Method and system for optimizing the filling, storage and dispensing of carbon dioxide from multiple containers without overpressurization

Patent metadata

Field	Value
Publication number	US-11242955-B2
Application number	US-201916671666-A
Country	US
Kind code	B2
Filing date	Nov 1, 2019
Priority date	Mar 30, 2016
Publication date	Feb 8, 2022
Grant date	Feb 8, 2022

Abstract

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.

First claim

The invention claimed is:

1. A method for filling an on-site CO2 delivery system with CO2 to avoid over pressurization, comprising the steps of:
providing a liquid CO2 container and a vapor CO2 container operatively connected to the liquid CO2 container;
introducing pressurized CO2 fluid into the liquid CO2 container;
creating a restricted flow pathway extending from a fill port to the vapor CO2 container in response to the flow of the pressurized CO2 fluid entering the liquid CO2 container;
introducing a predetermined portion of the pressurized CO2 fluid through the restricted flow pathway and into the vapor CO2 container;
filling the system with said pressurized CO2 fluid such that a total weight of said pressurized CO2 fluid occupying the system is no more than 68 wt % by water weight.

2. The method of claim 1 , further comprising substantially equalizing pressures in the liquid CO2 container and the vapor CO2 container during the filling.

3. The method of claim 1 , wherein a pressure differential device is configured in the open position, said pressure differential device is situated between the liquid CO2 container and the vapor CO2 container.

4. The method of claim 1 , wherein the restricted flow path is created by a predetermined clearance between a valve body and the piston.

5. The method of claim 1 , further comprising:
monitoring a liquid level of the pressurized CO2 fluid in the vapor CO2 container;
determining a liquid CO2 level in the vapor CO2 container to reach a predetermined maximum level, and in response thereto;
stopping the filling of the pressurized CO2 fluid into the liquid CO2 container.

6. The method of claim 1 , wherein the step of introducing pressurized CO2 fluid through the restricted flow pathway and into the vapor CO2 container is in an amount that comprises less than approximately 30 wt % of the pressurized CO2 fluid introduced from a CO2 source.

7. An on-site system for selectively filling and dispensing CO2 vapor product from a liquid CO2 container and a vapor CO2 container, respectively, comprising:
a liquid CO2 container operably connected to a vapor CO2 container,
the liquid CO2 container comprising a fill port to receive pressurized and refrigerated liquid CO2;
a shuttle valve comprising a reciprocating piston;
a pressure differential device situated between the liquid CO2 container and the vapor CO2 container;
the on-site system adapted to switch between a first configuration for filling and a second configuration for use;
the on-site system in the first configuration, during filling, that is defined, at least in part, by the pressure differential device activated to an open position, and the shuttle valve configured into a biased state in response to the pressurized refrigerated liquid CO2 pushing the reciprocating piston away from the fill port of the liquid container towards the vapor CO2 container, thereby unobstructing the fill port and directing a substantial fraction of the flow of the pressurized and refrigerated liquid CO2 into the liquid CO2 container while permitting a portion of the flow of the pressurized and refrigerated liquid CO2 to enter into the vapor CO2 container along a restricted flow path at a second pressure that is substantially equalized with a first pressure in the liquid CO2 container, said restricted flow path created by a clearance between a valve body of the shuttle valve and the reciprocating piston;
the on-site system in the second configuration, during use, that is defined, at least in part, by the shuttle valve in an unbiased position that allows fluid communication between the liquid CO2 container and the vapor CO2 container in an amount that is greater than that permitted by the restrictive flow path when the pressure differential device is activated to open at a predetermined pressure difference between the liquid CO2 container and the vapor CO2 container, thereby allowing CO2 fluid to transfer from the liquid CO2 container along an internal pathway of the reciprocating piston of the shuttle valve, through the pressure differential device and into the vapor CO2 container, and further wherein the pressure differential device is activated to close below the predetermined pressure difference, thereby allowing a substantial fraction of the CO2 product to be dispensed from the vapor CO2 container while (i) minimizing or eliminating the transfer of the CO2 fluid from the liquid CO2 container to the vapor CO2 container; and/or (ii) minimizing or eliminating the dispensing of CO2 vapor product from the liquid CO2 container, where either (i) or (ii) is defined as occurring 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.

8. The on-site system of claim 7 , wherein the pressure differential device is integrated with the shuttle valve.

9. The on-site system of claim 7 , wherein the restricted flow path has the clearance between the valve body and the reciprocating piston that is no more than about 0.003 inches to create less than about 25 wt % of the total CO2 pressurized and refrigerated liquid CO2 that is charged into the system to enter into the vapor CO2 container with the balance charged to occupy the liquid CO2 container.

10. The on-site system of claim 7 , wherein the pressure differential device is selected from the group consisting of a critical orifice, a capillary, a pressure relief valve, an active in-line spring-loaded backpressure device and any other suitable device capable of being set to activate into an open position at the predetermined pressure difference between the liquid container and the vapor container so as to maintain transfer of the CO2 fluid from the liquid CO2 container to the vapor container upon preferential depletion of the CO2 liquid in the vapor CO2 container.

11. The on-site system of claim 7 , further comprising a flow leg extending between the liquid CO2 container and the vapor CO2 container.

12. The on-site system of claim 11 , wherein the shuttle valve and the pressure differential device is situated on the flow leg.

13. The on-site system of claim 7 , further comprising a means for measuring the pressurized refrigerated CO2 liquid level in the vapor CO2 container.

14. The on-site system of claim 7 , wherein the vapor CO2 container is configured to be the same size or larger in volume than the liquid CO2 container.

15. The on-site system of claim 7 , further comprising a residual pressure control device.

16. A method for assembling an on-site multiple container system capable of dispensing CO2 vapor product to an end-user or customer, comprising:
providing a liquid CO2 container, the liquid CO2 container comprising a fill port to receive pressurized refrigerated liquid CO2;
providing a vapor CO2 container that is the same size or larger than the liquid CO2 container;
providing a pressure differential device;
providing a shuttle valve comprising a reciprocating piston;
operably connecting the liquid CO2 container with the vapor CO2 container with a conduit extending between the liquid CO2 container and the vapor CO2 container;
configuring the shuttle valve along the conduit extending between the liquid CO2 container and the vapor CO2 container, wherein the shuttle valve is configured into a biased state during filling of the liquid CO2 container in response to receiving pressurized refrigerated liquid CO2 along the fill port whereby the pressurized refrigerated liquid CO2 pushes the reciprocating piston away from the fill port of the liquid container towards the

Assignees

• Song Xuemei
• Cecula Shawn M
• Gerristead William R
• Praxair Technology Inc

Inventors

• Song Xuemei
• Cecula Shawn M
• Gerristead William R

Classifications

• F17C5/005 Primary

  for gas bottles, such as on a continuous belt or on a merry-go-round · CPC title

• F17C2260/042

  Reducing risk of explosion · CPC title

• F17C2223/0153

  Liquefied gas, e.g. LPG, GPL · CPC title

• F17C2203/0648

  Alloys or compositions of metals · CPC title

• F17C1/005

  Storage of gas or gaseous mixture at high pressure and at high density condition, e.g. in the single state phase · CPC title