Flow-type electrochemical cell

Patent metadata

Field	Value
Publication number	US-9680172-B2
Application number	US-201314424901-A
Country	US
Kind code	B2
Filing date	Aug 29, 2013
Priority date	Sep 3, 2012
Publication date	Jun 13, 2017
Grant date	Jun 13, 2017

Abstract

Flow type electrochemical cells are disclosed. The electrochemical cell has an anode half-cell, a cathode half-cell, and permeable separating layer. The half-cells are bounded by side elements. Respective porous electrodes are housed in the half-cells. The permeable separating layer is disposed between the anode half-cell and the cathode half-cell. An electrolyte region connected to an electrolyte feed and an electrolyte outflow region connected to an electrolyte drain are further provided. An electrolyte inflow region and an electrolyte outflow region are disposed on opposite sides of the porous electrodes such that inflowing electrolyte flows through the porous electrode perpendicularly to the permeable separating layer.

First claim

The invention claimed is:

1. A flow type electrochemical cell, comprising:
an anode half-cell and a cathode half-cell bounded by side elements, each half-cell further comprising porous electrodes;
a permeable separating layer disposed between the anode half-cell and the cathode half-cell;
an electrolyte inflow region connected to an electrolyte feed; and
an electrolyte outflow region connected to an electrolyte drain;
wherein:
the electrolyte inflow region and the electrolyte outflow region are disposed on opposite sides of the porous electrode;
inflowing electrolyte flows through the porous electrode perpendicularly to the permeable separating layer; and
at least one of the electrolyte inflow region and the electrolyte outflow region further comprises a wide-mesh support structure, wherein the wide-mesh support structure presents a lower flow resistance than the porous electrode.

2. The electrochemical cell of claim 1 , wherein:
the electrolyte inflow region is disposed between the permeable separating layer and the porous electrode; and
the electrolyte outflow region is disposed between the porous electrode and the side elements, or vice versa.

3. The electrochemical cell of claim 1 , wherein:
the electrolyte inflow region is disposed between the porous electrode and the side elements; and
the electrolyte outflow region is disposed between the permeable separating layer and the porous electrode.

4. The electrochemical cell of claim 1 , wherein at least one of the electrolyte inflow region and the electrolyte outflow region is integrated into at least one of the porous electrodes and the side elements by means of one or more flow channels.

5. The electrochemical cell of claim 1 , wherein the wide-mesh support structure is a woven fabric or a knitted fabric.

6. The electrochemical cell of claim 1 , wherein the wide-mesh support structure is made of an electrically conducting material or of a material with electrically conductive coating.

7. The electrochemical cell of claim 1 , wherein the wide-mesh support structure represents a carbon support structure.

8. The electrochemical cell of claim 1 , wherein the porous electrode comprises a nonwoven carbon web, foams, or metal foams.

9. A cell stack of a flow type electrolytic cell as claimed in claim 1 .

10. A method for operating a flow type electrochemical cell, wherein flow of an electrolyte is caused to pass through the porous electrode perpendicularly to the permeable separating layer;
wherein:
the electrolyte is supplied via an electrolyte inflow region connected to an electrolyte feed;
the electrolyte is guided from the cell via an electrolyte outflow region which is disposed on the opposite side of the porous electrode from the electrolyte inflow region; and
at least one of the electrolyte inflow region and the electrolyte outflow region further comprises a wide-mesh support structure, wherein the wide-mesh support structure presents a lower flow resistance than the porous electrode.

Assignees

• Thyssenkrupp Ind Solutions Ag

Inventors

• Polcyn Gregor Damian
• Bredemeyer Niels
• Roosen Christoph
• Donst Dmitri
• Toros Peter
• Woltering Peter
• Hoormann Dirk
• Hofmann Philipp
• Köberle Stephan
• Funck Frank
• Stolp Wolfram
• Langanke Bernd

Classifications

• Y02E60/50

  Fuel cells · CPC title

• C25B15/08 Primary

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

• H01M8/20

  Indirect fuel cells, e.g. fuel cells with redox couple being irreversible (H01M8/18 takes precedence) · CPC title

• H01M2300/0011

  Sulfuric acid-based · CPC title

• H01M8/08

  Fuel cells with aqueous electrolytes · CPC title