Liquefied natural gas transfer

• US 5,415,001 A
• Filed: 03/25/1994
• Issued: 05/16/1995
• Est. Priority Date: 03/25/1994
• Status: Expired due to Term

• Current Assignee: Gas Technology Institute (GTI Energy)
• Original Assignee: Gas Research Institute (GTI Energy)
• Inventors: Powars, Charles A.
• Primary Examiner(s): Capossela, Ronald C.
• Application Number:
  US08/217,929
• Time in Patent Office: 417 Days
• Field of Search: 62/9, 62/50.2, 62/47.1
• US Class Current: 62/50.2
• CPC Class Codes: F17C 2221/033 Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
• CPC Class Codes: F17C 2223/0169 subcooled
• CPC Class Codes: F17C 2223/033 Small pressure, e.g. for liquefied gas
• CPC Class Codes: F17C 2227/0107 by pressurising the ullage
• CPC Class Codes: F17C 2227/0341 using another fluid
• CPC Class Codes: F17C 2227/0374 in the liquid
• CPC Class Codes: F17C 2250/032 using computers
• CPC Class Codes: F17C 2250/0626 Pressure
• CPC Class Codes: F17C 2250/0636 Flow or movement of content
• CPC Class Codes: F17C 2260/025 Reducing transfer time
• CPC Class Codes: F17C 2260/031 due to heat transfer
• CPC Class Codes: F17C 2265/065 for refuelling vehicle fuel tanks
• CPC Class Codes: F17C 9/00 Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
• CPC Class Codes: F17C 9/04 Recovery of thermal energy

Abstract

A process and apparatus for transfer of liquefied natural gas from a storage tank in subcooled condition using liquefied nitrogen to subcool the liquefied natural gas and nitrogen vapor formed by thermal transfer between the liquefied natural gas and liquefied nitrogen as pressurant to drive the transfer of subcooled liquefied natural gas. This invention provides a liquefied natural gas vehicle refueling station which utilizes nitrogen as a propellant and avoids venting natural gas to the atmosphere.

Claims

1. In a process for transfer of liquefied natural gas from a storage tank, the improvement comprising;

passing liquid nitrogen in heat exchange relation with said liquefied natural gas in said storage tank subcooling said liquefied natural gas to about 10°

to about 60°

F. below the boiling temperature of said liquefied natural gas in said storage tank, and vaporizing liquid nitrogen by said heat exchange with said liquefied natural gas causing pressurization of nitrogen vapor in the ullage of said storage tank sufficient to act as a pressurant for said transfer in a transfer mode.

2. In a process for transfer according to claim 1 wherein said liquefied natural gas in said storage tank is subcooled to about 15°

to about 40°

F. below the boiling temperature of said liquefied natural gas in said storage tank.

3. In a process for transfer according to claim 1 wherein the pressure in said storage tank is maintained at above atmospheric to about 20 psia in a storage mode.

4. In a process for transfer according to claim 1 wherein the pressure in said storage tank is maintained at about 30 to about 90 psia above desired transfer pressure in said transfer mode.

5. In a process for transfer according to claim 1 wherein the pressure in said storage tank is maintained at about 50 to about 70 psia above desired transfer pressure in said transfer mode.

6. In a process for transfer according to claim 1 wherein said liquefied natural gas storage tank pressure is reduced by venting said nitrogen vapor from said ullage.

7. In a process for transfer according to claim 1 additionally comprising circulating said subcooled liquefied natural gas through a transfer line and back to said storage tank prior to said transfer.

8. A process for transfer of liquefied natural gas from a liquefied natural gas storage tank comprising:

passing liquid nitrogen in heat exchange relation with said liquefied natural gas in said liquefied natural gas storage tank producing subcooled liquefied natural gas;

vaporizing at least a portion of said liquid nitrogen by said heat exchange with said liquefied natural gas sufficient to cause pressurization of substantially nitrogen vapor in the ullage of said liquefied natural gas storage tank; and

passing said subcooled liquefied natural gas from said liquefied natural gas storage tank in a delivery mode driven by said pressurization of said substantially nitrogen vapor in the ullage of said liquefied natural gas storage tank.

