Electrolysis unit and method for operating the electrolysis unit

Patent metadata

Field	Value
Publication number	US-2021292919-A1
Application number	US-201917259610-A
Country	US
Kind code	A1
Filing date	Jul 8, 2019
Priority date	Jul 27, 2018
Publication date	Sep 23, 2021
Grant date	—

Abstract

An electrolysis unit and to a method for electrochemically decomposing water into hydrogen and oxygen. The electrolysis unit has at least two electrolysis modules. The electrolysis unit also has exactly one first gas separation device for a first product gas including oxygen and exactly one second gas separation device for a second product gas including hydrogen. The first gas separation device is connected to the at least two electrolysis modules by respective first lines. The second gas separation device is connected to the at least two electrolysis modules by respective second lines. The at least two first lines have the same first length. The at least two second lines likewise have the same second length.

First claim

1 . An electrolysis unit for the electrochemical dissociation of water (H 2 O) into hydrogen (H 2 ) and oxygen (O 2 ), comprising:
at least two electrolysis modules; exactly one first gas separation device for a first product gas comprising oxygen, exactly one second gas separation device for a second product gas comprising hydrogen, wherein the first gas separation device is connected to each of the at least two electrolysis modules by means of a first conduit in each case and the second gas separation device is connected to each of the electrolysis modules by means of a second conduit in each case and the at least two first conduits have the same first length and the at least two second conduits have the same second length.

2 . The electrolysis unit as claimed in claim 1 ,
wherein an electrolysis module of the at least two electrolysis modules comprises at least two electrolysis cells and each electrolysis cell comprises an anode space having an anode and a cathode space having a cathode and the anode space is separated from the cathode space by means of a proton exchange membrane and the anode space is suitable for taking up water (H 2 O) and oxidizing it at the anode to give a first product comprising oxygen (O 2 ) and the cathode space is suitable for taking up water (H 2 O) and reducing it at the cathode to give a second product comprising hydrogen (H 2 ).

3 . The electrolysis unit as claimed in claim 2 ,
wherein the cathode space is connected to the second gas separation device and the anode space is connected to the first gas separation device.

4 . The electrolysis unit as claimed in claim 1 ,
wherein the first gas separation device and the second gas separation device are arranged inside one another, with the first or the second gas separation device being configured as an outer shell and a bottom and the other second or first gas separation device projecting as tube into the shell.

5 . The electrolysis unit as claimed in claim 4 ,
wherein the tube has a closing face in the direction of the bottom and the closing face is configured as a grid, as a perforated plate or as a mesh.

6 . The electrolysis unit as claimed in claim 4 ,
wherein a cross section of the shell and/or of the tube is round or is a polygon.

7 . The electrolysis unit as claimed in claim 1 ,
wherein the first gas separation device is connected to a first pressure maintenance device and the second gas separation device is connected to a second pressure maintenance device.

8 . The electrolysis unit as claimed in claim 1 ,
wherein at least one pump is arranged between the first and/or second gas separation device and the electrolysis modules.

9 . The electrolysis unit as claimed in claim 4 comprising:
at least three electrolysis modules,
wherein the electrolysis modules are arranged in a circle and the first and second gas separation devices are arranged centrally in the middle between the modules.

10 . The electrolysis unit as claimed in claim 4 ,
wherein the first and/or second gas separation device is connected to exactly one heat exchanger for cooling the water (H 2 O) which has been separated off.

11 . The electrolysis unit as claimed in claim 4 ,
wherein the first or second gas separation device is connected to exactly one water treatment device.

12 . The electrolysis unit as claimed in claim 11 ,
wherein the water treatment device comprises a pump, a cooling device and an ion exchange device.

13 . The electrolysis unit as claimed in claim 1 ,
wherein the electrolysis module comprises a module end plate, which has an exterior covering surface, on each of two opposite sides and a first electrolysis module is electrically connected to a second electrolysis module in such a way that a contacting device contacts a covering surface of the first electrolysis module and a covering surface of the second electrolysis module to a large extent.

14 . A method for operating an electrolysis unit comprising:
providing an electrolysis unit comprising at least two electrolysis modules, with water (H 2 O) being dissociated into hydrogen (H 2 ) and oxygen (O 2 ) in the electrolysis module, providing a first gas separation device for a first product gas comprising oxygen, providing a second gas separation device for a second product gas comprising hydrogen, wherein the first gas separation device is connected to each of the at least two electrolysis modules by means of a first conduit in each case and the second gas separation device is connected to each of the electrolysis modules by means of a second conduit in each case and the at least two first conduits have the same first length and the at least two second conduits have the same second length.

15 . The method as claimed in claim 14 ,
wherein the electrolysis unit is operated at a pressure in the range from 1 bar to 5 bar.

Assignees

• Siemens Energy Global Gmbh & Co Kg

Inventors

• Purucker Thomas
• Rückert Stephan
• Straub Jochen
• Utz Peter

Classifications

• C25B15/087

  Recycling of electrolyte to electrochemical cell · CPC title

• C25B15/083

  Separating products · CPC title

• C25B9/70

  Assemblies comprising two or more cells · CPC title

• C25B1/04 Primary

  by electrolysis of water · CPC title

• C25B13/00

  Diaphragms; Spacing elements · CPC title