WO2011000522A2 - Centrale à collecteur cylindro-parabolique avec accumulation de l'énergie solaire, procédé pour faire fonctionner une centrale à collecteur cylindro-parabolique et accumulateur de chaleur à haute température - Google Patents

Centrale à collecteur cylindro-parabolique avec accumulation de l'énergie solaire, procédé pour faire fonctionner une centrale à collecteur cylindro-parabolique et accumulateur de chaleur à haute température Download PDF

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Publication number
WO2011000522A2
WO2011000522A2 PCT/EP2010/003862 EP2010003862W WO2011000522A2 WO 2011000522 A2 WO2011000522 A2 WO 2011000522A2 EP 2010003862 W EP2010003862 W EP 2010003862W WO 2011000522 A2 WO2011000522 A2 WO 2011000522A2
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Prior art keywords
heat
heat storage
power plant
energy
mass
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PCT/EP2010/003862
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German (de)
English (en)
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WO2011000522A3 (fr
Inventor
Vladan Petrovic
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Vladan Petrovic
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Publication of WO2011000522A2 publication Critical patent/WO2011000522A2/fr
Publication of WO2011000522A3 publication Critical patent/WO2011000522A3/fr

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/14Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
    • F01K23/04Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled condensation heat from one cycle heating the fluid in another cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K25/00Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
    • F01K25/06Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using mixtures of different fluids
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K25/00Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
    • F01K25/08Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
    • F01K25/10Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K3/00Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K3/00Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein
    • F01K3/18Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters
    • F01K3/20Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters with heating by combustion gases of main boiler
    • F01K3/205Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters with heating by combustion gases of main boiler more than one circuit being heated by one boiler
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24SSOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S20/00Solar heat collectors specially adapted for particular uses or environments
    • F24S20/20Solar heat collectors for receiving concentrated solar energy, e.g. receivers for solar power plants
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24SSOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S23/00Arrangements for concentrating solar-rays for solar heat collectors
    • F24S23/70Arrangements for concentrating solar-rays for solar heat collectors with reflectors
    • F24S23/74Arrangements for concentrating solar-rays for solar heat collectors with reflectors with trough-shaped or cylindro-parabolic reflective surfaces
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24SSOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S23/00Arrangements for concentrating solar-rays for solar heat collectors
    • F24S23/70Arrangements for concentrating solar-rays for solar heat collectors with reflectors
    • F24S23/79Arrangements for concentrating solar-rays for solar heat collectors with reflectors with spaced and opposed interacting reflective surfaces
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24SSOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S30/00Arrangements for moving or orienting solar heat collector modules
    • F24S30/40Arrangements for moving or orienting solar heat collector modules for rotary movement
    • F24S30/42Arrangements for moving or orienting solar heat collector modules for rotary movement with only one rotation axis
    • F24S30/425Horizontal axis
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24SSOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S60/00Arrangements for storing heat collected by solar heat collectors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24SSOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S90/00Solar heat systems not otherwise provided for
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/0056Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using solid heat storage material
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24SSOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S23/00Arrangements for concentrating solar-rays for solar heat collectors
    • F24S23/70Arrangements for concentrating solar-rays for solar heat collectors with reflectors
    • F24S2023/87Reflectors layout
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2270/00Thermal insulation; Thermal decoupling
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers
    • Y02E10/47Mountings or tracking
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E70/00Other energy conversion or management systems reducing GHG emissions
    • Y02E70/30Systems combining energy storage with energy generation of non-fossil origin

Definitions

  • the invention relates to a solar power plant in the form of parabolic trough power plants with the features of the preamble of claim 1 and a method having the features of the preamble of claim 12 and a high-temperature heat storage, in particular large-capacity heat storage. Accordingly, it is provided that the solar power plant in the form of a parabolic trough power plant comprises at least one reflector in the form of a parabolic trough and at least one heat storage.
  • Parabolic trough solar power plants are today the cheapest and most efficient technology for generating electricity from solar energy. They work in a similar way to conventional power plants except that they do not have the continuity of being able to produce electricity without interruption.
  • the parabolic trough power plants comprise a solar field consisting of several parallel rows of collectors. These collector rows each have a length of about 100 meters and are in turn divided into smaller individual collectors.
  • the mirrors of the individual collectors have a parabolic cross-section. At the focal point of the mirror runs an absorber tube through which a heat-resistant synthetic oil flows. The sunlight is concentrated 80 times and reflected on this tube. The oil is thereby heated to about 400 0 C.
  • the energy will transported via the carrier medium in the power plant headquarters, where it is discharged via a heat exchanger to water.
  • the resulting water vapor then drives a turbine and the turbine drives the generator.
  • Systems of this type come to an efficiency of 20% in the summer, or 14% in the annual average. Compared to other solar power plants, this technology can be described as the most effective.
  • the newer power plants have thermal storage, which means that the power plants can be operated in a predictable manner, even in cloudy weather or after sunset.
  • the required heat is stored in a liquid salt mixture of 60% sodium nitrate (N 3 NO 3 ) and 40% potassium nitrate (KNO 3 ). Both substances are used, among other things, as fertilizer, as well as for preservation in food production.
  • the liquid salt storage tanks operate at atmospheric pressure and consist of two tanks per power plant. When pumping from the "cold” into the "hot” tank, the molten salt mixture absorbs additional heat at an initial temperature of about 290 ° C., so that it is heated to about 390 ° C. A full memory, the turbine can operate about 7.5 hours.