9. A process according to claim 8 wherein said subcooled liquefied natural gas is about 10°

to about 60°

F. below the boiling temperature of said liquefied natural gas in said liquefied natural gas storage tank.

10. A process according to claim 9 wherein said temperature is about 15°

to about 40°

F.

11. A process according to claim 8 wherein said pressurization in said delivery mode is about 30 to about 90 psia above desired transfer pressure.

12. A process according to claim 11 wherein said pressurization is about 50 to about 70 psia above desired transfer pressure.

13. A process according to claim 8 further comprising:

venting said substantially nitrogen vapor from said ullage of said liquefied natural gas storage tank following said passing said subcooled liquefied natural gas from said liquefied natural gas storage tank so as to reduce pressure in said liquefied natural gas storage tank to a pressure above atmospheric up to about 20 psia for a storage mode.

14. A process according to claim 8 further comprising:

storing saturated liquid nitrogen in a liquid nitrogen storage tank; and

vaporizing a portion of said saturated liquid nitrogen sufficient to maintain saturated nitrogen vapor in the ullage of said liquid nitrogen storage tank under pressure sufficient to pass a portion of said liquid nitrogen to said heat exchange relation with said liquefied natural gas.

15. A process according to claim 14 further comprising:

passing said subcooled liquefied natural gas to a vehicle liquefied natural gas tank; and

introducing said subcooled natural gas into the ullage of said vehicle liquefied natural gas tank condensing at least a portion of any vaporized natural gas in said ullage of said vehicle liquefied natural gas tank.

16. A process according to claim 14 wherein said subcooled liquefied natural gas is about 10°

to about 60°

F. below the boiling temperature of said liquefied natural gas in said liquefied natural gas storage tank.

17. A process according to claim 14 further comprising:

venting said substantially nitrogen vapor from said ullage of said liquefied natural gas storage tank following said passing said subcooled liquefied natural gas from said liquefied natural gas storage tank so as to reduce pressure in said liquefied natural gas storage tank to a pressure above atmospheric up to about 20 psia for a storage mode.

18. A process according to claim 14 further comprising:

passing said subcooled liquefied natural gas to a vehicle liquefied natural gas tank;

introducing said subcooled natural gas into the ullage of said vehicle liquefied natural gas tank condensing at least a portion of any vaporized natural gas in said ullage of said vehicle liquefied natural gas tank;

maintaining said subcooled liquefied natural gas at about 10°

to about 60°

F. below the boiling temperature of said liquefied natural gas in said liquefied natural gas storage tank; and

venting said substantially nitrogen vapor from said ullage of said liquefied natural gas storage tank following said passing said subcooled liquefied natural gas from said liquefied natural gas storage tank so as to reduce pressure in said liquefied natural gas storage tank to above atmospheric to about 20 psia for a storage mode.

19. A process according to claim 14 wherein said liquefied natural gas storage tank and said liquid nitrogen storage tank are on-board a vehicle to supply vehicle fuel supply pressures and lengthen said vehicle tank hold-time.

20. An apparatus for transfer of liquefied natural gas from a storage tank comprising:

a liquefied natural gas storage tank having liquefied natural gas therein;

a pressure control valve in gaseous communication with the ullage of said liquefied natural gas storage tank;

a liquefied natural gas transfer line having one end in liquid communication with said liquefied natural gas;

a flow control valve in said liquefied natural gas transfer line;

flow through heat exchanger means in thermal exchange relation with said liquefied natural gas, said flow through heat exchanger means having a downstream open end;

liquefied natural gas temperature and pressure sensing means;

a liquefied nitrogen storage tank having liquefied nitrogen therein;

a nitrogen pressure control valve in gaseous communication with the ullage of said liquefied nitrogen storage tank;

a liquefied nitrogen transfer line having an upstream end in liquid communication with said liquefied nitrogen and a downstream end in liquid communication with the upstream end of said flow through heat exchanger means;

a flow control valve in said liquefied nitrogen transfer line;

adjustable heater means in thermal exchange relation with said liquefied nitrogen; and

liquefied nitrogen temperature and pressure sensing means.