• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a heat storage system using sand as a solid heat storage medium, comprising: a storage vessel (1) for cold sand; a storage tank (2) for hot sand; an interposed fluidized bed heat exchanger (3) separated by weirs (4, 5) from the storage tanks (1, 2) and divided by weirs (6) into a plurality of chambers (7), the weirs (4 , 5, 6) are formed as a combination of overflow and underflow weirs; wherein in the chambers (7) of the heat exchanger (3) there are provided means (8) for transferring heat from a heat source to the sand fluidized therein and means (9) for transferring heat from the sand fluidized therein to a heat transfer medium; and a fan disposed below the heat exchanger (3) for fluidizing the sand.
    公开号:AT510897A1
    申请号:T1477/2010
    申请日:2010-09-03
    公开日:2012-07-15
    发明作者:Markus Dipl Ing Dr Haider；Roland Dr Eisl；Franz Dipl Ing Holzleithner
    申请人:Univ Wien Tech；
    IPC主号:
    专利说明:

    The present invention relates to a heat storage system using sand as a solid heat storage medium.
    STATE OF THE ART
    The use of sand as a heat carrier or storage is basically known. For example, US 4,338,919 A discloses a solar collector system in which a particulate energy collector medium, such as sand, trickles through a solar collector while absorbing thermal energy. This is delivered to a gaseous (e.g., air) or liquid medium (e.g., water) in a fluidized bed heat exchanger, after which the solid is again passed through the solar collector.
    In contrast, DE 101 49 806 C2 formally provides an additional heat transfer medium between the solar collector and the sand as well as a sand storage system. Specifically, this document discloses a solar tower power plant in which a mirror heliostat field focuses sunlight on a radiation receiver and thus heats it. The radiation receiver located at the top of the tower is traversed by air, which absorbs heat, then comes into contact with an underlying heat exchanger in countercurrent with trickling sand and thereby transfers the heat to the sand. This, e.g. 800 ° C hot, sand is stored in a turn below arranged hot storage to release the heat when needed. For this purpose, the sand is passed through a fluidized bed cooler where it releases the heat to a liquid or gaseous medium carried in heat exchange coils. Subsequently, the, e.g. 150 ° C hot, sand in a cold store located outside the tower, from where he can be redirected to the tower if necessary.
    The disadvantage of these embodiments lies in the fact that large amounts of sand between the places of heat absorption and heat dissipation or between the two sand stores must cover considerable distances. The transport takes place through sand pipes, which contain, for example, a pneumatic conveying system, which accounts for a significant proportion of the energy gained. 1 . * * · Ψ consumed immediately on site and thus significantly reduces the efficiency of the respective solar power plant.
    In addition, especially in solar power plants, especially at Paraboirinnen, the presence of sand for several reasons problematic. First, sand can lead to corrosion and abrasion of various components, secondly contaminate the mirrors and thirdly lead to blockages of mechanical connections, e.g. from those for adjusting the mirrors, but also those for sand transport itself (cf., for example, US 2008/01279667 A1, DE 101 60 577 A1 and US 2010/0058703 A1, where this problem is addressed).
    The aim of the invention was therefore an improved sand heat storage system, which can be operated with less energy and does not cause problems with corrosion or contamination with sand.
    DISCLOSURE OF THE INVENTION
    The invention achieves this goal in a first aspect by providing a heat storage system using sand as a solid heat storage medium, the system comprising: a cold sand storage vessel; a storage tank for hot sand; an interposed fluidized bed heat exchanger separated by weirs from the storage tanks and divided by weirs into a plurality of chambers, the weirs formed as a combination of overflow and underflow weirs; wherein means are provided in the chambers of the heat exchanger for transferring heat from a heat source to the sand fluidized therein and means for transferring heat from the sand fluidized therein to a heat transfer medium; and a fan disposed below the heat exchanger for fluidizing the sand. - 2 -
    By means of such a heat storage system according to the invention, it is possible to shift sand in a simple and energy-saving manner between the two storage containers, which are positioned in close proximity to each other, i. are separated only by the intermediate fluidized bed heat exchanger. The sand covers only small distances and can be transported within the heat exchanger exclusively by means of a Fluidisierungsmediums, whereby mechanical components in the heat exchanger are superfluous. However, the control of the flow rates of the sand from the storage containers is preferably carried out by means of controlled mechanical conveyors therein, especially as a fluidization and the storage container although according to the present invention also possible, but not economical. The combination of overflow and underflow weirs ensures that the solid mass flow rate specified by the mechanical conveyors is efficiently routed through the fluidized bed heat exchanger. By providing a plurality of chambers of the fluidized bed heat exchanger can be carried out in the respective chambers targeted heat exchange between the sand and the heat transfer means, whereby a higher heat transfer efficiency can be achieved.
