Gas supply system
US-2015010839-A1 · Jan 8, 2015 · US
US10508771B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10508771-B2 |
| Application number | US-201715472928-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 29, 2017 |
| Priority date | Mar 30, 2016 |
| Publication date | Dec 17, 2019 |
| Grant date | Dec 17, 2019 |
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Official abstract text for this publication.
This invention relates to a novel method and system for dispensing CO2 vapor without over pressurization from a system having multiple containers. The system includes one or more liquid containers and one or more vapor containers. The system is designed to operate in a specific manner whereby a restricted amount of CO2 liquid is permitted into the vapor container through a restrictive pathway that is created and maintained by a shuttle valve during the filling operation so that equalization of container pressures is achieved, thereby allowing shuttle valve to reseat when filling has stopped. During use, a pressure differential device is designed to specifically isolate the vapor container from the liquid container so as to preferentially deplete liquid CO2 from the vapor container and avoid over pressurization of the system until the vapor container becomes liquid dry. The system can be operated so that at least 50% of the CO2 vapor product is dispensed from the vapor container.
Opening claim text (preview).
The invention claimed is: 1. A method for dispensing CO2 product to an end-user from an on-site carbon dioxide (CO2) multiple container system comprising a liquid CO2 container operatively connected with a vapor CO2 container, said method comprising the steps of: dispensing CO2 vapor substantially from the vapor CO2 container to the end-user; and depleting CO2 liquid from the vapor CO2 container, such that the dispensing of the CO2 vapor substantially from the vapor CO2 container to the end-user occurs until a pressure difference between the liquid CO2 container and the vapor CO2 container acquires a set point value; creating the pressure difference between the liquid CO2 container and the vapor CO2 container equal to the set point value, and in response thereto, creating a temporary flow path defined, at least in part, as an internal pathway of a reciprocating piston of a shuttle valve configured in an unbiased position, said internal pathway in fluid communication with a passageway through a pressure differential device activated into an open position when the pressure difference is equal to the set point value, said pressure differential device located downstream of the shuttle valve and upstream of the vapor CO2 container; and transferring the CO2 vapor and/or the CO2 liquid from the liquid CO2 container into the temporary created flow path followed by entry of the CO2 vapor and/or the CO2 liquid into the vapor CO2 container. 2. The method of claim 1 , wherein a weight ratio of the CO2 product dispensed from the vapor container to the CO2 product dispensed from the liquid container is approximately 1:1 or higher. 3. The method of claim 1 , further comprising consuming a greater amount by weight of CO2 vapor from the vapor CO2 container than the liquid CO2 container prior to a subsequent or successive refill of CO2 liquid into the liquid CO2 container or a transfer of CO2 fluid from the liquid CO2 container to the vapor CO2 container. 4. The method of claim 1 , further comprising the step of substantially avoiding accumulation of liquid CO2 in the vapor CO2 container after one or more subsequent or successive refills of the CO2 liquid into the liquid CO2 container or one or more transfers of the CO2 liquid from the liquid CO2 container to the vapor CO2 container. 5. The method of claim 1 , further comprising vaporizing at least 75 wt % of CO2 liquid in the vapor CO2 container prior to introducing CO2 liquid and/or CO2 vapor from the liquid CO2 container to the vapor CO2 container. 6. The method of claim 1 , wherein the pressure difference between the liquid CO2 container and the vapor CO2 container increases to the set point value that causes a transfer of CO2 fluid from the liquid CO2 container to the vapor CO2 container. 7. The method of claim 6 , further comprising the steps of: isolating the vapor CO2 container from the liquid CO2 container when the pressure difference between the liquid CO2 container and vapor CO2 container has decreased to below the set point value. 8. The method of claim 2 , wherein the weight ratio of the CO2 product dispensed from the vapor container to the CO2 product dispensed from the liquid container is approximately 1.5:1 or higher.
Apparatus utilising compressed air or other gas acting directly or indirectly on beverages in storage containers · CPC title
Carbon dioxide · CPC title
Alloys or compositions of metals · CPC title
Avoiding overfilling · CPC title
for gas bottles, such as on a continuous belt or on a merry-go-round · CPC title
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