CN210035434U - Multi-energy complementary steam energy-saving system - Google Patents
Multi-energy complementary steam energy-saving system Download PDFInfo
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- CN210035434U CN210035434U CN201920833300.6U CN201920833300U CN210035434U CN 210035434 U CN210035434 U CN 210035434U CN 201920833300 U CN201920833300 U CN 201920833300U CN 210035434 U CN210035434 U CN 210035434U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
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Abstract
The utility model discloses a multi-energy complementary steam energy-saving system, which comprises a molten salt circulation path, a heat-conducting oil circulation path and a steam-water circulation path, wherein the molten salt circulation path is connected with the heat-conducting oil circulation path through an oil-salt heat exchanger, and the heat-conducting oil circulation path is connected with the steam-water circulation path through a heat-conducting oil steam generator; the molten salt circulation path comprises a low-temperature molten salt tank and a high-temperature molten salt tank which are sequentially connected, a low-temperature molten salt pump in the low-temperature molten salt tank is communicated with the high-temperature molten salt tank through a molten salt electric heater, and a high-temperature molten salt pump of the high-temperature molten salt tank is communicated with the low-temperature molten salt pump through an oil-salt heat exchanger. The utility model adopts the above structure complementary steam economizer system of multipotency source, make full use of solar energy, millet electric energy and the intercoupling of natural gas energy have not only realized the clean energy of industrial heat and have replaced, moreover greatly reduced the production running cost of enterprise.
Description
Technical Field
The utility model relates to a clean energy utilizes equipment technical field, especially relates to a complementary steam economizer system of multipotency source.
Background
With the rapid development of social economy, the atmospheric pollution in China is more and more serious, and the serious influence is brought to the health of people, the nation calls for winning the blue sky guard war, the emission of atmospheric pollutants is greatly reduced, coal-fired steam boilers of industrial enterprises are gradually banned, and the development of green clean energy heating systems is urgently needed in the field of industrial heat.
Steam consumption in China is increased by 10% every year, coal-fired boilers are used for heat supply of industrial enterprises at present, combustion efficiency is low, pollution is large, elimination and shutdown are urgently waited, a plurality of enterprises use gas-fired boilers or electric boilers to replace the coal-fired boilers, but due to the fact that energy price is high, operation cost is high and the like, heavy burden is brought to the enterprises, a clean energy steam system with low operation cost is urgently needed, and the current problems of the industrial enterprises are solved.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a complementary steam economizer system of multipotency source preferentially utilizes solar energy to produce steam, secondly uses the millet electric energy, uses the natural gas energy at last, and make full use of solar energy, millet electric energy and the intercoupling of natural gas energy have not only realized the clean energy of industrial heat and have replaced, moreover greatly reduced the production running cost of enterprise.
In order to achieve the purpose, the utility model provides a complementary steam economizer system of multipotency source, including fused salt circulation route, conduction oil circulation route and steam-water circulation route, the fused salt circulation route with connect through the oil salt heat exchanger between the conduction oil circulation route, the conduction oil circulation route with connect through conduction oil steam generator between the steam-water circulation route;
the molten salt circulation passage comprises a low-temperature molten salt tank and a high-temperature molten salt tank which are sequentially connected, a low-temperature molten salt pump in the low-temperature molten salt tank is communicated with the high-temperature molten salt tank through a molten salt electric heater, and a high-temperature molten salt pump of the high-temperature molten salt tank is communicated with the low-temperature molten salt pump through the oil-salt heat exchanger;
the heat conducting oil circulation passage comprises a groove type heat collector, an electric three-way valve, a heat conducting oil circulation pump and an oil-gas separator which are sequentially connected, an oil inlet of the oil-gas separator is communicated with an oil outlet of the heat conducting oil steam generator, an oil inlet of the heat conducting oil steam generator is respectively communicated with the oil outlet of the groove type heat collector and the oil outlet of the oil-salt heat exchanger, and the electric three-way valve is also communicated with an oil inlet of the oil-salt heat exchanger;
the steam-water circulation path comprises a steam distributing cylinder, a gas steam boiler, a deoxidizing water feeding pump, a thermal deaerator and a closed condensed water recovery device which are sequentially connected, a first steam outlet of the thermal oil steam generator is communicated with the steam distributing cylinder, a second steam outlet of the thermal oil steam generator is communicated with the thermal deaerator through a temperature and pressure reducing device, and a deoxidizing water feeding pump is communicated with a water inlet of the thermal oil steam generator.