    Furthermore, the space required for such a heat storage system over the prior art can be significantly reduced, since no different lines for sand transport from one storage tank in the other and back are needed, but the transport in both cases through the fluidized bed heat exchanger takes place through In addition, heat energy can be extracted from the sand in both directions. In addition, no separate conduits are required for passing a hot fluid serving as a heat source and a fluid fluid serving as a heat transport medium through the fluidized bed heat exchanger, since in preferred embodiments, it is possible to switch between different fluids passing through the same conduits.
    Moreover, a heat storage system according to the invention can be implemented as a closed system, so that there are no problems with corrosion, abrasion or abrasion
    Pollution of equipment, such as Solar energy or industrial equipment, comes, which can be combined with the heat storage system of the invention.
    The nature of these installations is not particularly limited, and all installations are possible in which large amounts of heat accumulate, which are to be cached until their use (for example for power generation). These include, for example, power plants, such as power plants to produce alternative energy, industrial plants that produce large amounts of waste heat (eg in exhaust gases), but also storage facilities for electrical energy, in which electricity is lost in the form of waste heat, by means of the heat storage system of the invention at least partially can be recovered and stored. The present invention is of course particularly well suited for solar power plants, since the problems with sand arising therefrom and described at the outset are virtually completely solvable by the invention and a more flexible provision of the recovered energy is made possible (for example by power generation even at night). The invention therefore relates, in a second aspect, to the use of the heat storage system according to the invention for the storage of heat generated in such installations.
    In preferred embodiments of the heat storage system according to the first aspect of the invention, the weirs between the individual chambers of the fluidized bed heat exchanger and between the heat exchanger and the two storage containers are at least partially and independently adjustable in height. In this way, for example, a particular weir when transporting the sand in one direction as overflow weir, the return transport, however, serve as underflow weir or vice versa. In addition, the sand does not need to be raised by a weir (by fluidization or mechanical) between the heat exchanger and a storage tank, but after lifting the weir it can simply trickle underneath into the next chamber of the heat exchanger or storage tank. The height adjustability of individual or all weirs thus simplifies the transport of the sand, which further reduces the energy required for this purpose. -4- •
    Due to the presence of fluidized beds in the chambers of the heat exchanger lateral guide rails for the höhenverstetlbaren weirs are just as little required as seals at its lower end, since the weirs can be easily lowered into the fluidized bed. Nevertheless, it is of course possible to provide such rails, seals or similar components thereto.
    The height adjustability of the weirs also allows control of the height of the sand bed in the respective chambers or the filling level in the storage containers, whereby the heat content in the entire heat storage system and in particular in the heat exchanger is controllable. In addition, the residence time of the sand in the chambers can be controlled by the combination of the height of the weirs and the strength of the introduced into the respective chambers fluidization flow.
    In underflow weirs, on the other hand, due to the pressure exerted on the fluidized bed particles, there is a direct transfer of the sand under the weir into the next chamber of the heat exchanger, which can be adjusted, for example, if particularly short residence times are desired, e.g. when the energy is to be recovered quickly from the heat storage.
    The manner in which the weirs are adjustable in height is not particularly limited, and any types of mechanical, hydraulic and pneumatic lifting devices are contemplated, such as e.g. Chain or cable hoists, lifting platforms, etc. For cost reasons, chain or cable hoists made of high-temperature resistant steels are preferred.