  • the absorber tubes were specially designed for this application in parabolic trough power plants. They absorb the solar radiation reflected by the mirrors, direct the trapped heat energy through a, flowing inside
  • the construction of the absorber tube allows maximum absorption of the
  • An absorber pipe is four meters long and consists of a multi-selectively coated stainless steel pipe which has an absorption degree of 95% and at a temperature of about 400 degrees Celsius a maximum of 14%
  • the steel tube is surrounded by a vacuum-insulated concentric cladding made of borosilicate glass with an antireflective coating, which is permeable to over 96% of solar radiation. Criteria for optimal heat storage:
  • the storage mass should be made of commercially available building materials. • The energy decoupling should be as close as possible to the storage mass.
  • the object of the invention is to improve the heat storage of generic parabolic trough power plants.
  • the invention solves this problem with a solar power plant having the features of claim 1. Accordingly, it is provided in a generic solar power plant in focus (1.1) or in a focus zone of at least a parabolic trough (1) to position at least one further reflector in the form of a counterpart parabolic trough (2), so that the sun's rays are concentrated again and then the apex region (1A) of the parabolic trough (1), in particular through an opening ( 12) and on the behind it, at least at least one heat storage mass (3) comprehensive heat storage, in particular on the surface (10) or the surface of a cavity (10.1) fall in the heat storage.
  • means for retrieving the stored heat in or on the heat storage mass (3) are provided.
  • water vapor from the stored energy is generated such that a condensate by means of a condensate feed pump, in particular via a condensate distribution vessel in which the condensate level rises, is passed and that the condensate by at least a condensate line on distributed with a ballast evaporation tubes, which are located in the heat accumulator, distributed, and there evaporates abruptly and that water and water vapor is passed by steam lines in a vapor collection container.
  • a large-capacity heat accumulator for storing solar energy, wind energy, night stream, energy from biomass or other types of energy, in which the heat energy is stored in a large-scale compact unit or in blocks (1, 23, 25, 30, 37, 37a, 39 52), which are cast from refractory material (2), is stored and the stored energy by means of refractory steel tubes (3), which are closed at one end and embedded in the refractory mass (2) is decoupled.
  • the steel tubes (3) are externally armored (3a) and / or provided with expansion compensators (20) and / or the interior of the steel tubes is a ballast (4) of molten corundum, refractory stainless steel or another refractory Material filled.
  • the large-capacity heat storage is of independent inventive importance. He can u. A. can be used to store the wind energy in such a way that in the refractory mass (2) electric heating rods (24) are introduced. In this case, electrical energy obtained from wind energy is converted into the heat energy and from the stored heat energy electric current is generated again as needed.
  • the openings for the heating rods (24) can be stenciled during casting of the refractory mass.
  • the large-capacity heat accumulator can be used to store the energy from the biomass in such a way that a firing system (26) for burning the biomass is integrated in the heat accumulator (25).
  • a firing system (26) for burning the biomass is integrated in the heat accumulator (25).
  • the biomass can one or more flue gas ducts (27) are foreseen, through which the flue gases flow to release their heat to the refractory mass (2).
  • burning biomass can supplement wind energy.
  • Parabolic trough a trough-like reflector that concentrates parallel to each other incident sunbeams on a burning line-like zone and its reflective cross-sectional area is not necessarily strictly parabolic, so that instead of a focal line and a sufficiently small focal spot line (focus zone I) is acceptable.
  • Parabolic trough power plant a solar-powered power plant to provide in particular electrical energy with parabolic troughs for concentrating the incident sunbeams on a heat adsorber.
  • Heat storage mass an accumulation of material for storing heat energy in a heat storage.
  • Anti-parabolic trough an elongated, possibly trough-like reflector, concentrating more or less concentrated to each other incident sunbeams on a burning line-like zone and whose reflective cross-sectional area is not necessarily strictly parabolic, so that instead of a focal line and a sufficiently small focal spot line (focus zone II) acceptable is.
  • the heat storage mass can be up to 800 °
  • the parabolic troughs can work without absorber tube and without synthetic heat carrier, but one In the focus of the primary parabolic trough, position a narrow counterpart parabolic trough so that solar radiation is concentrated twice.
  • the solar radiation falls directly onto a heat storage. There it is converted into heat and heats up a heat storage mass. The heat is dissipated throughout the volume in the heat storage mass; This can be done by heat conduction.
  • a refractory mass can be used as a heat storage mass. It may be selected from a group of materials including refractory concrete, chamomile flour, calcined magnesia, basalt stone, lignite fly ash products, ground porcelain, or other refractory suitable for correspondingly high temperatures.
  • reinforced pipes may be embedded, e.g. Steel pipes made of heat-resistant steel.
  • the pipes can be cast in the heat storage mass.
  • the tubes can be closed or sealed at the lower end, in particular airtight, and can be designed for high pressures.
  • the tubes embedded in the heat storage mass can be filled with particles, in particular spheres, in particular corundum or steel.
  • the particles have the task to increase the heat transfer from the heat storage mass to a heat transfer fluid, such as evaporating water.
  • Balls have a large specific surface and when water as condensate hits the balls, it evaporates abruptly. In this way, the heat storage mass, preferably from top to bottom, cooled to provide the heat to the power plant process available.
  • the parabolic trough can be mounted on a load-bearing steel structure and is electronically controlled to track the sun.
  • the drive can be done by an electric motor, which is equipped with gear.
