Humidification and dehymidification process and apparatus for chilling beverages and other food products and process of manufacture
11898796 ยท 2024-02-13
Inventors
Cpc classification
F25D5/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25D5/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
Abstract
A novel self-cooling food product container apparatus (10) and a process for manufacturing the same is disclosed. A self-cooling food product container (20) combined with a substantive vapor transport system producing a humidification cooling process for cooling food and beverage products P. Methods of assembling and operating the apparatus (10) are also provided.
Claims
1. A cooling apparatus, comprising: a container having a container wall and being surrounded by atmospheric pressure; a first chamber containing granulated endothermic chemicals with interstitial spaces filled with a dry gas having a dew point temperature range 10 F. to 150 F. for a humidification liquid at said A DRY GAS pressure greater than atmospheric pressure; and a second chamber within said container and being filled with said humidification liquid that is removed from said dry gas at said dew point temperature range; separated from said first chamber by a barrier material insoluble in said humidification liquid, an interconnection structure interconnecting said first chamber and said second chamber, said interconnection structure containing barrier material insoluble in said humidification liquid and internally abutting and initially sealing said interconnection structure; such that when said container is opened and said container interior is exposed to atmospheric pressure, said dry gas pressure expands said interconnection structure collapsible wall away from said barrier material and exposes said humidification liquid vapor to said dry gas and said dry gas absorbs said humidification liquid vapor forming a vacuum within said second chamber; and said vacuum collapses said collapsible wall into a minimal volume by absorption of said humidification liquid in to said interstitial spaces causing a first cooling of said apparatus collapsible walls; and said endothermic compounds react with said humidification liquid to cause a second endothermic cooling of said apparatus collapsible walls and said first and second cooling cools any medium surrounding said collapsible walls.
2. The apparatus of claim 1, wherein said at least one endothermic reaction compound is a dry gas contained within said first chamber.
3. The apparatus of claim 2, wherein the endothermic reaction compound comprises at least one of potassium nitrate, potassium chloride and urea.
4. The apparatus of claim 1, wherein said barrier material comprises a plastic material.
5. The apparatus of claim 1, wherein said medium surrounding said collapsible walls is a beverage.
6. The apparatus of claim 1, wherein said humidification liquid comprises dimethylether.
7. The apparatus of claim 1, wherein said humidification liquid comprises SOLSTICE L41y (R-452B), SOLSTICE 452A (R-452A), SOLSTICE L40X (R-455A), SOLSTICE zd, SOLSTICE ze (R-1234ze), SOLSTICE yf (R-1234YF).
8. A self-cooling beverage container apparatus, comprising: a beverage container surrounded by atmospheric pressure and having a container wall and a container opening mechanism and a carbonated beverage contained within said container and producing a carbonation pressure which increases container internal pressure above atmospheric pressure subsequent to assembly of said container, filling of said container with said carbonated beverage and sealing of said container; a cooling assembly at least partly submerged in said carbonated beverage and comprising a cooling assembly vessel with a collapsible volume and having a vessel wall and a vessel first region and a vessel second region; a compressible plug member formed of a plug member material which lacks resilience to return to its initial cross-section area after being compressed and has a plug member initial cross-sectional area when said container is sealed and is contained within said vessel and abuts a plug member abutment portion of said vessel wall which is compressible and has resilience to return at least partly to its initial cross-sectional area after having been compressed and said plug member abutment portion defining an interconnection structure comprising said plug abutment portion, separating said vessel into said first vessel first region defining a humidification liquid chamber having a humidification liquid chamber wall and a humidification liquid contained within said humidification liquid chamber and the vessel second region defining a dry gas chamber having a dry gas chamber wall, and at least one endothermic reaction compound contained within said dry gas chamber, wherein said interconnection structure fluidly interconnects said humidification liquid chamber and said dry gas chamber; said plug member abutment portion having a plug member abutment portion initial cross-sectional area and the interconnection structure having an interconnection structure initial cross-sectional area at atmospheric pressure prior to container assembly and sealing, and being compressed to a plug member abutment portion compressed cross-sectional area by a subsequent increase in container internal pressure to carbonation pressure subsequent to container assembly and sealing which is less than the interconnection structure initial cross-sectional area, thereby compressing the plug member initial cross-sectional area to a plug member compressed cross-sectional area, such that the plug member compressed cross-sectional area and shape matches the plug member abutment portion compressed cross-sectional area and shape and circumferentially abuts said plug member abutment portion, thereby maintaining its sealing of said interconnection structure against the passage of fluid; such that operating said container opening mechanism and thereby opening said container to the surrounding atmosphere causes a decrease in the container internal pressure bearing upon said plug member abutment portion from the carbonation pressure to atmospheric pressure, permitting said plug member abutment portion to resiliently expand relative to said plug member to a plug member abutment portion expanded cross-sectional area, creating space between said plug member and said plug member abutment portion and thereby opening fluid communication between said humidification liquid chamber and said dry gas chamber through said interconnection structure, causing said humidification liquid to mix and react with said at least one endothermic reaction compound endothermically, extracting heat from said beverage, and thereby cooling said beverage.
