System for Producing Vehicle Fuel

• US 20180259248A1
• Filed: 03/13/2017
• Published: 09/13/2018
• Est. Priority Date: 03/13/2017
• Status: Abandoned Application

• Current Assignee: Baker Hughes, a GE Company, LLC (Baker Hughes Company)
• Original Assignee: General Electric Company
• Inventors: Repasky, John Michael
• Application Number:
  US15/457,607
• Publication Number:
  US 20180259248A1
• Time in Patent Office: Days
• CPC Class Codes: F17C 2270/0581 Power plants
• CPC Class Codes: F17C 5/04 requiring the use of refrigeration, e.g. filling with helium or hydrogen
• CPC Class Codes: F17C 5/06 for filling with compressed gases
• CPC Class Codes: F25J 1/0022 Hydrocarbons, e.g. natural gas
• CPC Class Codes: F25J 1/004 by flash gas recovery F25J1/0267 takes precedence
• CPC Class Codes: F25J 1/0052 by vaporising a liquid refrigerant stream
• CPC Class Codes: F25J 1/0212 as a single flow MCR cycle
• CPC Class Codes: F25J 1/023 for the combustion as fuels, i.e. integration with the fuel gas system
• CPC Class Codes: F25J 1/0242 Waste heat recovery, e.g. from heat of compression
• CPC Class Codes: F25J 1/0284 Electrical motor as the prime mechanical driver
• CPC Class Codes: F25J 2210/06 Splitting of the feed stream, e.g. for treating or cooling in different ways
• CPC Class Codes: F25J 2220/64 Separating heavy hydrocarbons, e.g. NGL, LPG, C4+ hydrocarbons or heavy condensates in general
• CPC Class Codes: F25J 2220/66 Separating acid gases, e.g. CO2, SO2, H2S or RSH
• CPC Class Codes: F25J 2230/30 Compression of the feed stream
• CPC Class Codes: F25J 2240/70 Steam turbine, e.g. used in a Rankine cycle
• CPC Class Codes: F25J 2240/82 with waste heat recovery, e.g. in a combined cycle, i.e. for generating steam used in a Rankine cycle
• CPC Class Codes: F25J 2245/90 the recycled stream being boil-off gas from storage

Abstract

Systems and methods for increasing the efficiency of liquefied natural gas (LNG) production, as well as facilitating coproduction of electric power, and compressed natural gas (CNG) are described. The systems and methods facilitate producing an intermediate LNG at a higher temperature, recovering refrigeration from flash gas and boil-off gas from the LNG, using flash-gas and boil-off gas as fuel to generate electric power, and providing LNG, CNG, and electric power to a vehicle fueling facility.

Claims

1. A system for producing vehicle fuel, comprising:

a liquefied natural gas (LNG) production facility configured to receive a natural gas from a natural gas source and to convert the natural gas to an LNG;

a compressed natural gas (CNG) production facility configured to receive a natural gas from the natural gas source and to compress the natural gas to form CNG; and

a power generation facility configured to receive at least one of a flash gas and a boil-off gas from the LNG production facility and to generate electric power.

2. The system of claim 1, wherein the power generation facility is configured to receive a natural gas from the natural gas source.

3. The system of claim 1, further comprising a vehicle fueling facility configured to receive the LNG from the LNG production facility and to dispense the LNG, to receive the electric power from the power generation facility and to dispense the electric power, and to receive the CNG from the CNG production facility and to dispense the CNG.

4. The system of claim 1, wherein the LNG production facility and the power generation facility are electrically coupled to facilitate delivering electric power from the power generation facility to the LNG production facility.

5. The system of claim 1, wherein the CNG production facility and the power generation facility are electrically coupled to facility delivering electric power from the power generation facility to the CNG production facility.

6. The system of claim 1, wherein the LNG production facility and the power generation facility are fluidly coupled to facilitate delivery of the at least one flash gas and boil-off gas from the LNG production facility to the power generation facility.

7. The system of claim 1, wherein the LNG production facility further includes a distillation system configured to separate heavy hydrocarbon components from a methane-containing fluid containing heavy hydrocarbon components.

8. The system of claim 1, further comprising a natural gas (NG) compression facility, the NG compression facility configured to receive a natural gas, and compress it such that portions of the compressed natural gas can be delivered to the LNG production facility and to the CNG production facility.

9. A vehicle fueling facility, comprising:

a first fuel source comprising a liquid natural gas (LNG) generated using natural gas from a natural gas source, a second fuel source comprising electric power generated using natural gas from the natural gas source, and a third fuel source comprising a compressed natural gas (CNG) generated using natural gas from the natural gas source.

10. The vehicle fueling facility of claim 9, wherein the vehicle fueling facility is coupled to an LNG production facility that supplies the first fuel source, a power generation facility that supplies the second fuel source, and a CNG production facility that supplies the third fuel source.

11. A method for producing vehicle fuel, comprising:

delivering a natural gas to a liquid natural gas (LNG) production facility, and condensing at least a portion of the natural gas to form an LNG for fueling a vehicle;

delivering a vapor comprising at least one of a flash gas and a boil-off gas formed from the LNG to a power generation facility, wherein at least a portion of the at least one flash gas and boil-off gas are used as fuel to generate electric power for fueling a vehicle; and

delivering a natural gas to a compressed natural gas (CNG) production facility that compresses at least a portion of the natural gas to form a CNG for fueling a vehicle.

12. The method of claim 11, wherein at least a portion of heat that is produced while generating electric power is delivered to at least one of a reboiler on an acid gas removal system, a dehydration dryer system, and a reboiler on a hydrocarbon distillation system.

13. The method of claim 12, wherein the heat is delivered using at least one of steam, oil, a gas produced from combustion of a fuel, natural gas, and air.

14. The method of claim 11, wherein the LNG is produced by pressure let-down and flash of a raw intermediate LNG which has a temperature greater than −

260°

F.

15. The method of claim 11, wherein the LNG is produced at a pressure less than 150 psig.

16. The method of claim 11, wherein the CNG is produced at a pressure less than 3600 psi.

17. The method of claim 11, wherein a portion of the electric power that is generated at the power generation facility is delivered to at least one of a local power consumer or a local power grid.

18. The method of claim 11, wherein the at least one of flash gas and boil-off gas is heated by at least one of a natural gas and a refrigerant fluid prior to being delivered to the power generation facility.

19. The method of claim 11, wherein a portion of the electric power generated in the power generation facility is delivered to the LNG production facility to power electric-motor driven compressors.

20. The method of claim 11, wherein a portion of the electric power generated in the power generation facility is delivered to the CNG production facility to power electric-motor driven compressors.