WO2002088608A1 - Method of manufacturing a multi-layered sorbent-driven self-cooling device - Google Patents
Method of manufacturing a multi-layered sorbent-driven self-cooling device Download PDFInfo
- Publication number
- WO2002088608A1 WO2002088608A1 PCT/US2001/050705 US0150705W WO02088608A1 WO 2002088608 A1 WO2002088608 A1 WO 2002088608A1 US 0150705 W US0150705 W US 0150705W WO 02088608 A1 WO02088608 A1 WO 02088608A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- placing
- layer
- sorbent
- liquid barrier
- container
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K5/00—Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
- C09K5/02—Materials undergoing a change of physical state when used
- C09K5/04—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
- C09K5/047—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for absorption-type refrigeration systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B17/00—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type
- F25B17/08—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type the absorbent or adsorbent being a solid, e.g. salt
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D31/00—Other cooling or freezing apparatus
- F25D31/006—Other cooling or freezing apparatus specially adapted for cooling receptacles, e.g. tanks
- F25D31/007—Bottles or cans
Definitions
- the present invention relates to the thermal chemical arts. More particularly to sorbent-driven cooling devices and their method of manufacture.
- Applicants' pending patent application Serial No. 09 ⁇ 691,473, filed on October 18, 2000 entitled “Evacuated Sorbent Assembly and Cooling Device,” herein incorporated by reference, teaches a self-cooling device having a small volume relative to the quantity of liquid to be cooled.
- the cooling device is driven by the 5 absorption and absorption of a liquid refrigerant, such as water. Both the adsorbing material and the liquid are held in separated evacuated chambers with the liquid refrigerant chamber in thermal contact with the medium to be cooled. Upon communication between the two evacuated chambers the liquid refrigerant starts to vaporize.
- the latent heat of vaporization channels heat away from the medium, the 0 adsorption of the initial vapor drives the vaporization of more liquid refrigerant, thereby continuing to cool the medium.
- the cooling device is symmetrical with a cooling region on its top and bottom surfaces and an insulated heat absorbing central region. In other embodiments the cooling device is asymmetrical with a cooling region on its top or bottom surface and the insulated heat-absorbing region on the opposite surface.
- a sequenced layering of materials sealed within a tray-like casing, under a vacuum, provides the cooling function of the device.
- Two basic configurations of materials are taught herein. A primary difference is the choice of either a wicking agent and thermal spacer or of an insulating material to wick the liquid refrigerant and insulate the sorbent layer from the outer cooling surface.
- the asymmetrical device is formed with a heat- removing material on the bottom, covered by a liquid barrier, followed by a sorbent layer (in thermal contact with the heat-removing material) and followed by the insulating material, which may be covered by a capillary membrane to direct the liquid refrigerant.
- a rupturable bag encases the liquid refrigerant. After layering it is evacuated from the casing and the casing seal is sealed with a flexible cover.
- the asymmetrical device is formed with a liquid refrigerant, covered by a rupturable bag containing refrigerant liquid followed by a layer of insulating material with a sorbent placed above the insulating material and covered with a liquid barrier. At the top of the casing is placed the heat removing material, which is sealed with the flexible cover.
- the layering sequence is to first place a heat-removing material on the bottom of the casing which is then covered by a liquid barrier, followed by a sorbent layer (in thermal contact with the heat removing material), followed by a thermal spacer, covered by a vapor permeable membrane, with a wicking material thereabove.
- the rupturable bag containing the refrigerant is positioned adjacent to the wicking material and the device is then sealed with a flexible cover.
- the above layering sequence may also be reversed with the liquid refrigerant at the bottom of the casing, or constructed to allow the wicking to direct a portion of the liquid refrigerant from the top of the device to the casing bottom.
- a symmetrical device, utilizing the insulating material may be constructed by duplicating the layers in a reversed order, either above or below the heat removing material.
- the cooling device may be affixed to a beverage container or integrated into the beverage container.
- FIG. 1 A is a partially cut-away elevational view of the cooling device in accordance with the invention.
- FIGS. IB- IF are plan views of alternate shapes for the cooling devices.
- FIG. 1G-1K are cross-sectional views of alternate shapes for the cooling devices.
- FIG 2 A is a cross-sectional view of a cooling device in accordance with the invention.
- FIG. 2B is a cross-sectional view of a first alternate embodiment of the cooling device.
