WO2012052661A2 - Dispositif collecteur d'energie solaire - Google Patents
Dispositif collecteur d'energie solaire Download PDFInfo
- Publication number
- WO2012052661A2 WO2012052661A2 PCT/FR2011/052386 FR2011052386W WO2012052661A2 WO 2012052661 A2 WO2012052661 A2 WO 2012052661A2 FR 2011052386 W FR2011052386 W FR 2011052386W WO 2012052661 A2 WO2012052661 A2 WO 2012052661A2
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- WO
- WIPO (PCT)
- Prior art keywords
- particles
- suspension
- receiver
- fluidized
- volume
- Prior art date
Links
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S10/00—Solar heat collectors using working fluids
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1809—Controlling processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1836—Heating and cooling the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/32—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with introduction into the fluidised bed of more than one kind of moving particles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
- B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
- B01J8/388—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K5/00—Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
- C09K5/08—Materials not undergoing a change of physical state when used
- C09K5/10—Liquid materials
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/006—Methods of steam generation characterised by form of heating method using solar heat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S10/00—Solar heat collectors using working fluids
- F24S10/70—Solar heat collectors using working fluids the working fluids being conveyed through tubular absorbing conduits
- F24S10/74—Solar heat collectors using working fluids the working fluids being conveyed through tubular absorbing conduits the tubular conduits are not fixed to heat absorbing plates and are not touching each other
- F24S10/742—Solar heat collectors using working fluids the working fluids being conveyed through tubular absorbing conduits the tubular conduits are not fixed to heat absorbing plates and are not touching each other the conduits being parallel to each other
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S20/00—Solar heat collectors specially adapted for particular uses or environments
- F24S20/20—Solar heat collectors for receiving concentrated solar energy, e.g. receivers for solar power plants
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S80/00—Details, accessories or component parts of solar heat collectors not provided for in groups F24S10/00-F24S70/00
- F24S80/20—Working fluids specially adapted for solar heat collectors
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D13/00—Heat-exchange apparatus using a fluidised bed
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/0056—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using solid heat storage material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00433—Controlling the temperature using electromagnetic heating
- B01J2208/00451—Sunlight; Visible light
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00513—Controlling the temperature using inert heat absorbing solids in the bed
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00884—Means for supporting the bed of particles, e.g. grids, bars, perforated plates
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/12—Heating the gasifier
- C10J2300/1284—Heating the gasifier by renewable energy, e.g. solar energy, photovoltaic cells, wind
- C10J2300/1292—Heating the gasifier by renewable energy, e.g. solar energy, photovoltaic cells, wind mSolar energy
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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
-
- 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
-
- 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
- Y02E10/46—Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
-
- 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
- Y02E70/00—Other energy conversion or management systems reducing GHG emissions
- Y02E70/30—Systems combining energy storage with energy generation of non-fossil origin
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
Definitions
- the present invention relates to a solar energy collector device. It relates in particular to a device comprising at least one dense suspension of particles fluidized by a gas.
- heat transfer fluid for example a molten salt
- the present invention aims to remedy these disadvantages.
- the invention thus relates to a solar energy collector device.
- the device according to the invention comprises at least one solar receiver comprising at least one suspension of solid particles fluidized by a gas, each suspension circulating between an input and an output of the receiver,
- volume of the particles being between 40 and 55% of the volume of the suspension, the average particle size being between 20 and 150 pm.
- the volume of the particles may be between 45 and 50% of the volume of the suspension.
- the density of the suspension can be between 1250 and 2000 kg / m 3 .
- the particles may be inert particles of sand, silicon carbide, alumina, metal particles, particles of metal oxides, carbides or nitrides or reactive particles.
- the solar receiver may also be a reactor in which a heat treatment of the solid or a solid-gas reaction such as drying, dehydration, decomposition, decarbonation or reduction occur. .
- the particles may be a mixture of chemically inert particles and reactive particles, and the solar receiver may also be a reactor in which a recovery reaction of organic products such as pyrolysis and gasification occurs.
- the flow rate of the solid particles is advantageously between 18 and 200 kg. m “2. s " 1 .
- Each suspension can be confined in one or more tubes.
- Each tube may be an opaque tube made of metallic or ceramic material.
- Each suspension of fluidized particles may be in upward or downward vertical flow.
- the device may include a storage element for storing the heated particles from the solar receiver, said storage element feeding a fluidized bed heat exchanger.
