Method and refuelling means for filling a cryotank

• US 5,365,981 A
• Filed: 08/19/1992
• Issued: 11/22/1994
• Est. Priority Date: 08/31/1991
• Status: Expired due to Fees

• Current Assignee: Deutsche Telekom AG
• Original Assignee: Deutsche Telekom AG
• Inventors: Schneider, Gottfried, Peschka, Walter
• Primary Examiner(s): JACYNA, J CASIMER
• Application Number:
  US07/932,066
• Time in Patent Office: 825 Days
• Field of Search: 141/1-5, 141/7, 141/11, 141/44, 141/45, 141/51, 141/59, 141/82, 141/98, 62/50.1, 62/50.7, 62/53.2, 62/54.1, 62/55.5, 123/541, 123/DIG. 12
• US Class Current: 141/7
• CPC Class Codes: B60S 5/02 Supplying fuel to vehicles; General disposition of plant in filling stations apparatus for transferring measured quantities of petrol, oil, or the like from storage space to vehicles B67D
• CPC Class Codes: F17C 2221/012 Hydrogen
• CPC Class Codes: F17C 2223/0161 cryogenic, e.g. LNG, GNL, PLNG
• CPC Class Codes: F17C 2223/033 Small pressure, e.g. for liquefied gas
• CPC Class Codes: F17C 2223/047 with a dip tube
• CPC Class Codes: F17C 2225/0161 cryogenic, e.g. LNG, GNL, PLNG
• CPC Class Codes: F17C 2225/033 Small pressure, e.g. for liquefied gas
• CPC Class Codes: F17C 2225/043 in the gas
• CPC Class Codes: F17C 2227/0142 with specified pump type, e.g. piston or impulsive type
• CPC Class Codes: F17C 2265/065 for refueling vehicle fuel tanks
• CPC Class Codes: F17C 2270/0139 Fuel stations
• CPC Class Codes: F17C 2270/0171 Trucks
• CPC Class Codes: F17C 2270/0176 Buses
• CPC Class Codes: F17C 2270/0178 Cars
• CPC Class Codes: F17C 6/00 Methods and apparatus for filling vessels not under pressure with liquefied or solidified gases
• CPC Class Codes: Y02E 60/32 Hydrogen storage
• CPC Class Codes: Y02P 90/45 Hydrogen technologies in production processes
• CPC Class Codes: Y10S 123/12 Hydrogen

Abstract

In order to improve a method for filling a cryotank with liquid hydrogen, in which thermal energy is introduced into the liquid hydrogen by the transfer of the liquid hydrogen to the cryotank, such that the amount of gas which results during filling of a cryotank and is carried away via the gas return line is reduced to as great an extent as possible, preferably to zero, it is suggested that for filling hydrogen be used at a pressure and a temperature corresponding to an undercooled state of the liquid hydrogen.

Claims

1. A method for filling a cryotank of a hydrogen-powered vehicle with liquid hydrogen from a storage tank, comprising the steps of:

connecting a liquid hydrogen line to said cryotank for transferring hydrogen therethrough;

connecting a gas return line between said cryotank and said storage tank for safety purposes, said gas return line being used for removal of hydrogen gas from said cryotank;

opening said gas return line to reduce the pressure in said cryotank prior to commencement of a hydrogen transferring step;

transferring hydrogen at a pressure and a temperature corresponding to an undercooled state of liquid hydrogen from said storage tank through said liquid hydrogen line to said cryotank, said undercooled state of said liquid hydrogen being sufficient to reduce the vaporization of the hydrogen caused by thermal energy introduced into the hydrogen during transfer to the cryotank to such a degree, that under normal conditions, no hydrogen gas has to be removed from said cryotank;

closing said gas return line during said hydrogen transferring step;

connecting said liquid hydrogen line to said gas return line by a short-circuit line opening said gas return line after said hydrogen transferring step; and

cooling said liquid hydrogen line, said short-circuit line and said gas return line with hydrogen flowing through said lines during the intervals between filling events.

2. The method of claim 1, wherein the hydrogen flows through said lines continuously during periods when hydrogen is not being transferred from said storage tank to said cryotank.

3. The method of claim 1, wherein the hydrogen flows through said lines in intervals during periods when hydrogen is not being transferred from said storage tank to said cryotank.

4. The method of claim 1, wherein the hydrogen flowing through said lines during periods when hydrogen is not being transferred from said storage tank to said cryotank is cooled prior to re-entering said storage tank.

5. The method of claim 1, wherein the pressure in said cryotank is reduced to atmospheric pressure prior to hydrogen transfer.

6. The method of claim 1, wherein the hydrogen is transferred to said cryotank by refuelling means which are constantly kept cold.

7. The method of claim 1, wherein after said step of transferring the hydrogen is complete, the hydrogen in said cryotank has a pressure and a temperature corresponding to a second undercooled state of liquid hydrogen.

8. The method of claim 1, wherein the hydrogen is transferred to said cryotank in the form of hydrogen sludge.

9. The method of claim 8, wherein the pressure in said cryotank is reduced to atmospheric pressure prior to hydrogen transfer.

10. The method of claim 1, wherein said liquid hydrogen is brought to said first undercooled state by using a cooling unit.

11. The method of claim 10, wherein the pressure in said cryotank is reduced to atmospheric pressure prior to hydrogen transfer.

12. The method of claim 10, wherein the hydrogen is transferred to said cryotank by a liquid hydrogen pump.