- FIG. 2C is a cross-sectional view of a second alternate embodiment of the cooling device.
- FIG. 2D is a cross-sectional view of a third alternate embodiment of the cooling device.
- FIG. 3 A is a cross-sectional view of a fourth alternate embodiment of the cooling device.
- FIG. 3B is a cross-sectional view of a fifth alternate embodiment of the cooling device prior to the completion of its assembly.
- FIG. 3C is a cross-sectional view of the embodiment of FIG. 3B fully assembled.
- FIG. 4 A is a component view of the preferred embodiment of the flexible self- cooling beverage pouch.
- FIG. 4B is a component view of a first alternate embodiment of the flexible self-cooling beverage pouch.
- FIG. 4C is a cross-sectional view of one embodiment of a flexible self-cooling beverage pouch.
- FIG. 4D is a cross-sectional view of another embodiment of a flexible self- cooling beverage pouch.
- FIG. 5 A is a perspective view of a self-cooling box container.
- FIG. 5B is a first alternate embodiment of the self-cooling box container.
- FIG. 5C is a second alternate embodiment of the self-cooling box container. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
- the word “absorption” refers to the occurrence of a substance (e.g., water vapor) penetrating the inner structure of another (the absorbent).
- the word “adsorption” refers to the occurrence of a substance (e.g., water vapor) being attracted and held onto the surface of another (the adsorbent).
- the words “absorption” and “adsorption” include derivatives thereof.
- the word “sorbent” refers to a material that is either an absorbent and/or an adsorbent.
- cooling device 10 is constructed with a tray-like casing 11, having sidewalls 18 (two shown) and a bottom 16.
- the casing is sealed with a cover 12.
- the shape, dimensions and configuration of the casing is a function of the materials used, the degree of cooling desired, the rate of cooling desired, the shape, size, and volume of the material to be cooled, and the nature of the material to be cooled.
- the casing has substantially rectangular cross section.
- casings 11 that have square, polygonal, circular, semi-circular or irregular cross sections.
- the casings can have a flat bottom 16 as shown in FIG. 1 A or, as shown FIGS. 1G and 1H, have one or more bottom indentations 13.
- Bottom indentations 13 act to partition at least a potion of the casing's interior into at least a first chamber 11a and a second chamber l ib (FIG. 1G) and in some embodiments a third chamber l ie (FIG. 1H).
- a portion 17 of the bottom 16 can protrude downward from the flat bottom surface.
- a stepped region 14, as shown in FIGS. II and K, may be formed in the casing 11 projecting outwardly from the portion of the top of a sidewall 18.
- Raised spikes 15 projecting into the interior of the casing can be formed on the substantially flat bottom 16 (FIG. 11), within the stepped region 14 (FIGS. II and IK) or at the bottom 16 of a protrusion 17 (FIGS. U and IK).
- the first layer added to the bottom 16 of the casing 11 is a layer of heat-removing material 21.
- the heat- removing material 21 may generate by-products such as water, aqueous salt solutions, and organics. Therefore, depending on the particular heat-removing material utilized, it is normally desirable to include a heat-conductive liquid barrier 22.
- the heat- conductive liquid barrier 22 is added on top of the heat-removing material 21.
- a sorbent layer 23 follows on top of the liquid barrier 22. The sorbent layer 23, through the interposed liquid barrier 22, is in thermal contact with the heat-removing material 21.
- a layer of insulating material 24, having a hydrophobic surface 24a and a hydrophilic surface 24b is then added, so that the hydrophilic surface is in direct contact with the sorbent layer 23.
- a predetermined amount of liquid refrigerant 25 contained within a rupturable bag 26 is added above the insulation 24 so that it is adjacent the hydrophilic surface 24b, and so that a portion of the bag extends into the interior of the stepped region 14.
- the filled casing is placed in a vacuum, the air evacuated, and the cover 12 sealed over the top edge 28 of the casing.
- an operator applies pressure along the line of arrows 1000 and 1001 causing the spike 15 to rupture the bag 26 thereby releasing the liquid refrigerant and initiating the cooling action. Because the bag containing the liquid refrigerant is adjacent the cover 12, in this embodiment, the active cooling region of the device is the cover's exterior surface.
- the layering sequence is reversed thereby forming a cooling device in which the active cooling region of the device is the exterior surface of the bottom of the casing 16.
- the casing 11 has a bottom protrusion 17 and a raised spike 15.