Preferably, an expansion tank connected with a nitrogen sealing device is arranged above the oil-gas separator, and an oil storage tank is further connected to one side of the expansion tank.
Preferably, one side of the thermal deaerator is connected with the full-automatic water softening device through a water replenishing pump.
Preferably, the bottom of the steam distributing cylinder is provided with a steam trap connected with the closed condensed water recovery device.
Preferably, the steam distributing cylinder is communicated with a main gas supply pipeline, and the closed condensed water recovery device is communicated with the main condensed water pipeline.
Preferably, the bottom of the high-temperature molten salt tank and the bottom of the low-temperature molten salt tank are both provided with anti-condensation electric heaters.
The utility model has the advantages of at least as follows:
(1) through the reasonable design of fused salt circulation path, conduction oil circulation path and steam-water circulation path, realized solar energy, millet electricity energy storage and the coupling heat supply of natural gas ability, production steam that can be stable satisfies the steam demand of enterprise, has realized replacing coal fired boiler completely, reduces the emission of atmospheric pollutants by a wide margin, is the novel industry clean energy steam system of environmental protection pollution-free.
(2) Preferentially using solar energy to heat conduction oil, and generating steam by high-temperature conduction oil through a conduction oil steam generator, so that when the sun is in the daytime, the solar energy is used for generating steam; the high-temperature molten salt tank is used for storing heat at night and is used in the daytime or in rainy, snowy and snowy days, so that higher energy price in the daytime is avoided, energy is saved, and the production and operation cost of enterprises is reduced; in the steam-water circulation path, by arranging the closed condensed water recovery device and the steam trap, not only the condensed water is softened water with low oxygen content, but also the waste heat in the condensed water can be utilized, and good economic benefit can be brought to enterprises through recycling of the condensed water, thereby being beneficial to further reducing the production cost of the enterprises.
The technical solution of the present invention is further described in detail by the accompanying drawings and examples.
Drawings
Fig. 1 is a schematic diagram of an embodiment of the multi-energy complementary steam economizer system of the present invention.
Reference numerals
101. A high temperature molten salt tank; 102. a low temperature molten salt tank; 103. a molten salt electric heater; 104. a high temperature molten salt pump; 105. an oil-salt heat exchanger; 106. a low temperature molten salt pump; 107. an anti-freezing electric heater;
201. a trough collector; 202. a heat transfer oil circulating pump; 203. an electric three-way valve; 204. an oil-gas separator; 205. an expansion tank; 206. an oil storage tank; 207. a nitrogen sealing device;
301. a heat conducting oil steam generator; 302. a gas-fired steam boiler; 303. a thermal deaerator; 304. a closed condensate recovery unit; 305. a cylinder is divided; 306. a deoxygenated water supply pump; 307. a water replenishing pump; 308. a full-automatic water softening device; 309. a temperature and pressure reducing device; 310. a steam trap; 311. a main steam supply pipeline; 312. a main condensate pipe.
Detailed Description
The following describes embodiments of the present invention with reference to the accompanying drawings.
Fig. 1 is a schematic diagram of an embodiment of the multi-energy complementary steam energy-saving system of the present invention, as shown in the figure, a multi-energy complementary steam energy-saving system, which includes a molten salt circulation path, a heat transfer oil circulation path and a steam-water circulation path, wherein the molten salt circulation path is connected with the heat transfer oil circulation path through an oil-salt heat exchanger 105, and the heat of the molten salt circulation path is transferred to the heat transfer oil circulation path through the oil-salt heat exchanger 105; the heat-conducting oil circulation passage is connected with the steam-water circulation passage through a heat-conducting oil steam generator 301, and heat of the heat-conducting oil circulation passage is transferred to the steam-water circulation passage through the heat-conducting oil steam generator 301.
