MXPA97002452A - Ac storage device - Google Patents
Ac storage deviceInfo
- Publication number
- MXPA97002452A MXPA97002452A MXPA/A/1997/002452A MX9702452A MXPA97002452A MX PA97002452 A MXPA97002452 A MX PA97002452A MX 9702452 A MX9702452 A MX 9702452A MX PA97002452 A MXPA97002452 A MX PA97002452A
- Authority
- MX
- Mexico
- Prior art keywords
- layer
- heat
- storage
- solar
- tracking
- Prior art date
Links
- 229910001338 liquidmetal Inorganic materials 0.000 claims abstract description 42
- 238000005338 heat storage Methods 0.000 claims abstract description 37
- 239000007788 liquid Substances 0.000 claims abstract description 24
- 239000007787 solid Substances 0.000 claims abstract description 5
- 229910052751 metal Inorganic materials 0.000 claims description 19
- 239000002184 metal Substances 0.000 claims description 19
- 239000011780 sodium chloride Substances 0.000 claims description 16
- 150000003839 salts Chemical class 0.000 claims description 14
- 238000000605 extraction Methods 0.000 claims description 7
- 239000012530 fluid Substances 0.000 claims description 6
- 230000035515 penetration Effects 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims 1
- 239000012071 phase Substances 0.000 description 30
- 235000002639 sodium chloride Nutrition 0.000 description 15
- 239000000463 material Substances 0.000 description 12
- 150000002739 metals Chemical class 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 229910000898 sterling silver Inorganic materials 0.000 description 3
- 239000010934 sterling silver Substances 0.000 description 3
- 239000011232 storage material Substances 0.000 description 3
- 229910052783 alkali metal Inorganic materials 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 230000002452 interceptive Effects 0.000 description 2
- 230000031700 light absorption Effects 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- PUZPDOWCWNUUKD-UHFFFAOYSA-M sodium fluoride Chemical compound [F-].[Na+] PUZPDOWCWNUUKD-UHFFFAOYSA-M 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- -1 Alkali metal salts Chemical class 0.000 description 1
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L MgCl2 Chemical class [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910002056 binary alloy Inorganic materials 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L cacl2 Chemical class [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 235000011148 calcium chloride Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000021615 conjugation Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000005712 crystallization Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000374 eutectic mixture Substances 0.000 description 1
- 150000004673 fluoride salts Chemical class 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000005286 illumination Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 235000011147 magnesium chloride Nutrition 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000002310 reflectometry Methods 0.000 description 1
- 235000013024 sodium fluoride Nutrition 0.000 description 1
- 239000011775 sodium fluoride Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N tin hydride Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
Abstract
The present invention relates to a two layer heat storage system comprising two layers in contact with one another, wherein one layer is a heat storage layer and the other layer is an intermediate phase layer used to extract heat, wherein the heat storage layer is a phase change layer, in which a solid form of the phase change layer has a lower density than a liquid form of the phase change layer, and the intermediate phase layer is a layer of liquid metal that has a greater density than both phases of the change layer of fa
Description
HEAT STORAGE DEVICE
FIELD OF THE INVENTION The present invention relates to an improved heat storage device, particularly for use in a solar energy system.
BACKGROUND OF THE INVENTION The storage of energy in the form of heat is very important in the management of many energy systems, but it is of greater importance for solar energy systems. The most mature systems are those that rely on systems of sensible heat or phase change. The advantage of phase change systems over sensitive heat systems is their greater heat capacity. For example, most storage materials based on sensible heat can provide less than one calorie per degree centigrade, while the phase change from solid to liquid can provide 160 calories per gram without any change in temperature. However, these systems are more difficult to use, since the solid material tends to precipitate in the heat exchanger, thus avoiding an efficient transfer of heat. Many solar receivers are tubular receivers and the precipitation of solid material inside the tubes can be fatal to the system.