- an operator applies pressure along the line of arrows 1002 and 1003 driving the spike 15 into the bag 26 thereby releasing the liquid refrigerant 25 and initiating the cooling action.
- the multi-chambered casing 11 shown in FIGS. 2C is designed to provide a device less prone to accidental initiation of the cooling function.
- the liquid refrigerant 25 within the bag 26 is placed into one chamber l ib with all the other materials layered in the second chamber 11a.
- a layer of heat-removing material is added to the bottom 16 of the casing 11 , within the chamber 1 a, then covered by the liquid barrier 22, followed by the sorbent layer 23 which is in thermal contact with the heat-removing material 21.
- the second chamber l ib receives the predetermined amount of liquid refrigerant 25 within the rupturable bag 26.
- a capillary membrane 29, providing fluid communication between the hydrophilic surface 24b of the insulating material 24 and the liquid refrigerant 25, is then added.
- the filled casing 11 is placed in a vacuum, the air evacuated, and a flexible cover 12 is sealed over the top edge 28 of the casing 11.
- an operator applies pressure along the line of arrows 1004 and 1005 breaking the rupturable bag 26. Once broken, the bag releases the refrigerant liquid which is transported via the capillary membrane 29 to the hydrophilic region 24b of the insulating material 24.
- FIG. 2D A symmetrical cooling device, i.e., a device having active cooling regions at both its top and bottom is shown in FIG. 2D.
- a first measure of liquid refrigerant 25 within a first rupturable bag 26 is added to the bottom 16 of the casing 11, followed by a first layer of insulating material 24, with its hydrophilic surface 24b against the first bag 26, and then followed by a first sorbent layer 23.
- a first liquid barrier 22 covers the first sorbent layer 23, followed by and the heat-removing material 21, in thermal contact with the first sorbent layer 23.
- a second liquid barrier 22* is then added above the heat-removing material 21, followed by a second sorbent layer 23' which is also in thermal contact with the heat-removing material 21.
- the filled containment casing 11 is then placed in a vacuum, the air evacuated, and a flexible cover 27 is sealed over the top edge 28 of the containment casing.
- an operator applies pressure along the line of arrows 1000 and 1001 and arrows 1002 and 1003 breaking the rupturable membranes 26 and 26' thereby supplying liquid refrigerant 25 and 25' to the hydrophilic surfaces 24b and 24b' of the insulating material 24 and 24'.
- FIGS. 3A-3C are cooling devices constructed without the insulating material 24 or the capillary membrane 29.
- a thermal spacer 30 and vapor permeable membrane 31 combine with a wicking material 32 to transport the liquid vapor to the sorbent layer 23 and control the thermal leakback.
- wicking material 32 acts to draw liquid refrigerant 25 from the ruptured bag 26 and to retain the liquid refrigerant 25 for subsequent vaporization and adsorption by the sorbent layer 23.
- the wicking material 32 absorbs any vaporized liquid refrigerant that re-condenses before reaching the sorbent layer 23.
- the thermal spacer 30 is interposed between the sorbent layer 23 and the vapor-permeable membrane 31 or between the sorbent layer 23 and the wicking material 32.
- the thermal spacer 30 is utilized to insulate heat generated by the sorbent layer 23.
- FIG. 3 A A layering sequence of such an asymmetrical cooling device is shown in FIG. 3 A, which begins by adding to the bottom 16 of the casing 11 a layer of the heat- removing material 21.
- the liquid barrier 22 is added above the heat-removing material 21 and the sorbent layer 23 in thermal contact with the heat removing material 21 follows the liquid barrier 22.
- a thermal spacer is added above the sorbent layer 23, which is covered by a vapor permeable membrane 31 and a wicking material 32 rests up against the vapor permeable membrane 31.
- a predetermined amount of liquid refrigerant 25 within a rupturable bag 26 is added on top of the wicking material 32 and extending into the stepped region 14.
- the filled casing 11 is then placed in a vacuum, the air evacuated, and a flexible cover 12 is sealed over the top edge 28 of the casing 11.
- the stepped region 14 of the casing 11 provides an easy to locate region to which an operator can apply pressure along the line of arrows 1000 and 1001 thereby causing spike 15 to break the rupturable bag 26 and initiate the cooling action.
- the symmetrical device shown in FIGS 3B and 3C is formed by applying sufficient wicking material 32 to the interior of the casing 11 to extend from the bottom 20 of the casing 11, up one of the sidewalls 18 and above the top edge 28.