    The fan for fluidizing the sand may preferably serve simultaneously as a means for transferring heat to the sand by blowing hot air in as a fluidizing medium which also functions as a heat source. In this way, already during the heating of the sand, which is subsequently conducted into the storage vessel for hot sand, a portion of the heat supplied with the hot air in the fluidized bed heat exchanger on the heat transport medium over -5- * φ * φ · φ carry and be won immediately. As hot air, for example, the air heated in a solar tower power plant of the prior art (e.g., DE 101 49 806 C2) can be used. On the other hand, for this purpose, for example, a hot exhaust gas from an industrial process can be used as a heat source.
    Alternatively, or in addition, as a means of transferring heat to the sand, one or more conduits may preferably serve to pass a hot fluid serving as the instantaneous heat source through the heat exchanger, more preferably using bundles of such conduits to maximize surface area to provide for the heat transfer. In these lines, for example, a gaseous or liquid medium are used, which is used in parabolic trough solar power plants, as described for example in the aforementioned US applications 2008/01279667 A1 and 2010/0058703 A1. Likewise, the means for transferring heat from the sand to a heat transport medium is preferably one or more conduits for passing a " cold fluid " serving as a heat transport medium. through the heat exchanger, more preferably in turn bundles of such lines.
    Neither the hot nor the cold fluid are particularly limited, so that all flowable liquid and gaseous media and mixtures thereof, which are able to absorb heat and deliver. For example, water or another liquid can be used directly, which evaporates on absorption of heat and is passed through the lines in vapor form. Especially when used as (initially) cold fluid, the liquid heated and vaporized by contact with the hot sand can then be used directly for the operation of steam turbines.
    Although, of course, both the hot and cold fluids are heat transport media, for purposes of clarity, the hot fluid is referred to herein as " heat source " for the -6- * I (* · »i f t t« «* * * * f *» · ft · »« · I | * * * · ft ft *
    Sand, while the cold fluid " heat transport medium " which extracts heat from the heat storage system when needed, which subsequently converts into usable energy, e.g. electric current, is converted. In fact, the actual source of heat is, for example, a power plant, an industrial plant, etc., in which a fluid is heated, which thereafter is called " hot fluid " represents the immediate source of heat for the sand. Collectively, both fluids will be referred to hereafter as " heat transfer media " designated.
    In the two sand storage containers, means for discharging sand are preferably provided therefrom in order to be able to convey sand from lower areas of the storage containers into the fluidized-bed heat exchanger. These sand discharging means are preferably selected from screw, belt and bucket conveyors and fluidizing blowers. Of these, mechanical conveyors are even more preferred to keep system energy consumption low. For different applications, however, other means of conveyance may be used instead of or in addition thereto. The particular means of choice depends both on the intended use and on the construction of the heat storage system according to the invention. In general, however, a conventional mechanical conveyor will be preferable.
    In preferred embodiments, a recuperative gas heat exchanger is provided in the heat storage system according to the invention as an additional component above the fluidized bed heat exchanger for recovering heat from the fluidizing medium, which further increases the energy yield of the system.
    By " sand " herein is meant in the broadest sense any solid, temperature resistant, abrasion resistant, unreactive, granular material which, for a given grain size distribution, has a grain size of about 0.03 to 2 mm. The definition thus does not only cover mineral clastic sediments, such as e.g. Quartz sands and industrial sands, but also, for example, granulated slag from the (iron) Hüt-tenwesen or from thermal power plant processes, olivine and the like. The grain size and distribution determine the fluidization properties of the -7- > · «T»
    Sand essential, so that the selection of suitable sand essential importance. Due to the geographical location of modern solar power plants, natural sea sand or dune sand, after appropriate cleaning or sighting, may be preferable for this particular area of application.
    The materials for the components of the heat storage system according to the invention, especially for the storage tanks, the walls of the heat exchanger and the weirs, are not particularly limited as long as temperature resistance, chemical inertness, abrasion resistance and corrosion resistance are ensured. Depending on the component, concrete and high-temperature-resistant precious and special steels are preferred. For height-adjustable weirs, for example, possibly reinforced, lightweight concrete is the material of choice.