9. The apparatus of claim 1, wherein said at least one endothermic reaction compound is a dry gas contained within said first chamber.
10. The apparatus of claim 1, wherein said medium surrounding said collapsible walls is a beverage.
11. A cooling apparatus with a collapsible walls subjected to a pressure greater than atmospheric pressure and forming a first chamber and a second chamber within said apparatus; said first chamber containing granulated endothermic chemicals with interstitial spaces filled with a dry gas having a dew point temperature range 10 F. to 150 F. fora humidification liquid at said pressure greater than atmospheric pressure; said second chamber separated from said first chamber by a barrier material insoluble in said humidification liquid; said second chamber filled with said humidification liquid that is removed from said dry gas at said dew point temperature range; such that when the apparatus is exposed to atmospheric pressure, said dry gas expands away from said barrier material and exposes said humidification liquid vapor to said dry gas and said dry gas absorbs said humidification liquid vapor forming a vacuum with said apparatus; and said vacuum collapses said collapsible walls into a minimal volume by absorption of said humidification liquid in to said interstitial spaces causing a first cooling of said apparatus collapsible walls; and said endothermic compounds react with said humidification liquid to cause a second endothermic cooling of said apparatus collapsible walls and said first and second cooling cools any medium surrounding said collapsible walls.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) Various other objects, advantages, and features of the invention will become apparent to those skilled in the art from the following discussion taken in conjunction with the following drawings representing the preferred embodiments of the invention, in which:
(2)
(3)
(4)
(5)
(6)
(7)
(8)
(9)
(10)
(11)
(12)
(13)
(14)
(15)
(16)
(17)
(18)
(19)
(20)
(21)
(22)
DETAILED DESCRIPTION OF THE INVENTION
(23) As required, detailed embodiments of the present invention are disclosed herein; however, it is to be understood that the disclosed embodiments are merely exemplary of the invention which may be embodied in various forms. Therefore, specific structural and functional details disclosed herein are not to be interpreted as limiting, but merely as a basis for the claims and as a representative basis for teaching one skilled in the art to variously employ the present invention in virtually any appropriately detailed structure.
(24) Reference is now made to the drawings, wherein like characteristics and features of the present invention shown in the various FIGURES are designated by the same reference numerals.
(25) For orientation purposes and clarity, the food product container is assumed to be standing in a vertical orientation and thus in its normal placement orientation. This invention uses the thermodynamic potential of the evaporation of a humidification liquid, such as water or other suitable liquid, and the ability of a substantially low vapor pressure medium such as a dry gas DG to force this evaporation from even cold liquids.
Method of Manufacture of the First Embodiment of the Present Invention
(26) A first embodiment of the invention is shown in
(27) In one preferred method of manufacture of the first embodiment, a humidification liquid chamber 104, a dry gas chamber 106 and the interconnection structure 107 are provided in the form of a contiguous flexible and collapsible structure such as a lay-flat tubing preferably in the form of metalized lay-flat tubing 105. A lay-flat-tube 105, preferably with an expanded diameter of about 2-3 inches and about 8-12 inches long, is first provided with open ends. In one embodiment as shown in
(28) As shown in
(29) As shown in
(30) The next step in manufacturing the apparatus 10 is filling the dry gas chamber 106 with granular forms of the endothermically reacting chemical compounds R through its open unsealed end. The endothermically reacting chemical compounds R should be made to fill and contact the maximum possible surface area of the dry gas chamber walls 110. Of course, while the surface area of the dry gas chamber 106 is fixed by the lay-flat tubing 105 material area available to form the dry gas chamber 106, the volume of the dry gas chamber 106 depends on the extent to which the lay-flat tubing 105 that forms the dry gas chamber 106 is expanded. Advantageously any volume between the maximum expanded volume and the minimum lay-flat volume of the two chambers can be accommodated in the same surface area of the dry gas chamber 106.
