Liquiefying a gaseous medium

Patent metadata

Field	Value
Publication number	US-10976102-B2
Application number	US-201816043742-A
Country	US
Kind code	B2
Filing date	Jul 24, 2018
Priority date	Jul 25, 2017
Publication date	Apr 13, 2021
Grant date	Apr 13, 2021

Abstract

An arrangement comprising at least one liquefaction plant for liquefying a gaseous medium to produce a liquefied medium; and at least one storage tank for storing the liquefied medium. At least one first transfer line is connected between the liquefaction plant and the storage tank, for transferring liquefied medium from the liquefaction plant into the storage tank. At least one second transfer line is connected between the liquefaction plant and the storage tank, for transferring gaseous medium from the storage tank into the liquefaction plant. At least one shut-off valve is provided in each transfer line. The apparatus further includes a bypass line.

First claim

The invention claimed is:

1. An arrangement comprising:
at least one liquefaction plant (V) for liquefying a gaseous medium to produce a liquefied medium;
at least one storage tank (S) for storing the liquefied medium;
at least one first transfer line ( 3 ) connected between the liquefaction plant (V) and the storage tank (S), for transferring liquefied medium from the liquefaction plant (V) into the storage tank (S), said at least one first transfer line having at least one first shut-off valve (a);
at least one second transfer line ( 4 , 4 ′, 4 ″), connected between the liquefaction plant (V) and the storage tank (S), for transferring gaseous medium from the storage tank (S) into the liquefaction plant (V), said at least one second transfer line having at least one second shut-off valve (b);
a bypass line ( 5 ) connecting the at least one first transfer line ( 3 ) to the at least one second transfer line ( 3 , 4 , 4 ′, 4 ″); and
a bypass shut-off valve (c) provided in the by-pass line ( 5 );
wherein the bypass line ( 5 ) connects said at least one first transfer line and said at least one second transfer line ( 3 , 4 , 4 ′, 4 ″) at a point between the liquefaction plant (V) and the shut-off valves (a, b) of the transfer lines.

2. The arrangement according to claim 1 , further comprising a control element, wherein the control element, after a standstill phase of the liquefaction plant (V) and before transfer of liquefied medium from the liquefaction plant (V) into the storage tank (S), performs a transfer line cooling phase, in which the shut-off valves (a, b) of the transfer lines are closed and the bypass line shut-off valve (c) is opened, so that liquefied medium from the liquefaction plant (V) can flow through partial sections of the at least one first transfer line ( 3 ), the bypass line ( 5 ), the at least one second transfer line ( 4 , 4 ′, 4 ″), and back into the liquefaction plant (V).

3. The arrangement according to claim 1 , wherein the bypass line ( 5 ) is arranged substantially adjacent to the storage tank (S).

4. The arrangement according to claim 1 , wherein said arrangement comprises only one first transfer line ( 3 ) having one first shut-off valve (a), and only one second transfer line ( 4 , 4 ′, 4 ″) having one second shut-off valve (b), and
wherein the bypass line ( 5 ) is connected between a point on the first transfer line ( 3 ) upstream of the first shut-off valve (a) and a point on the second transfer line ( 4 , 4 ′, 4 ″) downstream of the second shut-off valve (b).

5. The arrangement according to claim 1 , wherein the second transfer line ( 4 ′, 4 ″) is routed at least partially through an area of the storage tank (S) in which the liquefied medium is stored in use.

6. The arrangement according to claim 5 , wherein an outlet of the first transfer line ( 3 ) into the storage tank (S) is provided adjacent to a first side wall of the tank (S) and an inlet of the second transfer line is provide adjacent to a second side wall, said second side wall being provided on the side of the tank (S) opposite to the first side wall.

7. The arrangement according to claim 1 , wherein the at least one second transfer line ( 4 ) is not routed through an area of the storage tank (S) in which the liquefied medium is stored in use.

8. The arrangement according to claim 1 , wherein the storage tank (S) is a double-walled tank, having an outer tank ( 1 ) and an inner tank ( 2 ).

9. The arrangement according to claim 1 , wherein at least some of the transfer lines are vacuum insulated.

10. A method for cooling the transfer lines ( 3 , 4 , 4 ′) of an arrangement according to claim 1 , after a standstill phase of the liquefaction plant (V), the method comprising:
operating a cooling mode wherein liquid medium is fed through the by-pass line that connects the at least one first transfer line and the at least one second transfer line, to by-pass the storage tank (S), and
switching to a normal transfer mode wherein liquefied medium is transferred from the liquefaction plant (V) into the storage tank (S).

11. The method according to claim 10 , wherein the cooling mode comprises:
closing transfer line shut-off valves (a, b) and
opening bypass line shut-off valve (c), so that liquefied medium is led from the liquefaction plant (V), through the at least one first transfer line ( 3 ), the bypass valve ( 5 ), and the at least one second transfer line ( 4 , 4 ′, 4 ″), and back into the liquefaction plant (V).

12. The method according to claim 10 , wherein the cooling mode is carried out until a predetermined temperature has been reached in at least one section of the transfer lines ( 3 , 4 , 4 ′, 4 ′).

13. The method according to claim 10 , wherein the medium to be liquefied is hydrogen, a noble gas, oxygen, nitrogen, or a hydrocarbon mixture.

14. The arrangement according to claim 1 , wherein the storage tank (S) is a vacuum insulated storage tank.

15. The method according to claim 13 , wherein the medium to be liquefied is hydrogen, neon, argon, oxygen, nitrogen, or natural gas.

16. A method for cooling the transfer lines ( 3 , 4 , 4 ′) of an arrangement according to claim 1 , after a standstill phase of the liquefaction plant (V), the method comprising:
(a) operating a cooling mode wherein liquid medium is fed through the by-pass line that connects the at least one first transfer line and the at least one second transfer line, to by-pass the storage tank (S) and conduct liquid medium through part of said at least one first transfer line, said by-pass line, and part of said at least one second transfer line back to the liquefaction plant (V), and
(b) switching to a normal transfer mode wherein liquefied medium is transferred from the liquefaction plant (V) into the storage tank (S).

Assignees

• Linde Ag

Inventors

• Fisel Wolfgang
• Keller Lukas
• Rautert Kim

Classifications

• F25J1/0007 Primary

  Helium · CPC title

• F25J1/0017

  Oxygen · CPC title

• F25J1/002

  Argon · CPC title

• F25J1/0247

  start-up of the process · CPC title

• F25J1/001

  Hydrogen · CPC title