    The fluidization of the sand in the fluidized bed heat exchanger can in principle be carried out with any fluidizing medium which undergoes no decomposition at the prevailing temperatures and is chemically inert accordingly. According to the present invention, it is preferable to use a gas or gas mixture, more preferably air or a flue gas or exhaust gas.
    BRIEF DESCRIPTION OF THE DRAWINGS
    Fig. 1 shows a schematic side view of a preferred embodiment of the heat storage system of the invention;
    Fig. 2 is a schematic plan view of the embodiment of the heat storage system of the invention of Fig. 1; and
    3 illustrates a schematic diagram of the possible operating modes of a heat storage system of the invention in combination with a heat generating plant.
    DETAILED DESCRIPTION OF THE INVENTION
    In the figures, preferred embodiments of the heat storage system of the present invention with height-adjustable weirs are shown schematically. * * * 4 * * * * »♦ * * *« • φ · Ψ «tl« »· < Of course, embodiments are not to be understood as limiting, but merely to illustrate the invention. FIG.
    In Fig. 1, reference numeral 1 denotes a storage tank for cold sand, 2 a storage tank for hot sand, 3 the fluidized bed heat exchanger which is divided into three chambers 7. The division takes place by means of two weirs 6 and the delimitation to the storage containers 1 and 2 by means of two weirs 4 and 5. All weirs are designed height adjustable by means of chain or cable 11, and both storage containers each include a bucket or bucket conveyor 10 for delivery of it stored sand. The fluidized-bed heat exchanger 3 is fluidized by means of a blower (not shown) which injects a fluidizing medium from below into the heat exchanger 3 to produce in the chambers 7 fluidized beds whose average height is represented by wavy lines.
    When operating the heat storage system in the " load " mode, i. to load the sand with heat, ie with relatively full cold sand storage 1 and relatively empty hot storage tank 2, cold sand from the storage tank 1 by means of a conveyor 10, shown in Fig. 1 as a cup or blade conveyor, transported in the fluidized bed heat exchanger 3. As a result, a slope is generated by the different choice of the height of the weirs to the storage tank 2 for hot sand. The weir 5, the storage tank 2 separates from the heat exchanger 3, is completely pulled up for this purpose, so that the sand from the third (in the figure: right) chamber 7 of the heat exchanger 3 can pass below the weir 5 in the storage container 2. The two weirs 6, which separate the three chambers 7 of the heat exchanger 3 from each other, are shown in a middle position and a lower position, and the migration of the sand is indicated by arrows.
    The left of the two weirs 6 is shown in an intermediate position, from which it can be brought into the position of both an overflow and an underflow weir. If a short dwell time of the sand in the first (ie, chamber) chamber 7 is desired, the weir will be left in this position, or even raised slightly so that the sand below the weir will be in place pass next (ie middle) chamber and - assuming about the same degree of fluidization of the two chambers - can provide a level balance. If the sand lingers for a long time in the left chamber to be loaded with heat, the left of the weirs 6 is lowered to the bottom of the heat exchanger 3, so that the sand can leave the left chamber only when the fluidizing current is amplified and the fluidized bed merges into a rapidly fluidized, solids-carrying fluidized bed. The same applies to the right of the weirs 6.
    The loading of the sand with heat can, as already mentioned, for example, be done by a hot fluid, e.g. Hot air is used as a fluidizing medium or by a hot fluid is passed through heat exchange lines, which are surrounded by the fluidized sand, or by a combination thereof. Such leads are indicated in Fig. 2 by reference numeral "8,9". This means that during the loading of the sand with heat, the conduit serves as a means 8 for transferring heat to the sand fluidized in the respective chamber, whereas in the case of " unloading " of the sand, that is, in the heat release, as a means 9 for transferring heat from the sand to a guided in the line heat transport medium. This represents a significant advantage of the invention, since in one and the same heat exchanger, both the loading and unloading can be done by simply different fluids are passed through the lines 8,9, between which can be switched depending on the operating mode.