SUMMARY OF THE INVENTION It is the object of this invention to provide a improved method for the storage of heat, based on two layers of different materials, one used for storage, and the other for the extraction of heat from the storage layer. hot. As an example, the heat storage phase of the system is a phase change material and it cooperates with another phase, which is a molten metal well above the melting point, and with a higher density (specific gravity) than that of the storage phase. After the heat is stored in the heat storage phase, it can be extracted by the liquid metal through heat exchange by direct contact with the storage layer, and then transferred to another medium for application in many different ways. : i. Liquid (molten) metal can be circulated to another environment where it can release heat. ii. The heat can then be transferred to submerged tubes in the liquid metal. The tubes can contain a liquid that circulates inside the tubes and removes the heat from the walls of the tubes. iii. The transfer of heat takes place through the walls of the tubes submerged in the liquid metal, but inside the tubes there is a material with high vapor pressure, and the boiling liquid inside the tubes is converted from liquid to vapor, stirring a large amount of heat, which is usually associated with the change of phase from liquid to vapor. Such a system is practically a "heat pipe". Then the steam can transfer the heat to another medium after condensing in the environment where it takes place. final heat transfer. Then the condensed liquid is returned to the source (preferably by gravitation) for recycling. iv. If the liquid metal is selected from metals: on a high vapor pressure, then the heat pipe can be formed by immersing a bell-shaped collector in the liquid metal, and the metal vapor is collected in tubes which are integrated in the upper part of the "bell". Alternatively, put. that the liquid metal with high vapor pressure must be confined in a container, the vapor can be collected in the free space above the liquid phase in that closed container. The advantage of this last mentioned system is the large contact area between the two phases that provides a very efficient transfer of heat, and the very high heat conductivity of the liquid metal. This last invented system is the most efficient since it includes a very efficient passage of heat transfer from liquid to vapor through a large area. Within each of the two phases of the previous systems, the heat is distributed efficiently by convection, using the large volume of each phase. A small inclination at the bottom of the container containing the lower phase can improve the free convection within that phase, at the interconnection between the layers, where the heat transfer from the storage layer to the conduction layer takes place. If the storage phase is a phase change system, then in the interconnection between the layers crystals will precipitate. If the storage phase is a material in which the solid has a lower density than the liquid, then it is preferred to choose the liquid metal of a material with a density higher than the storage phase. The liquid metal will remain below the storage phase, and the solid that forms in the interconnection will float to the top of the system, without interfering with heat transfer. If the storage phase of a material in which the solid phase has a higher density than the liquid phase is selected, then the liquid metal must be a metal with a density lower than the storage phase, such that the metal It will float in the storage phase, and the exchange of heat from the liquid metal to an external system can be carried out efficiently. The chips that are formed by the crystallization of the heat storage material will precipitate at the bottom of the container, without interfering with the heat exchange. If the storage system is part of a solar system, then the preferred structure is such that the solar receiver is the storage system, and the sun is directly illuminating the upper surface of the storage phase. It is preferred to select that phase of a material relatively transparent to sunlight, so that light can penetrate into the mass, and a very efficient convective heat transfer can take place. If the material is not transparent, then the metal layer may be a candidate to facilitate the absorption of light. The use of the metal layer for the absorption of sunlight is limited to metals with low reflectivity, and preferably the metal layer is used in the lower layer. In order to obtain an illumination of the upper layer in a large central receiving system (heliostatic field based on a plurality of sun-reflecting mirrors that reflect sunlight to a tower), a reflective tower system can be used, wherein a mirror placed in the tower reflects the light downwards. A convex mirror can be placed below the focal point (or target point) of the heliostat, and a concave mirror above that point. In a plate system, a secondary mirror is placed near the focal point of preference, to reflect the light to the main axis of the tracking system, thus maintaining a receiver at a fixed point, and the collection system will be placed in that location. point. In this way, the heavy collection system is stationary, while the main mirror is tracking. Alternatively, the secondary mirror is not kept stationary, but is controlled by computer to reflect light to a previously selected station, where the collection system is parked. The new solar systems, according to the invention, include different thermal machines operated by the sun, which convert heat energy to mechanical energy. These can be gas turbines (Brayton cycles), steam turbines, machines made of sterling silver and any other thermal machine. Usually gas turbines and steam turbines are specific to large systems, while plate systems are often used for small machines made of sterling silver. It is important to note that steam