The molten salt circulation passage comprises a low-temperature molten salt tank 102 and a high-temperature molten salt tank 101 which are sequentially connected, a low-temperature molten salt pump 106 in the low-temperature molten salt tank 102 is communicated with the high-temperature molten salt tank 101 through a molten salt electric heater 103, and a high-temperature molten salt pump 104 of the high-temperature molten salt tank 101 is communicated with the low-temperature molten salt pump 106 through an oil-salt heat exchanger 105. The low-temperature molten salt in the molten salt circulation passage is pumped out of the low-temperature molten salt tank 102 through the low-temperature molten salt pump 106, then is heated under the action of the molten salt electric heater 103 and then enters the high-temperature molten salt tank 101, the low-temperature molten salt is pumped out of the high-temperature molten salt pump 104 and then is subjected to heat exchange to the heat transfer oil circulation passage through the oil salt heat exchanger 105, and the high-temperature molten salt is changed into low-temperature molten salt and returns to the low-temperature molten salt tank 102. The bottom parts of the high-temperature molten salt tank 101 and the low-temperature molten salt tank 102 are provided with anti-condensation electric heaters 107 for preventing the molten salt from being solidified.
The heat conducting oil circulation passage comprises a groove type heat collector 201, an electric three-way valve 203, a heat conducting oil circulation pump 202 and an oil-gas separator 204 which are sequentially connected, an oil inlet of the oil-gas separator 204 is communicated with an oil outlet of the heat conducting oil steam generator 301, an oil inlet of the heat conducting oil steam generator 301 is communicated with an oil outlet of the groove type heat collector 201, and heat collected by the groove type heat collector 201 enters the heat conducting oil steam generator 301 for heat dissipation and then returns to the groove type heat collector 201 through the oil-gas separator 204 under the power of the heat. The oil inlet of the heat-conducting oil steam generator 301 is also communicated with the oil outlet of the oil-salt heat exchanger 105, the electric three-way valve 203 is also communicated with the oil inlet of the oil-salt heat exchanger 105, and the medium oil heat of the oil-salt heat exchanger 105 returns to the oil-salt heat exchanger 105 through the oil-gas separator 204 under the power action of the heat-conducting oil circulating pump 202 after the heat is dissipated by the heat-conducting oil steam generator 301. By adjusting the communication between the electric three-way valve 203 and the oil-salt heat exchanger 105 and the trough heat collector 201, different channels of heat circulation can be adjusted.
An expansion groove 205 connected with a nitrogen sealing device 207 is arranged above the oil-gas separator 204, an oil storage groove 206 is connected with one side of the expansion groove 205, the oil-gas separator 204 is used for discharging low boiling point substances and air generated in the system operation process to the system through the expansion groove 205 to ensure the stable operation of the system, one main function of the expansion groove 205 is to store the volume of heat conducting oil expanded due to the temperature rise, the damage caused by the thermal expansion and pressure rise of pipelines and valves in the system is prevented, the other function is to supplement oil to the system when the system is in oil shortage, the oil storage groove 206 can emergently discharge the heat conducting oil in the system under the emergency condition that the system is overhauled or the system is in accident or the like, in addition, the oil storage groove 206 can receive the heat conducting oil overflowed from the expansion groove 205 to prevent the waste of the heat conducting oil, the nitrogen sealing device 207 uses the nitrogen heat conducting oil expansion groove 205, and can prevent the, the service life of the heat transfer oil can be prolonged.
The steam-water circulation path comprises a steam-distributing cylinder 305, a gas-steam boiler 302, a deoxygenation water-feeding pump 306, a thermal deoxygenator 303 and a closed condensed water recovery device 304 which are sequentially connected, water of the closed condensed water recovery device 304 passes through the thermal deoxygenator 303 and then enters the gas-steam boiler 302 under the power of the deoxygenation water-feeding pump 306 to be heated, and high-heat steam is discharged outside after passing through the steam-distributing cylinder 305. The first steam outlet of the heat conduction oil steam generator 301 is communicated with the steam distributing cylinder 305, the second steam outlet of the heat conduction oil steam generator is communicated with the thermal deaerator 303 through the temperature and pressure reducing device 309, hot steam of the heat conduction oil steam generator 301 directly enters the steam distributing cylinder 305, and the temperature and pressure reducing device 309 connected with the thermal deaerator 303 is used for adjusting the temperature and the pressure of the steam, so that the production requirement is met. The deoxygenation water feed pump 306 is communicated with the water inlet of the conduction oil steam generator 301, and the thermal deoxygenator 303 can provide a water source for the conduction oil steam generator.