  • the axis of rotation for tracking is in or near the surface of or within the heat storage mass, the focused sunrays can always be in line fall on the heat storage mass or its surface. This happens regardless of the angle at which the parabolic trough is aligned.
  • the radiant heat t is emitted to the heat storage mass over the entire surface of the cavity.
  • the cavity may be molded into the heat-storage mass during the casting process.
  • the interior surface of the cavity may be or may be pigmented black so that the cavity forms a black body in which the absorption of the radiant energy is maximal.
  • a movable plate may be provided above the heat storage mass.
  • a reflective surface for. B. may be provided from a polished metal.
  • a slit-shaped zone or opening is provided through which the sun's rays pass. The opening and / or the plate moves in one or the other direction depending on the direction of rotation of the parabolic trough.
  • the plate can be thermally insulated.
  • the plate can be supported on both sides on rollers that move along a guide, such as a U-profile. The plate can be moved electrically, pneumatically or hydraulically.
  • the movable plate In a heat storage, it is crucial to keep heat losses to a minimum.
  • the movable plate is therefore of independent inventive importance.
  • an insulating layer or mat of about 200 mm thickness is provided as the first layer. It can withstand about 1200 0 C in continuous operation.
  • the air layer is 1000 to 2000mm, preferably about 1500 mm thick.
  • a sheath preferably made of stainless steel sheet. This may be glossy inside and have an antireflective surface on the outside, from the heat storage reflect incoming heat radiation.
  • an insulating layer or mat of mineral or rock wool of preferably 100mm to 300mm, preferably about 200mm in thickness may follow.
  • the complete insulation can be hermetically sealed so that convective cooling of the heat storage mass is prevented.
  • a corresponding reinforcement can first be provided in order to be able to support the heat storage mass.
  • On the ground a fine sand slurry can be poured about 1m thick and compacted by the vibrator.
  • the fine sand fill should not exceed a grain size of 0 to 1 mm in order to keep its thermal conductivity low.
  • the fine sand fill can be encapsulated with concrete, so that the bed can not be displaced by the pressure load.
  • the storage temperature should be up to about 1000 0 C. It is necessary to weigh with which thermodynamic parameters the power plant should be operated, ie, the relation of the steam power plant to the storage capacity has to be balanced.
  • the heat storage blocks can be factory made and placed under the parabolic troughs, isolated and connected together.
  • a glass pane can be set up, through which the focused sun rays pass and fall on the surface of the heat storage mass over the entire length of the heat storage.
  • the glass is z. B. made of temperature-resistant thermal glass, so that they can withstand the prevailing temperatures. Assuming that the sun shines on average 8 hours a day, it is possible to interpret the volume of heat storage so that, during 8 hours, stored energy, for the remaining 16 hours is sufficient to generate electricity until the next day in continuity. This would be the cheapest option. You can also design the heat storage so that when the sun fails, for example, it generates electricity for a week from stored energy. In any case, it is interesting to know how long one can generate electricity from stored solar energy under economic conditions.
  • the granules have a particle diameter between 20 mm and 50 mm, so that the heat between the individual particles is predominantly transmitted by the radiation. It is conceivable that the upper layers of the heat storage mass have a relatively larger granules and the lower layers consist of granules of smaller diameter, because the heat is better transmitted to the finer granules by the air circulation. Evaporation tubes, which are or are immersed in the granules, can be ribbed on the outside. In this way, the heat is transferred by the radiation and convection from the bed to the tube ribs and to the tube wall. From the pipe inner wall, the heat is further (if provided) to the corundum balls in the pipe interior through the Heat conduction and transmitted by the radiation. Instead of the corundum balls you can use the cast steel balls.
  • the thermal power process represents a new arrangement and operating method of inherently inventive significance. Accordingly, the new cycle process is composed of four partial cycle processes. On one shaft there is a steam turbine and three turbines working with binary mixture. All four turbines together drive the shaft in rotation. In a steam turbine, the steam relaxes to 5 bar and up to a temperature which is greater than 152 0 C (saturation temperature). After expansion, the exhaust steam is led into a heat exchanger where it transfers some of its heat to a heating water circuit. The binary mixture vaporizes in turn by passing through three evaporators and vaporizing a subset in each of the three vaporizers. In the evaporators for binary mixture there are different thermodynamic states.
  • each turbine process is responsible for each cycle.
  • the heating water enters the first evaporator with the temperature of 150 0 C and leaves the last evaporator with the temperature of 55 0 C. In this way one reaches in the steam cycle a theoretical efficiency of 25% (this was a vapor pressure of 100 bar and the steam temperature is based on 500 ° C.).
  • a theoretical efficiency of 25% this was a vapor pressure of 100 bar and the steam temperature is based on 500 ° C.
  • a total of 25.5% theoretical efficiency is achieved. It can be seen that in this way the overall efficiency of the system can be increased to 50.5%.
  • feedwater preheating and multi-stage steaming have been taken into account.
