Hydrogen quality differentiation at refueling station

Patent metadata

Field	Value
Publication number	US-9856142-B2
Application number	US-201414766840-A
Country	US
Kind code	B2
Filing date	Feb 7, 2014
Priority date	Feb 12, 2013
Publication date	Jan 2, 2018
Grant date	Jan 2, 2018

Abstract

The present invention provides a process for dispensing gaseous hydrogen at a refueling station comprising before dispensing dividing an initial hydrogen stream into at least two streams, wherein at least one of the streams is purified in a hydrogen purification step. In a further aspect the invention provides a system for dispensing gaseous hydrogen.

First claim

That which is claimed is:

1. A process for dispensing gaseous hydrogen at a refueling station comprising before dispensing dividing an initial hydrogen stream into at least two streams, wherein at least one, but not all, of the streams is purified in a hydrogen purification step or steps.

2. The process according to claim 1 , further comprising passing the initial stream of hydrogen from a supply into a low pressure buffer tank, subsequently passing the stream via a compressor into a high pressure buffer tank, followed by passing the stream via a chiller to a final dispenser, wherein the process further comprises a step in which a part of the hydrogen stream is separated and passed through a purifier which is located in line after the low pressure tank.

3. The process according to claim 2 , wherein the part of the hydrogen that is separated is passed through a purifier before it is compressed.

4. The process according to claim 3 , wherein the hydrogen is compressed using the same compressor as for compressing the remaining part of the hydrogen.

5. The process according to claim 4 , wherein compression of the separated part of the hydrogen takes place at a different time than that of the remaining part of the hydrogen.

6. The process according to claim 4 , wherein the system runs on a schedule which maintains the buffer tanks full for as much of the time as possible.

7. The process according to claim 2 , wherein the stream of hydrogen is first passed through the compressor and thereafter a part is separated for passing through a purifier.

8. The process according to claim 7 , wherein the separated part of hydrogen is subsequently led into a second high pressure buffer tank followed by passing it into the same chiller as is used for chilling the remaining part of the hydrogen.

9. The process according to claim 8 , wherein chilling of the separated part of the hydrogen takes place at a different time than that of the remaining part of the hydrogen.

10. The process according to claim 8 , wherein the system runs on a schedule which maintains the buffer tanks full for as much of the time as possible.

11. The process according to claim 2 , wherein the stream of hydrogen is first passed through both the compressor and the high pressure buffer tank and thereafter a part is separated for passing it through a purifier.

12. The process of claim 11 , wherein the purification is followed by passing the separated part into the same chiller as is used for chilling the remaining part of the hydrogen.

13. The process of claim 1 , wherein the purification comprises using a membrane or a palladium catalyst.

14. The process of claim 1 , wherein a separate dispenser is used for the purified hydrogen.

15. A system for dispensing gaseous hydrogen comprising in a subsequent line-up a combination of the following: a low pressure buffer tank, a compressor, a high pressure buffer tank, a chiller and at least one dispenser, wherein at least one of the low pressure buffer tank, compressor, and high pressure buffer tank has two exits, one for separating a part of a hydrogen stream, the other for the remaining part of the hydrogen stream, and wherein the system further comprises a purifier, the inlet of the purifier being located in line after one exit of one of the low pressure buffer tank, compressor, and high pressure buffer tank for the separated part of the hydrogen stream.

Assignees

• Shell Oil Co

Inventors

• Louis Jurgen Johannes Jacobus

Classifications

• C01B2203/0435

  Catalytic purification · CPC title

• F17C2265/065

  for refuelling vehicle fuel tanks · CPC title

• C01B3/50 Primary

  Separation of hydrogen or hydrogen-containing gases from gaseous mixtures, e.g. purification · CPC title

• Y02E60/324

  Cross-Sectional Technologies · mapped topic

• F17C5/06

  for filling with compressed gases · CPC title