- a layer of vapor permeable membrane 31 having opposing ends 31a and 31 b is then added on top and the wicking material 32 with the opposing ends extending along opposing sidewalls 18, the casing 11 and above the top edge 28.
- a first thermal spacer 30 is placed above the portion of the vapor permeable membrane 31 covering the bottom 20 of the casing 11 , followed by the first sorbent layer 23, covered with the first liquid barrier 22, followed by the heat-removing material 21.
- the second liquid barrier 22' is then added above the heat-removing material 21 and followed by the second sorbent layer 23' and a second thermal spacer 30'.
- the first end 31a of the vapor permeable membrane 31 is folded along the lines of arrow 1006 so that the vapor permeable membrane covers the second thermal spacer 30'.
- the second end 31b of the vapor permeable membrane 31 then folded along the line of arrow 1007 and affixed over the first end 31a thereby sealing of the second thermal spacer 30'.
- the wicking material 32 is then folded over the vapor permeable membrane 31 along the line of arrow 1008 and finally a predetermined amount of liquid refrigerant 25 within a rupturable bag 26 is added above the wicking material 32.
- the filled casing casing 11 is then placed in a vacuum, the air evacuated, and the flexible cover 12 is sealed over the top edge 28.
- an operator applies pressure along the line of arrows 1000 and 1001, breaking the rupturable bag 26 supplying liquid refrigerant 25 to the wicking material 32 which transports the liquid refrigerant to the top and bottom 20 of the containment casing 11.
- Liquid vapor migrates across the vapor permeable membrane 31 through the first and second thermal spacers 30 and 30' and into the first and second sorbent layers 23 and 23'.
- the casing 11 and the cover 12 are constructed from a material that is impervious to air and moisture so as to provide the cooling device 10 with a suitable shelf-life (to allow for several years of storage/inactivation prior to use).
- Useful materials have an oxygen transmission rate (OTR) preferably less than about 1 cm 3 /m 2 /day, more preferably less than 0.1 cm /m /day, and most preferably less than 0.01 cm 3 /m 2 /day.
- OTR oxygen transmission rate
- the vapor transmission rate of useful materials is preferably less than about 2 g/m /day, more preferably less than 1 g/m /day, and most preferably less than about 0.1 g/m /day.
- Suitable materials for the casing include thermoplastic materials.
- Suitable materials for the cover 12 include a metallicized plastic laminate or a metal foil plastic laminate.
- Preferred materials for the cover include flexible films such as those produced by the Rexam Corporation located in Bedford Park, Illinois, and Toyo Aluminum located in Osaka, Japan.
- the sorbent layer 23 preferably is formed of an absorbent material dispersed on, impregnated in, affixed to, or otherwise combined with a porous support material.
- the porous support material preferably has a high pore volume, and therefore a high surface area, to accommodate the absorption of large amounts of liquid refrigerant 25, in vapor form, by the sorbent.
- the pore volume is expressed in units of volume per unit mass.
- the porous support material has a pore volume of at least about 0.8 cc/g, more preferably at least about 1 cc/g, and even more preferably at least about 1.5 cc/g.
- the average pore diameter is preferably at least about 1 nanometer, and typically in the range from about 1 to about 20 nanometers.
- the average pore diameter distribution is such that there are very few pores having a diameter of less than about 0.5 nanometers.
- the porous support material can be selected from virtually any material having the above-identified properties. Preferred materials for the porous support material include activated carbon and silica.
- the porous support material can come in a variety of shapes and sizes selected for a particular application.
- the porous support material is comprised of small activated carbon pellets having a size in the range of from about 0.5 to 2 millimeters.
- the porous support material is silica pellets having a size from about 0.25 to 0.5 millimeters. The size of the pellets can be selected to influence the rate at which the vapor from the liquid refrigerant 16 is absorbed. Larger pellets absorb liquid refrigerant vapor at a slower rate due to increased path length.
- the sorbent material have a pore volume that is at least about 50 percent of the pore volume of the porous support material, and even more preferably at least about 66 percent of the pore volume of the porous support material. That is, it is preferred that if the pore volume of the porous support material is about 1.5 cc/g, then the pore volume of the absorbent material is preferably no less than about 0.75 cc/g, more preferably no less than about 1.0 cc/g.
- the absorbent material is preferably capable of absorbing at least about 100 percent of its weight in water, more preferably at least about 150 percent of its weight in water, and even more preferably at least about 200 percent of its weight in water.