from the heat pipe can be used as part of the thermal machine, for example, in the case of machines made of sterling silver, where sodium vapor can be used as an internal component in the machine, and in such arrangement sodium is selected as the liquid metal in the storage and transfer system. hot. The system of the invention can also be used to transfer solar energy to solar chemical reactors such as solar reformers or solar gasification systems, or to store solar energy for process heat. Molten salts can be used as the heat storage materials, both for sensible heat storage, and for phase change material. In accordance with this invention, it is particularly convenient to select pairs of metals and salts of the same metal as the binary system. This selection or combination minimizes the possibilities of chemical reactions between the layers. Alkaline metals have low melting points and relatively high vapor pressure and low specific gravity, therefore, these are especially useful for applications in these systems. Many fluorides have a high melting heat value, are relatively stable at high temperature and can be used in the inventive heat transfer and storage system. Magnesium can be used in conjugation with its salts, 6: 1 magnesium has a high vapor pressure, low density, and is generally safer for use than alkali metals. Aluminum has a low melting point, but a very high boiling point, and can be used when safety is important and a heat pipe application is not needed. Zinc is a relatively heavy metal and can be used as a lower metal layer. The relatively high vapor pressure of zinc allows its use for heat pipe applications. Lead and tin can be used in the invention, and are examples of heavy liquid metals with low vapor pressure. Alkali metal salts such as sodium chloride or fluoride, potassium chloride, calcium chlorides and magnesium chlorides are examples of salts that can be used in the invention. Its molten form can be used in different applications of the invention including heat storage. Also useful are eutectic mixtures or mixed salts in the invention. These examples of specific materials show that there is a large selection of salts and metals that can be used for different conditions and applications of the present invention. When a heavy metal is used in the system, then a large hydraulic pressure is formed in the lower part of the system. This pressure can compensate the internal pressure in a tubular heat exchanger associated with high pressure systems such as gas turbines. This effect is very important because the mechanical strength of many materials degrades at high temperature. Blowing the working gas through the heavy liquid layer is another important possibility in the present invention because the direct contact heat exchange of the two phases is much more efficient than the heat exchange through the two phases. walls of tubes or other containers. In the invention, heat transfer by free convection within each of the phases of the system is the preferred way of carrying out the invention. However, in some cases, as in the case where the heating is done in the upper part of one of the layers, or when the heat extraction is made from the lower layer, the convection can be used forced as an alternative, or as a supplement to achieve the desired heat transfer. Forced convection can be achieved by mechanical systems such as circulation pumps, or mixers, or by boiling an inert gas through one of the liquid layers of each of them separately. Other objects and advantages of the present invention will become apparent from the following detailed description of the preferred embodiments when taken in conjunction with the drawings.
DESCRIPTION OF THE FIGURES OF THE DRAWING Figures ad show a two-layer system where the upper layer is the heat extraction layer and the lower layer is the heat storage with the Figure showing the layers one on top of the other in the For example, Figure Ib shows the circulation of the extracycling layer of heat used to transfer the heat, the Figure showing submerged tubes in the phase of heat extraction which contains a fluid that circulates inside tubes to transfer heat to an external system, and Figure Id showing an external heat pipe submerged in the upper layer used for heat transfer. The figure shows you two configurations of heat pipes based on the volatility of the heat extraction phase. Figure lg shows the heat pipe equipped with micrometer tubes inside the receiving systems to facilitate the transfer of heat instead of the metal fins} as shown in Figures Id, 12 and lf Figures 2a, b, c, d, and e show similar systems, wherein the metal layer is the bottom layer. Figure 2f shows a system where the vessel is provided with a slope in the bottom to improve J | to free convection of the lower level. Figures 3a ad show solar systems with Figure 3a showing a transparent heat storage system and a top liquid metal layer, Figure 3b showing a top liquid metal layer and the metal layer used to absorb sunlight, 3c showing the metallic layer as the layer of the fondci and the absorption of light in the upper layer, and Figure 3d showing the lower metallic layer used pa_j * to absorb the light. Figure 4 shows a solar system where sunlight is collected by means of a heliostatic field and a mirror is placed over the tower and the light is reflected to the storage system. Figure 5 shows a solar plate with the storage system placed on the axis of rotation so that the light recollected by the plate is reflected by means of a mirror secondary to the storage system. Figure 5b shows a solar plate with the recollection system placed on the ground with the light reaching the storage system from the plate that is braking to the sun continuously through a secondary mirror which moves in a responsive manner to a separate control that continuously positions the secondary mirror in such a way that the light is reflected to the storage system.
