Method of operating a cold cryogenic liquid supply chain

Patent metadata

Field	Value
Publication number	US-12366330-B2
Application number	US-202418642410-A
Country	US
Kind code	B2
Filing date	Apr 22, 2024
Priority date	Nov 22, 2021
Publication date	Jul 22, 2025
Grant date	Jul 22, 2025

Abstract

A cryogen storage vessel at an installation is filled with liquid cryogen from a liquid cryogen storage tank that has a pressure lower than that of the vessel. After headspaces of the vessel and tank are placed in fluid communication with another via a gas transfer vessel and are pressure-balanced, a pump in a liquid transfer line connected between the tank and the vessel is operated to transfer amounts of liquid cryogen from the tank to the vessel via the liquid transfer line and pump as amounts of gaseous cryogen are transferred, through displacement by the pumped cryogenic liquid, from the vessel to the tank.

First claim

What is claimed is:

1. A method of filling a liquid cryogen storage vessel installed at an installation with liquid cryogen from a liquid cryogen storage tank, the method comprising the steps of:
connecting a liquid transfer conduit from the liquid cryogen storage tank to the liquid cryogen storage vessel, the liquid transfer conduit having a first liquid cryogen pump disposed in-line, the connected liquid transfer conduit being in selectable fluid communication, via one or more valves, between a liquid cryogen space in the liquid cryogen storage tank, in which is stored an amount of liquid cryogen, and a liquid cryogen space in the liquid cryogen storage vessel, in which is stored an amount of the liquid cryogen, wherein, prior to said step of connecting a liquid transfer conduit, the liquid cryogen storage vessel has an initial pressure higher than an initial pressure of the liquid cryogen storage tank;
connecting a gas transfer conduit between the liquid cryogen storage vessel and the liquid cryogen storage tank that is in selectable fluid communication between headspace of the liquid cryogen storage vessel, which contains an amount of the liquid cryogen in gaseous form, and a headspace of the liquid cryogen storage tank, which contains an amount of the gaseous cryogen, via one or more valves disposed in the gas transfer conduit;
precooling the gas transfer conduit and/or the liquid transfer conduit using amounts of a cryogenic fluid, wherein the cryogenic fluid is selected from the group consisting of gaseous cryogen from the liquid cryogen storage vessel headspace, liquid cryogen from the liquid cryogen space of the liquid cryogen storage tank, and combinations thereof;
reducing a pressure difference between the liquid cryogen storage vessel and liquid cryogen storage tank headspaces by opening one or more of the valves in the gas transfer conduit, thereby allowing the cryogenic gas to be transferred from the liquid cryogen storage vessel headspace to the liquid cryogen storage tank headspace by virtue of a difference between their initial pressures;
opening the one or more valves in the liquid transfer line thereby allowing fluid communication between the liquid cryogen spaces of the liquid cryogen storage tank and the liquid cryogen storage vessel; and
pumping an amount of the liquid cryogen from the liquid cryogen space of the liquid cryogen storage tank to the liquid cryogen space of the liquid cryogen storage vessel via the liquid transfer line and first pump as amounts of the gaseous cryogen flow from the liquid cryogen storage vessel headspace to the liquid cryogen storage tank headspace caused by said pumping.

2. The method of claim 1 , wherein said step of reducing the pressure difference occurs without the use of a compressor or vacuum pump.

3. The method of claim 1 , wherein the liquid cryogen is transferred from the liquid cryogen space of the liquid cryogen storage tank to the liquid cryogen space of the liquid cryogen storage vessel without the use of a pressure-building circuit.

4. The method of claim 1 , further comprising the step of, prior to said step of reducing the pressure difference, purging the gas transfer conduit and/or the liquid transfer conduit with amounts of gaseous cryogen from the liquid cryogen storage vessel headspace.

5. The method of claim 1 , wherein the cryogenic fluid comprises the gaseous cryogen from the liquid cryogen storage vessel headspace.

6. The method of claim 1 , wherein the cryogenic fluid comprises the liquid cryogen from the liquid cryogen space of the liquid cryogen storage tank.