    Fig. 2 is a schematic plan view of the embodiment of Fig. 1, in which like components are identified by like reference numerals. In addition, two screw conveyors 12 are shown in the two sand storage containers 1 and 2, by means of which the sand in the horizontal direction to each bucket or bucket conveyor 10 can be transported. The bucket conveyors 10 are arranged for this purpose in each case at the lateral edge of the storage container in order to be able to empty the latter as completely as possible in the corresponding operating mode. Due to the fluidization of the fluidized-bed heat exchanger 3, the position of the conveyors 10 in the horizontal direction is irrelevant since the fill level in the respective chamber of the heat exchanger is automatically leveled off in any case. As can also be seen in FIG. 2, the weirs 4 and 5 do not extend over the entire width of the heat exchanger 3.
    While providing a pneumatic delivery within the storage container 1 and 2, both conveyors 10 and 12 could be omitted. However, due to the high energy requirements for fluidizing the large quantities of sand in the storage tanks, fluidization thereof is preferred only in exceptional cases.
    Although the line 8, 9 is shown as a single line in FIG. 2 for reasons of clarity, it will be understood that in practice a line bundle will be used in order to improve the heat transfer. The transition of the lines 8,9 from one chamber 7 to the next takes place in the illustrated case below the weirs 6, as indicated by the dashed line in this area. Alternatively or additionally, however, the lines can also be led around the weirs 6 outside the fluidized-bed heat exchanger 3. The option of routing above the weirs 6, however, is hardly practicable due to the height adjustability of the latter.
    In the second mode of operation, i. at " unload " of the sand, that is, the discharge of heat to a heat transport medium, the configuration of the heat storage system according to the invention shown in Fig. 1 is reversed, i. the weir 5 is in the height shown for weir 4 and vice versa, and the weirs 6 are arranged according to the desired residence time as overflow or underflow weirs. Has during loading of the sand with heat as the heat source or heat transfer medium through the line 8,9 passed fluid (possibly in addition to hot air as Fluidisierungsmedium), just needs to be switched when unloading the power of the line 8,9, so that this now is traversed by a heat transfer medium, which absorbs heat from the hot sand. -11 - i :: :: ::. :. • t k »·» · · · · · · · · · · · ·
    A first example of a use of a heat storage system according to the invention in combination with a power generation plant is shown in the form of a schematic circuit diagram in FIG. In this figure, reference numerals denote the following constituents: 13 ... an external heat source, e.g. a power plant, an industrial plant, a power storage or the like; 14,15 ... distributor or collector for connecting the corresponding supply and discharge lines with the line bundle 8,9; 21-29 ... conduits for transporting heat transfer fluids to and from the heat storage system of the invention; 31-35 ... flow regulators, e.g. Valves, with 31-32 three-way valves and 33-35 check valves.
    The bundle of wires 8, 9 passes through a heat storage system (not shown) according to the invention to release heat from the sand fluidized therein to a heat transfer medium or vice versa.
    In the first mode of operation of the heat storage system of the invention, i. When the sand is charged with heat, a heat transfer medium serving as a source of heat for the sand is sent via conduit 21, valve 31 and conduit 22 to the external heat source 13, e.g. a solar power plant, directed where it absorbs heat, so is heated high. Via valve 32, line 23 and valve 33, the now hot fluid enters the manifold 14, which splits the line 23 into a line bundle 8.9 (in this case 8), which passes through the fluidized bed heat exchanger of the heat storage system and there the heat to most of it on the sand contained in it. Shut-off valve 34 is closed in this case. The collector 15 reunifies the line bundle to line 24, through which, as well as via valve 35 and line 25, the cooled fluid is discharged from the system (e.g., into a storage tank) or directly recycled via line 21. In the event that no heat is to be stored in or removed from the heat storage system, the system of Fig. 3 is set in a " bypass " mode. * * * * · ♦ · «« * * * * 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 # 4 · »· 4 4 4 switches. In this case, the heat transfer medium again passes via line 21, valve 31 and line 22 into the external heat source where it is heated. Thereafter, however, it is not passed through the heat storage system, but leaves the plant via lines 26, 27 and 25 with the check valves 33, 34 and 35 closed. Outside the system shown, the heat carried by the fluid is converted into usable energy, e.g. in steam turbines into electricity, converted.
