# US 2013/0157097 A1 · Compact frameless bipolar stack for a multicell electrochemical reactor with planar bipolar electrical interconnects and internal ducting of circulation of electrolyte solutions through all respective cell compartments

> Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt

- Number: US 2013/0157097 A1
- Document ID: US20130157097A1
- Status: Published application
- Kind: A1
- Application number: 13/805,959
- Filed: 2010-06-29
- Published: 2013-06-20
- Earliest claimed: 2010-06-29
- Assignees: Squirrel Holdings Ltd.
- Inventors: Krisada Kampanatsanyakorn; Suradit Holasut
- Web page: https://patentgrep.com/patent/US20130157097A1

## CPC

- H01M 8/188: {by recharging of redox couples containing fluids; Redox flow type batteries}
- H01M 8/0273: with sealing or supporting means in the form of a frame
- H01M 8/0276: Sealing means characterised by their form (H01M8/0273 takes precedence)
- H01M 8/0284: Organic resins; Organic polymers
- H01M 8/04276: Arrangements for managing the electrolyte stream, e.g. heat exchange
- H01M 8/1009: with one of the reactants being liquid, solid or liquid-charged (H01M8/12 takes precedence)
- H01M 8/2459: {Comprising electrode layers with interposed electrolyte compartment with possible electrolyte supply or circulation}
- H01M 8/247: Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
- H01M 8/2483: characterised by internal manifolds
- H01M 8/0278: {O-rings}
- Y02E 60/50: Fuel cells
- 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

A frameless bipolar cell stack architecture with either internal manifolds of circulation of electrolyte solutions “in parallel” through all respective cell compartments or internal ducting adapted to provide for “serial” flow paths of the electrolyte solutions in succession through all respective cell compartments of the stack, does not employ any plastic frame and employs substantially planar bipolar electrical interconnects (I) of substantially homogeneous electrical conductivity with a perimeter that super-imposes to the perimeter of any other element of the stack. Whenever useful for the particular application, the planar interconnects may have a protruding “lug portion” that projects beyond the outer perimeter side of the other stacked elements, providing an externally contactable area sufficiently large for the power (current rating) of an electrical tap, at an intermediate voltage relative to the voltage difference between the end terminals of the stack, connectable to an external circuit.

## Claims

### Claim 1

A frameless multi-cell bipolar electrochemical reactor composed of stackable elements between two headers, hydraulically sealed by compressing the stacked elements, including planar bipolar electrical conductive elements alternated to a permionic membrane assembly fixture adapted to separate anodic and cathodic solution flow compartments defined between said permionic membrane separator and one and the other of said bipolar electrical elements and through which the two distinct electrolyte solutions are respectively flown, comprising
two identical parallelepiped elastomer gaskets defining a central aperture and having at least two through holes along two opposite perimeter sides thereof, a flat perimeter seal surface on a backside and on the opposite or front side thereof: a bas-relief patterned perimeter seal area contouring one every two through holes along said two opposite perimeter sides and two similar pluralities of patterned seal areas defining there between flow channels extending from a rim region of non-contoured through holes to the edge of the nearest juxtaposed side of said central aperture of the gasket;
the permionic membrane having perimeter edge portions sealingly held between said flat perimeter seal surfaces of the two identical gaskets, disposed back-to-back;
the bas-relief patterned seal areas over the front side of the two identical gaskets, compressed between the surfaces of respective planar electrically conductive bipolar elements in alignment with the through holes of the gaskets for hydraulically sealing the perimeter of the two flow compartments in hydraulically communication with through holes non-contoured by said perimeter seal area of the patterned front side of the respective gasket.

### Claim 2 (depends on 1)

The frameless multi-cell bipolar electrochemical reactor of claim 1, wherein said planar bipolar elements are electrical interconnects of the cells and said anodic and cathodic compartments contain conductive felt or compressible mat anodes and cathodes, respectively, compressed between the permionic membrane separator and a respective planar bipolar conductive interconnect and said permionic membrane assembly includes non-conductive perimeter spacers adapted to limit compression of said bas-relief patterned elastomer gaskets and maintain parallelism among the stacked elements upon tightening them together.

### Claim 3 (depends on 1)

The frameless multi-cell bipolar electrochemical reactor of claim 1, wherein said planar electrically conductive bipolar elements have a perimeter adapted to overlap the outermost perimeter of said gaskets and optionally include a protruding lug portion that projects beyond the outer perimeter side of the gaskets for electrical connection to an external circuit.

### Claim 4 (depends on 1)

The frameless multi-cell bipolar electrochemical reactor of claim 1, wherein said planar conductive bipolar electrodes or interconnects are of homogeneously conductive material and the surfaces of the holes there through and planar surfaces over which seal areas of the counter opposed patterned elastomer gasket press have a nonconductive coat.

