Metal halogen batteries and method of operating same

• US 4,105,829 A
• Filed: 04/07/1976
• Issued: 08/08/1978
• Est. Priority Date: 04/07/1976
• Status: Expired due to Term

• Current Assignee: Exxon Research and Engineering Company (Exxon Mobil Corporation)
• Original Assignee: Exxon Research and Engineering Company (Exxon Mobil Corporation)
• Inventors: Venero, Agustin F.
• Primary Examiner(s): Mack, John H.
• Assistant Examiner(s): Feeley, H. A.
• Application Number:
  US05/674,583
• Time in Patent Office: 853 Days
• Field of Search: 429/14, 429/15, 429/17, 429/19, 429/51, 429/199, 429/200, 429/201, 429/29, 429/50, 429/101, 429/198, 429/70
• US Class Current: 429/51
• CPC Class Codes: H01M 10/365 Zinc-halogen accumulators
• CPC Class Codes: Y02E 60/10 Energy storage using batteries

Abstract

A metal halogen cell, especially a zinc-bromine cell, employs a circulating electrolyte system containing a complexing agent to effectively remove cathodic halogen from the electrolyte during charging of the cell. The complexing agent is one which in the presence of halogen forms a water insoluble halogen complex. This separated and stored source of cathodic halogen can be returned to the cell during cell discharge.

Claims

1. An electrochemical cell having a metal bromine couple comprising:

an electrode structure on which to deposit the metal of the metal bromine couple;

an inert counterelectrode structure at which to generate the bromine of the metal bromine couple;

an aqueous electrolyte containing a metal bromide and a bromine complexing agent, the metal of said metal bromide being selected from zinc and cadmium, said bromine complexing agent being selected from water soluble organic quaternary ammonium compounds and mixtures of quaternary ammonium compounds with water soluble organic solvents which in the presence of bromine and at temperatures in the range of about 10°

C to about 60°

C form a substantially water immiscible liquid;

means for circulating said electrolyte between said electrode structures during charging of the cell;

a separation zone communicating with said cell whereby bromine complex formed during charging of the cell is separated from said aqueous electrolyte; and

,

means for circulating separated bromine complex from said separation zone to said cell during discharge of said cell.

2. The cell of claim 1 wherein said metal is zinc.

3. The cell of claim 2 wherein said metal is cadmium.

4. The cell of claim 1 whereby said means for circulating separated bromine complex to said cell during discharge of said cell includes mixing means for emulsifying said complex in said electrolyte.

5. The cell of claim 1 including a cationic exchange membrane separator between said electrode and said counterelectrode thereby defining an anolyte compartment and a catholyte compartment;

means for separately circulating electrolyte through said anolyte compartment and said catholyte compartment during charging of the cell; and

,

said separation zone communicating with said catholyte compartment only.

6. An electrochemical cell comprising:

a metal anode selected from zinc and cadmium;

an inert counterelectrode;

a bromine cathode;

an aqueous metal bromide electrolyte system, the metal of the metal bromide being the same as the metal of the anode;

a bromine complexing substituent present in said aqueous electrolyte, said complexing substituent being selected from water soluble organic quaternary ammonium compounds and mixtures of quaternary ammonium compounds with water soluble organic solvents, said bromine complexing substituent being one which in the presence of bromine forms a substantially water insoluble liquid at temperatures of about 10°

C to about 60°

C;

means for circulating said aqueous electrolyte system between said anode and said counterelectrode during charging of the cell;

a holding tank external said cell and communicating therewith whereby liquid bromine complex formed during charging of the cell is removed from said cell and substantially separated from said electrolyte;

mixing means for emulsifying said bromine complex in said electrolyte; and

means for circulating liquid bromine complex through said cell during discharge of said cell.

7. The cell of claim 6 wherein the metal anode is zinc.

8. The cell of claim 7 wherein the metal anode is cadmium.

9. An aqueous zinc-bromine electrochemical cell comprising:

a positive electrode and a negative electrode disposed within a housing;

an aqueous zinc bromide solution containing a water soluble quaternary ammonium compound complexing agent which in the presence of bromine forms a substantially water insoluble bromine complex which is liquid at temperatures in the range of about 10°

C. to about 60°

C.;

a tank external said cell for holding aqueous electrolyte when said cell is in a discharged state and for holding said electrolyte and said bromine complex when said cell is in a charged state;

circulating means communicating with said holding tank and said cell whereby said electrolyte is circulated between said electrodes during charging of said cell and said electrolyte and bromine complex is circulated between said electrodes during discharging of said cell.

10. An aqueous zinc-bromine electrochemical cell comprising:

a positive electrode and a negative electrode disposed in a housing and separated by a cationic exchange membrane thereby defining an anode compartment and a cathode compartment;

an aqueous catholyte containing a source of bromine ions and a complexing agent, said complexing agent being selected from insoluble quaternary ammonium compounds and mixtures of water soluble quaternary ammonium compounds with water soluble organic solvents, said complexing agent being one which in the presence of bromine forms a water insoluble liquid bromine complex at temperatures in the range of 10°

C to 60°

C;

an aqueous anolyte containing a source of zinc ions;

means for circulating anolyte through said anode compartment;

means for circulating catholyte through said cathode compartment;

a separation zone communicating with said cathode compartment whereby liquid bromine complex is separated from said circulating catholyte during cell charging; and

,

means for circulating said liquid bromine complex through said cathode compartment during discharging of said cell.

11. A method of operating a metal bromine electrochemical cell comprising:

providing an aqueous electrolyte containing a metal bromide, and a bromine complexing agent, said metal bromide being selected from zinc and cadmium bromides, said bromine complexing agent being selected from water soluble quaternary ammonium compounds and mixtures of quaternary ammonium compounds with water soluble organic solvents which complexing agent in the presence of bromine forms a substantially water insoluble liquid bromine complex at temperatures in the range of 10°

C to 60°

C;

circulating said aqueous electrolyte between two electrodes while simultaneously impressing an electric potential thereon whereby the metal of the metal bromide is deposited on one electrode substantially free of dendrites and bromine is generated at the other electrode and complexed thereat by said complexing agent;

circulating said bromine complex and said electrolyte through a separation zone whereby said bromine complex is substantially removed from said electrolyte whereby said cell remains substantially in a charged state; and

,

circulating said bromine complex between said electrodes when withdrawing power from said cell.

12. The method of claim 11 wherein said metal halide is zinc bromide.

13. The method of claim 12 wherein said complexing agent is a quaternary ammonium compound.

14. The method of claim 11 wherein said cell is provided with a cationic exchange membrane separator defining a catholyte compartment and an anolyte compartment and wherein said electrolyte is circulated through the catholyte compartment and an aqueous solution containing metal ions selected from zinc and cadmium is circulated through the anolyte compartment while impressing an electric potential between the two electrodes, and wherein the bromine complex formed and the electrolyte are circulated through said separation zone and said bromine complex is returned to said catholyte compartment when withdrawing power from said cell.