- the fluidized bed heat exchanger can supply steam to a steam turbine.
- the fluidized bed heat exchanger can feed a gas turbine.
- the invention also relates to the use of a device described above for hybridization between solar energy and biomass.
- the invention also relates to a method for storing solar energy.
- the method according to the invention comprises a step of implementing, in a solar receiver, at least one suspension of solid particles fluidized by a gas, each suspension circulating between an input and an output of the receiver, the volume of the particles being between 40 and 55% of the volume of the suspension, the average particle size being between 20 and 150 pm.
- FIG. 1 schematically illustrates a solar energy collector device according to the invention, implementing particles as a transfer fluid and as a heat storage material,
- FIG. 2 illustrates a device according to a first embodiment
- FIG. 3 illustrates a device according to a second embodiment
- the device 1 as illustrated in FIG. 1, comprises a solar receiver 2 using dense suspensions of particles in a gas in upward or downward vertical flow, in tubes which constitute the active elements of the receiver 2. These tubes, metal or ceramic, are subjected to concentrated solar radiation using concentration means 3, for example using a heliostats field.
- This radiation absorbed by the tubes is transmitted by conduction to the suspension which heats up in contact with the hot walls.
- This suspension circulates between the input and output of the solar receiver 2 and thus ensures the transport of the energy absorbed to a set of energy storage and conversion.
- This set of “storage-conversion” includes a hot storage element 4 connected to the output of the solar receiver 2.
- the hot storage element 4 is intended to store the heated particles from the solar receiver 2 and can supply a fluidized-bed heat exchanger in which the particles transfer their energy to submerged tubes in which a working fluid is heated.
- a working fluid for example steam, this steam can be expanded in a steam turbine 6.
- the working fluid can also be a gas, in this case we use a gas turbine.
- a turbine is a conventional device for generating electricity.
- the cooled particles are removed from the exchanger 5, the particles circulating continuously, and are directed to a cold storage element 7 which is connected to the input of the solar receiver 2.
- the particle suspension used in the solar receiver 2 is set in motion by a gas in a tube or other equivalent container.
- the average particle size of the suspension is between 20 and 150 ⁇ m.
- Group A particles of the Geldart classification may be used.
- the average size of the particles may for example be determined by laser granulometry.
- the average particle size is small enough to avoid heterogeneous fluidization, and large enough to prevent aggregation and poor fluidization.
- This average particle size also makes it possible to fluidize the suspension with low gas velocities of the order of a few cm / s. This property is an advantage over conventional solutions for suspending particles per circulating bed which require gas speeds of the order of several m / s, because the energy expenditure due to the compression of the gas is reduced.
- the porosity is small enough to fluidize the particles and large enough to prevent the formation of a dilute bed with poor heat transfer and heat exchange with the wall.
- the density of the suspension is advantageously between 1250 and 2000 kg / m 3 .
- the density of the sand being 2500 kg / m 3
- a suspension of sand particles having a porosity of 50% will have a density of 1250 kg / m 3 , a density approximately 1000 times greater than that of air at atmospheric pressure.
- almost all of the energy is transported by the solid and the medium has the properties of a quasi-liquid.
- the flow rate of the solid particles is advantageously between 18 and 200 kg. m “2. s " 1 . It is thus small enough to provide good conduction and to avoid pressure losses related to the power of pumping air, and large enough to prevent overheating of the tubes and thus secure the device.
- the local exchange coefficient between the wall receiving the concentrated solar radiation and the suspension of particles may be of the order of 500 to 1000 Wm -2 0 C -1 , a coefficient approximately 10 times greater than the exchange coefficient between a gas and a wall and of the same order of magnitude as that between a liquid and a wall.
- the solar receiver 2 can comprise one or more multitubular exchangers which are the absorber modules of the receiver 2.
- the walls of the tubes whose diameter is for example between 30 mm and 100 mm are heated by solar radiation while inside. tubes circulates the dense suspension of solid particles.
- the rows of the tubes may be replaced by fluidized beds of parallelepiped shape of small thickness.
- the suspension is in downward vertical flow.
- two flow regimes of the gas-solid suspension can be observed: a fluidized descending dense flow exchanger or a moving bed.
- FIG. 2 This first embodiment is illustrated in FIG. 2, in which the elements identical to those of FIG. 1 bear the same references.
- a fluidized buffer tank 8 supplies a bundle of tubes.
- a fluidized bed recovers the solid particles
- the buffer tank 8 is supplied with particles by a feed tank 9.