### Claim 5 (depends on 1)

The frameless multi-cell bipolar electrochemical reactor of claim 1, with internal inlet and outlet manifolds for flowing said electrolyte solutions in parallel through all the respective cell compartments, comprising
two identical parallelepiped elastomer gaskets defining a central aperture and having two through holes, respectively at the two corner ends, of said opposite perimeter sides thereof, a flat perimeter seal surface on a backside and the opposite or front side thereof: a bas-relief patterned perimeter seal area contouring one through hole of one of the opposite perimeter sides and the diametrically opposite through hole of the other perimeter side and two similar pluralities of patterned seal areas defining there between tortuously elongated channels originating from a rim region of the two diagonally opposite through holes non-contoured by said perimeter seal area and reaching spaced points along said nearest juxtaposed side of said central aperture of the gasket, respectively;
planar conductive bipolar electrodes or interconnects having through holes at the four corners matching with the two gaskets in sealing therebetween an anode flow compartment and a cathode flow compartment communicating with respective inlet and outlet internal manifolds constituted by said diagonally opposite through holes respectively.
said permionic membrane having perimeter edge portions sealingly held between said flat perimeter seal surfaces on the back side of the identical gaskets, disposed back-to-back;
said bas-relief patterned seal areas over the front side of the two identical gaskets compressed between the surfaces of respective planar electrically conductive bipolar elements having through holes in alignment with the through holes of the gaskets for hydraulically sealing the perimeter of the two flow compartments communicating with respective inlet and outlet internal manifolds through said non contoured holes of the respective gasket.

### Claim 6 (depends on 5)

The frameless multi-cell bipolar electrochemical reactor of claim 5, wherein the length of said tortuously elongated parallel split flow channels of electrolyte solution is such to prevent ion discharge current densities exceeding a critical maximum value over conductive parts of other cells.

### Claim 7 (depends on 1)

The frameless multi-cell bipolar electrochemical reactor of claim 1, with internal ducting for flowing said electrolyte solutions in series through the respective cell compartments of all the cells of the stack, comprising
two identical parallelepiped elastomer gaskets defining a central aperture and having two or more through holes on said opposite perimeter sides thereof, a flat perimeter seal surface on a backside and on the opposite or front side thereof: a bas-relief patterned perimeter seal area contouring one through hole every two on said opposite perimeter sides, and similar pluralities of patterned short seal areas over said opposite perimeter sides, defining there between intermixing flow channels, leading the electrolyte solution from a rim region of non-contoured through holes to the nearest juxtaposed side of said central aperture and vice versa, respectively;
planar conductive bipolar electrodes or interconnects having through holes matching with the through holes of the gaskets counter opposed to it over opposite sides sealing there between an anode flow compartment and a cathode flow compartment communicating with preceding and with following anode and cathode flow compartments, respectively, of adjacent bipolar cells though said contoured through holes in said two perimeter sides of the gaskets;
said permionic membrane having perimeter edge portions sealingly held between said flat perimeter seal surfaces on the back side of the identical gaskets, disposed back-to-back;
said bas-relief patterned seal areas over the front side of the two identical gaskets compressed between the surfaces of respective planar electrically conductive bipolar elements having through holes in alignment with the through holes of the gaskets for hydraulically sealing the perimeter of the two flow compartments each communicating with respective preceding and following compartments of adjacent cells through said non contoured holes of the respective gasket.

### Claim 8 (depends on 1)

The frameless multi-cell bipolar electrochemical reactor of claim 1 used in a redox flow battery system, wherein the assembly of stackable elements between two end headers, hydraulically sealed by compressing the stacked elements is segmented by comprising a certain number of intermediate headers coupled at both sides as would-be end headers of groups of bipolar cells on one side and on the opposite side thereof and having inlets and inner ducting for allowing the two electrolyte solutions to be flown in parallel through the respective compartments of one group of bipolar cells and exit the stack from outlets of a successive intermediate header; said two end headers and intermediate headers connecting through primary manifolds external to the stack, from and to respective electrolyte solution source and sink tanks.

### Claim 9 (depends on 8)

The frameless multi-cell bipolar electrochemical reactor of claim 8, wherein each group of bipolar cells are in number adapted to generate a maximum open circuit total voltage lesser than a critical voltage that would cause excessively large ion discharge current densities on conductive parts of the cells of a group sharing internal manifolds of distribution of the two electrolyte solutions into respective flow compartments of the cells.

### Claim 10 (depends on 1)

The frameless multi-cell bipolar electrochemical reactor according to claim 1, wherein each header comprises a parallelepiped body having defined in it two chambers or ducts hydraulically connectable to external pipes and at least a planar conductive bipolar interconnect applied onto a planar surface of the parallelepiped body and having through holes aligned with holes in said body communicating respectively with said chambers or ducts.