Systems and methods for vacuum cooling a beverage
US-2016348962-A1 · Dec 1, 2016 · US
US10539344B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10539344-B2 |
| Application number | US-201515516295-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 8, 2015 |
| Priority date | Oct 15, 2014 |
| Publication date | Jan 21, 2020 |
| Grant date | Jan 21, 2020 |
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An adsorber includes: a closed container in which an adsorption medium is included; an adsorption part that is provided in the closed container and includes an adsorbent, which adsorbs and desorbs the adsorption medium; and an evaporation/condensation part that is provided in the closed container and that exchanges heat between the adsorption medium and a heat exchanging medium, which is supplied from outside of the closed container, to evaporate and condense the adsorption medium. The evaporation/condensation part includes a heat transfer part that transfers heat of the heat exchanging medium to the adsorption medium. The heat transfer part is capable of holding the adsorption medium, an amount of which is capable of being adsorbed by the adsorbent of the adsorption part.
Opening claim text (preview).
The invention claimed is: 1. An adsorber comprising: a closed container in which an adsorption medium is included; an adsorptioner that is provided in the closed container and includes an adsorbent, which adsorbs and desorbs the adsorption medium; and an evaporator/condenser that is provided in the closed container and that exchanges heat between the adsorption medium and a heat exchanging medium, which is supplied from outside of the closed container, to evaporate and condense the adsorption medium, wherein: the evaporator/condenser includes a heat transfer surface that transfers heat of the heat exchanging medium to the adsorption medium; the heat transfer surface is capable of holding the adsorption medium, an amount of which is capable of being adsorbed by the adsorbent of the adsorptioner; the heat transfer surface is a porous heat transfer body; the porous heat transfer body is formed of a metal fiber; and a clearance corresponding diameter of the heat transfer surface is within a range from 7 to 260 μm, and is expressed by a mathematical formula 1: (clearance corresponding diameter)= d·{ 3π/(4(1−Φ))−1}, where: d is a line diameter, which is a framework diameter of the porous heat transfer body; and Φ is a porosity of the porous heat transfer body. 2. The adsorber according to claim 1 , wherein the amount of the adsorption medium that the heat transfer surface is capable of holding is set to be equal to or smaller than a capacity of the adsorptioner to adsorb the adsorption medium. 3. The adsorber according to claim 1 , wherein the heat transfer surface is made of sintered metal or foam metal. 4. The adsorber according to claim 1 , wherein the adsorptioner includes a heat transfer surface for adsorption that is a porous body having the same configuration as the heat transfer surface of the evaporator/condenser, the adsorbent provided for the porous body. 5. The adsorber according to claim 1 , wherein the clearance corresponding diameter of the heat transfer surface is within a range from 7 to 140 μm. 6. An adsorber comprising: a closed container in which an adsorption medium is included; an adsorptioner that is provided in the closed container and includes an adsorbent, which adsorbs and desorbs the adsorption medium; and an evaporator/condenser that is provided in the closed container and that exchanges heat between the adsorption medium and a heat exchanging medium, which is supplied from outside of the closed container, to evaporate and condense the adsorption medium, wherein: the evaporator/condenser includes a heat transfer surface that transfers heat of the heat exchanging medium to the adsorption medium; the heat transfer surface is capable of holding the adsorption medium, an amount of which is capable of being adsorbed by the adsorbent of the adsorptioner; the heat transfer surface is a porous heat transfer body, and a relationship of a first passage space<a second passage space<a third passage space is satisfied where: the first passage space is a space of a first passage formed by a plurality of clearances formed in the heat transfer surface; the second passage space is a space of a second passage, wherein the adsorption medium, which has flowed through the first passage, flows through the second passage immediately after the first passage; and the third passage space is a space of a third passage, wherein the adsorption medium, which has flowed through the second passage, flows through the third passage immediately after the second passage. 7. The adsorber according to claim 1 , wherein the heat transfer surface of the evaporator/condenser is in contact with a bottom surface of the closed container. 8. The adsorber according to claim 1 , further comprising a pan that is provided vertically below the heat transfer surface of the evaporator/condenser to be in contact with the heat transfer surface. 9. The adsorber according to claim 1 , wherein the porous heat transfer body is constructed of a sintered metal made by heating metal fibers and by bonding the metal fibers without melting them into a dendrite shape tangled together to form a void therebetween. 10. The adsorber according to claim 6 , wherein each one of the plurality of clearances formed in the heat transfer surface is diamond shaped.
using a solid as sorbent · CPC title
the absorbent or adsorbent being a solid, e.g. salt (F25B17/12 takes precedence) · CPC title
for absorption-type refrigeration systems · CPC title
Absorbers; Adsorbers (boiler-absorbers F25B35/00) · CPC title
with two or more boiler-sorber/evaporator units · CPC title
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