System and method for refueling and backup power generation

Patent metadata

Field	Value
Publication number	US-11608938-B2
Application number	US-202117371175-A
Country	US
Kind code	B2
Filing date	Jul 9, 2021
Priority date	Jul 9, 2021
Publication date	Mar 21, 2023
Grant date	Mar 21, 2023

Abstract

A system such as a hydrogen refueling station and a method are provided. The system includes a cryotank for storing a liquefied fuel having liquid and vapor phases, a pump for providing a first stream of the liquefied fuel in the liquid phase from the cryotank, a heat exchanger for converting at least a portion of the first stream to a gaseous fuel, a dispenser for dispensing at least a portion of the gaseous fuel to a receiving fuel tank, a refrigeration unit integrated with the heat exchanger, and a backup power unit. The refrigeration unit and the heat exchanger exchange heat with each other, and the refrigeration unit provides cooling capacity to a facility of environment where cooling is needed. The backup power unit generate electric power by using a second stream of the liquefied fuel in the vapor phase or in the liquid phase or both.

First claim

What is claimed is:

1. A system, comprising:
a cryotank configured to store a liquefied fuel therein, the liquefied fuel comprising a liquid phase and a vapor phase;
a pump fluidly coupled with the cryotank and configured to provide a first stream of the liquefied fuel in the liquid phase from the cryotank;
a heat exchanger coupled with the pump and configured to convert at least a portion of the first stream of the liquefied fuel in the liquid phase to a gaseous fuel; a
dispenser configured to dispense at least a portion of the gaseous fuel to a receiving fuel tank;
a refrigeration unit integrated with the heat exchanger, wherein the refrigeration unit is configured to provide heat duty to the heat exchanger, and the heat exchanger is configured to provide cooling duty to the refrigeration unit; and
a backup power unit configured to receive a second stream of the liquefied fuel in the vapor phase or in the liquid phase or both from the cryotank and generate electrical power.

2. The system of claim 1 , wherein the liquefied fuel comprises hydrogen.

3. The system of claim 1 , wherein the pump is a submerged liquid pump disposed inside the cryotank and configured to compress the first stream of the liquefied fuel in the liquid phase.

4. The system of claim 1 , further comprising a splitter disposed between the pump and the heat exchanger and configured to split the first stream of the liquefied fuel into a first portion and a second portion, wherein the heat exchanger is configured to convert the first portion to the gaseous fuel.

5. The system of claim 4 , further comprising a mixer configured to combine the gaseous fuel and the second portion to form a compressed gaseous fuel or a liquid fuel to be dispensed.

6. The system of claim 1 , wherein the gaseous fuel is compressed hydrogen having a pressure in a range of from 25 MPa to 90 MPa and a temperature in a range of from −50° C. to ambient temperature.

7. The system of claim 1 , wherein the backup power unit is configured to receive less than 30% by weight of a total storage capacity for the liquefied fuel in the cryotank in one day.

8. The system of claim 1 , wherein the backup power unit is configured to receive no more than 20% by weight of a total storage capacity for the liquefied fuel in the cryotank in one day.

9. The system of claim 1 , wherein the backup power unit is configured to provide the electricity power to a data center, and the refrigeration unit is configured to provide cooling capacity to the data center.

10. The system of claim 1 , wherein the backup power unit comprises one or more fuel cells or combustion engines to generate the electrical power from the second stream of the liquefied fuel in the vapor phase or the liquid phase or both.

11. The system of claim 1 , wherein the backup power unit is configured to further receive at least a portion of the gaseous fuel from the heat exchanger to generate the electrical power.

12. The system of claim 1 , further comprising a liquefier fluidly coupled with the cryotank and a production unit fluidly coupled with the liquefier, wherein the liquefier is configured to compress a gas generated in the production unit to the liquefied fuel.

13. The system of claim 12 , wherein the production unit comprises at least one electrolyzer for producing hydrogen gas from water, and the at least one electrolyzer or the liquefier or both configured to be at least partially powered by solar or wind power.

14. A method, comprising:
providing a liquefied fuel stored inside a cryotank, the liquefied fuel comprising a liquid phase and a vapor phase;
pumping a first stream of the liquefied fuel in the liquid phase from the cryotank through a pump fluidly coupled with the cryotank;
converting at least a portion of the first stream of the liquefied fuel in the liquid phase to a gaseous fuel through a heat exchanger coupled with the pump;
dispensing at least a portion of the gaseous fuel to a receiving fuel tank;
providing cooling capacity from a refrigeration unit integrated with the heat exchanger to a facility in need thereof; and
generating electrical power in a backup power unit using a second stream of the liquefied fuel in the vapor phase or in the liquid phase or both from the cryotank.

15. The method of claim 14 , wherein the liquefied fuel comprises hydrogen.

16. The method of claim 14 , wherein the first stream of the liquefied fuel in the liquid phase is pumped from the cryotank by compressing the liquefied fuel using a submerged liquid pump disposed inside the cryotank.

17. The method of claim 14 , further comprising providing heat duty from the refrigeration unit to the heat exchanger; and providing cooling duty from the heat exchanger to the refrigeration unit.

18. The method of claim 14 , further splitting the first stream of the liquefied fuel into a first portion and a second portion, wherein the first portion goes through the heat exchanger.

19. The method of claim 18 , further comprising combining the gaseous fuel and the second portion to form a compressed gaseous fuel or a liquid fuel to be dispensed.

20. The method of claim 14 , wherein less than 30% by weight of a total storage capacity for the liquefied fuel in the cryotank is provided to the backup power unit in one day when backup power is needed.

21. The method of claim 14 , wherein electricity power is provided from the backup power unit to a data center, and the cooling capacity from the refrigeration unit is used for cooling the data center.

22. The method of claim 14 , wherein the electrical power is generated through one or more fuel cells or combustion engine in the backup power unit.

23. The method of claim 22 , further comprising supplying at least a portion of the gaseous fuel from the heat exchanger to the backup power unit for generating the electrical power.

24. The method of claim 14 , wherein the liquefied fuel in the cryotank is provided from a liquefier fluidly coupled with the cryotank, wherein the liquefier is configured to compress a gas generated in a production unit to the liquefied fuel.

25. The method of claim 24 , wherein the production unit comprises at least one electrolyzer for producing hydrogen gas from water, and the at least one electrolyzer or the liquefier or both are at least partially powered by solar or wind power.

Assignees

• China Energy Investment Corp Ltd
• Nat Inst Clean & Low Carbon Energy

Inventors

• Ku Anthony
• Li Xianming
• Ramteke Ashwin
• Stager Jerad Allen

Classifications

• F17C2227/0302

  by heating · CPC title

• C25B1/04

  by electrolysis of water · CPC title

• F17C2225/0123

  gaseous, e.g. CNG, GNC · CPC title

• F17C2265/063

  for supply of refuelling stations · CPC title

• F17C2227/0135

  Pumps · CPC title