CN204358977U - A kind of clean energy resource steam boiler adopting Molten Salt Heat Transfer heat accumulation - Google Patents
A kind of clean energy resource steam boiler adopting Molten Salt Heat Transfer heat accumulation Download PDFInfo
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- CN204358977U CN204358977U CN201420522338.9U CN201420522338U CN204358977U CN 204358977 U CN204358977 U CN 204358977U CN 201420522338 U CN201420522338 U CN 201420522338U CN 204358977 U CN204358977 U CN 204358977U
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/44—Heat exchange systems
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Abstract
The utility model " a kind of clean energy resource steam boiler adopting Molten Salt Heat Transfer heat accumulation ", belongs to solar utilization technique.It is characterized in that: comprise and connect following a few part in closed circuit successively by heat transfer medium conveyance conduit: heating plant, high temperature melting salt cellar, take hot output device and low-temperature molten salt tank, described high temperature lava tank also comprises electric heater unit, and described electric heater unit is powered by paddy electricity period electric energy and heated the fused salt in described high temperature melting pipe.According to different environmental requirements, different mode of heatings can being selected, ensureing the confession steam that also can continue when not having sunlight, good in economic efficiency, environmental protection and energy saving, the quartz sand composite fused salt that heat accumulating can utilize our company to invent, reduces the cost of investment at initial stage.
Description
Technical field
The utility model relates to solar utilization technique, particularly a kind of clean energy resource steam boiler adopting Molten Salt Heat Transfer heat accumulation.
Background technology
In technical field of solar utilization technique, do not see that can select according to varying environment can not mode of heating at present, good in economic efficiency, environmental protection and energy saving, and drop into and solar energy steam boiler that operating cost is low.Along with energy scarcity, how effective exploitation utilizes solar energy, becomes the problem thought and expect to solve always.
Utility model content
The blank that the utility model exists according to above-mentioned field and demand, the utility model provides a kind of clean energy resource steam boiler adopting Molten Salt Heat Transfer heat accumulation, and can ensure in different environments to continue to provide steam, technical scheme is as follows:
Adopt a clean energy resource steam boiler for Molten Salt Heat Transfer heat accumulation, it is characterized in that:
Comprise heat transfer heat-storage medium carrier pipe, heating plant, high temperature melting salt cellar, output device and low-temperature molten salt tank; Described heat transfer medium conveyance conduit is return capable of circulation, and successively with heating plant, high temperature melting salt cellar, output device connect, and is communicated with described low-temperature molten salt tank inside;
Heat transfer medium in described heat transfer medium conveyance conduit and the heat-storage medium in high temperature melting salt cellar are composite fused salt;
Described heating plant is for collecting solar energy with the heat transfer medium in heat transfer medium conveyance conduit;
Described heat transfer medium conveyance conduit is provided with circulating pump, and described circulating pump is used for providing power for institute's heat transfer medium circulates in described heat transfer medium carrier pipe way;
Heat transfer medium in described heat transfer medium conveyance conduit absorbs heat successively from heating plant, then to high temperature melting salt cellar, output device heat release, a part of heat is stored in high temperature melting salt cellar, part heat is supplied to output device, and the heat transfer medium after release heat energy flows in described low-temperature molten salt tank; Heat transfer medium in low-temperature molten salt tank flow back into after in described heating plant or high temperature melting salt cellar and starts next recuperated cycle under the power of circulating pump;
Described high temperature melting salt cellar is also provided with electric heater unit, described electric heater unit by paddy electric power supply to heat the heat-storage medium in described high temperature melting salt cellar;
Described output device comprises the steam generator and preheater that are connected successively by described heat transfer medium conveyance conduit; Under using state, heat transfer medium enters described preheater after steam generator flows out, and finally gets back to heating plant; Described steam generator is for becoming water vapour by the hot water heating be provided after the heat that absorbs described heat transfer medium and carry and exporting; Described preheater is used for providing hot water to described steam generator; The heat of described preheater preheats hot water partly or entirely derives from the waste heat in the heat transfer medium flowed through.
