Apparatus for dispensing compressed natural gas and liquified natural gas to natural gas powered vehicles

• US 7,222,647 B2
• Filed: 02/02/2005
• Issued: 05/29/2007
• Est. Priority Date: 05/09/2003
• Status: Active Grant

• Current Assignee: Battelle Energy Alliance LLC (Battelle Memorial Institute)
• Original Assignee: Battelle Energy Alliance LLC (Battelle Memorial Institute)
• Inventors: Wilding, Bruce M., Palmer, Gary L., Clark, Michael L., Bingham, Dennis A.
• Primary Examiner(s): Douglas; Steven O.
• Application Number:
  US11/050,032
• Publication Number:
  US 20060169352A1
• Time in Patent Office: 846 Days
• Field of Search: 141/1, 141/2, 141/4, 141/5, 141/11, 141/18, 141/82, 62/501, 62/502
• US Class Current: 141/82
• CPC Class Codes: F17C 2221/033 Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
• 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 2225/0123 gaseous, e.g. CNG, GNC
• 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 2225/036 Very high pressure, i.e. above 80 bars
• CPC Class Codes: F17C 2227/0393 using a vaporiser
• CPC Class Codes: F17C 2265/05 Regasification
• CPC Class Codes: F17C 2270/00 Applications
• CPC Class Codes: F17C 2270/0139 Fuel stations
• CPC Class Codes: F17C 7/02 Discharging liquefied gases
• CPC Class Codes: F17C 7/04 with change of state, e.g. vaporisation

Abstract

A fueling facility and method for dispensing liquid natural gas (LNG), compressed natural gas (CNG) or both on-demand. The fueling facility may include a source of LNG, such as cryogenic storage vessel. A low volume high pressure pump is coupled to the source of LNG to produce a stream of pressurized LNG. The stream of pressurized LNG may be selectively directed through an LNG flow path or to a CNG flow path which includes a vaporizer configured to produce CNG from the pressurized LNG. A portion of the CNG may be drawn from the CNG flow path and introduced into the CNG flow path to control the temperature of LNG flowing therethrough. Similarly, a portion of the LNG may be drawn from the LNG flow path and introduced into the CNG flow path to control the temperature of CNG flowing therethrough.

Claims

1. A fueling station comprising:

a multiplex pump configured to boost the pressure of a volume of liquified natural gas (LNG) supplied thereto, the multiplex pump including at least two pistons wherein each piston has an individual pressurized output configured to supply pressurized LNG;

at least one LNG dispensing unit in selective fluid communication with the pressurized output of each of the at least two pistons of the multiplex pump;

a vaporizer in selective fluid communication with the pressurized output of each of the at least two pistons of the multiplex pump, the vaporizer configured to receive and convert pressurized LNG to compressed natural gas (CNG); and

at least one CNG dispensing unit in fluid communication with the vaporizer.

2. The fueling station of claim 1, further comprising at least one diverter valve operably coupled to the pressurized output at least one piston of the at least two pistons, wherein the at least one diverter valve is configured to selectively divert the flow of any pressurized LNG flowing from the pressurized output of the at least one piston between the at least one LNG dispensing unit and the vaporizer.

3. The fueling station of claim 1, further comprising at least two diverter valves, each diverter valve of the at least two diverter valves being operably coupled to the pressurized output of one piston of the at least two pistons and wherein each diverter valve is configured to selectively divert the flow of any pressurized LNG flowing from the pressurized output of an associated piston between the at least one LNG dispensing unit and the vaporizer.

4. The fueling station of claim 3, wherein the at least two diverter valves are configured such that at least one of the at least two diverter valves may be in an open state while at least one other diverter valve is in a closed state.

5. The fueling station of claim 4, wherein the multiplex pump further comprises a triplex pump wherein the at least two pistons includes three pistons and wherein the at least two diverter valves includes three diverter valves.

6. The fueling station of claim 5, wherein the triplex pump is configured to increase the pressure of the volume of LNG passing therethrough up to approximately 5,000 psia.

7. The fueling station of claim 6, wherein the vaporizer is configured to receive any pressurized LNG passing therethrough at a pressure of up to approximately 5,000 psia and to produce CNG at a flow rate of up to 1,600 standard cubic feet per minute (scfm).

8. The fueling station of claim 4, wherein the at least two diverter valves are configured to reduce the pressure of any pressurized LNG passing therethrough from up to approximately 5,000 psia to approximately 300 psia.

9. The fueling station of claim 5, further comprising a CNG warming line configured to draw a portion of CNG produced by the vaporizer and to inject the portion of CNG into an LNG flow path between at least one of the three diverter valves and the LNG dispensing unit.

10. The fueling station of claim 9, further comprising a pressure regulating valve operably coupled to the CNG warming line.

11. The fueling station of claim 10, wherein the pressure regulating valve is configured to reduce the pressure of a volume of CNG flowing therethrough from a pressure of up to approximately 5,000 psia to a pressure of approximately 300 psia.

12. The fueling station of claim 10, wherein the pressure regulating valve further comprises a pilot-controlled pressure regulating valve.

