# US 9,752,240 B2 · Electrochemical cell and reactor formed by the cell

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- Number: US 9,752,240 B2
- Document ID: US9752240B2
- Status: Granted
- Kind: B2
- Application number: 14/367,399
- Filed: 2011-12-21
- Published: 2015-10-22
- Granted: 2017-09-05
- Earliest claimed: 2011-12-21
- Assignees: Ingeteam Power Technology, S.A.; Acciona Energia, S.A.
- Applicants: Sergio López De Echazarreta Elvira; Maria Santa María Iruzubieta; Raquel Rojo Ochoa; Isabel Carrilero Borbujo
- Inventors: Sergio López De Echazarreta Elvira; Maria Santa María Iruzubieta; Raquel Rojo Ochoa; Isabel Carrilero Borbujo
- Web page: https://patentgrep.com/patent/US9752240B2

## CPC

- C25B 9/19: with diaphragms
- C25B 9/73: of the filter-press type
- C25B 9/75: having bipolar electrodes
- C25B 11/036: Bipolar electrodes
- C25B 13/02: characterised by shape or form
- C25B 15/08: Supplying or removing reactants or electrolytes; Regeneration of electrolytes
- H01M 8/0206: Metals or alloys
- H01M 8/0265: the reactant or coolant channels having varying cross sections
- H01M 8/0273: with sealing or supporting means in the form of a frame
- H01M 8/04104: {Regulation of differential pressures}
- H01M 8/242: comprising framed electrodes or intermediary frame-like gaskets (H01M8/2425, H01M8/244 take precedence)
- H01M 8/2483: characterised by internal manifolds
- Y02E 60/50: Fuel cells
- C25B: ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR (anodic or cathodic protection C23F13/00; single-crystal growth C30B)
- H01M: PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION

## Abstract

The present invention relates to an electrochemical cell (20) comprising a bipolar plate (26); an annular support next to the bipolar plate (26); a first electrode (22) separated from the bipolar plate (26) defining a first half-cell (10′) (cationic or anionic) together with the plate and the annular support. The cell also has a membrane (23) next to the first electrode (22); a second electrode (24) next to the membrane (23); and a closure element (21) defining a second half-cell (10″) (cationic or anionic depending on the nature of the second electrode) together with the second electrode (24). In the present invention the closure element (21) is housed within the annular support (25).

## Claims

### Claim 1

Electrochemical cell comprising:
a bipolar plate;
an annular support next to the bipolar plate,
a first electrode separated from the bipolar plate defining a first half-cell together with the bipolar plate and the annular support;
a membrane next to the first electrode;
a second electrode next to the membrane; and
a closure element together with the second electrode defining a second half-cell
wherein the closure element is housed within the annular support,
the closure element which is not a structural element mechanically supporting the pressure of the cell including:
at least one inlet conduit for delivering an ion conductive liquid to one of the half-cells; and,
at least one collection conduit for collecting the reaction products which are produced in one of the half-cells.

### Claim 2 (depends on 1)

Electrochemical cell according to claim 1, characterized in that the annular support includes:
the at least one inlet conduit for delivering an ion conductive liquid to one of the half-cells;
the at least one collection conduit for collecting the reaction products which are produced in one of the half-cells,
at least a first common inlet channel for delivering an ion conductive liquid to the first half-cell;
at least a second common inlet channel for delivering an ion conductive liquid to the second half-cell
at least a first common collection channel for collecting the reaction products of the first half-cell
at least a second common collection channel for collecting the reaction products of the second half-cell.

### Claim 3 (depends on 2)

Electrochemical cell according to claim 2, characterized n that equivalent passage sections of the at least one inlet conduit, of the at least on collection conduit, of the first common inlet channel and the second common inlet channel as well as of the first common collection channel and the second common collection channel with be equal to or different from one another, depending on the fluid which goes through it.

### Claim 4 (depends on 3)

Electrochemical cell according to claim 3, characterized in that the at least one inlet conduit of the annular support and the closure element has an equivalent passage section which is different with respect to the at least one collection conduit of the annular support and the closure element.

### Claim 5 (depends on 3)

Electrochemical cell according to claim 3, characterized in that the at least one inlet conduit of the annular support and the closure element has a passage section which is different from one another.

### Claim 6 (depends on 3)

Electrochemical cell according to claim 3, characterized in that at least one collection conduit of the annular support and the closure element has an equivalent passage section which is different from one another.

### Claim 7 (depends on 3)

Electrochemical cell according to claim 3, characterized in that the at least first common inlet channel and the at least second common inlet channel have a passage section which is different from one another.

### Claim 8 (depends on 3)

Electrochemical cell according to claim 3, characterized in that the at least first common collection channel and the at least second common channel collection have an equivalent passage section which is different from one another.

### Claim 9 (depends on 2)

Electrochemical cell according to claim 2, characterized in that a passage section of the at least one inlet conduit of the annular support and the closure element have a passage section which is between 1 and 4 times smaller with respect to the at least one collection conduit of the annular support and the closure element.

### Claim 10 (depends on 1)

Electrochemical cell according to claim 1, characterized in that the annular support and the closure element are made of materials which are different from one another.

### Claim 11 (depends on 1)

Electrochemical cell according to claim 1, characterized in that the annular support and the closure element are made of the same material.

### Claim 12 (depends on 1)

Electrochemical cell according to claim 1, characterized in that the bipolar plate comprises a conductive section with two main faces; and a gasket joined to each face of the conductive section.

### Claim 13 (depends on 12)

Electrochemical cell according to claim 12, characterized in that the bipolar plate additionally comprises a flap extending outwards from the conductive section thereof that is accessible from the outside.

### Claim 14 (depends on 12)

Electrochemical cell according to claim 12, characterized in that the conductive section of the bipolar plate is flat or shaped with a particular geometry.

### Claim 15 (depends on 12)

Electrochemical cell according to claim 12, characterized in that the gasket is manufactured from rubbers or plastic materials.

### Claim 16 (depends on 1)

Electrochemical reactor comprising:
two common inlet channels configured to deliver an ion conductive liquid to at least one electrochemical cell as defined in claim 1; and
two common collection channels for collecting reaction products from the at least one electromechanical cell.

### Claim 17 (depends on 16)

Electrochemical reactor according to claim 16, further characterized in that it includes a current collector.