Mobile cryogenic tank and provisioning method

Patent metadata

Field	Value
Publication number	US-11946594-B2
Application number	US-202117794208-A
Country	US
Kind code	B2
Filing date	Jan 14, 2021
Priority date	Jan 24, 2020
Publication date	Apr 2, 2024
Grant date	Apr 2, 2024

Abstract

Mobile cryogenic tank for transporting cryogenic fluid, notably liquefied hydrogen or helium, comprising an internal shell intended to contain the cryogenic fluid, an external shell arranged around the internal shell and delimiting a space between the two shells, said space containing a thermal insulator, the first shell having a cylindrical overall shape extending along a central longitudinal axis (A), when the tank is in the configuration for transport and use, the central longitudinal axis (A) being oriented horizontally, the tank comprising a set of temperature sensors measuring the temperature of the fluid in the internal shell, characterized in that the set of temperature sensors is situated on the external face of the internal shell and measure the temperature of said shell, the set of temperature sensors comprising a lower sensor positioned at the lower end of the internal shell situated below the central longitudinal axis (A), the set of temperature sensors further comprising a plurality of intermediate sensors distributed over two lateral faces of the internal shell on each side of the central longitudinal axis (A), the plurality of intermediate sensors being distributed vertically between the lower end of the internal shell situated below the central longitudinal axis (A) and the upper end of the internal shell situated above the central longitudinal axis (A).

First claim

What is claimed is:

1. A mobile cryogenic tank for transporting cryogenic fluids, comprising:
a. an inner shell configured to contain the cryogenic fluid that has a lower end and an upper end, the inner shell having a cylindrical overall shape extending along a central longitudinal axis (A) when the tank is in a transport and usage configuration, the central longitudinal axis (A) being oriented horizontally and being disposed between the lower and upper ends;
b. an outer shell positioned around the inner shell and delimiting a space between the inner and outer shells, said space containing a thermal insulant;
c. a set of temperature sensors measuring the temperature of the cryogenic fluid in the inner shell each of which is situated on an outer face of the inner shell and measures a temperature of said shell, the set of temperature sensors comprising:
i. a lower temperature sensor positioned at a lower end of the inner shell situated below the central longitudinal axis (A); and
ii. a plurality of intermediate temperature sensors distributed over two lateral faces of the inner shell on either side of the central longitudinal axis (A), the plurality of intermediate sensors also being distributed vertically between the lower and upper ends; and

d. an electronic data storage and processing member comprising a microprocessor and/or a computer, said electronic data storage and processing member being connected to the set of temperature sensors and being configured to receive temperature values measured by said sensors and determine at least one of the following: a level of cryogenic liquid in the tank and a volume of cryogenic liquid in the tank,
wherein said electronic data storage and processing member is further configured to:
deliver cryogenic fluid to a first station and then to a second station;
prior to delivering cryogenic fluid to the first station, increasing a pressure in the mobile cryogenic tank by a determined addition of energy by withdrawing some of the cryogenic fluid from the mobile cryogenic tank and heating the withdrawn cryogenic fluid before re-injecting the heated withdrawn cryogenic fluid into the mobile cryogenic tank;
calculate future pressure and temperature equilibrium conditions that would exist in the mobile cryogenic tank after the delivery of cryogenic fluid to the first station on the basis of the aforementioned quantity of added energy and on the basis of the temperature and pressure of the cryogenic fluid in the mobile cryogenic tank, and
interrupt delivery of cryogenic fluid to the first station when the calculated future pressure and temperature equilibrium conditions in the mobile cryogenic tank are higher than the determined thermodynamic temperature and pressure conditions for the store of the second station.

2. The tank of claim 1 , wherein each of the temperature sensors of the set of temperature sensors is situated in the central part of the tank between the two longitudinal ends.

3. The tank of claim 1 , wherein:
a. the plurality of intermediate sensors comprises first and second sets of 3-10 intermediate sensors each;
b. the first and second sets of intermediate sensors are situated, respectively, on two opposite lateral faces of the inner shell on either side of the central longitudinal axis (A);
c. each of the intermediate sensors in the first set of intermediate sensors is spaced apart vertically between the lower and upper end; and
d. each of the intermediate sensors in the second set of intermediate sensors is spaced apart vertically between the lower and upper end.