7. The method of claim 1 , wherein the first pump compresses the liquid cryogen from the liquid cryogen storage tank to a pressure that is a predetermined value above a pressure of the liquid cryogen storage vessel.

8. The method of claim 1 , wherein the predetermined value is less than 3 bar.

9. The method of claim 1 , wherein the first pump is a centrifugal pump.

10. The method of claim 1 , wherein one or more of the gas transfer conduit, the liquid transfer conduit, and the first pump are vacuum-jacketed.

11. The method of claim 1 , wherein, prior to said step of pumping, the liquid cryogen in the liquid cryogen space of the liquid cryogen storage vessel has an initial temperature higher than an initial temperature of the liquid cryogen in the liquid cryogen space of the liquid cryogen storage tank.

12. The method of claim 1 , wherein: prior to said step of pumping, the liquid cryogen in the liquid cryogen space of the liquid cryogen storage vessel has an initial saturation temperature; and after performance of said method, the liquid cryogen in the liquid cryogen space of the liquid cryogen storage vessel has a saturation temperature lower than the initial saturation temperature.

13. The method of claim 1 , wherein heat is removed from the liquid cryogen storage vessel by performance of said method.

14. The method of claim 1 , wherein a coupled system is made up of the liquid cryogen storage tank and liquid cryogen storage vessel connected by the gas and liquid transfer conduits and no heat is added to the coupled system other than through heat leak from ambient and addition of heat from operation of the pump.

15. The method of claim 1 , wherein said step of pumping commences when a difference in pressure between the tank headspace and the liquid cryogen storage vessel headspace, prior to initiating said pumping, reaches zero or a predetermined pressure of less than 1 bar.

16. The method of claim 1 , wherein the liquid cryogen is liquid hydrogen or liquid helium.

17. A method of filling a liquid cryogen storage vessel installed at an installation with liquid cryogen from a liquid cryogen storage tank, the method comprising the steps of:
connecting a liquid transfer conduit from the liquid cryogen storage tank to the liquid cryogen storage vessel, the liquid transfer conduit having a first liquid cryogen pump disposed in-line, the connected liquid transfer conduit being in selectable fluid communication, via one or more valves, between a liquid cryogen space in the liquid cryogen storage tank, in which is stored an amount of liquid cryogen, and a liquid cryogen space in the liquid cryogen storage vessel, in which is stored an amount of the liquid cryogen, wherein, prior to said step of connecting a liquid transfer conduit, the liquid cryogen storage vessel has an initial pressure higher than an initial pressure of the liquid cryogen storage tank;
connecting a gas transfer conduit between the liquid cryogen storage vessel and the liquid cryogen storage tank that is in selectable fluid communication between headspace of the liquid cryogen storage vessel, which contains an amount of the liquid cryogen in gaseous form, and a headspace of the liquid cryogen storage tank, which contains an amount of the gaseous cryogen, via one or more valves disposed in the gas transfer conduit;
reducing a pressure difference between the liquid cryogen storage vessel and liquid cryogen storage tank headspaces by opening one or more of the valves in the gas transfer conduit, thereby allowing the cryogenic gas to be transferred from the liquid cryogen storage vessel headspace to the liquid cryogen storage tank deadspace by virtue of a difference between their initial pressures;
opening the one or more valves in the liquid transfer line thereby allowing fluid communication between the liquid cryogen spaces of the liquid cryogen storage tank and the liquid cryogen storage vessel; and
pumping an amount of the liquid cryogen from the liquid cryogen space of the liquid cryogen

Assignees

• Air Liquide

Inventors

• Light Joshua
• Hayes Jerry
• Allidieres Laurent
• Fayer Thomas
• Benistand-Hector Cyril

Classifications

• F17C2227/0302

  by heating · CPC title

• F17C2205/0352

  Pipes · CPC title

• F17C2205/0323

  Valves · CPC title

• F17C2205/0134

  characterised by the presence of fluid connection between vessels · CPC title

• F17C7/02

  Discharging liquefied gases · CPC title