DETAILED DESCRIPTION OF THE PREFERRED MODALITIES Referring now to the drawings in detail, the Figure shows a two-layer system contained in a container 20. The upper layer 22 is liquid metal (heat extractor) and the lower layer 24 is liquid salt ( heat collector). The materials are selected from those to which reference was made and which were described in detail above. Heat exchange occurs at the interconnection between the two layers. Figure Ib shows the pipes 26 which open towards the layer 22 and which lead out of the container 20 to remove the liquid metal towards the point of use or heat transfer and return the liquid metal to the container 20. The figure shows the pipes 28 submerged in the upper layer 22. A suitable fluid flows through the pipes 28 to extract the heat from the upper layer of liquid metal 22. The pipes 28 extend outward from the container 20 and provide a circulation system. which can be closed or opened as required. Figure Id shows an external pipe 30 submerged in the upper layer 22. The liquid metal of the upper layer 22 can flow down the pipe 30. The upper part of the pipe 30 is adjusted with the fins 32 and the upper part and the fins are contained in the container 34 through which a luid may flow to extract heat via the fins 32. In Figure 11, the pipe 30 is not submerged in the upper layer 22., but rather is separated from it, opening within the vapor space 36 on the layer 22. In this embodiment, the upper layer of liquid metal 22 is sufficiently volatile for the hot vapors to enter the pipe 30. and transfer the heat to the fluid flowing in the container 34 via the fins 32. In Figure lf, the pipe 30 is fitted with a larger nozzle bell 38 to facilitate the collection of the liquid metal or vapor from the upper layer 22. In Figure 1, the upper end of the tube 30 is assembled with miniature tubes 40 that open inside the tube 30 to improve the heat transfer of the vapor or liquid. Figures 2a-e show systems in which the liquid metal layer is below the liquid salt layer. Similar parts have been designated with similar reference numerals. Note in Figures 2c and d, the pipe 30 should not extend through the liquid salt layer 24 to be submerged in the liquid metal layer 22. In Figure 2e, the liquid metal layer 22 extends laterally beyond of the liquid salt layer to provide a lateral extension 50 accessible from the outside. In this case, the pipe 30 is immersed with a nozzle bell 38 at its lower end in the layer 22 in the lateral extension 50. In Figure 2f, the container 20 is provided with a tapered bottom to 'improve the convection in the lower layer 22. Figures 3a-d show the novel heat storage and transfer system incorporated into a solar system. Figure 3a shows a transparent heat storage system using the upper liquid metal layer 22 separated from the lower liquid salt by a baffle 60 to allow the solar energy 62 to fall directly and be absorbed by the exposed liquid salt. In Figure 3b, the upper liquid metal is transparent. Figure 3c: shows the absorption of solar energy 62 by the now upper layer 24 of liquid salt. The container 20 has a tapered bottom 21 and the heat transfer pipes 28 are submerged in the liquid metal layer 22. The solar energy enters the container 20 through the transparent section 64. In Figure 3d, the container is provided. 20 with a side extension 50 having a transparent top to allow penetration of solar energy 62 and absorption by the lower layer of liquid metal 22. Figure 4 shows a solar energy system where sunlight is collected 62 by means of a heliostatic field 70 consisting of mirrors 72 on mounts 74 supported on the ground on a suitable platform 76. The mirrors 72 are appropriately directed towards the convex mirror r'8 mounted on a tower (not shown). The mirror 78 focuses the reflected solar energy on the novel heat storage device 80 of the invention (in a previously described manner). Figure 5a shows a solar dish 90 reflecting the solar energy 62 for storing the device 80. The dish 80 rotates around the axis 92 and reflects the solar energy in all positions (two positions are shown) to the secondary mirror 94 which is focuses on the device 80. In Figure 5b, the solar plate 90 rotates about the axis 92. The device 80 is positioned on the ground. The secondary mirror 94 is actuated by a motor and articulation suitable to constantly reflect the light of the mirror 90 to the device 80. A detector detects the reflection of the solar energy of the mirror 90 and a controller in the control 96 drives the articulation of the motor 98 and the secondary mirror 94 for directing the solar energy reflected from 90 to the device 80. Although the invention has been shown and described with reference to the preferred embodiments, changes and modifications that do not depart from the teachings will become apparent to those skilled in the art. of the present invention. It is considered that such changes and modifications fall within the substance and scope of the invention as claimed.
Claims (43)
- CLAIMS 1. A two-layer heat storage system comprising two layers in contact with each other, wherein one layer is a heat storage layer, and the other layer is an intermediate phase layer that is used to extract heat, in which where the heat storage layer is a phase change layer, in which a solid form of the phase change layer has a lower density than a liquid form of the heat phase change layer, and the layer intermediate phase is a liquid metal layer that has a higher density than both phases of the phase change layer.