- the feed tank 9 is also fluidized by air, so as to create a movement. particles and to homogenize the temperature of the particles.
- the particle suspension thus flows from top to bottom, from the buffer tank 8 to the lower end of the receiver 2.
- the flow rate of the solid particles as well as the residual flow rate of the air in the tubes are controlled by adjusting the pressure in the hot storage tank 4.
- the operation can be carried out by:
- the suspension is in vertical upward flow.
- the particles circulate from the feed tray 9 towards the fluidized bed located at the lower end of the solar receiver 2, then back into the tubes of the receiver 2 towards the buffer tank 8 located at the upper end of the receiver 2.
- the particles heated in the receiver 2 then flow from the buffer tank 8 to the hot storage tank 4 located under the receiver 2.
- FIG. 4 shows the implementation of the device in a solar receiver, for example according to the first embodiment (it can also be adapted to the second mode).
- the device 1 can thus comprise four solar receiver modules 2, fed by a single feed tank 9.
- the particles heated by the solar receivers 2 are conveyed to a single hot storage tank 4.
- the solar receivers 2 can be illuminated by a circular or north-south heliostatic field (cavity-type receiver) as shown in FIG.
- the dense suspensions of solid particles fluidized by a gas allow high operating temperatures, greater than or equal to 600 ° C, ideal for power plants and solar reactors for generating electricity or heat, and only for solar heating of chemical reactors for the production, for example, of hydrogen.
- the device according to the invention also makes it possible to easily hybridize solar energy and biomass through an exchanger / fluidized bed reactor used to produce steam.
- suspensions can also be used to heat a chemical reactor in which endothermic reactions are carried out, such as thermochemical cycles of solar hydrogen production or the treatment of solids.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Sustainable Energy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Sustainable Development (AREA)
- Materials Engineering (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Cyclones (AREA)
- Photovoltaic Devices (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/879,869 US9267709B2 (en) | 2010-10-20 | 2011-10-13 | Device for collecting solar energy |
EP11832109.0A EP2630219B1 (fr) | 2010-10-20 | 2011-10-13 | Dispositif collecteur d'énergie solaire |
ES11832109T ES2699649T3 (es) | 2010-10-20 | 2011-10-13 | Dispositivo colector de energía solar |
AU2011317414A AU2011317414B2 (en) | 2010-10-20 | 2011-10-13 | Device for collecting solar energy |
CN201180050807.0A CN103270144B (zh) | 2010-10-20 | 2011-10-13 | 用于收集太阳能的装置 |
IL225816A IL225816B (en) | 2010-10-20 | 2013-04-18 | A device for collecting solar energy |
ZA2013/02874A ZA201302874B (en) | 2010-10-20 | 2013-04-19 | Device for collecting solar energy |
MA35899A MA34664B1 (fr) | 2010-10-20 | 2013-05-13 | Dispositif collecteur d'energie solaire |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1058565A FR2966567B1 (fr) | 2010-10-20 | 2010-10-20 | Dispositif collecteur d'energie solaire |
FR1058565 | 2010-10-20 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2012052661A2 true WO2012052661A2 (fr) | 2012-04-26 |
WO2012052661A3 WO2012052661A3 (fr) | 2013-02-14 |
Family
ID=44146555
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FR2011/052386 WO2012052661A2 (fr) | 2010-10-20 | 2011-10-13 | Dispositif collecteur d'energie solaire |
Country Status (9)
Country | Link |
---|---|
US (1) | US9267709B2 (fr) |
EP (1) | EP2630219B1 (fr) |
AU (1) | AU2011317414B2 (fr) |
ES (1) | ES2699649T3 (fr) |
FR (1) | FR2966567B1 (fr) |
IL (1) | IL225816B (fr) |
MA (1) | MA34664B1 (fr) |
WO (1) | WO2012052661A2 (fr) |