In steam boiler in the utility model, heating plant is for assembling solar energy as thermal source, energy-conserving and environment-protective.The solar energy that heat transfer unit (HTU) absorbs according to different environmental requirements, can select different mode of heatings.In boiler, a high temperature melting salt cellar is provided with in the downstream of heating plant, the heat energy that the illumination good period is collected can partly be stored in high temperature melting salt cellar, water to be heated in part circulating-heating output device is to export steam, heat transfer medium after heat release is got back in low-temperature molten salt tank, the period that illumination is good, the heat transfer medium reclaimed in low-temperature molten salt tank is pumped to heating plant position and described heating plant carries out heat exchange heat absorption.The period that illumination is bad, under the power of circulating pump, the heat transfer medium reclaimed in low-temperature molten salt tank flows through the heat that in high temperature melting salt cellar Absorbable rod high temperature melting salt cellar, heat-storage medium stores, and heat is sent to output device.In the utility model, adopting heat transfer/storage media is composite fused salt, has thermal conductivity factor good, the focus that storage density is large, both be applicable to heat transfer and be also applicable to heat accumulation, serviceability temperature is high, and efficiency is high, the output steam that also can continue when not having sunlight can be ensured, good in economic efficiency, environmental protection and energy saving.
In steam generator system of the present utility model, high temperature melting salt cellar is also provided with electric heater unit, adopt the paddy electrical heating high-temperature fused salt tank in evening, supplement the shortage of solar energy at night, the paddy electricity that make use of evening avoids the waste of electric power energy, reduce production cost, improve boiler operating efficiency simultaneously, make boiler of the present invention provide superheated steam efficiently in 24 hours.
Described heating plant is selected from slot type, tower, linear Fresnel formula employing solar light-heat power-generation gathering solar device.
Heat transfer medium conveyance conduit between described heating plant to described high temperature melting salt cellar is provided with valve 1;
The nearly heating plant one end of heat transfer medium conveyance conduit between described low-temperature molten salt tank and described heating plant is provided with valve 2.For closing/opening the closed circuit that heat transfer medium conveyance conduit is formed.
Further, also be provided with one section and can avoid valve 2, described heat transfer medium is also delivered directly to cold heat transfer media conveyance conduit with described high-temperature molten salt tank connected heat transfer medium conveyance conduit from described low-temperature molten salt tank by heating plant and valve 1, and described cold heat transfer media conveyance conduit is provided with valve 3.In the utility model, when illumination is bad time, heat transfer heat-storage medium in low-temperature molten salt tank needs to be transported in the heat transfer medium conveyance conduit of high temperature melting salt cellar position the store heat absorbed in high temperature melting salt cellar, in order to increase the flowing fluency of heat transfer heat-storage medium, avoid line clogging, preferably between low-temperature molten salt tank and high temperature melting salt cellar, set up a cold heat transfer media conveyance conduit.And valve 3 is set on this pipeline so that open and close.Valve-off 3 when illumination is good, illumination difference or night Open valve 3 to utilize the heat of the storage in high-temperature molten salt tank.
Described heat transfer heat-storage medium is quartz sand composite fused salt.In the utility model, preferred quartz sand composite fused salt, is shown in number of patent application 201310732738.2,201310040070.5, quartz sand composite fused salt described in 201310040909.5.There is the advantage reducing fused salt use cost.Those skilled in the art also can adopt the fused salt with approximate characteristic having and report in prior art as heat transfer heat-storage medium.
In above-mentioned arbitrary boiler, described heat exchanger is also connected with oxygen-eliminating device.For except oxygen contained in anhydrating, ensure feed water quality, make the pipeline of boiler flow passage component and heat-exchange system and equipment from corrosion, increase the service life.