  • Figure 1 is a schematic diagram of the parabolic trough with counter-mirror and with heat storage, which is made of refractory concrete and poured in block form, and the insulation of the heat storage at a vertical position of the parabolic trough;
  • Figure 2 shows the same parabolic trough with heat storage as in Figure 1 at a position of the parabolic trough in western position (northern hemisphere of the earth and viewed from north to south)
  • Figure 3 the same parabolic trough with heat storage as shown in Figure 1 at a position of the parabolic trough in the east (northern hemisphere of the earth and viewed from north to south)
  • FIG. 4 shows an evaporation tube with filler balls with a condensate feed line, as well as an exhaust steam line;
  • Figure 5.1 is a side view of the system of Figure 1;
  • Figure 5.2 is a plan view of the system of Figure 1;
  • Figure 6.1 is a schematic diagram of the parabolic trough with counter-mirror and heat storage in cross section; the parabolic mirror is in a vertical position; of the
  • Heat storage is filled with granules of refractory stone, also is a
  • Circulation fan to equalize the temperature in the heat storage rather provided and insulation of the heat accumulator, shown;
  • FIG. 6.2 shows the arrangement according to FIG. 6.1 in a side view (section along the line B-B according to FIG. 6.1)
  • FIG. 6.3 shows the arrangement according to FIG. 6.1 in plan view (section along the line A-A according to FIG. 6.1);
  • FIG. 7 shows a ribbed tube according to FIG. 6.1;
  • Figure 8 is a schematic diagram of the ribbed tubes and the intervening
  • Figure 9 is a schematic diagram of the combined cycle processes, water vapor binary system, connected to a heat storage system;
  • Figure 9.1 shows the system, according to Figure 9 in plan view;
  • Figure 10 is a vertical view of another heat storage with concentric mirrors lying around;
  • Figure 11 shows the same heat storage in horizontal section from above;
  • Figure 12 shows a similar embodiment of the heat storage for the area-to
  • Figure 13 shows an embodiment of a further heat storage according to the same or additional wind energy and energy from biomass can be stored, in vertical section view;
  • FIG. 14 shows an embodiment of an even further heat accumulator, according to which the solar rays emit their energy via an absorber to compressed air by means of a concentrating mirror, in vertical section view;
  • Figure 15 shows a further possible application of a heat storage for storing wind energy shown schematically, in vertical section view
  • Figure 16 shows a further heat storage, poured from refractory concrete mass poured out as a monoblock, in vertical section view;
  • FIG. 18 shows a further embodiment of a heat accumulator according to which solar energy and wind energy can be stored simultaneously or separately, depending on how large the energy supply is, in vertical section view;
  • FIG. 19 shows a further heat accumulator in vertical section view
  • FIG. 19A shows the same heat accumulator in horizontal sectional view
  • Figure 20 shows a variant for storing various types of energy, which shows an economical and inexpensive alternative with a heat storage, in vertical section view;
  • Figure 20 A the same heat storage in detail;
  • FIG. 21 shows a still further embodiment possibility, which can be stored simultaneously according to solar and wind energy, in vertical section view
  • FIG. 22 shows a further embodiment which is used in accordance with a heat accumulator only for the storage of wind energy, in vertical section view; such as
  • FIG. 23 shows a heat accumulator shaped in such a way that it simultaneously serves as a furnace and
  • Heat storage is used, in vertical section view.
  • FIG. 5.1, FIG. 5.2 provides that the parabolic troughs 1 operate without an absorber tube and without a synthetic heat carrier, but that in the focus 1.1 of the primary Parabolic trough 1 a narrow Jacobparabolrinne 2 positioned so that the sun's rays are concentrated again and fall through the apex of the primary parabolic trough 1 directly on the surface 10 of a heat storage mass 3 through an opening.
  • the opening is formed during casting of the heat accumulator 3 and it opens into a cavity 10.1 whose surface is pigmented black, so that the sun's rays are captured in this cavity 10.1 (the cavity behaves like a black body), where they are converted into heat and thereby heat the heat storage mass 3 up to a relatively high temperature.
  • the heat is then distributed in the heat storage mass 3 over the entire volume through the heat conduction.
  • armored steel tubes 4 are cast from heat-resistant steel.
  • the steel tubes 4 are hermetically sealed at the bottom and can withstand relatively high pressures.
  • refractory mass 3 refractory concrete made of fireclay flour or burned magnesia or basalt stone, milled porcelain or other refractory suitable for high temperatures may be used.
  • the products with the participation of lignite fly ash are used.
  • the cast in the refractory mass 3 steel tubes 4 are filled with balls 5 from Ko round or steel.
  • the balls 5 have the task to increase the heat transfer of refractory mass 3 to evaporating water.
  • the balls 5 have a large specific surface area. When water falls on the balls, it evaporates abruptly. In this way, the refractory mass 3 is cooled from top to bottom.
  • the parabolic trough 1 is mounted on a supporting steel structure 6, is electronically controlled and tracked the sun. The drive takes place via an electric motor 7 equipped with gear 8.
  • the axis of the adjustment WeIIe 9 is in a plane with the surface 10 of the heat storage mass 3, so that the focused sun rays always fall on the surface 10 of the heat storage mass 3, regardless of which angle the parabolic trough 1 to the sun accepts.
  • a movable plate 11 is provided, on the lower side of which an anti-reflection surface 11.1 made of a polished sheet metal is attached.
  • a slot-shaped opening 12 is provided through which pass the sun's rays.
  • the plate 11 slides in one or the other direction depending on the direction of rotation of the parabolic trough 1. During the night, the entire surface of the heat storage material 10 is shielded with this plate 11. From the upper side, the plate 11 is thermally insulated. The whole plate 11 is supported on both sides of the rollers which move on a U-profile. The plate 11 can be operated electrically, pneumatically or hydraulically. In a heat storage 3, it is crucial to prevent heat loss maximum.
