Method for operating a high-pressure electrolysis system, high-pressure electrolysis system and hydrogen filling station comprising a high-pressure electrolysis system

Patent metadata

Field	Value
Publication number	US-9464357-B2
Application number	US-201414888867-A
Country	US
Kind code	B2
Filing date	Mar 4, 2014
Priority date	May 16, 2013
Publication date	Oct 11, 2016
Grant date	Oct 11, 2016

Abstract

The invention relates to a method for operating a high-pressure electrolysis system ( 2 ), wherein a hydrogen stream ( 6 ) and an oxygen stream ( 8 ) are produced in a high-pressure electrolyzer ( 4 ), and these are passed out of the high-pressure electrolyzer ( 4 ) under high pressure. In order to increase the efficiency of the high-pressure electrolysis system ( 2 ) with respect to cooling of the hydrogen produced in the high-pressure electrolysis system ( 2 ), the oxygen stream ( 8 ) is passed into a vortex tube ( 20 ) for decompression, in which the pressure energy of the oxygen is converted to refrigeration. This produces a cold oxygen stream ( 22 ) which is used to cool the hydrogen stream ( 6 ).

First claim

The invention claimed is:

1. A method for operating a high-pressure electrolysis system, comprising:
producing a hydrogen stream and an oxygen stream in a high-pressure electrolyzer;
conveying the hydrogen stream and the oxygen stream at high pressure out of the high-pressure electrolyzer;
introducing the oxygen stream into a vortex tube for decompression to convert pressure energy of oxygen into cold and thereby create a cold oxygen stream; and
using the cold oxygen stream for cooling the hydrogen stream.

2. The method of claim 1 , wherein the high-pressure electrolyzer is a PEM high-pressure electrolyzer.

3. The method of claim 1 , further comprising storing the oxygen stream before decompression in a pressure vessel.

4. The method of claim 3 , further comprising supplying an additional gas from an external source at high pressure to the pressure vessel.

5. The method of claim 4 , wherein the additional gas is oxygen.

6. The method of claim 1 , wherein the oxygen stream is cooled down in the vortex tube below 0° C.

7. The method of claim 1 , wherein the oxygen stream is cooled down in the vortex tube below −20° C.

8. The method of claim 1 , wherein the oxygen stream is cooled down in the vortex tube to about −40° C.

9. The method of claim 1 , further comprising decompressing the hydrogen stream to a pressure of at least about 700 bar, as the hydrogen stream is cooled by the cold oxygen stream.

10. The method of claim 1 , further comprising decompressing the hydrogen stream to a pressure of at least about 800 bar, as the hydrogen stream is cooled by the cold oxygen stream.

11. The method of claim 1 , wherein the hydrogen stream is cooled by the cold oxygen stream before hydrogen is used for fuelling a motor vehicle.

12. A high-pressure electrolysis system, comprising:
a high-pressure electrolyzer configured to produce a hydrogen stream and an oxygen stream;
a hydrogen line connected to the high-pressure electrolyzer for conveying the hydrogen stream out of the high-pressure electrolyzer;
an oxygen line connected to the high-pressure electrolyzer for conveying the oxygen stream out of the high-pressure electrolyzer;
a vortex tube integrated into the oxygen line for decompression of the oxygen stream to thereby produce a cold oxygen stream; and
a cold oxygen line for conveying the cold oxygen stream from the vortex tube, said cold oxygen line being connected in flow communication to the hydrogen line.

13. The high-pressure electrolysis system of claim 12 , wherein the high-pressure electrolyzer is a PEM high-pressure electrolyzer.

14. The high-pressure electrolysis system of claim 12 , further comprising a pressure vessel disposed in the oxygen line upstream of the vortex tube.

15. The high-pressure electrolysis system of claim 14 , wherein the pressure vessel is connected to an external source for supply of a gas at high pressure.

16. The high-pressure electrolysis system of claim 15 , wherein the gas is oxygen.

17. The high-pressure electrolysis system of claim 12 , further comprising a compressor integrated into and in fluid communication with the hydrogen line for compressing hydrogen to a pressure of at least about 700 bar, especially to a pressure of about 800 bar.

18. The high-pressure electrolysis system of claim 17 , further comprising a fuel pump connected downstream of the compressor in the hydrogen line.

19. A hydrogen filling station, comprising a high-pressure electrolysis system which includes a high-pressure electrolyzer configured to produce a hydrogen stream and an oxygen stream, a hydrogen line connected to the high-pressure electrolyzer for conveying the hydrogen stream out of the high-pressure electrolyzer, an oxygen line connected to the high-pressure electrolyzer for conveying the oxygen stream out of the high-pressure electrolyzer, a vortex tube integrated into the oxygen line for decompression of the oxygen stream to thereby produce a cold oxygen stream, and a cold oxygen line for conveying the cold oxygen stream from the vortex tube, said cold oxygen line being connected in flow communication to the hydrogen line.

20. The hydrogen filling station of claim 19 , further comprising a cooling network for supplying devices of the filling station with cold, said cold oxygen line being part of the cooling network.

Assignees

• Siemens Ag

Inventors

• Herold Jochen
• Kautz Martin

Classifications

• Y02E60/366

  Cross-Sectional Technologies · mapped topic

• F17C2221/012

  Hydrogen · CPC title

• F17C2270/01

  for fluid transport or storage · CPC title

• F17C2227/0341

  using another fluid · CPC title

• C25B15/08 Primary

  Supplying or removing reactants or electrolytes; Regeneration of electrolytes · CPC title