To sum up, the utility model has the advantage of following several respects:
1. the utility model adopts the paddy electricity of the solar energy of gathering and paddy electricity period at night to complement each other and provides heat, i.e. energy-conserving and environment-protective, ensures that again boiler efficiently provides steam or water vapour in 24 hours.
2. three kinds of modes can be adopted to provide thermal source: slot type, Jing Chang that is tower, linear Fresnel formula solar light-heat power-generation mode assemble solar energy.According to different environmental requirements, different mode of heatings can be selected.
3. the utility model utilizes Molten Salt Heat Transfer heat accumulation, and fused salt serviceability temperature is high, and efficiency is high, and heat accumulation ensures the confession steam that also can continue when not having sunlight, good in economic efficiency, environmental protection and energy saving.
4. the utility model utilizes two tank to carry out heat accumulation, the composite fused salt that heat accumulation material preferably utilizes our company to invent, and thermal conductivity factor is good, and storage density is large.
Accompanying drawing explanation
Fig. 1. for generation of the clean energy resource steam boiler of the employing Molten Salt Heat Transfer heat accumulation of the present utility model of steam;
Wherein 1-heat transfer medium conveyance conduit, 2-heating plant, 3-high temperature melting salt cellar, 4-1 steam generator, 4-2 preheater, 5-low-temperature molten salt tank, 6-circulating pump, 7-1 valve 1,7-2 valve 2,7-3 valve 3,8-oxygen-eliminating device, 9-cold heat transfer media conveyance conduit, 10-paddy electricity power supply.
Detailed description of the invention
As shown in Figure 1, a kind of clean energy resource steam boiler adopting Molten Salt Heat Transfer heat accumulation that the utility model provides, is characterized in that:
Comprise heat transfer medium feed track 1, heating plant 2, high temperature melting salt cellar 3, output device and low-temperature molten salt tank 5; Described heat transfer medium conveyance conduit 1 is return capable of circulation, and successively with heating plant 2, high temperature melting salt cellar 3, output device connect, and is communicated with described low-temperature molten salt tank 5 inside;
Heat transfer medium in described heat transfer medium conveyance conduit 1 and the heat-storage medium in high temperature melting salt cellar 3 are composite fused salt;
Described heating plant 2 is for collecting solar energy to heat the heat transfer medium in described heat transfer medium conveyance conduit 1;
Described heat transfer medium conveyance conduit 1 is provided with circulating pump 6, and described circulating pump 6 is for providing power for described heat transfer medium circulates in described heat transfer medium conveyance conduit 1;
Heat transfer medium in described heat transfer medium conveyance conduit 1 absorbs heat successively from heating plant 2, then to high temperature melting salt cellar 3, output device heat release, a part of heat is stored in high temperature melting salt cellar 3, the water flowed through in part heat heating output device, the heat transfer medium after release heat energy flows in described low-temperature molten salt tank 5; Heat transfer medium in low-temperature molten salt tank 5 flow back in described heating plant or high temperature melting salt cellar 3 and starts next recuperated cycle under the power of circulating pump;
Described high temperature melting salt cellar is also provided with electric heater unit, and described electric heater unit is powered to heat the heat-storage medium in described high temperature melting salt cellar by paddy electricity power supply 10;
Described output device comprises the steam generator 4-1 and preheater 4-2 that are connected successively by described heat transfer medium conveyance conduit; Under using state, heat transfer medium enters described preheater after steam generator flows out, and finally gets back to heating plant; Described steam generator is for becoming water vapour by the hot water heating be provided after the heat that absorbs described heat transfer medium and carry and exporting; Described preheater is used for providing hot water to described steam generator; The heat of described preheater preheats hot water partly or entirely derives from the waste heat in the heat transfer medium flowed through.