- the amount of water that can be absorbed will also be influenced by the relative humidity and temperature.
- absorbent material any suitable absorbent material can be used.
- Representative absorbent materials include salts such as calcium chloride, lithium chloride, lithium bromide, magnesium chloride, calcium nitrate, and potassium fluoride.
- Other suitable absorbent materials include phosphorous pentoxide, magnesium perchlorate, barium oxide, calcium oxide, calcium sulfate, aluminum oxide, calcium bromide, barium perchlorate, and copper sulfate, zeolite 13x, zeolite 5a, silicalite, silica gel, alumina, carbon, modified carbons and the like.
- the absorbent material may comprise combinations of two or more of these materials.
- the heat-removing material 21 is one of three types: (1) a material that undergoes a change of phase when heat is applied (phase-change material); (2) a material that has a heat capacity greater than the sorbent layer 23; or (3) a material that undergoes an endothermic reaction when brought in contact with a vaporized liquid refrigerant 25. It will be understood by the skilled artisan that the heat- removing material, for use in a particular application may vary depending on the sorbent utilized, the thermal insulation, if any, between the phase-change material, the liquid refrigerant, and the desired cooling rate.
- Suitable heat-removing materials 21 include paraffin, naphthalene sulphur, hydrated calcium chloride, bromocamphor, cetyl alcohol, cyanamide, eleudic acid, lauric acid, hydrated calcium silicate, sodium thiosulfate pentahydrate, disodium phosphate, hydrated sodium carbonate, hydrated calcium nitrate, neopentyl glycol, hydrated inorganic salts including Glauber's salt, inorganic salts encapsulated in paraffin, hydrated potassium and sodium sulfate, and hydrated sodium and magnesium acetate.
- the preferred heat-removing material is an inorganic salt that has been melted and re-solidified to form a monolith (thereby reducing the volume of the heat-removing material by approximately 30%).
- the heat-removing material 21 removes some of the heat from the sorbent layer 23 simply through the storage of sensible heat, because the heat-removing material heats up as the sorbent sections heat up, thereby removing heat from the sorbent sections.
- the most effective heat-removing material typically undergoes a change of phase. A large quantity of heat is absorbed in connection with a phase change (i.e., change from a solid phase to a liquid phase, change from a solid phase to part solid phase and part liquid phase, or change from a liquid phase to a vapor phase).
- phase-change heat-removing material 21 it change phase at a temperature greater than the expected ambient temperature of the material to be cooled, but less than the temperature achieved by the sorbent layer 23 upon absorption of a substantial fraction (i.e., one-third or one-quarter) of the liquid refrigerant 75.
- the phase change should take place at a temperature above about 30°C, preferably above about 35°C but preferably below about 70°C, and most preferably below about 60°C.
- the insulating material 24 is chosen to inhibit thermal leakback from the sorbent sections 28 and 30 to the exterior of the device.
- the insulating material has thermal conductivity limits less than 0.05 W/mK, preferably less than about 0.035 W/mK, and most preferably, less than about 0.025 W/mK.
- the insulating material 71 has a collapse strength sufficient to resist about one bar uniaxial load, and limit the shrinkage, due to evacuation, to less than about 20%, more preferably less than about 5%, and most preferably less than about 2%.
- an anisotropic insulating material containing both a hydrophilic region 72 and a hydrophobic region 73 is preferred.
- Such an insulating material inhibits the passage of liquid refrigerant 16 into the sorbent sections 28 and 30, yet allows the vapor of the liquid refrigerant to pass into the sorbent sections 28 and 30.
- the hydrophilic region 72 of the insulating material has pores with a relatively large diameter, not less than 10 mm in diameter, on average. The large pores of the hydrophilic region 72 encourage the rapid flow of liquid refrigerant 16 into the material.
- the hydrophobic region 73 has pores of a relatively small diameter, typically less than about 2 mm in diameter, so that the un- vaporized liquid refrigerant 16 is inhibited from passing into the sorbent section 28 and 30, but rather only the vapor from the liquid refrigerant 16 is directed into the sorbent section 28 and 30.
- the insulating material 73 can be formed by laminating a hydrophilic material such as cellulose, paper, non- woven or woven cloth formed from fibers of glass, plastic, ceramic or cellulose, to a hydrophobic material.