4. The tank of claim 3 , wherein each of the first and sets of intermediate sensors comprises 4-8 sensors.

5. The tank of claim 1 , wherein the set of temperature sensors further comprises an upper sensor positioned at the upper end.

6. The tank of claim 1 , wherein the plurality of intermediate sensors comprises first and second groups of intermediate temperature sensors situated at two distinct longitudinal locations along the longitudinal direction (A), each of the first and second groups of intermediate temperature sensors comprising a plurality of intermediate temperature sensors distributed vertically between the lower and upper ends.

7. The tank of claim 1 , wherein said electronic data storage and processing member are further configured to determine a temperature of the cryogenic fluid in the tank.

8. The tank of claim 1 , further comprising a pressure sensor for measuring a pressure in the inner shell.

9. The tank of claim 1 , further comprises a set of pipes equipped with a valve or valves connected to the inner shell and opening to outside the tank for filling and withdrawing from the inner shell.

10. The tank of claim 1 , wherein at least one intermediate temperature sensor of the plurality of intermediate temperature sensors is situated at a vertical position of the inner shell that corresponds to a maximum fill level for filling the tank with cryogenic fluid in liquid form and at which the filling of said tank is stopped.

11. The tank of claim 1 , wherein the maximum fill level corresponds to 90-98% of the volume of the inner shell.

12. A method for provisioning a plurality of usage stations with cryogenic fluid using the mobile cryogenic tank of claim 1 , wherein:
each of the plurality of usage stations comprises a liquefied gas fluid storage configured to store the cryogenic fluid, in liquid and gaseous phases, at determined thermodynamic pressure and temperature conditions; and
the mobile cryogenic tank further comprises a pressure sensor for measuring the pressure in the inner shell;
said method comprising the steps of:
measuring a temperature and pressure of the cryogenic fluid in the mobile cryogenic tank;
determining thermodynamic temperature and pressure conditions in each of the liquefied gas fluid stores of the plurality of stations; and
delivering cryogenic fluid, using the mobile cryogenic tank, to said plurality of stations, respective cryogenic fluid quantities that are dependent on the cryogenic fluid temperature and pressure measured in the mobile cryogenic tank and on the respective determined thermodynamic temperature and pressure conditions of respective ones of said plurality of stations,
wherein said plurality of stations comprises first and second stations;
said step of delivering cryogenic fluid comprises delivering cryogenic fluid to the first station and then to the second station; and
said method further comprises:
prior to said step of delivering cryogenic fluid to the first station, a step of increasing a pressure in the mobile cryogenic tank by a determined addition of energy by withdrawing some of the cryogenic fluid from the mobile cryogenic tank and heating the withdrawn cryogenic fluid before re-injecting the heated withdrawn cryogenic fluid into the mobile cryogenic tank; and
calculating future pressure and temperature equilibrium conditions that would exist in the mobile cryogenic tank after the delivery of cryogenic fluid to the first station on the basis of the aforementioned quantity of added energy and on the basis of the temperature and pressure of the cryogenic fluid in the mobile cryogenic tank,
wherein delivery of cryogenic fluid to the first station is interrupted when the calculated future pressure and temperature equilibrium conditions in the mobile cryogenic tank are higher than the determined thermodynamic temperature and pressure conditions for the store of the second station.

13. The method of claim 12 , wherein said step of delivering cryogenic fluid is performed in a chronological order that is determined on the basis of the temperature and pressure of the cr

Assignees

• Air Liquide

Inventors

• Varrassi Lucien
• Cadeau Philippe
• Fayer Thomas
• Duval Stephane

Classifications

• F17C13/026 Primary

  having the temperature as the parameter · CPC title

• F17C3/04 Primary

  by insulating layers (F17C3/08 takes precedence) · CPC title

• F17C9/00

  Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure · CPC title

• F17C2201/0109

  with exteriorly curved end-piece · CPC title

• F17C2201/035

  with substantially horizontal main axis · CPC title