- 2. A system as in Claim 1, wherein the heat storage layer is a molten salt.
- 3. A system as in Claim 1, wherein the transfer of heat to an external system is achieved by the circulation of a heat transfer liquid.
- 4. A system as in Claim 1, wherein the transfer of heat to an external system is achieved by a fluid circulating in tubes that are immersed in a heat transfer fluid.
- 5. A system as in Claim 1, wherein the transfer of heat to an external system is achieved by an external heat pipe submerged in a heat transfer liquid. A system as in Claim 1, wherein the intermediate phase is vaporizable liquid metal, and the heat exchange to an external system is achieved by condensing the vapor from the liquid metal heat extraction layer, and returning the metal condensed to the heat extraction layer by gravitation or by pumping. 7. A system as in Claim 4, wherein the gravitational hydraulic pressure in the system is used to compensate the pressure used for the fluid in the external system. 8. A system as in Claim 7, wherein the heat transfer is achieved by direct contact of working gas with the liquid heat transfer layer. 9. A system as in Claim 1, wherein the heat storage system is a component in a solar system. 10. A system as in Claim 9, wherein the solar system includes a concentration system based on: a tracking of a sun axis. 11. A system as in Claim 9, wherein the solar system is a concentration system based on a two-axis tracking of the sun. 12. A system as in Claim 11, wherein the tracking system is a single-mirror or multi-mirror system. 13. A system as in Claim 12, wherein the storage system is placed near the focal point of the tracking mirror. A system as in Claim 12, wherein the sunlight is reflected to the storage system, which is placed on the tracking axis, and a fixed mirror is placed near the focal point of the tracking mirror, and reflects the sunlight to the storage system. 15. A system as in Claim 12, wherein the storage system is placed at a fixed point, and the lu ?: solar is pointing to the target storage system by a separate control of the orientation of a secondary mirror. 16. A system as in Claim 11, wherein the solar system is a heliostatic field that reflects sunlight to a high target, where it is directed to the storage system. 17. A system as in claim 13, wherein the solar light is reflected down to the storage system by a mirror placed in the solar tower. 18. A system as in Claim 1, wherein the liquid metal layer is separated from the heat storage layer by a baffle, whereby the heat storage layer directly receives and absorbs solar energy. 19. A system as in Claim 1, wherein the liquid metal layer has a transparent top to allow penetration of solar energy into the liquid metal layer. 20. A system as in Claim 1, where the liquid metal layer is placed under the heat storage layer. 21. A system as in Claim 20, wherein the heat storage layer, which is in an upper layer, directly receives the solar energy. 22. A system as in Claim 20, wherein the container is provided with a lateral extension having * a transparent upper part, whereby the liquid metal layer receives and absorbs the solar energy. 23. A two-layer heat storage system comprising two layers in contact with one another, wherein one layer is a heat storage layer, and the other layer is an intermediate phase layer that is used to extract heat , wherein the liquid metal layer is separated from the heat storage layer by a deflector, by which the heat storage layer directly receives and absorbs the solar energy. 24. A two-layer heat storage system comprising two layers in contact with each other, wherein one layer is a heat storage layer, and the other layer is an intermediate phase layer that is used to extract heat , wherein the liquid metal layer has a transparent top to allow the penetration of solar energy into the liquid metal layer. 25. A two-layer heat storage system comprising two layers in contact with each other, wherein one layer is a heat storage layer, and the other layer is an intermediate phase layer that is used to extract heat, where the intermediate phase layer is placed under; the heat storage layer. 