The steam-distributing cylinder 305 is communicated with a steam supply main pipe 311, a temperature and pressure reducing device 309 is installed on the steam supply main pipe 311, and hot air of the steam-distributing cylinder 305 is conveyed outwards after temperature and pressure adjustment through the steam supply main pipe 311. The closed condensed water recovery device 304 is communicated with the main condensed water pipe 312, and the heat-dissipated hot steam is changed into condensed water and returns to the closed condensed water recovery device 304. The bottom of steam-distributing cylinder 305 is equipped with the steam trap 310 of being connected with closed condensate recovery unit 304, during condensate water in the steam-distributing cylinder 305 got back to closed condensate recovery unit 304 through steam trap 310, can in time discharge the condensate water in the steam-distributing cylinder 305, and in carrying closed condensate recovery unit 304 through the pipeline, reuse, like this through the closed recovery system of condensate water, can make the steam waste heat obtain abundant recovery cyclic utilization, can make steam system move more steadily. One side of the thermal deaerator 303 is connected with a full-automatic water softening device 308 through a water replenishing pump 307, and the full-automatic water softening device 308 can remove the content of calcium and magnesium ions in water.
1. The working principle of the steam energy-saving system is as follows:
1) solar energy supplies steam alone: on daytime, detect sunshine intensity through the radiometer, when the solar charging is sufficient, slot type heat collector 201 begins to track the sun, collect solar energy, electric three-way valve 203 and slot type heat collector 201 intercommunication conduction oil circulating pump 202 carry the slot type heat collector 201 mirror field with the low temperature conduction oil this moment, the back high temperature conduction oil that heats up gets into conduction oil steam generator 301 and produces steam with the water heat transfer, steam passes through gas-distributing cylinder 305 and behind the decompression 309 device, carry the main pipe that supplies vapour, satisfy the demand of enterprise's production vapour.
2) And (3) molten salt valley electricity energy storage and steam supply: at night, the solar energy is insufficient, at the moment, the low-temperature molten salt in the low-temperature molten salt tank 102 is discharged to the molten salt electric heater 103 through the low-temperature molten salt pump 106, the molten salt electric heater 103 heats the low-temperature molten salt by using valley electricity, and the heated high-temperature molten salt enters the high-temperature molten salt tank 104 to be stored. Next day, when solar energy is not enough, carry the high temperature fused salt to the oil salt heat exchanger 105 through high temperature fused salt pump 104 in, electric three-way valve 203 and oil salt heat exchanger 105 intercommunication this moment, low temperature conduction oil gets into oil salt heat exchanger 105, through the heat transfer, high temperature fused salt temperature reduces, be carried in low temperature fused salt jar 102, the conduction oil is heated and is heaied up and become high temperature conduction oil, high temperature conduction oil gets into conduction oil steam generator 301 and water heat transfer steam production, steam passes through branch cylinder 305 and behind the decompression 309 device, carry the main pipe that supplies vapour, satisfy the demand of the vapour for production of enterprise.
3) Solar energy and molten salt valley electricity energy storage steam supply: through detecting solar irradiance and heat conduction oil temperature, the switch of intelligent control electric three-way valve 203 can adjust the flow of heat conduction oil in slot type heat collector 201 and oil salt heat exchanger 105, use solar energy and fused salt valley electricity energy storage coupling to heat the heat conduction oil, high temperature heat conduction oil gets into heat conduction oil steam generator 301 and water heat transfer steam production, steam passes through gas-distributing cylinder 305 and behind the device of reducing temperature and pressure 309, carry the main pipe that supplies vapour, satisfy the demand of enterprise's production vapour.