(31) A further step is making a cooling assembly 100 of the invention is to fill the interconnection structure 107 between the humidification liquid chamber 104 and the dry gas chamber 106 with a compressible plug member 108. The compressible plug member 108 is preferably made from a suitable deformable material, one of non-resilient and only partially resilient material such as a non-water-soluble wax, a rubber, cork, closed foam, a plastic, and a putty. In
(32) The compressible plug member 108 is placed to sealingly fill either a portion or the entire interconnection structure 107 to separate the dry gas chamber 106 from the humidification liquid chamber 104. The compressible plug member 108 can also be made as one of a deformable metal and plastic disc such that the disc can irreversibly deform in cross-section when compressed by beverage pressure acting against the interconnection structure 107. Thus the compressible plug member 108 is made from materials that fluidly seal and separate the humidification liquid chamber 104 from the dry gas chamber 106. The interconnection structure 107 sealingly connects the dry gas chamber wall 110 to the humidification liquid chamber wall 109. Both the dry gas chamber 106 and the humidification liquid chamber 104 can also be made as separate bags connected sealingly to the ends of the interconnection structure 107 by means of thermal welding. As shown in
(33) Alternatively, the narrowing of the lay-flat tubing 105 to form a narrow neck for a smaller interconnection structure 107 is only necessary if the amount of material used to form the compressible plug member 108 needs to be reduced to minimize its thermal penalty on the cooling capacity of the apparatus 10. The cooling assembly 100 may also be formed from a single unaltered tube material as shown in
(34) If lay-flat tubing 105 material that is used to form the cooling assembly 100 is too thin, i.e., in the order of magnitude of thickness less than 1 mil, a supporting flexible rubber tube segment may be added to form the interconnection structure 107 to permit the interconnection structure 107 to be compressible by carbonation pressure P to a smaller cross-sectional area, and also to permit the interconnection structure 107 to bounce back to its original shape when the pressure is released, using the rubber material's elasticity. Thus, the interconnection structure 107 may be made as a separate segment of the cooling assembly 100 as shown in
(35) The next step in manufacturing the apparatus 10 is filling the dry gas chamber 106 with granular particles of the endothermically reacting chemical compounds R through its open unsealed end. The endothermically reacting chemical compounds R should be made to fill and contact the maximum possible surface area of the dry gas chamber wall 109. Of course, while the surface area of the dry gas chamber wall 109 is fixed by the lay-flat tubing 105 material's available area, the volume of the dry gas chamber 106 depends on the extent to which the lay-flat tubing 105 forming the dry gas chamber 106 can be expanded. Advantageously, both the dry gas chamber 106 and the humidification liquid chamber 104 can have any volume between the maximum expanded cylindrical volume of lay-flat tubing 105, and the minimum lay-flat volume of lay-flat tubing 105, while both chambers maintain a constant surface area respectively.
(36) The next step is to flood the dry gas chamber 106 with a dry gas DG, preferably one of dry CO.sub.2, dry dimethyl ether (DME), and one or combinations of DME, CO.sub.2, Solstice L41y (R-452B), Solstice 452A (R-452A), Solstice L40X (R-455A), Solstice zd, Solstice ze, (R-1234ze), and Solstice yf (R-1234y). The dry gas DG is filled by simply blowing it at a low flow rate through the granules of the endothermically reacting chemical compounds R to replace any air that fills the interstitial spaces between the granules of the endothermically reacting chemical compounds R. The next step is to thermally seal the dry gas chamber 106 by heat sealing the open end of the dry gas chamber 106 to form a sealed chamber.
(37) If the amount of dry gas DG needed exceeds the pressure rating of the dry gas chamber 106, a simple remedy is shown in
(38) The next step in the assembly of the apparatus 10 is to fill the humidification liquid chamber 104 with humidification liquid HL. The humidification liquid HL must be chosen to react endothermically with the endothermically reacting chemical compounds R and to also evaporate when subjected to the dry gas DG. Preferably, the humidification liquid HL is water. The humidification liquid HL should contact the maximum possible surface area of the humidification liquid chamber 104 that is available. Of course while the surface area of the dry gas chamber 106 is fixed by the lay-flat tubing 105 material, the volume of the humidification liquid chamber 104 depends on the extent to which the lay-flat tubing 105 that forms the humidification liquid chamber 104 can be expanded. Advantageously any volume between the maximum expanded volume and the minimum lay-flat volume of the two chambers can be accommodated. The next step is to thermally seal the humidification liquid chamber 104 by heat sealing its open end to form a closed humidification liquid chamber 104.
