Mobile natural gas storage and transportation unit based on adsorption

Patent metadata

Field	Value
Publication number	US-11149905-B2
Application number	US-201916591907-A
Country	US
Kind code	B2
Filing date	Oct 3, 2019
Priority date	Oct 3, 2019
Publication date	Oct 19, 2021
Grant date	Oct 19, 2021

Abstract

Systems and methods for natural gas storage and transport with a mobile unit, the method including charging a mobile natural gas storage and transport unit with natural gas via adsorption of the natural gas on adsorbent materials disposed within the natural gas storage and transport unit; transporting the natural gas storage and transport unit a distance to proximate a natural gas power generation unit; and discharging the natural gas over time via desorption of the natural gas from the adsorbent materials to power the natural gas power generation unit.

First claim

What is claimed is:

1. A method for natural gas storage and transport with a mobile unit, the method comprising the steps of:
charging a mobile natural gas storage and transport unit with natural gas via adsorption of the natural gas on adsorbent materials disposed within the mobile natural gas storage and transport unit;
transporting the mobile natural gas storage and transport unit a distance to proximate a natural gas power generation unit; and
discharging the natural gas over time via desorption of the natural gas from the adsorbent materials to power the natural gas power generation unit.

2. The method according to claim 1 , where the step of charging lasts for between about 1 hour and about 5 hours.

3. The method according to claim 1 , where the step of charging lasts for about 3 hours.

4. The method according to claim 1 , where the adsorbent materials comprise microporous adsorbent materials.

5. The method according to claim 4 , where the microporous adsorbent materials comprise at least one of activated carbon or silica zeolites.

6. The method according to claim 1 , where the step of transporting does not consume natural gas adsorbed to the adsorbent materials.

7. The method according to claim 1 , where the step of transporting includes at least one mode of transportation selected from the group consisting of: a truck, a train, a ship, and a plane.

8. The method according to claim 1 , where the step of discharging lasts for between about 5 hours and about 10 hours.

9. The method according to claim 1 , where the step of discharging lasts for about 6 hours.

10. The method according claim 1 , where the step of charging includes separating components of the natural gas by adsorption of components with a greater molecular weight than methane in a guard bed separate from the adsorbent materials.

11. The method according to claim 1 , where the step of charging includes the step of cooling a portion of the natural gas storage and transport unit.

12. The method according to claim 1 , where the step of discharging includes the step of compressing at least a portion of discharged natural gas.

13. The method according to claim 12 , where the portion of natural gas is compressed to between about 300 pounds per square inch absolute (psia) and about 500 psia.

14. The method according to claim 1 , where the step of discharging includes the step of cooling at least a portion of discharged natural gas.

15. The method according to claim 1 , where the step of charging occurs with the adsorbent materials at between about 10° C. to about 30° C.

16. The method according to claim 1 , where a majority of the adsorbent materials have pore diameters of between about 10 Å to about 50 Å.

17. The method according to claim 1 , where the step of charging includes charging at least one guard bed comprising microporous materials with pore sizes between about 25 Å and about 50 Å, and charging at least one adsorbent bed with the adsorbent materials, where a majority of the adsorbent materials have pore diameters of between about 10 Å to about 20 Å.

18. The method according to claim 1 , where the step of discharging the natural gas over time occurs at least in part due to pressure built up in the mobile natural gas storage and transport unit from the step of charging.

19. The method according to claim 1 , where the step of charging charges between about 0.1 to about 0.5 million standard cubic feet (MMSCF) of natural gas to the adsorbent materials.

20. The method according to claim 1 , where at least about 90% of the natural gas charged during the step of charging is discharged during the discharging step and used to generate power in the natural gas power generation unit.

21. The method according to claim 1 , where the step of discharging occurs during and throughout a period of peak demand for electricity.

22. The method according to claim 1 , where the step of charging results in adsorbed natural gas at about 1 atm pressure and about 100° F. temperature.

23. A system for natural gas storage and transport with a mobile unit, the system comprising:
a guard bed, the guard bed comprising guard bed adsorbent materials operable to adsorb natural gas components with a molecular weight greater than methane, the guard bed operable to fluidly connect to a natural gas charging station to charge the system with natural gas;
an adsorber bed, the adsorber bed comprising adsorber bed adsorbent materials operable to adsorb methane from natural gas, where the adsorber bed is fluidly coupled to the guard bed; and
a mobile platform operable to hold the guard bed and adsorber bed during transport from the natural gas charging station to a discharging station, where the system is operable to discharge the natural gas over time at the discharging station via desorption of the natural gas from the adsorbent materials.

24. The system according to claim 23 , where the system includes two adsorber beds and where the system charges with natural gas from a natural gas sales pipeline in between about 1 hour and about 5 hours.

25. The system according to claim 24 , where the system charges with natural gas from a natural gas sales pipeline in about 3 hours.

26. The system according to claim 23 , where the adsorbent materials comprise microporous adsorbent materials.

27. The system according to claim 26 , where the microporous adsorbent materials comprise at least one of activated carbon or silica zeolites.

28. The system according to claim 23 , where the system does not consume natural gas adsorbed to the adsorbent materials during transport for fuel for the system.

29. The system according to claim 23 , where the mobile platform is suitable for transport with at least one mode of transportation selected from the group consisting of: a truck, a train, a ship, and a plane.

30. The system according to claim 23 , where the system discharging at the discharging station lasts for between about 5 hours and about 10 hours.

31. The system according to claim 30 , where the system discharging at the discharging station lasts for about 6 hours.

32. The system according to claim 23 , where the system further comprises a cooling unit to cool the natural gas.

33. The system according to claim 23 , where the system further comprises a compressor, where the compressor is operable to compress a portion of natural gas to between about 300 pounds per square inch absolute (psia) and about 500 psia proximate the discharging station.

34. The system according to claim 23 , where the system is charged with natural gas at between about 10° C. to about 30° C.

35. The system according to claim 23 , where a majority of the adsorbent materials have pore diameters of between about 10 Å to about 50 Å.

36. The system according to claim 23 , where the guard bed adsorbent materials comprise microporous materials having pore sizes between about 25 Å and about 50 Å, and where the adsorber bed adsorbent materials comprise adsorbent materials where a majority of the adsorbent materials have pore diameters of between about 10 Å to about 20 Å.

37. The system according to claim 23 , where the system is operable to discharge the natural gas over time at least in part due to pre

Assignees

• Saudi Arabian Oil Co

Inventors

• Wang Yuguo
• Othman Rashid
• Lithoxoos Georgios

Classifications

• B01D2253/108

  Zeolites · CPC title

• B01D2259/4525

  for storage and dispensing systems · CPC title

• B01D2253/102

  Carbon · CPC title

• F17C2221/033

  Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG · CPC title

• B01D53/04

  with stationary adsorbents {(B01D53/025 takes precedence)} · CPC title