Device and method for filling pressurized gas tanks

Patent metadata

Field	Value
Publication number	US-11155459-B2
Application number	US-201916580730-A
Country	US
Kind code	B2
Filing date	Sep 24, 2019
Priority date	Sep 25, 2018
Publication date	Oct 26, 2021
Grant date	Oct 26, 2021

Abstract

Device and method for filling pressurized gas tanks, particularly vehicle pressurized hydrogen tanks, the device comprising a liquefied gas source, a transfer circuit comprising two parallel transfer lines each having an upstream end linked to the liquefied gas source, at least two separate downstream ends intended to be each removably connected to a tank to be filled, each of the two transfer lines comprising: a pump, a vaporizer for evaporating the pumped fluid, a branch for bypassing the vaporizer and a distribution valve(s) set configured to control the flow of fluid pumped and distributed between the vaporizer and the branch line, the device further comprising a storage buffer(s), which storage buffer(s) is(are) connected in parallel to each of the two transfer lines via a set of valves.

First claim

What is claimed is:

1. A device for filling pressurized gas tanks, comprising:
a liquefied gas source containing liquefied gas;
a storage buffer(s); and
a transfer circuit, the transfer circuit comprising two parallel transfer lines each having an upstream end linked to the liquefied gas source, each of the two parallel transfer lines comprising a downstream end intended to be removably connected to a tank to be filled, each of the two transfer lines comprising: a pump for pumping the liquefied gas, a vaporizer line receiving the pumped liquefied gas from the pump, a vaporizer disposed in the vaporizer line for evaporating a first portion of the pumped liquefied gas, a branch line receiving a second portion of the pumped liquefied gas and allowing the second portion of liquefied gas to bypass the vaporizer, and at least one distribution valve, the at least one distribution valve being configured to control a flow of pumped liquefied gas and distributed between the vaporizer and the branch line, the storage buffer(s) being connected in parallel to each of the two parallel transfer lines via a set of valves, the two parallel transfer lines comprising first and second parallel transfer lines, wherein:
the vaporizer line and the branch line of the first parallel transfer line split off from one another downstream of the pump of the first parallel transfer line and upstream of a mixing point where evaporated fluid from the vaporizer of the first parallel transfer line is mixed with the pumped liquefied gas in the branch line of the first parallel transfer line; and
the transfer circuit comprises a connection duct linking the two parallel transfer lines at outlets of the two pumps, said connection duct comprising an isolation valve.

2. The device of claim 1 , wherein the buffer storage(s) set is connected to each of the two parallel transfer lines between the vaporizer and the point of mixing between the fluid having passed through the vaporizer and the fluid having passed through the branch line.

3. The device of claim 1 , wherein the set of valves connecting the storage buffer(s) and each of the two parallel transfer lines comprises expansion valves each one of which is associated with a respective one of the two transfer lines.

4. The device of claim 1 , wherein each of the at least one distribution valves comprises a first distribution valve located downstream of the vaporizer and upstream of a mixing point where fluid that has gone through the branch line from the pump is mixed with fluid that has not gone through the branch line from the pump and a second distribution valve located in the branch line.

5. The device of claim 1 , wherein the storage buffer(s) comprises two or more storage buffers connected in parallel to each of the two parallel transfer lines and the set of valves includes a respective two or more isolation valves, each storage buffer being connected to each transfer line via a respective one of said isolation valves.

6. The device of claim 1 , wherein the two parallel transfer lines comprise at least one thermally insulated portion.

7. The device of claim 1 , wherein each of the two parallel transfer lines comprises at least one pressure sensor and/or at least one temperature sensor measuring a pressure and temperature of pressurized gas in a respective one of the two parallel transfer lines.

8. The device of claim 1 , wherein the pressurized gas tanks are vehicle pressurized hydrogen tanks.

9. The device of claim 1 , wherein:
the two parallel transfer lines comprise first and second transfer lines;
the at least one distribution valve of the first transfer line comprises a first distribution valve downstream of the pump of the first transfer line and upstream of the vaporizer and the branch lines of the first transfer line, a second distribution valve downstream of the vaporizer of the first transfer line and upstream of the mixing point of the first transfer line, and a third distribution valve disposed in the branch line of the first transfer line; and
control of the openings of the second and third distribution valves of the first transfer line operates to control relative amounts of the liquefied gas pumped by the pump of the first transfer line that are allocated between the vaporizer line of the first transfer line and the branch line of the first transfer line.

10. A method of filling at least one pressurized gas tank with a determined gas flow rate at a determined temperature to establish a determined filling gradient in the tank, comprising the steps of:
providing the filling device of claim 1 , wherein the downstream end of the first parallel transfer line is connected to a first tank to be filled;
pumping a first flow of liquefied gas from the liquefied gas source with the pump of the first parallel transfer line;
allowing a first portion of the pumped flow of liquefied gas to be evaporated at the vaporizer of the first parallel transfer line;
allowing a second portion of the pumped flow of liquefied gas to flow through the branch line thereby bypassing the vaporizer of the first parallel transfer line;
allowing the first portion of the pumped flow of liquefied gas that has evaporated in the vaporizer of the first parallel transfer line to mix with the second portion of the pumped flow of liquefied gas from the branch line to provide a r flow of gas;
controlling the relative amounts of the first and second portions of the pumped flow of liquefied gas from the pump of the first parallel transfer line allocated between the vaporizer of the first parallel transfer line and the branch of the first parallel transfer line using the at least one distribution valve of the first parallel transfer line; and
filling the first tank with pressurized gas obtained either from the storage buffer(s), from a combination of the first flow of gas and pressurized gas from the storage buffer(s), or directly from the first flow of gas.

11. The filling method of claim 10 , wherein a flow rate of the first flow of gas is variable and modified over time.

12. The filling method of claim 10 , wherein, when a flow rate of pressurized gas used to fill the first tank is greater than a maximum flow rate of the pump of the first parallel transfer line, the pressurized gas used to fill the first tank is obtained from the combination of the first flow of gas and pressurized gas from the storage buffer(s).

13. The method of claim 10 , wherein, when a flow rate of pressurized gas used to fill the first tank is less than or equal to a maximum flow rate of the pump of the first parallel transfer line, the pressurized gas used to fill the first tank is obtained from the first flow of gas and not from the storage buffer(s).

14. The method of claim 10 , further comprising the steps of:
pumping a second flow of liquefied gas from the liquefied gas source with the pump of the second parallel transfer line;
allowing a first portion of the pumped flow of liquefied gas to be evaporated at the vaporizer of the second parallel transfer line;
allowing a second portion of the pumped flow of liquefied gas to flow through the branch for bypassing the vaporizer of the second parallel transfer line;
allowing the first portion of the pumped flow of liquefied gas that has evaporated in the vaporizer of the second parallel transfer line to mix with the second portion of the pumped flow of liquefied gas that has bypassed the vaporizer of the second parallel transfer line to provide a second flow of gas; and
controlling the relative amounts of the first and second portions of the pumped flow of liquefied gas from the pump of the second parallel transfer li

Assignees

• Air Liquide

Inventors

• Crispel Simon
• Buck Marcus
• Thieu Anh Thao
• Fairy Vincent

Classifications

• F17C2250/0439

  Temperature · CPC title

• F17C2250/043

  Pressure · CPC title

• F17C2227/0393

  using a vaporiser · CPC title

• F17C2250/032

  using computers · CPC title

• F17C2225/0123

  gaseous, e.g. CNG, GNC · CPC title