- the hydrophobic material can be made by modifying a hydrophilic material with a hydrophobic agent, such as by impregnating a hydrophilic material with wax or adding a hexamethyldisiliazane or a flourinated reactive group to the hydrophilic material.
- the insulating material can be formed by surface modification, whereby a sheet of material (either hydrophilic or hydrophobic) is modified to change the surface on one side.
- a sheet of material either hydrophilic or hydrophobic
- the surface of one side of a hydrophobic material can be made hydrophilic by exposure to thermal or plasma treatments or by impregnation with surfactants.
- the surface of a hydrophilic material can be made hydrophobic by treatment with hydrophobing agents or impregnation of wax-like material.
- the liquid barrier may be constructed of any suitable material, such as polyethylene or polypropylene film.
- suitable wicking materials 32 include hydrophilic materials such as microporous metals, porous plastics (polyethylene, polypropylene), cellulose products, sintered heat pipe material, or glass paper, and the like.
- the thermal spacer 30 has a thermal resistance (thermal conductivity at package conditions divided by thickness) preferably less than 100 W/m K, more preferably less than 50 W/m K, and most preferably less than 20 W/m 2 K.
- the materials utilized for the thermal spacer 30 can be selected from a range of materials known to the art that provide sufficient vapor permeability such as fiberglass, plastic fibers, and plastic foams.
- the rupturable membrane 26 is a plastic, typically polyethylene, that is filled and heat sealed along its edges 62 enclosing the liquid refrigerant 25.
- the liquid refrigerant 25 should have a high vapor pressure at ambient temperature so that a reduction of pressure will produce a high vapor production rate.
- the liquid refrigerant has a high heat of vaporization.
- the vapor pressure of the liquid refrigerant at 20°C is typically at least about 9 mm Hg, preferably at least about 15 or 20 mm Hg.
- Suitable liquid refrigerants include various alcohols, such as methyl alcohol or ethyl alcohol; ketones or aldehydes such as acetone and acetaldehyde; and hydrofluorocarbons such as C318, 114, 21, 11, 114B2, 113, 112, 134A, 141B, and 245FA.
- the preferred liquid refrigerant is water because it is plentiful and does not pose any environmental problems while providing the desired cooling characteristics.
- the liquid refrigerant 25 is mixed with an effective quantity of a miscible nucleating agent (or a partial miscible nucleating agent) having a greater vapor pressure than the liquid refrigerant to promote ebullition so that the liquid refrigerant evaporates even more quickly and smoothly, while preventing the liquid refrigerant from super-cooling and thereby decreasing the adsorption rate in the sorbent layer 23.
- a miscible nucleating agent or a partial miscible nucleating agent having a greater vapor pressure than the liquid refrigerant to promote ebullition so that the liquid refrigerant evaporates even more quickly and smoothly, while preventing the liquid refrigerant from super-cooling and thereby decreasing the adsorption rate in the sorbent layer 23.
- Suitable nucleating agents include ethyl alcohol, acetone, methyl alcohol, isopropyl alcohol and isobutyl alcohol, all of which are miscible with water.
- a combination of a nucleating agent with a compatible liquid might be a combination of 5% ethyl alcohol in water or 5% acetone in methyl alcohol.
- the nucleating agent preferably has a vapor pressure at 25°C of at least about 25 mm Hg, and, more preferably, at least about 35 mm Hg.
- a solid nucleating agent may be used, such as a conventional boiling stone used in chemical laboratory applications.
- FIGS. 4 A through 4H illustrate flexible pouch containers which may contain a beverage, with a cooling device attached to, or integrated into, one or more side walls.
- FIG. 4 A shows the panels used to form a juice pouch without a bottom
- FIG. 4B shows the components to construct a juice pouch with a substantially flat bottom.
- the side panels and bottom panel are heat sealed at the edges to form the pouch containers (FIGS. 4C and 4D).
- FIG. 4C illustrates a partially cutaway side view of a flexible pouch beverage container with a single cooling device according to FIG. 2A, integrated into a side panel.
- FIG. 4D illustrates a flexible pouch beverage container with multiple cooling devices integrated into the side panels.
- the cover 12 of the casing 11 is extended to form all, or a portion, of the panel being used to construct the beverage container.
- FIGS. 4E and 4G are shown alternate embodiments of the flexible pouch beverage containers with integrated cooling devices.
- a casing such as that shown in FIG. 1H is integrated into the wall panels by the cover 12.