(39) A standard beverage container 20 is provided in the form of a conventional metal can or in the form of a plastic bottle. The cooling assembly 100 comprising the humidification liquid chamber 104, the dry gas chamber 106 and chamber contents, and the interconnection structure 107 with the compressible plug member 108 separating the two, is then inserted into the beverage container 20. Carbonated beverage B is then filled into the beverage container 20 by conventional means. A beverage container lid 102 with a beverage container opening means 103 is provided for sealing off the beverage with the cooling assembly 100 to form the apparatus 10 according to the first embodiment.
(40) When the beverage container 20 is sealed off by the beverage container lid 102, carbonation pressure P builds up. The carbonation pressure P of the beverage B compresses the humidification liquid chamber 104 and the dry gas chamber 106 and the interconnection structure 107 until the internal pressure of the humidification liquid chamber 104 and the dry gas chamber 106 equals the carbonation pressure P. The carbonation pressure P also deforms the interconnection structure 107 and compresses the interconnection structure 107 and the compressible plug member 108 to a smaller cross-sectional area than their starting cross-sectional areas while the compressible plug member 108 still remains in a sealing configuration. The apparatus 10 is now ready for use.
Method of Operation of the First Embodiment of the Invention
(41) Upon opening the beverage container opening means 103, the change in the container 20's internal carbonation pressure P to atmospheric pressure, causes the interconnection structure 107 to substantially expand preferably back to its original state, leaving the compressed compressible plug member 108 at a smaller cross-sectional area. The difference in dimensions between the final compressed state of the compressible plug member 108 and the starting uncompressed state of the compressible plug member 108 forms a gap that permits fluid communication between the dry gas chamber 106 and the humidification liquid chamber 104. The stages of compression and area reductions are shown in
Method of Manufacture of the Second Embodiment of the Present Invention
(42) A second embodiment of the invention is shown in
(43) The first step in forming a cooling assembly 100 of the present invention is to prepare a preform to form the two chambers and the interconnection structure 107 as a single or multiple stretch-blown plastic pieces, preferably as thin-walled structures with flexible walls. The humidification liquid chamber 104 is preferably a bellows-shaped structure, while the dry gas chamber 106 is preferably a cylindrically-shaped structure, and the interconnection structure 107 is preferably a small tube connecting the two chambers respectively. Preferably, a plastic material such as one of PET, PVC, Polyethylene, and Polycarbonate, is used for this example. The material used preferably is made from substantially impervious plastic materials that prevent to a great extent beverage and carbonation from passing through its walls.
(44) The second step in the making of the cooling assembly 100 of the apparatus 10 is to fill the humidification liquid chamber 104 (the bellows) with humidification liquid HL through the blow spout 120. The humidification liquid HL must be chosen to react endothermically with the endothermically reacting chemical compounds R and to also evaporate when subjected to the dry gas DG. Preferably, the humidification liquid HL is water. Of course while the surface area of the dry gas chamber 106 is preferably substantially fixed as a cylinder, the volume of the humidification liquid chamber 104 depends on the extent to which its bellows shape can be expanded and contracted. Advantageously, any volume between the maximum expanded volume of the humidification liquid chamber 104 and the minimum possible contracted volume of the bellows can be accommodated.
(45) The third step in making cooling assembly 100, according to the second embodiment of the invention, is to fill the interconnection structure 107 between the humidification liquid chamber 104 and the dry gas chamber 106 with a compressible plug member 108. The compressible plug member 108 is preferably made from a suitable deformable material, one of non-resilient and only partially resilient material such as a non-water-soluble wax, a rubber, cork, closed foam, a plastic, and a putty. The compressible plug member 108 is passed through the blow spout 120 and placed to sealingly fill either a portion or the entire interconnection structure 107 to separate the dry gas chamber 106 from the humidification liquid chamber 104. The compressible plug member 108 also can be made as a deformable metal disc and as a deformable metal cylinder such that it irreversibly or only partially reversibly deforms in cross-sectional area under beverage carbonation pressure, P. Thus, the compressible plug member 108 fluidly seals and separates the humidification liquid chamber 104 from the dry gas chamber 106. The interconnection structure 107 sealingly connects to the dry gas chamber 106 and to the humidification liquid chamber 104. The compressible plug member 108, if made from a wax, can be simply melted and poured to fill the interconnection structure 107. Since a wax floats on water, for example, it is possible to fill the water in the humidification liquid chamber 104 up to the start of the interconnection structure 107 and then pour molten wax to float above the humidification liquid HL and fill the interconnection structure 107.