26. A system as in claim 25, wherein the heat storage layer, which is a top layer, directly receives the solar energy. 27. A system as in Claim 25, wherein the container is provided with a lateral extension having a transparent top, whereby the liquid metal layer receives and absorbs the solar energy. 28. A system as in Claim 23, wherein the heat storage system is a component in a solar system. 29. A system as in Claim 28, wherein the solar system includes a concentration system based on a tracking of a sun axis. 30. A system as in Claim 28, wherein the solar system is a concentration system based on a tracking of two sun axes. 31. A system as in Claim 30, wherein the tracking system is a single-plate or multi-plate system. 32. A system as in Claim 31, wherein the storage system is positioned near the focal point of the tracking mirror. 33. A system as in claim 31, wherein the sunlight to the storage system, which is placed in the tracking axis, and a fixed mirror is placed near the focal point of the scan mirror reflects, and reflects the sunlight to the storage system. 34. A system as in claim 31, wherein the storage system is placed at a fixed point, and sunlight is pointing to the target storage system by a separate control of the orientation of a secondary mirror. 35. A system as in Claim 30, wherein the solar system is a heliostatic field that reflects sunlight to a high target, where it is directed to the storage system. 36. A system as in Claim 31, wherein the sunlight is reflected down to the storage system by means of a mirror placed in the solar tower. 37. A system as in Claim 24, wherein the heat storage system is a component in a solar system. 38. A system as in Claim 37, wherein the solar system includes a concentration system based on a tracking of a sun axis. 39. A system as in Claim 37, wherein the solar system is a concentration system based on a tracking of two axes of the sun. 40. A system as in Claim 39, wherein the tracking system is a single-plate or multi-plate system. 41. A system as in Claim 40, wherein the storage system is positioned near the focal point of the tracking mirror. 42. A system as in Claim 40, wherein the sunlight is reflected to the storage system, which is positioned on the tracking axis, and a fixed mirror is placed near the focal point of the tracking mirror, and reflects the sunlight to the storage system. 43. A system as in Claim 40, wherein the storage system is placed at a fixed point, 51. A system as in Claim 49, wherein the sunlight is reflected to the storage system, which is placed on the tracking axis, and a fixed mirror is placed near the focal point of the tracking mirror, and reflects the sunlight to the storage system. 52. A system as in Claim 49, wherein the storage system is placed at a fixed point, and sunlight is pointing to the target storage system by separate control of the orientation of a secondary mirror. 53. A system as in Claim 48, wherein the solar system is a heliostatic field that reflects sunlight to a high target, where it is directed to the storage system. 54. A system as in Claim 50, wherein sunlight is reflected down to the storage system by a mirror placed in the solar tower.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/317,815 US5685289A (en) | 1994-10-04 | 1994-10-04 | Heat storage device |
US08317815 | 1994-10-04 | ||
PCT/US1995/012458 WO1996010722A1 (en) | 1994-10-04 | 1995-10-04 | Heat storage device |
Publications (2)
Publication Number | Publication Date |
---|---|
MXPA97002452A true MXPA97002452A (en) | 1997-06-01 |
MX9702452A MX9702452A (en) | 1997-06-28 |
Family
ID=23235387
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX9702452A MX9702452A (en) | 1994-10-04 | 1995-10-04 | Heat storage device. |
Country Status (9)
Country | Link |
---|---|
US (1) | US5685289A (en) |
EP (1) | EP0784774A4 (en) |
AU (1) | AU711568B2 (en) |
BR (1) | BR9509233A (en) |
IL (1) | IL115488A (en) |
MX (1) | MX9702452A (en) |
NZ (1) | NZ294489A (en) |
RU (1) | RU2138751C1 (en) |
WO (1) | WO1996010722A1 (en) |
Families Citing this family (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IL130545A0 (en) | 1999-06-18 | 2000-06-01 | Yeda Res & Dev | Safety system for storage of high temperature heat |
