# US 8,273,472 B2 · Shunt current interruption in electrochemical energy generation system

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- Number: US 8,273,472 B2
- Document ID: US8273472B2
- Status: Granted
- Kind: B2
- Application number: 12/656,664
- Filed: 2010-02-12
- Published: 2011-08-18
- Granted: 2012-09-25
- Earliest claimed: 2010-02-12
- Assignees: Primus Power Corporation
- Inventors: Rick Winter
- Web page: https://patentgrep.com/patent/US8273472B2

## CPC

- H01M 50/529: Intercell connections through partitions, e.g. in a battery casing
- H01M 12/085: {Zinc-halogen cells or batteries}
- H01M 50/70: Arrangements for stirring or circulating the electrolyte
- Y02E 60/10: Energy storage using batteries
- 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

An electrochemical energy generation system includes plural electrochemical cells connected electrically in series that utilize a common electrolyte that can be delivered to each of the cells and/or collected from each of the cells using one or more manifolds. The system provides a possibility for reducing shunt currents by applying a shunt-current minimizing voltage to terminals of the manifolds from the terminal electrodes of the cells connected in series.

## Claims

### Claim 1

A method of operating an electrochemical system comprising:
(A) providing an electrochemical system comprising:
(a) a plurality of cells connected in series, wherein each of the cells comprises:
a first electrode;
a second electrode; and
a reaction zone between the first and second electrodes;
(b) a halogen reactant;
(c) a metal halide electrolyte; and
(d) at least one of (i) a first manifold configured to deliver at least one of the halogen reactant and the metal halide electrolyte to the reaction zone for each of the cells and (ii) a second manifold configured to collect at least one of the halogen reactant and the metal halide electrolyte from the reaction zone for each of the cells;
(B) conveying a flow of the metal halide electrolyte and the halogen reactant through the reaction zone of each of the cells; and
(C) applying a shunt-current minimizing voltage to terminals of at least one of the first manifold and the second manifold during said conveying.

### Claim 2 (depends on 1)

The method of claim 1, wherein the first electrode comprise a porous, electrically conductive material.

### Claim 3 (depends on 1)

The method of claim 1, wherein the halogen reactant comprises molecular chlorine.

### Claim 4 (depends on 3)

The method of claim 3, wherein the metal halide electrolyte comprises zinc chloride and the second electrode comprises metallic zinc.

### Claim 5 (depends on 3)

The method of claim 3, wherein the halogen reactant comprises a liquid chlorine reactant.

### Claim 6 (depends on 1)

The method of claim 1, wherein said conveying comprises conveying a flow of the metal halide electrolyte and the halogen reactant through a loop circuit that includes the first manifold, the second manifold and the reaction zone of each of the cells.

### Claim 7 (depends on 1)

The method of claim 1, wherein the system further comprises at least one pump and wherein said conveying comprising is performed used said at least one pump.

### Claim 8 (depends on 7)

The method of claim 7, wherein the at least one pump comprises a discharge pump and a charge pump and wherein said conveying comprises a) conveying the flow of at least one of the metal halide electrolyte and the halogen reactant through the reaction zone of each of the cell in a first direction using the discharge pump or b) conveying the flow of at least one of the metal halide electrolyte and the halogen reactant through the reaction zone of each of the cell using the charge pump in a second direction, that is opposite to the first direction.

### Claim 9 (depends on 8)

The method of claim 8, wherein said conveying is conveying the flow of at least one of the metal halide electrolyte and the halogen reactant through the reaction zone of each of the cell in the first direction using the discharge pump and wherein the shunt current minimizing voltage is substantially equal to an output voltage of the series of cells.

### Claim 10 (depends on 8)

The method of claim 8, wherein said conveying is conveying the flow of at least one of the metal halide electrolyte and the halogen reactant through the reaction zone of each of the cell in the second direction using the charge pump and wherein the shunt current minimizing voltage is substantially equal to a charge voltage applied to the cells.

### Claim 11 (depends on 1)

The method of claim 1, wherein the cells comprise a vertical stack of horizontal cells.

### Claim 12 (depends on 11)

The method of claim 11, wherein the shunt current minimizing voltage is applied to the terminals of at least one of the first manifold and the second manifold from terminal electrodes of the stack.

### Claim 13 (depends on 12)

The method of claim 12, wherein the first and second manifolds are vertical manifolds.

### Claim 14 (depends on 12)

The method of claim 12, wherein the second manifold comprises an upward flowing section.

### Claim 15 (depends on 12)

The method of claim 12, wherein said applying comprises applying the shunt current minimizing voltage between upper and lower terminals of the first manifold and between upper and lower terminals of the second manifold.

### Claim 16 (depends on 1)

The method of claim 1, wherein the system further comprises a pressurized sealed vessel that contains the cells, the halogen reactant, the metal halide electrode and the first and the second manifolds and wherein a pressure in an inner volume of the vessel is above a liquefication pressure for the halogen reactant.