ZA (1) | ZA201302874B (fr) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110197585A1 (en) * | 2008-09-12 | 2011-08-18 | Internew Electronics S.R.L. | Thermal vector system for solar concentration power plant |
CN103291437A (zh) * | 2012-02-29 | 2013-09-11 | 顾飞舟 | 以固体颗粒作为流动热导体的冷却系统 |
US20140311479A1 (en) * | 2013-04-22 | 2014-10-23 | Babcock & Wilcox Power Generation Group, Inc. | Concentrated solar power solids-based system |
WO2014044254A3 (fr) * | 2012-09-18 | 2015-03-19 | Technische Universität Chemnitz | Système de production d'eau chaude et/ou de vapeur comportant un accumulateur à haute température pour une utilisation dans une centrale électrique à turbine à gaz |
CN104981668A (zh) * | 2012-12-28 | 2015-10-14 | 阿文戈亚太阳能有限责任公司 | 使用经聚集的太阳能的金属再熔化和发电 |
EP2975263A1 (fr) * | 2014-07-17 | 2016-01-20 | The Babcock & Wilcox Company | Installation de production d'énergie intégrant un récepteur d'énergie solaire concentrée et un échangeur de chaleur pressurisé |
EP2862912A4 (fr) * | 2013-05-07 | 2016-03-09 | Inst Modern Physics Cas | Agent d'échange thermique, système d'échange thermique et système de réacteur nucléaire |
US9651313B2 (en) | 2012-10-10 | 2017-05-16 | Research Triangle Institute | Particulate heat transfer fluid and related system and method |
EP3434360A1 (fr) | 2017-07-27 | 2019-01-30 | Centre National De La Recherche Scientifique | Dispositif de collecte d'énergie solaire |
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US9038386B2 (en) * | 2008-09-12 | 2015-05-26 | Internew Electronics S.R.L. | Thermal vector system for solar concentration power plant |
US20110197585A1 (en) * | 2008-09-12 | 2011-08-18 | Internew Electronics S.R.L. | Thermal vector system for solar concentration power plant |
CN103291437A (zh) * | 2012-02-29 | 2013-09-11 | 顾飞舟 | 以固体颗粒作为流动热导体的冷却系统 |
WO2014044254A3 (fr) * | 2012-09-18 | 2015-03-19 | Technische Universität Chemnitz | Système de production d'eau chaude et/ou de vapeur comportant un accumulateur à haute température pour une utilisation dans une centrale électrique à turbine à gaz |
US9651313B2 (en) | 2012-10-10 | 2017-05-16 | Research Triangle Institute | Particulate heat transfer fluid and related system and method |
CN104981668A (zh) * | 2012-12-28 | 2015-10-14 | 阿文戈亚太阳能有限责任公司 | 使用经聚集的太阳能的金属再熔化和发电 |
WO2014176098A1 (fr) * | 2013-04-22 | 2014-10-30 | Babcock & Wilcox Power Geration Group, Inc. | Système à énergie solaire concentrée à base de matières solides |
US20140311479A1 (en) * | 2013-04-22 | 2014-10-23 | Babcock & Wilcox Power Generation Group, Inc. | Concentrated solar power solids-based system |
US9829217B2 (en) * | 2013-04-22 | 2017-11-28 | The Babcock & Wilcox Company | Concentrated solar power solids-based system |
EP2862912A4 (fr) * | 2013-05-07 | 2016-03-09 | Inst Modern Physics Cas | Agent d'échange thermique, système d'échange thermique et système de réacteur nucléaire |
US10699818B2 (en) | 2013-05-07 | 2020-06-30 | Institute Of Modern Physics, Chinese Academy Of Sciences | Heat exchange medium, heat exchange system, and nuclear reactor system |
EP2975263A1 (fr) * | 2014-07-17 | 2016-01-20 | The Babcock & Wilcox Company | Installation de production d'énergie intégrant un récepteur d'énergie solaire concentrée et un échangeur de chaleur pressurisé |
EP3434360A1 (fr) | 2017-07-27 | 2019-01-30 | Centre National De La Recherche Scientifique | Dispositif de collecte d'énergie solaire |
Also Published As
Publication number | Publication date |
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FR2966567B1 (fr) | 2014-11-14 |
IL225816A0 (en) | 2013-06-27 |
ZA201302874B (en) | 2014-10-29 |
US9267709B2 (en) | 2016-02-23 |
AU2011317414B2 (en) | 2016-11-24 |
MA34664B1 (fr) | 2013-11-02 |
EP2630219B1 (fr) | 2018-08-29 |
CN103270144A (zh) | 2013-08-28 |
EP2630219A2 (fr) | 2013-08-28 |
ES2699649T3 (es) | 2019-02-12 |
US20130284163A1 (en) | 2013-10-31 |
WO2012052661A3 (fr) | 2013-02-14 |
IL225816B (en) | 2019-12-31 |
FR2966567A1 (fr) | 2012-04-27 |
AU2011317414A1 (en) | 2013-05-30 |
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