  • an insulating mat 13 of 200 mm thick is provided as the first layer, which can withstand 1200 0 C in continuous operation. Then comes an air layer 14 of 1500 mm thickness and then stainless steel sheet (gloss) 15 as Antire- flexblech to reflect the coming heat radiation from the heat storage 3 and the end is followed by an insulating mat 16th
  • the complete insulation is hermetically sealed, so that a convective flow and thus a cooling of the heat storage mass 3 is prevented.
  • a concept is provided, according to which an insulating plate 17 is placed on a fine sand fill of refractory insulating concrete, which at the same time as Tragplat- te for the heat accumulator 3 is used.
  • On the concrete floor a fine sand bearing bed 18 is poured about 1m thick and compacted by a vibrator.
  • the fine sand 18 should have the grain size of 0 to 1 mm so that its thermal conductivity is kept low.
  • the fine sand bed 18 is encapsulated in a concrete pit 19, so that the bed 18 can not be displaced by the pressure load.
  • the heat storage blocks 3 are factory-made and placed on site under the parabolic troughs 1, insulated and connected to each other.
  • a glass plate 20 is provided, through which the sun rays pass and on the surface 10.1 of the heat storage mass 3 fall.
  • the glass sheet 20 is made of temperature-resistant thermal glass, so that it can withstand the prevailing temperatures.
  • the evaporation tubes 4 are connected to a condensate line 21 and a steam line 22. The condensate is distributed by means of the condensate line 21 on the ball-5. Because the ball bed 5 is hot, the water evaporates abruptly and the steam is passed by means of the steam lines 22 in a vapor storage tank 39.
  • the evaporation tubes 4 are provided on the surface with a reinforcement 23, so that they form a network with refractory material 3.
  • the condensate supply to the evaporation tubes 4 is made through a condensate distribution vessel 24 by keeping the condensate level equal to the condensate level in the condensate supply lines 21 according to the law of communicating vessels.
  • the condensate is conveyed by means of the piston pump 25.
  • the grains should have a diameter between 20 mm and 50 mm, because the heat between the individual grains is usually transmitted by the radiation. It is conceivable that the upper layers should have a granulate with a larger grain and the lower layers are made of granules of smaller diameter, because the heat is better transmitted to the finer granules by the air circulation.
  • the tubes 27, which are immersed in the granules 26, are highly fused, so that the heat is transferred by the radiation and convection from the bed to the tubular ribs 27.1 and to the tube wall. From the tube inner wall, the heat is transferred to the corundum balls 5 through the heat conduction and through the radiation. Instead of the corundum balls 5 you can use the cast steel balls.
  • the inventive concept according to FIG. 9 and FIG. 9.1 is a new conception of the thermal power process.
  • the cycle consists of four partial cycle processes.
  • On a shaft 29 is a steam turbine 30 and three turbines 31, 32, 33 which operate with binary mixture. All four turbines 30, 31, 32, 33 are placed on a shaft 29 and together they set the shaft 29 in rotary motion.
  • the steam turbine 30 the steam relaxes to 5 bar pressure and up to a temperature which is greater than 152 0 C (saturation temperature).
  • exhaust steam is passed into a heat exchanger 34 where it transfers its heat to a Walkerwassernikmaschinevier 35, the row after three evaporators 36, 37, 38 passes and in each of the three evaporators 36, 37, 38 evaporates the binary mixture.
  • a large-capacity heat accumulator 101 according to FIG. 10 has a cuboidal, round or other shape cast from casting compound 102, which constitutes a compact heat storage block.
  • the casting compound 102 may be made of refractory concrete which hardens after the casting process in a certain time.
  • Tubes 103 made of heat-resistant steel are embedded in the refractory mass and previously reinforced if necessary and provided with compensators for absorbing thermal expansion and cast with the casting compound.
  • the tubes are closed at the bottom and open at the top.
  • the pipes can be filled with a pouring pad 104, which can withstand high temperatures.
  • the ballast material may be made of molten corundum, refractory grade stainless steel or another temperature resistant material.
  • the tubes protrude out of the refractory concrete mass and are directed into a vapor collection vessel 105.
  • the tubes may be airtight welded to the bottom of the vapor collection container 105.
  • Water inlet openings 106 can be provided, through which water or condensate can drip into the pipes.
  • the basic form of the refractory mass can be designed arbitrarily.
  • the solar radiation surfaces 107 are convex, and can be airtightly shielded with a glazing, in particular a double glazing 108, in such a way that no circulating movement of the air between the double glazing and the solar irradiation surface is possible.
  • the sunshine surface can be pigmented black and serves as an absorber surface.
  • the sun's rays are concentrated by concentric mirror 109 through the double glazing on the irradiation surface, thereby producing a temperature up to 1000 0 C.
  • the heat is then transported through the concrete mass by heat conduction.
  • the temperature in the concrete mass tends to a steady state.
  • the energy of the sun's rays should always be greater than the decoupled energy from the concrete mass so that the temperature varies between a maximum and a minimum value.
  • the heat decoupling from the heat storage mass is carried out in such a way that condensate is passed into the vapor collection tank 105, through which openings 6 flows into the evaporation tubes, is distributed to the ballast located in the evaporation tubes, which has a high temperature and high specific surface, and there vaporized suddenly.
  • the steam rises in the Dampfsammeiraum 110, wherein a vapor pressure builds up.
  • the water vapor thus formed having a certain vapor pressure is then conducted into a steam turbine 111 and electric current is generated by means of the current generator 112.
  • the system is regulated in such a way that the vapor pressure in the vapor collection chamber 110 is kept constant by means of a condensate feed pump 113.