4) Supplying steam by using solar energy and a gas steam boiler: when the molten salt circulation passage needs to be overhauled or has faults, solar energy is preferentially used for generating steam, when the solar energy is insufficient, the gas-steam boiler 302 is used for supplementing, so that the steam generated by the heat-conducting oil steam generator 301 and the gas-steam boiler 302 simultaneously enters the steam-distributing cylinder 305, and the steam is conveyed to a steam supply main pipe after passing through the steam-distributing cylinder 305 and the temperature and pressure reducing device 309, so that the requirement of steam for production of enterprises is met.
5) Molten salt valley electricity energy storage and steam supply of a gas steam boiler: when the solar energy resource is not available in the continuous rainy and snowy days, the high-temperature molten salt pump 104 conveys the high-temperature molten rock to the oil-salt heat exchanger 105, the electric three-way valve 203 is communicated with the oil-salt heat exchanger 105 at the moment, low-temperature heat conduction oil enters the oil-salt heat exchanger 105, the temperature of the high-temperature molten salt is reduced through heat exchange and is conveyed to the low-temperature molten salt tank 102, the heat conduction oil is heated and heated to become high-temperature heat conduction oil, the high-temperature heat conduction oil enters the heat conduction oil steam generator 301 to exchange heat with water to generate steam, meanwhile, the gas-steam boiler 302 is started to generate steam, the steam generated by the heat conduction oil steam generator 301 and the gas-steam boiler 302 simultaneously enters the steam-distributing cylinders 305, the steam is conveyed to.
6) Supplying steam to the gas-steam boiler: when the molten salt circulation passage and the heat conduction oil circulation passage need to be overhauled or have faults, the gas-steam boiler 302 is started to generate steam, and the steam is conveyed to a steam supply main pipe after passing through the steam-distributing cylinder 305 and the temperature and pressure reducing 309 device, so that the requirement of production steam of enterprises is met.
2. The energy-saving and water-saving working principle of condensed water recovery is as follows:
the closed condensate recovery device 304 is arranged on the condensate main pipe 312, and the condensate recovery device is used for automatically conveying the condensate to the thermal deaerator 303.
The utility model discloses abundant high-efficient coupling utilizes solar energy, the industrial steam is produced to three kinds of clean energy of millet electric energy and natural gas ability, through fused salt circulation route, conduction oil circulation route and steam-hydrologic cycle route's rational design, make three kinds of energy intercoupling utilize, preferentially use solar energy to produce steam, secondly use millet electric energy storage to produce steam, use the natural gas ability at last as the replenishment, pass through the fused salt like this, the conduction oil, the effective combination of three kinds of media of water, the utilization of the energy step that can be complementary has been realized, the slot type heat collector can gather the heat all the year round, high-usage, energy-saving effect is better. The condensate recovery device is arranged in the system, so that the softened condensate with low oxygen content can be recycled, the repeated deoxidization and softening are avoided, the energy consumption is reduced, and the waste heat of the condensate can be utilized, so that the traditional steam supply mode with high energy consumption is changed. To sum up, according to the particularity of industrial enterprise's steam, adopt multiple energy-conserving technique coupling to use, can effectively reduce system's working costs, alleviate the clean energy burden of enterprise, the utility model discloses a complementary steam economizer system of multipotency source, no smoke and dust, SO2And pollutants such as NOx, PM2.5 and the like are discharged, so that the atmospheric environment is improved, and a blue sky defense war is won.
Therefore, the utility model adopts the above structure complementary steam economizer system of multipotency source, make full use of solar energy, millet electric energy and the intercoupling of natural gas energy have not only realized the clean energy of industrial heat and have replaced, moreover greatly reduced the production running cost of enterprise.
Finally, it should be noted that: the above embodiments are only for illustrating the technical solutions of the present invention and not for limiting the same, and although the present invention is described in detail with reference to the preferred embodiments, those skilled in the art should understand that: the technical solution of the present invention can still be modified or replaced by other equivalent means, and the modified technical solution can not be separated from the spirit and scope of the technical solution of the present invention.
