Liquiefying a gaseous medium

Patent metadata

Field	Value
Publication number	US-10760740-B2
Application number	US-201816042215-A
Country	US
Kind code	B2
Filing date	Jul 23, 2018
Priority date	Jul 25, 2017
Publication date	Sep 1, 2020
Grant date	Sep 1, 2020

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. A first transfer line is provided which is connected between the liquefaction plant and the storage tank, for transferring liquefied medium from the liquefaction plant into the storage tank. A 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. The second transfer line, which used for transferring medium from the storage tank into the liquefaction plant, is arranged so that it is routed at least partially through the area of the storage tank in which the liquefied medium is stored in use.

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,
a 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),
a second transfer line ( 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), 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,
at least one first shut-off valve (a) provided in said first transfer lines ( 3 ) and at least one second shut-off valve provided in said second transfer line ( 4 ′, 4 ″),
a bypass line ( 5 ) connecting the first and second transfer lines ( 3 , 4 ′, 4 ″), and a bypass shut-off valve (c) provided in the by-pass line ( 5 ), wherein the bypass line ( 5 ) connects the first and second transfer lines ( 3 , 4 ′, 4 ″) at a point between the liquefaction plant (V) and the shut-off valves (a, b) of the first and second transfer lines, and
a control element, wherein the control element is configured such that, after a standstill phase of the liquefaction plant (V) and before the transfer of liquefied medium from the liquefaction plant (V) into the storage tank (S), the control element 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 via partial sections of the first transfer line ( 3 ), the bypass line ( 5 ), the second transfer line ( 4 ′, 4 ″) transfer lines ( 3 , 4 ′, 4 ″), and back into the liquefaction plant (V).

2. An arrangement according to claim 1 , 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 ( 4 ′, 4 ″) 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.

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

4. The arrangement according to claim 1 ,
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 4 , 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 ( 4 ′, 4 ″) is provide adjacent to a second side wall, provided on the side of the tank (S) opposite to the first side wall.

6. The arrangement according to claim 1 , wherein the second transfer line ( 474 ″) is routed through the area of the storage tank (S) from one end of the storage tank to another end of the storage tank.

7. 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 ).

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

9. 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 in a cooling mode wherein
liquid medium is fed through the by-pass line that connects the first transfer line and the second transfer line, so as 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).

10. The method according to claim 9 , wherein the cooling mode comprises:
closing the shut-off valves (a, b) in the first and second transfer lines, and
opening the bypass line shut-off valve (c), so that liquefied medium is led from the liquefaction plant (V), through the first transfer line ( 3 ), the bypass valve ( 5 ), and the second transfer line ( 4 ′, 4 ″), and back into the liquefaction plant (V).

11. The method according to claim 9 , wherein the cooling mode is carried out until a predetermined temperature has been reached in at least one section of the first and second transfer lines ( 3 , 4 , 4 ′, 4 ′).

12. The method according to claim 9 , wherein the medium to be liquefied is hydrogen, a noble gas, oxygen, nitrogen, or a hydrocarbon mixture.

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

14. The arrangement according to claim 8 , wherein all of the transfer lines are vacuum insulated.

15. The method according to claim 9 , wherein the medium to be liquefied is hydrogen, helium, neon, argon, oxygen, nitrogen, or natural gas.

16. A method for cooling the transfer lines ( 3 , 4 , 4 ′) of an arrangement, said 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,
a 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),
a second transfer line ( 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), 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,
at least one first shut-off valve (a) provided in said first transfer lines ( 3 ) and at least one second shut-off valve provided in said second transfer line ( 4 ′, 4 ″),
a bypass line ( 5 ) connecting the first and second transfer lines ( 3 , 4 ′, 4 ″), and a bypass shut-off valve (c) provided in the by-pass line ( 5 ), wherein the bypass line ( 5 ) connects the first and second transfer lines ( 3 , 4 ′, 4 ″) at a point between the liquefaction plant (V) and the shut-off valves (a, b) of the first and second transfer lines,
the method comprising, after a standstill phase of the liquefaction plant (V):
(a) operating in a cooling mode wherein liquid medium is fed through the by-pass line that connects the first transfer line and the second transfer line, so as to by-pass the storage tank (S), wherein the cooling mode comprises:
closing the shut-off valves (a, b) in the first and second transfer lines, and
opening the bypass line shut-off valve (c), so that liquefied medium is led from the liquefaction plant (V), through the first transfer line ( 3 ), the bypass valve ( 5 ), and the second transfer line ( 4 ′, 4 ″), and back into 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).

17. A method for cooling the transfer lines ( 3 , 4 , 4 ′) of an arrangement, said 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

Assignees

• Linde Ag

Inventors

• Dachauer Christian
• Wilhelm Hanspeter
• Keller Lukas

Classifications

• F25J2215/32

  Neon · CPC title

• F25J1/0022

  Hydrocarbons, e.g. natural gas · CPC title

• F25J1/0017

  Oxygen · CPC title

• F25J1/0007

  Helium · CPC title

• F25J1/004

  by flash gas recovery (F25J1/0267 takes precedence) · CPC title