  • the condensate feed pump When there is a demand for steam, the condensate feed pump is activated, the pump feeds the condensate into the steam collecting tank and the further procedure proceeds as described above.
  • the speed of the steam turbine is controlled by means of the steam control valve 114.
  • the isolation of the heat storage is z. B. designed as described above.
  • facilities 119 are provided, such as heat-insulated gates which cover the irradiation area 107 at night.
  • FIG. 11 is a plan view of the heat storage with concentric mirrors lying around 109 shown.
  • FIG. 12 shows a similar embodiment of the heat accumulator for use for storing wind energy. From a wind turbine 122 electrical power is passed to the heat storage. In the heat storage electric heating elements 124 are placed in a horizontal arrangement in openings, which are taken into account during the casting process of the heat accumulator 123. The wind stream is directed into the heating rods, which release the heat to the heat storage mass.
  • FIG. 13 shows an embodiment which, according to simultaneous or supplementary wind energy and energy from the biomass, can be stored.
  • a furnace 126 In front of the heat storage 125, a furnace 126 is mounted.
  • a flue gas channel 127 In the heat storage mass, a flue gas channel 127 is recessed so that the flue gases flow from the furnace through the flue gas channel. There they give off their heat to the heat storage mass 102 and heat them.
  • heating rods 124 (as in Figure 12).
  • the flue gases are conveyed by means of a blower 128 through the heat storage mass.
  • FIG. 14 shows an embodiment according to which the solar rays emit their energy via an absorber 129 to the compressed air by means of a concentrating mirror 109.
  • the hot air from the absorber flows through pipes which are embedded in the heat storage block 130a and may be potted with heat storage mass. She gives her heat to the heat storage mass and it is velvet their residual heat passed into an air turbine 131, there relaxed to atmospheric pressure and by means of a power generator 132, electric power is generated. Part of the power generated in the turbine is delivered to a compressor 133 to compress the outside air. The outside air is sucked through an inlet 134 into the compressor and compressed to a certain pressure. In air compression, the air temperature rises.
  • the system can be put into operation when the heat storage mass is a temperature of z. B. 400 0 C reached. At this temperature and an air pressure of about 10 bar, the power generator 131 and compressor 133 can be operated. For the specific operating conditions, the air pressure of 10 bar, the compression end temperature of the air is 292 0 C. To heat the air to 400 0 C requires a ⁇ T of 108 0 C. For these conditions after the turbine 132, the final relaxation temperature of the air 75 0 C. Thus, the theoretical efficiency for adiabatic relaxation and adiabatic compression is 30%.
  • FIG. 15 schematically shows a further application possibility for storing the wind energy.
  • the heating elements 124 are inserted. introduced. By means of the heating rods, the power from the wind turbine 122 in the storage blocks is converted into heat energy.
  • the execution principle is identical to the embodiment according to FIG.
  • the atmospheric air is compressed to a specific pressure by means of the compressor 133 and is subsequently conducted into the heat storage blocks 130. There it is heated to a higher temperature than the compression temperature and is then passed into the turbine 131. In the turbine, the air relaxes to atmospheric pressure and to a temperature higher than the ambient temperature. By the air release in the turbine electric current is generated by means of the current generator 132. Part of the power is delivered to the compressor 133 to compress the outside air.
  • the heat accumulator 101 made of refractory concrete mass 102 is shown poured out as a modular block.
  • fireproof steel tubes 103 are embedded with reinforcement 103a made of stainless steel wire.
  • reinforcement 103a made of stainless steel wire.
  • steel tubes there is a ball bed 104 to intensify the heat transfer to the air flowing through the steel tubes.
  • the relevant embodiment is provided for the purpose of storing the solar energy.
  • the basic form of the refractory mass can be designed arbitrarily.
  • the solar radiation surfaces 7 are convex, and airtightly shielded with a double glazing 108 such that no circulating movement of the air between the double glazing and the sun radiation surface is possible.
  • the sunshine surface is pigmented black and serves as an absorber surface.
  • the sun's rays are concentrated by means of concentrating mirrors 109 through the double glazing on the irradiation surface, the temperature is up to 1000 0 C and the heat is then transferred through the concrete mass by heat conduction. From the stored in the heat storage mass high temperature heat, the energy is decoupled by means of the air. In the compressor 133, the outside air is compressed to a certain pressure, is then passed into the heat accumulator and warmed to a temperature which is insignificantly lower than the temperature of the heat storage mass. The hot air is then passed into the air turbine 131. There it relaxes to the atmospheric pressure and to a temperature higher than the ambient temperature. The Turbine power is converted into electrical power by the power generator 132.
  • FIG. 17 shows an embodiment according to which the solar energy and the wind energy can be stored simultaneously or separately depending on how large the energy supply is. The embodiment is as shown in Figure 16, but with the introduced in the heat storage mass 102 heating rods 124 give their heat to the heat storage mass.
  • FIG. 19 schematically shows the geometry of the optimum design of a heat accumulator.
  • FIG. 19A schematically shows the top view of an optimized heat accumulator.
  • the irradiation surface is formed as a cavity 140 so that the sun rays radiate through a narrow gap 141 over the entire storage height. They are absorbed by the black pigmented surface 107 and thereby converted into heat.
  • the cavity 140 behaves almost like a black body.
  • the gap opening 141 is provided with double glazing 108 and with inner coating from the inner side of the glass sheet, so that the heat radiation is minimized.
  • a shielding gate 119 with its own drive is brought into position, so that the gap opening is completely covered, so that the radiation losses are kept to a minimum can.