- the edges of the cover which form the side panel may be heat sealed to another side panel and the bottom panel is also heat sealed to the bottom edges forming the beverage containers shown in FIGS. 4C and 4D.
- the cooling device is in the form of the casing shown in FIG. 1H which provides single actuation for both cooling devices 11a from one common liquid reservoir l ib.
- the liquid reservoir 1 lb may be positioned on the side of the beverage container (FIG. 4H) on the top FIG. 4F.
- FIGS. 5 A through 5D show a box-type beverage container such as an asepic box folded from a single blank to which one or more cooling devices may be attached.
- a cooling device is attached to opposite side walls with each cooling device with its own actuator, in a casing akin to that shown in FIG. 1G.
- FIG. 5B and 5D there is a common liquid reservoir l ib, thereby both devices may be initiated at once, one on each side wall in a casing configuration similar to that of FIG. 1H.
- a weakened region may be formed in the box to allow for a straw to pierce there through.
- Embodiments of the cooling device decrease the temperature of a beverage in a beverage container by at least about 12 °C and in some embodiments at least 15 °C or even 20 °C after actuation.
- the liquid refrigerant reservoir contains less than 1.5 grams of liquid refrigerant per fluid ounce of beverage in the container.
- the refrigerant liquid is water.
- the sorbent section has a mass of less than 3 grams of sorbent per fluid ounce of beverage.
- the cooling device may decrease the beverage temperature in 10 minutes, or only 5 minutes, or even only 3 minutes.
- the sorbent section occupies less than 5 cubic centimeters per fluid ounce of beverage, and the cooling device occupies less than 0.5 fluid ounces per fluid ounce of a beverage in a beverage container.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Packages (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IL15860501A IL158605A0 (en) | 2001-04-25 | 2001-10-16 | Method of manufacturing a multi-layered sorbent-driven self-cooling device |
CA002445525A CA2445525A1 (en) | 2001-04-25 | 2001-10-16 | Method of manufacturing a multi-layered sorbent-driven self-cooling device |
JP2002585868A JP3989011B2 (en) | 2001-04-25 | 2001-10-16 | Method for manufacturing self-cooling device using multilayer adsorbent as power source |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US84429401A | 2001-04-25 | 2001-04-25 | |
US09/844,294 | 2001-04-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002088608A1 true WO2002088608A1 (en) | 2002-11-07 |
Family
ID=25292310
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2001/050705 WO2002088608A1 (en) | 2001-04-25 | 2001-10-16 | Method of manufacturing a multi-layered sorbent-driven self-cooling device |
Country Status (4)
Country | Link |
---|---|
JP (1) | JP3989011B2 (en) |
CA (1) | CA2445525A1 (en) |
IL (1) | IL158605A0 (en) |
WO (1) | WO2002088608A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2346111A1 (en) * | 2010-01-07 | 2011-07-20 | Siemens Aktiengesellschaft | Electrochemical energy storage device, in particular lithium-ion energy storage device |
EP3150947A1 (en) * | 2015-09-29 | 2017-04-05 | Rüdiger Passehl | Cooling stick, self-cooling vessel, and process of manufacture |
Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3683889A (en) * | 1969-09-16 | 1972-08-15 | Viktoria Hoffman | Heating container |
US3763622A (en) * | 1972-09-18 | 1973-10-09 | Kay Laboratories Inc | Method of making a pack for absorbing or adding heat |
US3887346A (en) * | 1971-09-07 | 1975-06-03 | Lynn Ellynn Erdman | Chemical thermal package with three separate chambers |
US4911740A (en) * | 1988-08-02 | 1990-03-27 | Schieder Hans B | Pressure responsive valve in a temperature changing device |
US4928495A (en) | 1989-06-22 | 1990-05-29 | Israel Siegel | Self cooling and self heating container |
EP0918198A2 (en) * | 1997-11-26 | 1999-05-26 | The BOC Group plc | Fluid chilling apparatus |
WO1999037958A1 (en) * | 1998-01-24 | 1999-07-29 | The University Of Nottingham | Heat transfer device |
US6151911A (en) | 1998-01-24 | 2000-11-28 | Bass Public Limited Company | Relating to cooling containers of beverages |
WO2001010738A1 (en) * | 1999-08-04 | 2001-02-15 | Crown Cork & Seal Technologies Corporation | Self-cooling can |