CN100370194C (en) * | 2003-10-31 | 2008-02-20 | 赵小峰 | Solar collecting and utilizing device |
US8584734B2 (en) * | 2008-02-11 | 2013-11-19 | Navatek, Ltd | Two material phase change energy storage system |
US20110024075A1 (en) * | 2008-03-31 | 2011-02-03 | Exencotech Ab | System and method for regenerating heat energy |
DE102008047557A1 (en) * | 2008-05-30 | 2009-12-03 | Deutsches Zentrum für Luft- und Raumfahrt e.V. (DLR) | Device and system for storing thermal energy |
DE102008032531A1 (en) | 2008-07-10 | 2010-01-21 | Delta T Gmbh | Temperature control element and method for operating an insulated container |
DE102009006784A1 (en) | 2009-01-26 | 2010-07-29 | Technische Universität Ilmenau | High-temperature latent heat storage |
US8636052B2 (en) * | 2009-09-08 | 2014-01-28 | International Business Machines Corporation | Dual-fluid heat exchanger |
IN2012DN02495A (en) * | 2009-09-18 | 2015-08-28 | Massachusetts Inst Technology | |
US20110108020A1 (en) * | 2009-11-11 | 2011-05-12 | Mcenerney Bryan William | Ballast member for reducing active volume of a vessel |
US20110259544A1 (en) * | 2010-04-21 | 2011-10-27 | Lehigh University | Encapsulated phase change apparatus for thermal energy storage |
US20120037337A1 (en) * | 2010-08-16 | 2012-02-16 | Zillmer Andrew J | Heat transfer system, apparatus, and method therefor |
CN113776203A (en) | 2010-09-16 | 2021-12-10 | 威尔逊太阳能公司 | Concentrator for solar receiver |
WO2012133790A1 (en) * | 2011-03-30 | 2012-10-04 | 学校法人東京理科大学 | Heat storage device, and system provided with heat storage device |
ITMI20111745A1 (en) * | 2011-09-28 | 2013-03-29 | Ansaldo Energia Spa | THERMAL ENERGY STORAGE TANK WITH INTEGRATED SOLAR RECEIVER |
ITMI20111746A1 (en) * | 2011-09-28 | 2013-03-29 | Ansaldo Energia Spa | CONCENTRATION OPTICAL GROUP FOR A THERMAL ENERGY ACCUMULATION SYSTEM |
CN104334978B (en) | 2012-03-21 | 2017-05-17 | 威尔逊太阳能公司 | Multi-thermal storage unit systems, fluid flow control devices, and low pressure solar receivers for solar power systems, and related components and uses thereof |
US9593866B2 (en) * | 2012-06-14 | 2017-03-14 | Sunlight Power, Inc. | Thermal heat storage system |
FR2995062B1 (en) * | 2012-09-04 | 2014-10-03 | Commissariat Energie Atomique | METHODS OF STORAGE AND RELEASE OF THERMAL ENERGY, REACTOR THEREFOR, AND APPLICATION TO INTERSESTONAL STORAGE OF SOLAR HEAT |
ITMI20121791A1 (en) * | 2012-10-22 | 2014-04-23 | Gioacchino Nardin | APPARATUS AND METHOD FOR THE TRANSFER OF THERMAL ENERGY BY PHASE CHANGE MATERIALS |
KR101381370B1 (en) * | 2013-02-18 | 2014-04-04 | 김병균 | Metal heat storage device |
CN103256728A (en) * | 2013-05-22 | 2013-08-21 | 山西大学 | Fast heating device of solar pond |
JP2017519173A (en) | 2014-05-13 | 2017-07-13 | マサチューセッツ インスティテュート オブ テクノロジー | An inexpensive parabolic cylindrical trough for concentrating solar power generation. |
JP6278021B2 (en) * | 2015-10-09 | 2018-02-14 | トヨタ自動車株式会社 | Thermal storage device and method using the same |
US10677536B2 (en) * | 2015-12-04 | 2020-06-09 | Teledyne Scientific & Imaging, Llc | Osmotic transport system for evaporative cooling |
US10356950B2 (en) | 2017-12-18 | 2019-07-16 | Ge Aviation Systems, Llc | Avionics heat exchanger |
US10641556B1 (en) * | 2019-04-26 | 2020-05-05 | United Arab Emirates University | Heat sink with condensing fins and phase change material |
US11686504B2 (en) * | 2020-07-29 | 2023-06-27 | Dipak R. Biswas | Method of using stored solar heat for water heating |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3848416A (en) * | 1973-05-23 | 1974-11-19 | Gen Electric | Power generating plant with nuclear reactor/heat storage system combination |
US4068474A (en) * | 1976-08-30 | 1978-01-17 | Boris Dimitroff | Apparatus and process for steam generation by solar energy |
SE408955B (en) * | 1977-11-14 | 1979-07-16 | Teknoterm Systems Ab | PROCEDURE AND DEVICE FOR STORING HEAT ENERGY |
US4249592A (en) * | 1978-12-21 | 1981-02-10 | Kohler Co. | High temperature, heat storage and retrieval system |
DE2926960A1 (en) * | 1979-07-04 | 1981-01-22 | Daimler Benz Ag | HEAT EXCHANGER COMBINED WITH HEAT STORAGE |