(46) The next step in manufacturing the apparatus 10 according to the second embodiment is filling the dry gas chamber 106 with granular forms of the endothermically reacting chemical compounds R through its open unsealed blow spout 120. The endothermically reacting chemical compounds R should be made to fill and contact the maximum possible surface area of the dry gas chamber walls 109.
(47) The next step is to flood the dry gas chamber 106 through the blow spout 120, with a substantially dry gas DG, preferably one of CO.sub.2, dimethyl ether (DME), and one or combinations of DME, CO.sub.2, Solstice L41 y (R-452B), Solstice 452A (R-452A), Solstice L40X (R-455A), Solstice zd, Solstice ze, (R-1234ze), and Solstice yf (R-1234yf). The dry gas DG is filled by simply blowing it at a low flow rate through blow spout 120 into the granules of the endothermically reacting chemical compounds R to replace any air that fills the interstitial spaces between the granules of the endothermically reacting chemical compounds R. The next step is to thermally seal the dry gas chamber 106 by heat sealing the open end of the blow spout 120 to form a closed dry gas chamber 106 and to form the completed cooling assembly 100, as shown in
(48) A standard beverage container 20 preferably is provided in the form of a conventional metal can or in the form of a plastic bottle. The cooling assembly 100, comprising the humidification liquid chamber 104, the dry gas chamber 106 and the interconnection structure 107 with the compressible plug member 108 separating the two, is then inserted into the beverage container 20. Carbonated beverage B is then filled into the beverage container 20 by conventional means. A beverage container lid 102 with a beverage container opening means 103 is provided for sealing off the beverage container 20 with the cooling assembly 100 inside to form the apparatus 10 according to the second embodiment.
(49) When the beverage container 20 is sealed off by the beverage container lid 102, carbonation pressure P builds up. The carbonation pressure P of the beverage compresses the humidification liquid chamber 104 and the dry gas chamber 106 and the interconnection structure 107 until the internal pressure of the humidification liquid chamber 104 and the internal pressure dry gas chamber 106 and the internal pressure of the interconnection structure equal the carbonation pressure P. The carbonation pressure P also deforms the interconnection structure 107 and compresses the interconnection structure 107 and the compressible plug member 108 to a substantially smaller cross-sectional area than its starting cross-sectional area, while the compressible plug member 108 still remains in a sealing configuration. The apparatus 10 is now ready for use.
Method of Operation of the Second Embodiment of the Invention
(50) Upon opening the beverage container opening means 103, the change in internal pressure within the beverage container 20, from carbonation pressure P to atmospheric pressure P.sub.a, causes the interconnection structure 107 to substantially expand back preferably to its cross-sectional area, leaving the compressed compressible plug member 108 at the smaller cross-sectional area than the expanded cross-sectional area of the interconnection structure 107. The difference in dimensions between the final compressed state of the compressible plug member 108 and the starting uncompressed state of the compressible plug member 108 forms a gap that permits fluid communication between the dry gas chamber 106 and the humidification liquid chamber 104. The stages of compression and area reductions are shown in
Method of Manufacture of the Third Embodiment of the Present Invention
(51) A third embodiment of the invention is shown in
(52) A thin cylindrical-walled humidification liquid chamber 104 is provided. Humidification liquid chamber 104 is configured as a cylindrical cup with a tubular cup side wall 104c with a cup open end 104a and a cup end wall 104b opposing the cup open end 104a. Humidification liquid HL such as water is held within the humidification liquid chamber 104 and a compressible plug member 108 preferably made from a suitable irreversibly deformable material which is one of non-resilient and only partially resilient material such as deformable wax, rubber, and plastic, is placed to seal off the humidification liquid chamber 104 open end and fluidly isolate the humidification liquid chamber 104. This can easily be achieved by filling the humidification liquid chamber 104 with water for example, heating the water, and melting a suitable wax over the water surface to form a wax sealing layer. When the wax dries, it forms a hermetic seal over the humidification liquid HL and seals off the open end of the humidification liquid chamber 104.