    In the second mode of operation of the heat storage system of the invention, i. During discharge, the heat transfer medium, which in this case serves as a heat transport medium, flows. a cold fluid, via line 21, valve 31 and line 28 into the manifold 15, where it is split up on the line bundle 8, 9 (in this case 9), thus passing through the fluidized bed heat exchanger where it absorbs heat from the hot sand. The line bundle is brought together in the collector 14 again to a line 29, via which and via valve 34 and the lines 27 and 25, the now hot fluid leaves the system shown and again converts the heat absorbed into usable energy. The check valves 33 and 35 are closed in this case.
    A second example is the use of the heat storage system for the continuous use of a pulsating, i. discontinuous, resulting hot exhaust gas from an industrial process, e.g. an industrial furnace.
    In this use case, " Load " the heat storage system used the hot exhaust gas as the fluidizing medium and heat source. In the "discharge" phase, the solids mass flow is reversed with the aid of the mechanical conveyors and the height-adjustable weirs, and the fluidization now takes place, for example, with cold exhaust gas, a mixture of exhaust gas and fresh air or only with fresh air.
    Through lines 8, 9 of the fluidized bed heat exchanger, both during loading and during unloading, i. without reverse flow, a heat transport medium is passed that can now continuously extract heat from the heat storage system of the invention. When loading the sand with heat, the heat transport medium absorbs the heat mainly directly from the hot exhaust gas, while it extracts the heat during discharge of the solid in ventar in the fluidized bed heat exchanger,
    The present invention thus provides a heat storage system that can be used for a variety of purposes and provides a much more economical form of thermal storage in sand than has been possible in the prior art. -14-
    权利要求:
    Claims (13)
    [1]
    CLAIMS 1. A heat storage system using sand as a solid heat storage medium, comprising: - a storage vessel (1) for cold sand; - A storage tank (2) for hot sand; - Interposed fluidized bed heat exchanger (3), which is separated by weirs (4, 5) from the storage containers (1, 2) and is divided by weirs (6) in a plurality of chambers (7), wherein the weirs ( 4, 5, 6) are formed as a combination of overflow and underflow weirs; wherein in the chambers (7) of the heat exchanger (3) there are provided means (8) for transferring heat from a heat source to the sand fluidized therein and means (9) for transferring heat from the sand fluidized therein to a heat transfer medium; and - a fan disposed below the heat exchanger (3) for fluidizing the sand.
    [2]
    2. Heat storage system according to claim 1, characterized in that the weirs (4, 5, 6) are at least partially and independently adjustable in height.
    [3]
    3. Heat storage system according to claim 1 or 2, characterized in that the blower by blowing hot air or an exhaust gas as a fluidizing medium and heat source at the same time as a means (8) for transferring heat to the sand.
    [4]
    4. A heat storage system according to claim 1 or 2, characterized in that the means (8) for transferring heat to the sand are one or more conduits for passing a hot fluid serving as a heat source through the heat exchanger (3). "II. II." r «« »♦ ·» * · fl «
    [5]
    Heat storage system according to one of the preceding claims, characterized in that the means (9) for transferring heat from the sand to a heat transport medium one or more lines for passing a serving as a heat transport medium cold fluid through the heat exchanger (3) are.
    [6]
    6. Heat storage system according to one of the preceding claims, characterized in that in the sand storage containers (1, 2) means (10) for discharging sand are provided therefrom.
    [7]
    7. heat storage system according to claim 6, characterized in that the means (10) for discharging sand from screw, belt and bucket conveyors and Fluidisierungsgebläsen are selected.
    [8]
    8. Heat storage system according to one of the preceding claims, characterized in that above the fluidized bed heat exchanger (3) is provided a recuperative gas heat exchanger for recovering heat from the fluidizing medium.
    [9]
    9. Use of a heat storage system according to one of claims 1 to 8 for the storage of heat generated in a power plant.
    [10]
    10. Use according to claim 9, characterized in that the heat generated by a power plant for the production of alternative energy is stored.