SE414504B (en) * | 1979-08-22 | 1980-08-04 | Bo Carlsson | SET AND DEVICE FOR STORAGE AND RECOVERY OF HEAT THROUGH Melting and crystallization of one or more chemical compounds |
DE2934321A1 (en) * | 1979-08-24 | 1981-06-11 | Interatom Internationale Atomreaktorbau Gmbh, 5060 Bergisch Gladbach | Solar latent heat storage unit - has heat exchangers in top and bottom of vessel containing storage medium |
US4402306A (en) * | 1980-03-27 | 1983-09-06 | Mcelroy Jr Robert C | Thermal energy storage methods and processes |
US4446910A (en) * | 1980-05-22 | 1984-05-08 | General Electric Company | Two-phase thermal storage means and method |
US4335578A (en) * | 1980-05-30 | 1982-06-22 | Ford Aerospace & Communications Corporation | Solar power converter with pool boiling receiver and integral heat exchanger |
US4397152A (en) * | 1980-09-26 | 1983-08-09 | Smith Derrick A | Solar furnace |
US4662354A (en) * | 1981-05-22 | 1987-05-05 | Bernd Stoy | Heating and/or cooking device using solar energy |
US4696338A (en) * | 1982-06-01 | 1987-09-29 | Thermal Energy Stroage, Inc. | Latent heat storage and transfer system and method |
US4454865A (en) * | 1982-06-07 | 1984-06-19 | Tammen Bobby J | Liquid metal solar power system |
US4513733A (en) * | 1982-11-12 | 1985-04-30 | The Babcock & Wilcox Company | Oil field steam production and use |
DD256434A3 (en) * | 1985-12-31 | 1988-05-11 | Ingenieurtechnik Halle Bt Kael | HEAT TRANSFER FOR DYNAMIC LATENT WASTE MEMORY |
US4993486A (en) * | 1989-12-05 | 1991-02-19 | Space Power, Inc. | Heat transfer loop with cold trap |
-
1994
- 1994-10-04 US US08/317,815 patent/US5685289A/en not_active Expired - Fee Related
-
1995
- 1995-10-02 IL IL11548895A patent/IL115488A/en active IP Right Revival
- 1995-10-04 MX MX9702452A patent/MX9702452A/en not_active IP Right Cessation
- 1995-10-04 WO PCT/US1995/012458 patent/WO1996010722A1/en not_active Application Discontinuation
- 1995-10-04 RU RU97106831A patent/RU2138751C1/en active
- 1995-10-04 NZ NZ294489A patent/NZ294489A/en unknown
- 1995-10-04 BR BR9509233A patent/BR9509233A/en not_active IP Right Cessation
- 1995-10-04 AU AU37309/95A patent/AU711568B2/en not_active Ceased
- 1995-10-04 EP EP95935193A patent/EP0784774A4/en not_active Withdrawn
Similar Documents
Publication | Publication Date | Title |
---|---|---|
MXPA97002452A (en) | Ac storage device | |
AU711568B2 (en) | Heat storage device | |
Zayed et al. | Applications of cascaded phase change materials in solar water collector storage tanks: a review | |
US3915147A (en) | Solar energy steam generator | |
US9488386B2 (en) | Concentrated solar power system receiver | |
US4335578A (en) | Solar power converter with pool boiling receiver and integral heat exchanger | |
US6057504A (en) | Hybrid solar collector for generating electricity and heat by separating solar rays into long wavelength and short wavelength | |
Sharma et al. | Solar cooker with latent heat storage systems: A review | |
WO2010083285A1 (en) | Ground-based, integrated volumetric receiver-storage system for concentrated solar power | |
GB2032613A (en) | Heat transfer system | |
EP2195583B1 (en) | Residential solar thermal power plant | |
Aggarwal et al. | Thermal characteristics of sensible heat storage materials applicable for concentrated solar power systems | |
US8701653B2 (en) | High energy density thermal storage device and method | |
CN1162353A (en) | Heat storage device | |
JP3610499B2 (en) | Multi-purpose thermal light concentrating power generator | |
WO2000079202A1 (en) | Safety system for storage of high temperature heat | |
WO2009041947A1 (en) | Residential solar thermal power plant | |
RU2107232C1 (en) | Solar energy collecting device | |
EP0015017B1 (en) | Heat transport tube solar collector and system comprising at least such a collector | |
JPS5866753A (en) | Solar light energy collector | |
JP2006329491A (en) | Solar heat collecting system | |
JPS5860162A (en) | Solar heat collecting device utilizing latent heat of heat accumulating agent | |
JPS58123056A (en) | Energy accumulator | |
Trolove et al. | The design and heat pipe tests for a line focus solar Stirling domestic generation system | |
CA2036979A1 (en) | Solar distiller |