13. The fueling station of claim 10, further comprising a first control valve operatively coupled to the CNG warming line downstream from the pressure regulating valve and configured to selectively control a flow rate of the portion of CNG injected into the LNG flow path.

14. The fueling station of claim 13, further comprising a cooling line configured to draw a portion of pressurized LNG from at least one piston of the three pistons and to inject the portion of LNG into a CNG flow path between the vaporizer and the CNG dispensing unit.

15. The fueling station of claim 14, further comprising a second control valve operatively coupled to the cooling line and configured to selectively control a flow rate of the portion of LNG injected into the CNG flow path.

16. The fueling station of claim 15, further comprising at least one source of an additive in fluid communication with the CNG flow path and configured to inject the additive thereinto.

17. The fueling station of claim 16, wherein the at least one source of an additive includes a source of odorant.

18. The fueling station of claim 17, wherein the source of odorant is coupled with the CNG flow path at a location upstream of the CNG warming line.

19. The fueling station of claim 16, wherein the at least one source of an additive includes a source of lubricant.

20. The fueling station of claim 19, wherein the source of lubricant is coupled with the CNG flow path at a location downstream of the CNG warming line.

21. The fueling station of claim 15, wherein the triplex pump is in fluid communication with a source of LNG.

22. The fueling station of claim 21, further comprising an LNG circulation line in fluid communication with the LNG flow path and configured to selectively circulate LNG back to the source of LNG.

23. The fueling station of claim 22, further comprising a CNG circulation line in fluid communication with the CNG flow path and configured to selectively circulate CNG back to the source of LNG.

24. The fueling station of claim 23, wherein the source of LNG includes a volume of LNG and a volume of vapor in fluid communication with the volume of LNG, and wherein the CNG circulation line is configured to selectively circulate CNG back to the volume of LNG and to selectively circulate CNG back to the volume of vapor.

25. The fueling station of claim 24, further comprising a cold box configured to house and thermally insulate the three diverter valves, the LNG flow path, at least a portion of the CNG warming line and the LNG circulation line from a surrounding environment.

26. The fueling station of claim 25, wherein the a majority of the triplex pump is configured and located to reside substantially outside of the cold box and wherein the three pistons of the triplex pump having their associated pressurized outputs located substantially inside the cold box.

27. The fueling station of claim 26, wherein the vaporizer, the CNG flow path and the at least one source of an additive are located outside of the cold box.

28. The fueling station of claim 27, wherein the vaporizer is configured as a forced-air ambient vaporizer.

29. The fueling station of claim 28, further comprising an LNG bypass line fluidly coupled between the source of LNG and the LNG flow path and configured to provide a volume of LNG to the LNG flow path prior to the presence of any pressurized LNG in the LNG flow path from the triplex pump.

30. The fueling station of claim 29, further comprising a check valve operatively coupled with the LNG bypass line and configured to prevent pressurized LNG from flowing back to the source of LNG.

31. The fueling station of claim 30, further comprising a skid wherein at least the triplex pump, the vaporizer and the cold box are mounted to the skid.

32. A natural gas fueling facility comprising:

a source of saturated liquified natural gas (LNG);

at least one fueling station comprising;

a multiplex pump in fluid communication with the source of LNG, the multiplex pump including at least two pistons wherein each piston has an individual pressurized output configured to supply pressurized LNG;

at least one LNG dispensing unit in selective fluid communication with the pressurized output of each of the at least two pistons of the multiplex pump;

a vaporizer in selective fluid communication with the pressurized output of each of the at least two pistons of the multiplex pump, the vaporized configured to receive and convert LNG to compressed natural gas (CNG); and

at least one CNG dispensing unit in fluid communication with the vaporizer.

33. The natural gas fueling facility of claim 32, wherein the source of LNG includes a pressure vessel containing a volume of LNG and a volume of vapor contiguous with the volume of LNG.

34. The natural gas fueling facility of claim 33, wherein the pressure vessel is configured to contain the volume of LNG and the volume of vapor at a pressure of up to approximately 30 pounds per square inch absolute (psia).

35. The natural gas fueling facility of claim 33, further comprising a skid, wherein the at least one fueling station is mounted on the skid.

36. The natural gas fueling facility of claim 32, wherein the at least one fueling station further comprises at least one diverter valve operably coupled to the pressurized output of at least one piston of the at least two pistons and wherein the at least one diverter valve is configured to selectively divert the flow of any pressurized LNG flowing from the pressurized output of the at least one piston between the at least one LNG dispensing unit and the vaporizer.

37. The natural gas fueling facility of claim 32, wherein the at least one fueling station further comprises at least two diverter valves, each diverter valve of the at least two diverter valves being operably coupled to the pressurized output of one piston of the at least two pistons and wherein each diverter valve is configured to selectively divert the flow of any pressurized LNG flowing from its associated piston'"'"'s pressurized output between the at least one LNG dispensing unit and the vaporizer.

38. The natural gas fueling facility of claim 37, wherein the at least two diverter valves are configured such that at least one of the at least two diverter valves may be in an open state while at least one other diverter valve is in a closed state.

39. The natural gas fueling facility of claim 38, wherein the at least one fueling station includes two fueling stations.