  • Openings may be left in the storage mass 102 when the storage mass 2 is poured out, so that heating rods can be introduced into these openings.
  • FIG. 20 shows an economical and economical alternative.
  • a heat storage 142 is provided with a riprap 143, which consists of refractory bricks. In the riprap, the refractory steel pipes 144 are embedded.
  • the steel tubes are filled with a ballast 104 of molten corundum or refractory stainless steel to intensify heat transfer.
  • the steel pipes are ribbed from the outside with refractory steel sheet 145 so that the riprap is in constant contact with the steel pipes and with the ribs.
  • the heat from the riprap is transmitted to the steel pipes and ribs mainly by radiation. Since the steel tubes can move linearly in the riprap, the expansion receptacle can be provided outside the accumulator 142. Because the ball bed provided in the steel tubes has a large specific surface area, the heat transfer from the steel tubes to the compressed air flowing through them is very efficient.
  • the evaporation pipes are provided as described in FIG.
  • the solar energy is stored in such a way that the sun's rays, which are concentrated by means of concentrating mirrors on at least one absorber surface 129. There, they convert their energy into the heat and heat the air flowing through the absorber to a maximum of 1000 ° C.
  • the hot air is circulated by means of a blower 146, so that it is conducted from the absorber 129 into the heat accumulator 142. There it gives off its heat to the riprap 143 and leaves again the memory 142.
  • the heat decoupling from the heat accumulator 142 takes place in such a way that a compressor compresses the outside air to a certain pressure.
  • the compressed air flows through the Stahlrohe 144 which are embedded in the riprap 143. There it is additionally heated by the heat decoupling from the riprap. It is then directed into an air turbine 131. In the turbine, the air relaxes to the ambient pressure and a temperature that is higher than the ambient temperature.
  • FIG. 20A shows the heat accumulator 142 with riprap 143 and steel pipes 144 embedded in the riprap.
  • the heat accumulator 142 rests on a fine sand fill 117b and the fine sand fill lies on a foundation of reinforced concrete 117a.
  • the fine sand fill 117b is shaken up and compacted on the concrete foundation.
  • the cylinder 142 which is filled with rock fill 143, is made of refractory firebrick 147 brick.
  • the port 148 and for the outlet of the port 149 is provided for the entry of hot air into the memory 142.
  • a port 150 is provided for the entry of compressed air into the accumulator 142 and a port 151 is provided for the discharge of the heated air from the accumulator 142.
  • FIG. 21 illustrates an embodiment that can be stored simultaneously according to solar and wind energy.
  • the basic principle is as described in FIG. 20, but the heat accumulator 142 is preceded by an air heater 152 in which electrical heating elements 124 are installed in order to heat up the wind system by means of the electrical energy. If the solar energy is insufficient, the energy of the wind turbine is taken or vice versa.
  • FIG. 22 shows an embodiment which, according to a heat accumulator 142, is used only for the storage of the wind energy.
  • the basic principle is already described in FIG.
  • a heat accumulator 152 is shaped such that it simultaneously serves as firing 153 and heat accumulator 152. So you can burn in the furnace 153, the biomass and store the energy of the combustion gases in the refractory mass.
  • the furnace 153 is stenciled so that the finished furnace 153 is produced after hardening of the casting compound.
  • openings 154 in the refractory mass for the flue gases are shaped such that flue gases flowing through the openings release their heat to the refractory mass and heat it up to a higher temperature.
  • steel pipes (as described for FIG. 10) are provided with reinforcement 103a and embedded with expansion compensators 120.
  • the steel tubes are filled with a ball bed 104 to increase the heat transfer from the refractory mass to the compressed air flowing through the steel tubes.
  • a motor 132 turns on (when starting, a generator 131 operates as a motor) and by means of a compressor 133, the outside air is compressed to a certain pressure.
  • the compressed air temperature increases and then the compressed air in the heat storage mass is heated to a higher temperature and relaxed in the turbine 131 to atmospheric pressure Qetzt the engine is switched as a generator).
  • the firing can be automated.
  • a flue gas fan 55 By means of a flue gas fan 55, the fresh air supply is secured in the furnace 153 and the flue gases are withdrawn from the furnace.
  • the flue gas temperature at the exit from the heat accumulator 152 should not exceed 300 ° C.
  • the rotational speed of the turbine 131 is regulated by means of a control valve 136 provided at the inlet of the air compressor 133.

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Abstract

L'invention concerne une centrale solaire comprenant des collecteurs cylindro-paraboliques (1) ainsi qu'un contre-miroir parabolique (2) qui concentre une nouvelle fois les rayons du soleil et les renvoie par le sommet du collecteur cylindro-parabolique (1) sur la surface (10.1) d'une cavité où se situe l'axe de pivotement (9) pour l'orientation du collecteur cylindro-parabolique et où le rayonnement solaire est converti en chaleur, la chaleur étant directement stockée à haut niveau de température (1000 °C) dans un accumulateur de chaleur (3). Le front de température dans l'accumulateur de chaleur (3) se diffuse dans tout le volume et réchauffe la masse de l'accumulateur de chaleur (3). L'accumulateur de chaleur (3) est isolé de toutes parts. Des tubes d'évaporation armés (4) en métal résistant à la chaleur y sont coulés et sont remplis de billes en vrac (5). Lorsque l'on répand de l'eau sur les billes en vrac (5) pour extraire la chaleur, il se produit une évaporation brusque de l'eau. La vapeur d'eau est collectée dans une cuve (39) puis est conduite dans une turbine (30) en vue de sa détente. La chaleur d'échappement en provenance de la turbine (30) est transmise à un circuit de chauffage (35), cette énergie servant à faire fonctionner trois cycles (II, III, IV) à mélange binaire. Le découplage d'énergie de l'accumulateur de chaleur (3) se fait jusqu'à basse température (100 °C).
