Method and device for filling a storage vessel with liquefied gas

Patent metadata

Field	Value
Publication number	US-11519554-B2
Application number	US-202016778149-A
Country	US
Kind code	B2
Filing date	Jan 31, 2020
Priority date	Jan 31, 2019
Publication date	Dec 6, 2022
Grant date	Dec 6, 2022

Abstract

Method for filling a storage vessel with liquefied gas by means of a tank of liquefied gas, the method comprising a step of transferring liquefied gas from the tank into the storage vessel by means of a pressure differential, wherein the storage vessel prior to the transfer step has an internal pressure higher than the internal pressure of the tank, the method comprising, prior to the transfer step, a step of placing the tank and the storage vessel in fluidic communication in order to ensure a drop in the pressure in the storage vessel to the benefit of the tank and a step of increasing the pressure in the tank using a pressurizing device.

First claim

What is claimed is:

1. A method for filling a storage vessel with liquefied hydrogen from a tank of liquefied hydrogen, the storage vessel initially being at a higher pressure than the tank, said method comprising the steps of:
providing a storage vessel;
providing:
a semitrailer carrying the tank of liquefied hydrogen;
a first fluid transfer pipe that has first and second ends, the first end of the first fluid transfer pipe being connected to an upper part of an interior of the tank of liquefied hydrogen, the first fluid transfer pipe including at least one transfer valve controllable or operable to allow or prevent fluid communication between the upper part of the interior of the tank of liquefied hydrogen and the second end of the first fluid transfer pipe;
a second fluid transfer pipe that has first and second ends, the first end of the second fluid transfer pipe being connected to a lower part of the interior of the tank of liquefied hydrogen, the second fluid transfer pipe including at least one transfer valve controllable or operable to allow or prevent fluid communication between the lower part of the interior of the tank of liquefied hydrogen and the second end of the second fluid transfer pipe;
a pressurizing device for increasing a pressure in the tank of liquefied hydrogen to a level higher than a pressure in storage vessel, thereby allowing a transfer of the liquefied hydrogen from the tank of liquefied hydrogen to the storage vessel through pressure differential, the pressurizing device being a tank-pressurizing circuit that comprises, between a fluid-aspiration first end connected to the tank of liquefied hydrogen and a fluid-return second end connected to the tank of liquefied hydrogen, a fluid heating member and a set of one or more heating valves for controlling the circulation of the hydrogen in the pressurizing circuit; and
an electronic control and data processing and storage member for controlling at least part of the set of one or more heating valves;

connecting the second end of the first fluid transfer pipe to a circuitry of the storage vessel that includes a plurality of valves allowing or preventing fluid communication between the second end of the first fluid transfer pipe with an upper part of an interior of the storage vessel or a lower part of the interior of the storage vessel;
connecting the second end of the second fluid transfer pipe to the circuitry, the plurality of valves of the circuitry allowing or preventing fluid communication between the second end of the second fluid transfer pipe with the upper or lower part of the interior of the storage vessel;
placing the upper part of the interior of the tank of liquefied hydrogen and the interior of the storage vessel in fluidic communication, via the at least one valve of the first fluid transfer pipe and the plurality of valves of the circuitry, to equalize pressure between them, resulting in a drop in the pressure in the storage vessel and an increase in pressure in the tank of liquefied hydrogen such that the pressure in the storage vessel, in comparison to the pressure in the tank of liquefied hydrogen, is lowered down to a predetermined level at which the pressure in the storage vessel is equal to the pressure in the tank of liquefied hydrogen or exceeds the pressure in the tank by a predetermined value of between 0.5 and 5 bar;
placing the lower part of the interior of the tank of liquefied hydrogen and the interior of the storage vessel in fluid communication, via the at least one valve of the second fluid transfer pipe and the plurality of valves of the circuitry; and
using the pressurizing device to increase the pressure in the tank of liquefied hydrogen to a level higher than the pressure in the storage vessel, thereby causing a transfer of liquefied hydrogen from the tank of liquefied hydrogen to the storage vessel through pressure differential, wherein:
after or during the transfer of pressure between the storage vessel and the tank of liquefied hydrogen, the electronic control and data processing and storage member controls an opening of the set of one or more heating valves in order to increase the pressure in the tank of liquefied hydrogen, and
the electronic control and data processing and storage member controls a closing of the set of one or more heating valves and an opening of the at least one valve of the first fluid transfer pipe and the at least one valve of the second fluid transfer pipe in order to ensure a transfer of liquefied hydrogen from the tank of liquefied hydrogen to the storage vessel using a pressure differential.

2. The method of claim 1 , wherein
when a pressure in the tank of liquefied hydrogen reaches a sufficient value above a pressure in the storage vessel, said step of using a pressurizing device is interrupted and a transfer of liquid hydrogen from the tank of liquefied hydrogen to the storage vessel is carried out by way a pressure differential between the tank and the storage vessel.

3. The method of claim 1 , wherein the step of using the pressurizing device increases the pressure in the tank up to a predetermined level at which the pressure in the tank exceeds the pressure in the storage vessel by a predetermined value of between 0.5 and 5 bar.

Assignees

• Air Liquide

Inventors

• Allidieres Laurent
• Thieu Anh Thao
• Fayer Thomas

Classifications

• F17C2223/0161

  cryogenic, e.g. LNG, GNL, PLNG · CPC title

• F17C2227/041

  vessel by vessel · CPC title

• F17C2260/025

  Reducing transfer time · CPC title

• F17C2250/043

  Pressure · CPC title

• F17C2265/063

  for supply of refuelling stations · CPC title