In steam boiler in the utility model, heating plant is for assembling solar energy as thermal source, energy-conserving and environment-protective.The solar energy that heat transfer unit (HTU) absorbs according to different environmental requirements, can select different mode of heatings.In boiler, a high temperature melting salt cellar is provided with in the downstream of heating plant, the heat energy that the illumination good period is collected can partly be stored in high temperature melting salt cellar, water to be heated in part circulating-heating output device is to export steam, heat transfer heat-storage medium after heat release is got back in low-temperature molten salt tank, the period that illumination is good, the heat transfer heat-storage medium reclaimed in low-temperature molten salt tank is pumped to heating plant position and described heating plant carries out heat exchange heat absorption.The period that illumination is bad, under the power of circulating pump, the heat stored in Absorbable rod high temperature melting salt cellar when the heat transfer heat-storage medium reclaimed in low-temperature molten salt tank flows through high temperature melting salt cellar, and heat is transmitted large output device.In the utility model, heat transfer heat-storage medium is fused salt, has thermal conductivity factor good, the focus that storage density is large, both be applicable to heat transfer and be also applicable to heat accumulation, serviceability temperature is high, and efficiency is high, the output steam that also can continue when not having sunlight can be ensured, good in economic efficiency, environmental protection and energy saving.
In steam generator system of the present utility model, high temperature melting salt cellar is also provided with electric heater unit, adopt the paddy electrical heating high-temperature fused salt tank in evening, supplement the shortage of solar energy at night, the paddy electricity that make use of evening avoids the waste of electric power energy, improve boiler operating efficiency simultaneously, make boiler of the present invention provide superheated steam efficiently in 24 hours.
Described heating plant 2 is selected from slot type, tower, linear Fresnel formula employing solar light-heat power-generation gathering solar device.
Heat transfer medium conveyance conduit 1 between described heating plant 2 to described high temperature melting salt cellar 3 is provided with valve 17-1; Nearly heating plant 2 one end of heat transfer medium conveyance conduit 1 between described low-temperature molten salt tank 5 and described heating plant 2 is provided with valve 27-2.The closed circuit that valve is formed for closing/opening heat transfer medium conveyance conduit.
Further, also be provided with one section and can avoid valve 27-2, described heat transfer medium is also delivered directly to cold heat transfer media conveyance conduit 9 with described high-temperature molten salt tank connected heat transfer medium conveyance conduit 1 from described low-temperature molten salt tank by heating plant 2 and valve 17-1, and described cold heat transfer media conveyance conduit 9 is provided with valve 37-3.In the utility model, when illumination is bad time, heat transfer heat-storage medium in low-temperature molten salt tank needs to be transported in the heat transfer medium conveyance conduit of high temperature melting salt cellar position the store heat absorbed in high temperature melting salt cellar, in order to increase the flowing fluency of heat transfer heat-storage medium, avoid line clogging, preferably between low-temperature molten salt tank and high temperature melting salt cellar, set up a cold heat transfer media conveyance conduit.And valve 3 is set on this pipeline so that open and close.Valve-off 3 when illumination is good, illumination difference or night Open valve 3 to utilize the heat of the storage in high-temperature molten salt tank.
Described heat transfer/heat-storage medium is quartz sand composite fused salt.In the utility model, preferred quartz sand composite fused salt, is shown in number of patent application 201310732738.2,201310040070.5, quartz sand composite fused salt described in 201310040909.5.There is the advantage reducing fused salt use cost.Those skilled in the art also can adopt the fused salt with approximate characteristic having and report in prior art as heat transfer heat-storage medium.
In above-mentioned arbitrary boiler, described heat exchanger is also connected with oxygen-eliminating device 8.For except oxygen contained in anhydrating, ensure feed water quality, make the pipeline of boiler flow passage component and heat-exchange system and equipment from corrosion, increase the service life.
To sum up, the utility model has the advantage of following several respects:
1. the utility model adopts the paddy electricity of the solar energy of gathering and paddy electricity period at night to provide heat, i.e. energy-conserving and environment-protective, ensures that again boiler efficiently provides steam or water vapour in 24 hours.