    [11]
    11. Use according to claim 10, characterized in that the heat generated by a solar power plant is stored.
    [12]
    12. Use of a heat storage system according to one of claims 1 to 8 for the storage of industrial waste heat. -17- • «
    [13]
    13. Use of a heat storage system according to one of claims 1 to 8 for the storage of accumulating in the storage of electrical energy waste heat. Vienna, on - 3 Sep m Technical f University by: Vienna
    类似技术:
    公开号 | 公开日 | 专利标题
    AT510897B1|2012-10-15|HEAT STORAGE SYSTEM
    DE2748635C2|1985-05-15|Heat storage
    EP2601456B9|2020-07-01|High-temperature heat store for solar-thermal power plants
    DE2522972C3|1980-03-13|Device for feeding an internal combustion engine with hydrogen gas released from metal hydride
    EP0124842B2|1993-06-30|Power plant with a fluidized bed combustor
    DE102010044200A1|2012-01-26|Plant for exothermic high-pressure wet chemical reactions
    DE102010055997A1|2012-06-28|Method for storing thermal energy in form of high temperature heat in solar-thermal power plant, involves partially filling ambient air with granular and/or porous storage medium, where ambient air is utilized as heat carrier medium
    EP3097368B1|2019-03-13|Solar power plant with pipeline system
    CH639477A5|1983-11-15|METHOD FOR EXCHANGING HEAT IN A LATENT HEAT STORAGE AND DEVICE FOR IMPLEMENTING THE METHOD.
    DE60217724T2|2007-10-18|CONTROL DEVICE FOR A WASTE MANAGER
    DE2712445C2|1984-10-11|Device for heat recovery from slag produced in a metallurgical process
    DE102007009759A1|2008-08-28|Distribution of solid flow drawn-off from cyclone/fluidized bed container, by conducting solid flow over first down pipe and then fluidizing at bottom of down pipe by supplying carrier gas, and conveying a part of solid flow towards the top
    DE102004020993B4|2009-12-31|Storage system for storing thermal energy
    WO2005118365A1|2005-12-15|Transport system comprising traveling wagons driven by means of fuel cells
    WO2014057014A1|2014-04-17|Storage device for temporarily storing thermal energy, and method for operating a storage device
    DE2853177A1|1979-06-13|METHOD AND SYSTEM FOR HEAT RECOVERY
    DE69910698T2|2004-02-26|Device for preventing carbon deposits on solid objects
    EP3441127B1|2020-02-12|Absorption column equipped with external heat exchange circuit
    DE1608023B1|1970-10-22|Oven with moving insert for the thermal treatment of coarse-grained goods
    EP3143351A1|2017-03-22|Device for storing a liquid
    DE2735180A1|1978-02-09|METHOD AND APPARATUS FOR DISPENSING A FLUIDIZABLE FINE-GRADE MATERIAL FROM A CONTAINER
    AT521611B1|2020-03-15|Fluidized bed reactor with buffer stores
    DE102012000143A1|2013-07-11|Transferring heat and storing heat using specific and latent heat content of substances, comprises absorbing heat from heat source through heat storage material, storing heat, discharging heat to load, and releasing specific heat in plants
    EP2390605A2|2011-11-30|Drying plant for biomass and/or sludge and related method
    DE1173870B|1964-07-16|Device for dry coke cooling
    同族专利:
    公开号 | 公开日
    WO2012027769A3|2012-10-26|
    EP2612098A2|2013-07-10|
    US20130220306A1|2013-08-29|
    PL2612098T3|2015-11-30|
    ES2546177T3|2015-09-21|
    EP2612098B1|2015-07-01|
    WO2012027769A2|2012-03-08|
    US9784475B2|2017-10-10|
    AT510897B1|2012-10-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE1909039A1|1969-02-22|1970-08-27|Metallgesellschaft Ag|Fluidized bed cooler|
    GB1301103A|1969-07-17|1972-12-29|Rolls Royce|Improvements in or relating to fluidised bed heat exchange devices|
    US4149586A|1978-02-21|1979-04-17|The Governing Council Of The University Of Toronto|Heat transfer process and apparatus|
