-conducting oil after being heated by the superheater 303 is reduced, the heat-conducting oil enters the steam generator 302 to heat condensed water to be low-temperature steam, the low-temperature steam is further cooled, and the low-temperature heat-conducting oil is collected into the second electric three-way valve 210 and returns to the oil inlet end of the heat-conducting oil pump 208 through the oil separator 212 to complete one cycle.
When the heat-rich heat conduction oil temperature collected by solar energy can maintain the normal power generation of the steam turbine 305, the low-temperature molten salt pump 205 is started to circulate 292 ℃ low-temperature molten salt in the low-temperature molten salt tank 203 to the oil-salt heat exchanger 202, after the low-temperature molten salt exchanges heat with 393 ℃ high-temperature heat conduction oil, the temperature is increased to 385 ℃ high-temperature molten salt, and the high-temperature molten salt is conveyed to the high-temperature molten salt tank 204 for storage, so that the high-temperature energy storage process is completed. When solar energy is insufficient in night or cloudy, rain and snow days, the high-temperature molten salt pump 206 is started, 385 ℃ high-temperature molten salt in the high-temperature molten salt tank 204 is circulated to the oil-salt heat exchanger 202, after heat exchange is carried out on the high-temperature molten salt and low-temperature heat conduction oil, the temperature is reduced to 292 ℃, the low-temperature molten salt is conveyed to the low-temperature molten salt tank 203 for storage, and therefore, the power generation time of the steam turbine 305 is stably prolonged through the molten salt high-temperature energy storage equipment.
The condensed water is respectively conveyed to the steam generator 302 and the biomass boiler 301 through a fourth electric three-way valve 312, is heated to be low-temperature steam through heat conduction oil, is conveyed to the superheater 303, is further heated to be high-temperature high-pressure 383 ℃ superheated steam, and the 383 ℃ superheated steam enters a high-pressure cylinder of the steam turbine 305 to drive the steam turbine 305 to do work and drive the steam turbine generator 306 to generate power. The superheated steam is cooled in a high-pressure cylinder to be changed into low-temperature low-pressure steam, the low-pressure steam is conveyed to a reheater 304 to be secondarily heated and warmed by high-temperature heat conduction oil, the low-pressure steam is conveyed to a low-pressure cylinder of a steam turbine 305 to continue turbine power, a turbine generator 306 is driven to generate power, and low-pressure dead steam at 50-70 ℃ is cooled in a condenser 307 to be changed into condensed water at about 50 ℃.
After a part of steam in a low-pressure cylinder of the steam turbine 305 is conveyed to a low-pressure heater 309 to preliminary preheat the condensate, a part of steam is conveyed to a deaerator 310 to thermally deaerate the condensate, a part of steam is conveyed to a high-pressure heater 311 to further preheat the condensate, a condensate pump 308 conveys the condensate in a condenser 307 to sequentially pass through the low-pressure heater 309, the deaerator 310 and the high-pressure heater 311, and after deaeration and waste heat of the condensate are completed, the condensate enters a steam generator 302 and a biomass boiler 301 through a fourth electric three-way valve 312 to complete the whole cycle.
In a non-heating season, the second port of the fifth electric three-way valve 402 is closed, the third port is opened, the second port of the sixth electric three-way valve 405 is opened, the third port is closed, the second port of the seventh electric three-way valve 406 is opened, the third port is closed, cooling water at 30-50 ℃ from the condenser 307 enters the cross-season heat storage unit 500 through the fifth electric three-way valve and the sixth electric three-way valve, heat is stored in the soil through heat exchange between the vertical buried pipe 501 and the soil, the cooling water temperature is reduced, then the cooling water returns to the condenser through the seventh electric three-way valve 406 and is reciprocally circulated in sequence, and exhaust steam and waste heat in the condenser 307 can be stored in the soil. When the temperature of the soil rises too high to affect the normal cooling of the condenser 307, a part of the second port is opened by proportionally adjusting the fifth electric three-way valve 402, the cooling water enters the cooling tower 407, the cooling tower releases heat into the air, and the cooling tower 407 serves as a standby cooling device of the cross-season heat storage unit 500, so that the normal operation of the power generation unit 300 is not affected when the temperature in the soil is too high or the system of the vertical buried pipe 501 fails.
In summer, when the agricultural facility unit 100 has a refrigeration requirement, steam with the temperature not less than 143 ℃ is extracted from the steam turbine 305 through the steam extraction pipeline 313, the lithium bromide unit is driven to refrigerate, 7-12 ℃ chilled water is generated, and the chilled water is conveyed to the refrigeration mechanism of the agricultural facility unit 100 through the refrigeration circulating pump 410, so that the requirement of refrigeration in summer is met.
At the initial stage and the final stage of heating season, the heat load is small, the waste heat of the condenser 307 is used for heating, the second ports of the fifth electric three-way valve 402, the sixth electric three-way valve 405 and the seventh electric three-way valve 406 are closed, the third port is opened, the evaporator side of the high-temperature ground source heat pump unit 404 absorbs the waste heat of the condenser 307, the condenser side is changed into high Wen Gongnuan hot water at 80 ℃ after the secondary temperature rise, and heating water is conveyed to a heating mechanism of the agricultural facility unit 100 through the heating circulating pump 409, so that the heating requirement is met.
In the middle of the heating season, the heat load is larger at this moment, the condenser 307 waste heat and the cross-season heat storage unit are adopted for compound heating, the second port of the fifth electric three-way valve 402 is closed, the third port is opened, the second port and the third port of the sixth electric three-way valve 405 and the seventh electric three-way valve 406 are proportionally adjusted, the corresponding valve opening is determined through heat calculation, the evaporator side of the high-temperature ground source heat pump unit 404 absorbs the condenser 307 waste heat and the heat stored by the cross-season heat storage unit, the condenser side becomes high Wen Gongnuan hot water at 80 ℃ after the secondary temperature rise, and the heating water is conveyed to a heating mechanism of the agricultural facility unit 100 through the heating circulating pump 409, so that the heating requirement is met.
Therefore, the photo-thermal power generation energy supply system for the agricultural industrial park adopts the structure, provides electric energy for the agricultural industrial park and external facilities throughout the year, can also utilize the power generation waste heat, realize the function of energy storage of waste heat in a non-heating season in a crossing season, meet the refrigeration requirement in summer, meet the heating requirement in a heating season, realize the cascade utilization of energy from high temperature to low temperature, and improve the economic benefit of the agricultural industrial park.
Finally, it should be noted that: the above embodiments are only for illustrating the technical solution of the present invention and not for limiting it, and although the present invention has been described in detail with reference to the preferred embodiments, it will be understood by those skilled in the art that: the technical scheme of the invention can be modified or replaced by the same, and the modified technical scheme cannot deviate from the spirit and scope of the technical scheme of the invention.