Claims (6)
1. A multi-energy complementary steam energy-saving system is characterized in that: the system comprises a molten salt circulation passage, a heat conduction oil circulation passage and a steam-water circulation passage, wherein the molten salt circulation passage is connected with the heat conduction oil circulation passage through an oil-salt heat exchanger, and the heat conduction oil circulation passage is connected with the steam-water circulation passage through a heat conduction oil steam generator;
the molten salt circulation passage comprises a low-temperature molten salt tank and a high-temperature molten salt tank which are sequentially connected, a low-temperature molten salt pump in the low-temperature molten salt tank is communicated with the high-temperature molten salt tank through a molten salt electric heater, and a high-temperature molten salt pump of the high-temperature molten salt tank is communicated with the low-temperature molten salt pump through the oil-salt heat exchanger;
the heat conducting oil circulation passage comprises a groove type heat collector, an electric three-way valve, a heat conducting oil circulation pump and an oil-gas separator which are sequentially connected, an oil inlet of the oil-gas separator is communicated with an oil outlet of the heat conducting oil steam generator, an oil inlet of the heat conducting oil steam generator is respectively communicated with the oil outlet of the groove type heat collector and the oil outlet of the oil-salt heat exchanger, and the electric three-way valve is also communicated with an oil inlet of the oil-salt heat exchanger;
the steam-water circulation path comprises a steam distributing cylinder, a gas steam boiler, a deoxidizing water feeding pump, a thermal deaerator and a closed condensed water recovery device which are sequentially connected, a first steam outlet of the thermal oil steam generator is communicated with the steam distributing cylinder, a second steam outlet of the thermal oil steam generator is communicated with the thermal deaerator through a temperature and pressure reducing device, and a deoxidizing water feeding pump is communicated with a water inlet of the thermal oil steam generator.
2. The multi-energy complementary steam economizer system of claim 1 wherein: an expansion tank connected with a nitrogen sealing device is arranged above the oil-gas separator, and an oil storage tank is further connected to one side of the expansion tank.
3. The multi-energy complementary steam economizer system of claim 1 wherein: one side of the thermal deaerator is connected with the full-automatic water softening device through a water replenishing pump.
4. The multi-energy complementary steam economizer system of claim 1 wherein: and a steam trap connected with the closed condensed water recovery device is arranged at the bottom of the steam distributing cylinder.
5. The multi-energy complementary steam economizer system of claim 1 wherein: the steam distributing cylinder is communicated with a gas supply main pipeline, and the closed condensed water recovery device is communicated with a condensed water main pipeline.
6. The multi-energy complementary steam economizer system of claim 1 wherein: and the bottoms of the high-temperature molten salt tank and the low-temperature molten salt tank are both provided with anti-condensation electric heaters.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113280320A (en) * | 2021-06-21 | 2021-08-20 | 西安热工研究院有限公司 | System for greatly improving industrial steam supply reliability based on electric heating heat storage technology |
| CN113776038A (en) * | 2021-10-15 | 2021-12-10 | 鸿蒙能源(山东)有限公司 | Ultralow-consumption electromagnetic induction evaporation industrial steam system |
| CN114961906A (en) * | 2022-06-28 | 2022-08-30 | 西安热工研究院有限公司 | System for quickly starting gas-steam combined cycle unit and operation method |
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2019
- 2019-06-04 CN CN201920833300.6U patent/CN210035434U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113280320A (en) * | 2021-06-21 | 2021-08-20 | 西安热工研究院有限公司 | System for greatly improving industrial steam supply reliability based on electric heating heat storage technology |
| CN113776038A (en) * | 2021-10-15 | 2021-12-10 | 鸿蒙能源(山东)有限公司 | Ultralow-consumption electromagnetic induction evaporation industrial steam system |
| CN113776038B (en) * | 2021-10-15 | 2023-09-22 | 鸿蒙能源(山东)有限公司 | Ultra-low power consumption electromagnetic induction evaporation industrial steam system |
| CN114961906A (en) * | 2022-06-28 | 2022-08-30 | 西安热工研究院有限公司 | System for quickly starting gas-steam combined cycle unit and operation method |
| CN114961906B (en) * | 2022-06-28 | 2024-05-17 | 西安热工研究院有限公司 | System for quickly starting gas-steam combined cycle unit and operation method |
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