2. three kinds of modes can be adopted to provide thermal source: slot type, Jing Chang that is tower, linear Fresnel formula solar light-heat power-generation mode assemble solar energy.According to different environmental requirements, different mode of heatings can be selected.
3. the utility model utilizes Molten Salt Heat Transfer heat accumulation, and fused salt serviceability temperature is high, and efficiency is high, and heat accumulation ensures the confession steam that also can continue when not having sunlight, good in economic efficiency, environmental protection and energy saving.
4. the utility model utilizes two tank to carry out heat accumulation, the composite fused salt that heat accumulating can utilize our company to invent, and thermal conductivity factor is good, and storage density is large.
Claims (6)
1. adopt a clean energy resource steam boiler for Molten Salt Heat Transfer heat accumulation, it is characterized in that:
Comprise heat transfer medium conveyance conduit, heating plant, high temperature melting salt cellar, output device and low-temperature molten salt tank; Described heat transfer medium conveyance conduit is return capable of circulation, and successively with heating plant, high temperature melting salt cellar, output device connect, and is communicated with described low-temperature molten salt tank inside;
Heat transfer medium in described heat transfer medium conveyance conduit and the heat-storage medium in high temperature melting salt cellar are composite fused salt;
Described heating plant is for collecting solar energy with the heat transfer medium in heat transfer medium conveyance conduit;
Described heat transfer medium conveyance conduit is provided with circulating pump, and described circulating pump is used for providing power for institute's heat transfer medium circulates in described heat transfer medium conveyance conduit;
Heat transfer medium in described heat transfer medium conveyance conduit absorbs heat successively from heating plant, then to high temperature melting salt cellar, output device heat release, a part of heat is stored in high temperature melting salt cellar, part heat is supplied to output device, and the heat transfer medium after release heat energy flows in described low-temperature molten salt tank; Heat transfer medium in low-temperature molten salt tank flow back into after in described heating plant or high temperature melting salt cellar and starts next recuperated cycle under the power of circulating pump;
Described high temperature melting salt cellar is also provided with electric heater unit, described electric heater unit by paddy electric power supply to heat the heat-storage medium in described high temperature melting salt cellar;
Described output device comprises the steam generator and preheater that are connected successively by described heat transfer medium conveyance conduit; Under using state, heat transfer medium enters described preheater after steam generator flows out, and finally gets back to heating plant; Described steam generator is for becoming water vapour by the hot water heating be provided after the heat that absorbs described heat transfer medium and carry and exporting; Described preheater is used for providing hot water to described steam generator; The heat of described preheater preheats hot water partly or entirely derives from the waste heat in the heat transfer medium flowed through.
2. the clean energy resource steam boiler of employing Molten Salt Heat Transfer heat accumulation according to claim 1, is characterized in that: heating plant is selected from slot type, tower, linear Fresnel formula employing solar light-heat power-generation gathering solar device.
3. the clean energy resource steam boiler of employing Molten Salt Heat Transfer heat accumulation according to claim 1, is characterized in that: the heat transfer medium conveyance conduit between described heating plant to described high temperature melting salt cellar is provided with valve (1); The nearly heating plant one end of heat transfer medium conveyance conduit between described low-temperature molten salt tank and described heating plant is provided with valve (2).
4. the clean energy resource steam boiler of employing Molten Salt Heat Transfer heat accumulation according to claim 3, it is characterized in that: be also provided with one section and can avoid valve (2) heating plant and valve (1) and described heat transfer medium is delivered directly to cold heat transfer media conveyance conduit with described high-temperature molten salt tank connected heat transfer medium conveyance conduit from described low-temperature molten salt tank, described cold heat transfer media conveyance conduit is provided with valve (3).
5., according to the clean energy resource steam boiler of the arbitrary described employing Molten Salt Heat Transfer heat accumulation of Claims 1 to 4, it is characterized in that: described heat transfer/heat-storage medium is quartz sand composite fused salt.