(53) Similarly, a dry gas chamber 106 is provided comprising a thin cylindrical-walled container having a tubular cup side wall 106c with a cup open end 106a and a cup end wall 106b opposing the cup open end 106a. The dry gas chamber 106 contains crystalline forms of endothermically reacting chemical compounds R such as potassium nitrate, potassium chloride and urea. Dry gas DG is flowed into the dry gas chamber 106 to fill the interstitial spaces between the crystals of the endothermically reacting chemical compounds R. When the humidification chamber 104 is slid into the dry gas chamber 106, the interconnection structure 107 is placed over the assembly not only to hold the two chambers in place and to snugly and frictionally and sealingly connect them but also to prevent them from sliding apart. Alternatively, compressible plug member 108 may be filled into the interconnection structure 107 to abut and seal against the interconnection structure 107, to separate the dry gas chamber 106 and the humidification liquid chamber 104.
(54) It is also important that the dry gas DG be chilled to a temperature to prevent fast pressure build up that can drive apart and separate the two chambers before the beverage container 20 is sealed off with the beverage container lid 102. The internal pressure of the dry gas DG will build up until it also equilibrates with the beverage carbonation pressure P. As such, the pressure of the dry gas DG as it heats up to room temperature and gasifies cannot exceed the carbonation pressure P. The carbonation pressure P compresses the interconnection structure 107, and this compresses the compressible plug member 108 to a smaller diameter than its starting diameter while remaining in a sealing configuration.
(55) The interconnection structure 107 preferably is made in the form of one of a plastic sleeve and a rubber sleeve, to tightly and slidingly seal off the open ends of the dry gas chamber 106 and the humidification liquid chamber 104. The dry gas chamber open end 106a is made to snugly and sealingly slide over the side wall and the end wall of the humidification liquid chamber wall 110. Thus, when the humidification liquid chamber 104 is sealingly slid into the dry gas chamber 106, the reduced combined volume of the two chambers will substantially and preferably be made to equal to the volume of the dry gas chamber 106 only. The entire cooling assembly 100 can be left to just float inside the beverage container 20 in the beverage B, and alternatively the cooling assembly 100 also may be affixed to the beverage container inner wall 20a at any place or orientation.
(56) When the beverage container 20 is filled and sealed off as before by the beverage container lid 102, carbonation pressure P builds up internally within the beverage container 20. The carbonation pressure P compresses the interconnection structure 107, which compresses around the compressible plug member 108 until the internal pressure of the humidification liquid chamber 104 and the dry gas chamber 106 equals the carbonation pressure P. The cross-sectional area of the compressible plug member 108 in turn reduces due to carbonation pressure P compression.
Method of Use of the Third Embodiment of the Present Invention
(57) Upon opening the beverage container opening means 103, the change in container 20's internal carbonation pressure P to atmospheric pressure P.sub.a, causes the interconnection structure 107 to relax its pressure compression grip that is transmitted to the compressible plug member 108. The compressible plug member 108 remains in a deformed smaller cross-section and the difference in dimensions between the final compressed state of the compressible plug member 108 and the uncompressed state of the compressible plug member 108 permits fluid communication between the dry gas chamber 106 and the humidification liquid chamber 104, and the and the dry gas DG starts to absorb humidification liquid HL forming a vacuum V and pulling humidification liquid HL into the dry gas chamber 106. The humidification liquid chamber 104 is pulled further into the dry gas chamber 106 by the generated vacuum. Some humidification liquid HL vapor is evaporated during this process as well. The endothermically reacting chemical compounds R react with the humidification liquid HL and dissolve endothermically to cool the beverage B. The solvation causes a further reduction in volume of the dry gas chamber 106 and this causes more humidification liquid HL and humidification liquid vapor to be pulled into the dry gas chamber 106. Thus a complete dissolving of the endothermically reacting chemical compounds R occurs and cooling of the beverage B occurs. It is important that the surface areas of the humidification liquid chamber 104 and dry gas chamber 106 be maximized for best cooling.
(58) While the invention has been described, disclosed, illustrated and shown in various terms or certain embodiments or modifications which it has assumed in practice, the scope of the invention is not intended to be, nor should it be deemed to be, limited thereby and such other modifications or embodiments as may be suggested by the teachings herein are particularly reserved especially as they fall within the breadth and scope of the claims here appended.