    DE2925649A1|1978-07-04|1980-01-17|Stal Laval Apparat Ab|HEAT EXCHANGER FOR THE TRANSFER OF HEAT BETWEEN GAS-SHAPED MEDIA|
    DE900578C|1950-07-20|1953-12-28|Aluminium Lab Ltd|Method and device for heat exchange between dust-like and liquid substances|
    DE1015775B|1952-01-23|1957-09-19|Aluminium Lab Ltd|Device for electrical heating of granular or powdery material, which is passed in a swirled state through a reaction chamber in horizontal flow|
    FR1150954A|1956-05-23|1958-01-22|Method for controlling the circulation of heat transport particles in heat exchangers between fluids|
    ES323698A1|1966-03-01|1966-12-01|Aux De La Ind Soc Anenima Empr|Apparatus for interacting particulate material with gas|
    US4338919A|1980-07-21|1982-07-13|University Of Pittsburgh|Solar collector system employing particulate energy collecting media|
    US4710100A|1983-11-21|1987-12-01|Oliver Laing|Wind machine|
    DE10144747A1|2001-09-11|2003-03-27|Buehler Ag|Apparatus for continuous heat treatment of granular materials, has fluidization chambers separated by partitions which have sieve bottom, below which fluidizing gas inlet is mounted|
    DE10149806C2|2001-10-09|2003-11-13|Deutsch Zentr Luft & Raumfahrt|Solar tower power plant|
    DE10160577A1|2001-12-10|2003-06-26|Joachim Lange Entwicklungs Und|Parabolic mirror system for solar energy recovery in form of heat, has glass mirror pieces corresponding to size of focal point in parabolic mirror with untreated surface to reflect solar rays|
    JP4219312B2|2004-09-08|2009-02-04|三井造船株式会社|High temperature corrosion reduction device for circulating fluidized bed boiler|
    DE102005001347A1|2005-01-11|2006-07-20|GEOTEX Ingenieurgesellschaft für Straßen- und Tiefbau mbH|Multi-chamber heat accumulator for generating electric energy/power has a trench-like structure, a surrounding wall, a cover and inner and outer areas with a solid trench-like filling|
    JP4274124B2|2005-01-11|2009-06-03|株式会社Ｉｈｉ|Method and apparatus for measuring fluid circulation rate of circulating fluidized bed combustion apparatus|
    CN101501410A|2006-06-08|2009-08-05|索波吉公司|Apparatus and methods for concentrating solar power|
    US8806834B2|2008-08-29|2014-08-19|Werner Extrusion Solutions LLC|Solar trough mirror frame, rolling rib, roller, cleaning apparatus and method|WO2014031605A1|2012-08-20|2014-02-27|Phase Change Energy Solutions, Inc.|Thermal energy storage systems|
    DE102013208973A1|2013-05-15|2014-11-20|Siemens Aktiengesellschaft|High-performance phase change|
    FR3023321B1|2014-07-03|2017-03-10|Ifp Energies Now|SYSTEM AND METHOD FOR STORING AND RECOVERING COMPRESSED GAS ENERGY WITH HEAT STORAGE BY HEAT TRANSFER FLUID|
    EP3538831A1|2016-11-09|2019-09-18|Technische Universität Wien|Method for storing thermal energy, heat reservoir, and steam power plant|
    US10488120B2|2017-02-16|2019-11-26|Gas Technology Institute|Air cooling day cycle-based processing and systems|
    AT521611B1|2018-11-13|2020-03-15|Univ Wien Tech|Fluidized bed reactor with buffer stores|
    AT521704B1|2019-03-25|2020-04-15|Berndorf Band Gmbh|Device for storing energy in the form of latent heat|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA1477/2010A|AT510897B1|2010-09-03|2010-09-03|HEAT STORAGE SYSTEM|ATA1477/2010A| AT510897B1|2010-09-03|2010-09-03|HEAT STORAGE SYSTEM|
    PCT/AT2011/000362| WO2012027769A2|2010-09-03|2011-09-05|Heat store system|
    US13/820,602| US9784475B2|2010-09-03|2011-09-05|Heat storage system with underflow and overflow weirs|
    EP11764074.8A| EP2612098B1|2010-09-03|2011-09-05|Heat storage system|
    ES11764074.8T| ES2546177T3|2010-09-03|2011-09-05|Heat storage system|
    PL11764074T| PL2612098T3|2010-09-03|2011-09-05|Heat storage system|
    [返回顶部]