6., according to the clean energy resource steam boiler of the arbitrary described employing Molten Salt Heat Transfer heat accumulation of Claims 1 to 4, it is characterized in that: described preheater is also connected with oxygen-eliminating device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201420522338.9U CN204358977U (en) | 2014-05-22 | 2014-09-12 | A kind of clean energy resource steam boiler adopting Molten Salt Heat Transfer heat accumulation |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2014102175443 | 2014-05-22 | ||
| CN201410217544 | 2014-05-22 | ||
| CN201420522338.9U CN204358977U (en) | 2014-05-22 | 2014-09-12 | A kind of clean energy resource steam boiler adopting Molten Salt Heat Transfer heat accumulation |
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| CN204358977U true CN204358977U (en) | 2015-05-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410466298.5A Pending CN104279538A (en) | 2014-05-22 | 2014-09-12 | Energy storage type solar overheat steam boiler adopting fused salt heat transfer and heat storage and method for preparing overheat steam by boiler |
| CN201420525832.0U Expired - Lifetime CN204421399U (en) | 2014-05-22 | 2014-09-12 | A kind of energy storage type solar superheated steam boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201410461991.3A Pending CN104266376A (en) | 2014-05-22 | 2014-09-12 | Clean energy superheated steam boiler adopting molten salt to transfer and store heat and method for preparing superheated steam |
| CN201420526343.7U Expired - Lifetime CN204421400U (en) | 2014-05-22 | 2014-09-12 | A kind of clean energy resource hot-water boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201420526492.3U Expired - Lifetime CN204421401U (en) | 2014-05-22 | 2014-09-12 | A kind of clean energy resource superheated steam boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201410462229.7A Pending CN104266379A (en) | 2014-05-22 | 2014-09-12 | Energy-storage solar hot water boiler adopting molten salt to transfer and store heat and method for preparing hot water |
| CN201410464923.2A Pending CN104266158A (en) | 2014-05-22 | 2014-09-12 | Energy-storage solar steam boiler adopting molten salt to transfer and store heat and method for preparing hot water |
| CN201420525850.9U Expired - Lifetime CN204420949U (en) | 2014-05-22 | 2014-09-12 | A kind of energy storage type solar steam boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201420526526.9U Expired - Lifetime CN204187872U (en) | 2014-05-22 | 2014-09-12 | A kind of energy storage type solar hot-water boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201410464816.XA Pending CN104266380A (en) | 2014-05-22 | 2014-09-12 | Clean energy hot water boiler adopting molten salt to transfer and store heat and method for preparing hot water |
| CN201420522338.9U Expired - Lifetime CN204358977U (en) | 2014-05-22 | 2014-09-12 | A kind of clean energy resource steam boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201410462127.5A Pending CN104266377A (en) | 2014-05-22 | 2014-09-12 | Clean energy steam boiler adopting molten salt to transfer and store heat and method for preparing steam |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410466298.5A Pending CN104279538A (en) | 2014-05-22 | 2014-09-12 | Energy storage type solar overheat steam boiler adopting fused salt heat transfer and heat storage and method for preparing overheat steam by boiler |
| CN201420525832.0U Expired - Lifetime CN204421399U (en) | 2014-05-22 | 2014-09-12 | A kind of energy storage type solar superheated steam boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201410461991.3A Pending CN104266376A (en) | 2014-05-22 | 2014-09-12 | Clean energy superheated steam boiler adopting molten salt to transfer and store heat and method for preparing superheated steam |
