Method and apparatus for dispensing compressed natural gas and liquified natural gas to natural gas powered vehicles

• US 6,899,146 B2
• Filed: 05/09/2003
• Issued: 05/31/2005
• Est. Priority Date: 05/09/2003
• Status: Expired due to Term

• Current Assignee: Battelle Energy Alliance LLC (Battelle Memorial Institute)
• Original Assignee: Battelle Energy Alliance LLC (Battelle Memorial Institute)
• Inventors: Wilding, Bruce M., Clark, Michael L., Bingham, Dennis A., Palmer, Gary L.
• Primary Examiner(s): Maust, Timothy L.
• Application Number:
  US10/435,166
• Publication Number:
  US 20040250871A1
• Time in Patent Office: 753 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: 141/11
• 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:

at least one pump configured to boost a pressure of a volume of liquefied natural gas (LNG) supplied thereto, the at least one pump having at least one pressurized output configured to supply pressurized LNG;

at least one diverter valve operably coupled to the at least one pressurized output of the at least one pump, wherein the at least one diverter valve is configured to selectively divert the flow of any pressurized LNG flowing from the at least one pressurized output of the at least one pump between a first flow path and a second flow path;

at least one LNG dispensing unit in fluid communication with the first flow path;

a vaporizer in fluid communication with the second flow path, the vaporizer being 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 pressure reducing apparatus positioned in fluid communication with the first flow path between the at least one diverter valve and the at least one LNG dispensing unit.

3. The fueling station of claim 1, wherein the at least one pump includes at least one multiplex pump having a plurality pistons, wherein the at least one pressurized output includes a pressurized output associated with each piston of the plurality.

4. The fueling station of claim 3, wherein the at least one diverter valve includes a plurality of diverter valves, each diverter valve of the plurality being operably coupled to the pressurized output of at least one piston of the plurality of pistons.

5. The fueling station of claim 1, wherein the at least one diverter valve includes a plurality of diverter valves, each diverter valve being operably coupled to the at least one pressurized output of the at least one pump.

6. The fueling station of claim 1, wherein the at least one diverter valve includes a first diverter valve operably coupled with the first flow path and a second diverter valve operably coupled with the second flow path.

7. The fueling station of claim 1, further comprising a warming line configured to draw a portion of CNG produced by the vaporizer and to inject the portion of CNG into the first flow path.

8. The fueling station of claim 7, further comprising a pressure regulating valve operably coupled to the warming line, the pressure regulating valve being configured to reduce a pressure of the portion of CNG prior to its injection into the first flow path.

9. The fueling station of claim 8, wherein the pressure regulating valve includes a pilot-controlled pressure regulating valve.

10. The fueling station of claim 8, further comprising a first control valve operably coupled to the warming line downstream of the pressure regulating valve and configured to selectively control a flow rate of the portion of CNG injected into the first flow path.

11. The fueling station of claim 10, further comprising a cooling line configured to draw a portion of pressurized LNG from the at least one pressurized output and to inject the portion of pressurized LNG into a CNG flow path between the vaporizer and the CNG dispensing unit.

12. The fueling station of claim 11, further comprising a second control valve operably coupled to the cooling line and configured to selectively control a flow rate of the portion of pressurized LNG into the CNG flow path.

13. The fueling station of claim 12, further comprising a cold box to house and partially insulate the at least one diverter valve, the first flow path and at least a portion of the warming line.

14. The fueling station of claim 13, wherein a first portion of the at least one pump including the at least one pressurized output is located substantially inside the cold box.

15. The fueling station of claim 14, further comprising a skid wherein the at least one pump, the vaporizer and the cold box are mounted to the skid.

16. A method of dispensing natural gas fuel comprising:

providing a supply of saturated liquified natural gas (LNG) at a first relatively low pressure to a pump;

flowing the LNG through a pump and increasing the pressure of the LNG to a second relatively high pressure;

providing a first flow path between the pump and an LNG dispensing unit;

providing a second flow path between the pump and a compressed natural gas (CNG) dispensing unit;

selectively flowing the LNG through the first flow path, the second flow path or through both the first and the second flow paths;

reducing the pressure of any LNG flowing through the first flow path to a third intermediate pressure lower than the second pressure and higher than the first pressure and dispensing at least a portion thereof through the LNG dispensing unit; and

vaporizing any LNG flowing through the second flow path to produce CNG therefrom and dispensing at least a portion of the CNG through the CNG dispensing unit.

17. The method according to claim 16 further comprising drawing a portion of the CNG from second flow path and introducing it into the first flow path.

18. The method according to claim 17, further comprising monitoring the temperature of any LNG flowing through the first flow path and selectively controlling a flow rate of the portion of the CNG introduced from the second flow path to the first flow path.

19. The method according to claim 18, further comprising introducing a volume of LNG into the second flow path to cool any CNG flowing therethrough.

20. The method according to claim 19, further comprising monitoring the temperature of any CNG flowing through the second flow path and controlling the flow rate of the volume of LNG introduced into the second flow path.

21. The method according to claim 20, further comprising introducing an additive into the second flow path.

22. The method according to claim 21, wherein introducing an additive into the second flow path includes introducing an odorant into the second flow path.

23. The method according to claim 21, wherein introducing an additive into the second flow path includes introducing a lubricant into the second flow path.

24. The method according to claim 20, further comprising flowing at least a portion of any LNG in the first flow path back to the supply of LNG.

25. The method according to claim 24, further comprising flowing at least a portion of any CNG in the second flow path back to the supply of LNG.

26. The method according to claim 25, wherein vaporizing any LNG flowing along the second flow path to produce CNG therefrom includes flowing LNG through an ambient forced-air vaporizer.

27. The method according to claim 26, further comprising insulating at least a portion of the first flow path from an ambient temperature.

28. The method according to claim 27, further comprising flowing a portion of LNG directly from the supply of LNG to the first flow path prior to selectively flowing the LNG through the first flow path, through the second flow path or through both the first and the second flow paths.

29. The method according to claim 16, wherein the first pressure is as great as approximately 30 pounds per square inch absolute (psia), the second pressure is as great as approximately 5,000 psia and the third pressure is as great as approximately 300 psia.

30. The method according to claim 16, wherein vaporizing any LNG flowing through the second flow path to produce CNG therefrom and dispensing at least a portion of the CNG through the CNG dispensing unit further comprises flowing the at least a portion of the CNG from the vaporizer substantially directly to the CNG dispensing unit.

31. A method of dispensing natural gas fuel comprising:

providing a supply of saturated liquified natural gas (LNG) at a first relatively low pressure to a pump;

flowing the LNG through a pump and increasing the pressure of the LNG to a second pressure greater than the first relatively low pressure;

providing a first flow path between the pump and an LNG dispensing unit;

providing a second flow path between the pump and a compressed natural gas (CNG) dispensing unit;

selectively flowing the LNG through the first flow path, the second flow path or through both the first and the second flow paths wherein, selectively flowing the LNG through the first flow path includes selectively flowing LNG through the first flow path substantially at the second pressure, and wherein selectively flowing LNG through the second flow path includes increasing the pressure of any LNG flowing through the second path to a third pressure greater than the second pressure; and

dispensing at least a portion of any LNG flowing through the first flow path through the LNG dispensing unit; and

vaporizing any LNG flowing through the second flow path to produce CNG therefrom and dispensing at least a portion of the CNG through the CNG dispensing unit.