WO2002040929A2 (en) * | 2000-10-18 | 2002-05-23 | Thermal Product Developments, Inc. | Evacuated sorbent assembly and cooling device |
-
2001
- 2001-10-16 WO PCT/US2001/050705 patent/WO2002088608A1/en active Application Filing
- 2001-10-16 JP JP2002585868A patent/JP3989011B2/en not_active Expired - Fee Related
- 2001-10-16 CA CA002445525A patent/CA2445525A1/en not_active Abandoned
- 2001-10-16 IL IL15860501A patent/IL158605A0/en unknown
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3683889A (en) * | 1969-09-16 | 1972-08-15 | Viktoria Hoffman | Heating container |
US3887346A (en) * | 1971-09-07 | 1975-06-03 | Lynn Ellynn Erdman | Chemical thermal package with three separate chambers |
US3763622A (en) * | 1972-09-18 | 1973-10-09 | Kay Laboratories Inc | Method of making a pack for absorbing or adding heat |
US4911740A (en) * | 1988-08-02 | 1990-03-27 | Schieder Hans B | Pressure responsive valve in a temperature changing device |
US4928495A (en) | 1989-06-22 | 1990-05-29 | Israel Siegel | Self cooling and self heating container |
EP0918198A2 (en) * | 1997-11-26 | 1999-05-26 | The BOC Group plc | Fluid chilling apparatus |
WO1999037958A1 (en) * | 1998-01-24 | 1999-07-29 | The University Of Nottingham | Heat transfer device |
US6151911A (en) | 1998-01-24 | 2000-11-28 | Bass Public Limited Company | Relating to cooling containers of beverages |
WO2001010738A1 (en) * | 1999-08-04 | 2001-02-15 | Crown Cork & Seal Technologies Corporation | Self-cooling can |
WO2002040929A2 (en) * | 2000-10-18 | 2002-05-23 | Thermal Product Developments, Inc. | Evacuated sorbent assembly and cooling device |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2346111A1 (en) * | 2010-01-07 | 2011-07-20 | Siemens Aktiengesellschaft | Electrochemical energy storage device, in particular lithium-ion energy storage device |
EP3150947A1 (en) * | 2015-09-29 | 2017-04-05 | Rüdiger Passehl | Cooling stick, self-cooling vessel, and process of manufacture |
Also Published As
Publication number | Publication date |
---|---|
JP2004525334A (en) | 2004-08-19 |
CA2445525A1 (en) | 2002-11-07 |
JP3989011B2 (en) | 2007-10-10 |
IL158605A0 (en) | 2004-05-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6474100B1 (en) | Evacuated sorbent assembly and cooling device | |
US6532762B2 (en) | Refrigeration cooling device with a solid sorbent | |
US6701724B2 (en) | Sorption cooling devices | |
US6584797B1 (en) | Temperature-controlled shipping container and method for using same | |
US7726139B2 (en) | Cooling sorption element with gas-impermeable sheeting | |
US4928495A (en) | Self cooling and self heating container | |
US4911740A (en) | Pressure responsive valve in a temperature changing device | |
US20110151740A1 (en) | Wrapper for refrigerating material and refrigerating device using this wrapper | |
US8074470B2 (en) | Sorption cooling element with regulator organ and additional heat source | |
WO2002088608A1 (en) | Method of manufacturing a multi-layered sorbent-driven self-cooling device | |
US20090114378A1 (en) | Heat exchanger and tempering container comprising a heat exchanger | |
EP1328763B1 (en) | Evacuated sorbent assembly and cooling device | |
AU623220B2 (en) | Vacuum insulated sorbent-driven refrigeration device | |
AU2002239784A1 (en) | Evacuated sorbent assembly and cooling device | |
CA2362571C (en) | Preparation of refrigerant materials | |
US6843071B1 (en) | Preparation of refrigerant materials |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PH PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG UZ VN YU ZA ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2445525 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: PA/A/2003/009799 Country of ref document: MX |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1020037014025 Country of ref document: KR |
|
WWE | Wipo information: entry into national phase |
Ref document number: 158605 Country of ref document: IL |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2002585868 Country of ref document: JP |
|
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
32PN | Ep: public notification in the ep bulletin as address of the adressee cannot be established |
Free format text: NOTING OF LOSS OF RIGHTS PURSUANT TO RULE 69(1) EPC (EPO FORM 1205 DATED 27.05.2004) |
|
122 | Ep: pct application non-entry in european phase |