| CN201420526343.7U Expired - Lifetime CN204421400U (en) | 2014-05-22 | 2014-09-12 | A kind of clean energy resource hot-water boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201420526492.3U Expired - Lifetime CN204421401U (en) | 2014-05-22 | 2014-09-12 | A kind of clean energy resource superheated steam boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201410462229.7A Pending CN104266379A (en) | 2014-05-22 | 2014-09-12 | Energy-storage solar hot water boiler adopting molten salt to transfer and store heat and method for preparing hot water |
| CN201410464923.2A Pending CN104266158A (en) | 2014-05-22 | 2014-09-12 | Energy-storage solar steam boiler adopting molten salt to transfer and store heat and method for preparing hot water |
| CN201420525850.9U Expired - Lifetime CN204420949U (en) | 2014-05-22 | 2014-09-12 | A kind of energy storage type solar steam boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201420526526.9U Expired - Lifetime CN204187872U (en) | 2014-05-22 | 2014-09-12 | A kind of energy storage type solar hot-water boiler adopting Molten Salt Heat Transfer heat accumulation |
| CN201410464816.XA Pending CN104266380A (en) | 2014-05-22 | 2014-09-12 | Clean energy hot water boiler adopting molten salt to transfer and store heat and method for preparing hot water |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410462127.5A Pending CN104266377A (en) | 2014-05-22 | 2014-09-12 | Clean energy steam boiler adopting molten salt to transfer and store heat and method for preparing steam |
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- 2014-09-12 CN CN201410466298.5A patent/CN104279538A/en active Pending
- 2014-09-12 CN CN201420525832.0U patent/CN204421399U/en not_active Expired - Lifetime
- 2014-09-12 CN CN201410461991.3A patent/CN104266376A/en active Pending
- 2014-09-12 CN CN201420526343.7U patent/CN204421400U/en not_active Expired - Lifetime
- 2014-09-12 CN CN201420526492.3U patent/CN204421401U/en not_active Expired - Lifetime
- 2014-09-12 CN CN201410462229.7A patent/CN104266379A/en active Pending
- 2014-09-12 CN CN201410464923.2A patent/CN104266158A/en active Pending
- 2014-09-12 CN CN201420525850.9U patent/CN204420949U/en not_active Expired - Lifetime
- 2014-09-12 CN CN201420526526.9U patent/CN204187872U/en not_active Expired - Lifetime
- 2014-09-12 CN CN201410464816.XA patent/CN104266380A/en active Pending
- 2014-09-12 CN CN201420522338.9U patent/CN204358977U/en not_active Expired - Lifetime
- 2014-09-12 CN CN201410462127.5A patent/CN104266377A/en active Pending
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| CN110906774A (en) * | 2019-12-09 | 2020-03-24 | 东方电气集团东方锅炉股份有限公司 | Concrete heat storage and exchange system for peak regulation heat supply of thermal power plant and operation method thereof |
| CN110906774B (en) * | 2019-12-09 | 2024-01-26 | 东方电气集团东方锅炉股份有限公司 | Concrete heat storage and exchange system for peak shaving and heat supply of thermal power plant and operation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN204421401U (en) | 2015-06-24 |
| CN104266377A (en) | 2015-01-07 |
| CN104266158A (en) | 2015-01-07 |
| CN104266380A (en) | 2015-01-07 |
| CN204421399U (en) | 2015-06-24 |
| CN204421400U (en) | 2015-06-24 |
| CN204420949U (en) | 2015-06-24 |
| CN104266379A (en) | 2015-01-07 |
| CN204187872U (en) | 2015-03-04 |
| CN104266376A (en) | 2015-01-07 |
| CN104279538A (en) | 2015-01-14 |
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Address after: 813 Building, New Industry Incubation Center, Zhongke Research and Development Park, No. 009 Gaoxin South 1st Road, Nanshan District, Shenzhen, Guangdong Province Patentee after: Guangchu Future (Shenzhen) Technology Co.,Ltd. Country or region after: China Address before: Room 201, Building A, Comprehensive Office Building, Qianhai Shenzhen Hong Kong Cooperation Zone Management Bureau, No.1 Liyumen Street, Qianwan 1st Road, Qianhai Shenzhen Hong Kong Cooperation Zone, Shenzhen, Guangdong Province Patentee before: SHENZHEN ENESOON EQUIPMENT TECHNOLOGY Co.,Ltd. Country or region before: China |
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