PCT/EP2010/003862 2009-06-30 2010-06-30 Centrale à collecteur cylindro-parabolique avec accumulation de l'énergie solaire, procédé pour faire fonctionner une centrale à collecteur cylindro-parabolique et accumulateur de chaleur à haute température WO2011000522A2 (fr)

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ITMI20111745A1 (it) * 2011-09-28 2013-03-29 Ansaldo Energia Spa Serbatoio di accumulo di energia termica con ricevitore solare integrato
CN103195675A (zh) * 2013-04-18 2013-07-10 北京国投军安投资管理有限公司 山区、丘陵、沟、坡地建造塔式太阳能光热发电站
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WO2011035232A3 (fr) * 2009-09-18 2013-10-31 Massachusetts Institute Of Technology Système à énergie solaire concentrée
ITMI20111745A1 (it) * 2011-09-28 2013-03-29 Ansaldo Energia Spa Serbatoio di accumulo di energia termica con ricevitore solare integrato
ITMI20111746A1 (it) * 2011-09-28 2013-03-29 Ansaldo Energia Spa Gruppo ottico a concentrazione per un sistema di accumulo di energia termica
WO2013110730A3 (fr) * 2012-01-24 2014-03-13 Jb Group Aps Système d'accumulation de chaleur
WO2013110804A3 (fr) * 2012-01-28 2013-10-24 Georg-Simon-Ohm-Hochschule Für Angewandte Wissenschaften Procédé de conversion de courant en chaleur et de stockage de ladite chaleur
WO2013167158A1 (fr) * 2012-05-11 2013-11-14 Vladan Petrovic Accumulateur de chaleur longue durée et procédé d'accumulation de chaleur à long terme d'une énergie solaire et d'autres types d'énergie à disponibilité variable
CH706970A1 (de) * 2012-09-10 2014-03-14 Ulrich Bech Receiver für konzentrierte Sonnenstrahlung.
WO2014037582A3 (fr) * 2012-09-10 2014-11-13 Ulrich Bech Récepteur d'un rayonnement solaire concentré
EP2865965A4 (fr) * 2013-02-18 2016-07-13 Byunggyun Kim Appareil métallique d'accumulation de chaleur
US9766018B2 (en) 2013-02-18 2017-09-19 Byunggyun Kim Metal heat storage apparatus
CN103195675A (zh) * 2013-04-18 2013-07-10 北京国投军安投资管理有限公司 山区、丘陵、沟、坡地建造塔式太阳能光热发电站
CN103629827A (zh) * 2013-12-11 2014-03-12 青海大学 一种大容量井式太阳能集热-蓄热装置
CN103629827B (zh) * 2013-12-11 2017-01-18 青海大学 一种大容量井式太阳能集热‑蓄热装置
US10488079B2 (en) 2014-05-13 2019-11-26 Massachusetts Institute Of Technology Low cost parabolic cylindrical trough for concentrated solar power
DE102014107804A1 (de) * 2014-06-03 2015-12-03 Deutsches Zentrum für Luft- und Raumfahrt e.V. Wärmespeichervorrichtung, Solarkraftwerk und Verfahren zum Bereitstellen von Wärme
DE102014107804B4 (de) * 2014-06-03 2020-02-27 Deutsches Zentrum für Luft- und Raumfahrt e.V. Wärmespeichervorrichtung, Solarkraftwerk und Verfahren zum Speichern und Bereitstellen von Wärme
WO2016161238A1 (fr) * 2015-04-01 2016-10-06 Tibbott Gina Anne Systèmes de collecte d'énergie solaire et leurs procédés
US10371126B2 (en) 2015-04-01 2019-08-06 Gina Tibbott Solar power collection systems and methods thereof
AU2016243916B2 (en) * 2015-04-01 2020-02-06 Neel KRISHNAN Solar power collection systems and methods thereof
US11085424B2 (en) 2015-04-01 2021-08-10 Gina Anne Tibbott Solar power collection system and methods thereof
CN105423258A (zh) * 2015-12-24 2016-03-23 广东石油化工学院 一种复合抛物面太阳能聚光式熔融盐蒸汽发生器
CN108302810A (zh) * 2018-03-06 2018-07-20 于献榕 分布式太阳能蓄热装置
WO2021091396A1 (fr) * 2019-11-07 2021-05-14 Andric, Milos Système à énergie solaire concentrée
WO2022038487A1 (fr) * 2020-08-19 2022-02-24 King Abdullah University Of Science And Technology Système en cascade de température, alimenté par l'énergie solaire, pour la production d'électricité
FR3114379A1 (fr) 2020-09-22 2022-03-25 Isaac WOERLEN Dispositif solaire a miroirs cylindro-paraboliques de chauffage d’un fluide caloporteur
WO2023049950A1 (fr) * 2021-10-01 2023-04-06 Ess Holding Gmbh Dispositif de chauffage photothermique d'un convertisseur d'énergie thermique
WO2023049949A1 (fr) * 2021-10-01 2023-04-06 Ess Holding Gmbh Dispositif pour le chauffage photothermique d'un convertisseur d'énergie thermique

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