Flow cell systems, flow cell batteries, and hydrogen production processes
US-11050076-B1 · Jun 29, 2021 · US
US11414766B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11414766-B2 |
| Application number | US-201916982507-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 20, 2019 |
| Priority date | Mar 20, 2018 |
| Publication date | Aug 16, 2022 |
| Grant date | Aug 16, 2022 |
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Provided are electrochemical cells and methods for generating hydrogen gas and oxygen gas.
Opening claim text (preview).
The invention claimed is: 1. An electrochemical system for generating hydrogen gas and/or oxygen gas, the system comprising: two or more electrochemical thermally activated chemical (ETAC) cells, wherein at least two of said two or more cells are non-partitioned cells, each cell configured for holding an aqueous solution and comprising at least one electrode assembly, each having a cathode electrode and an anode electrode, said two or more ETAC cells being configured to generate hydrogen gas in the presence of electrical bias, and generate oxygen gas in the absence of bias, and a control unit configured to operate the two or more cells in a continuous hydrogen generation mode, wherein the continuous mode comprises two or more operation cycles, wherein in a first operation cycle, generation of hydrogen gas in at least one of the two or more cells, in parallel to generation of oxygen gas in at least one different cell of the two or more cells and in a second operation cycle, generation of hydrogen gas in the at least one different cell of the two or more cells, in parallel to generation of oxygen gas in the at least one of the two or more cells. 2. The system according to claim 1 , the system comprising: two or more ETAC cells, each configured for holding an aqueous solution and comprising at least one electrode assembly, each having a cathode electrode and an anode electrode, said cathode electrode being configured to affect reduction of water in said aqueous solution in response to an applied electrical bias, to thereby generate hydrogen gas and hydroxide ions, said anode electrode being capable of reversibly undergoing oxidation in the presence of hydroxide ions, and undergoing reduction in the absence of bias, to generate oxygen gas, and a control unit configured to operate the two or more cells in accordance with a predetermined operational pattern. 3. The system according to claim 1 , comprising a heat source or a heat exchanger. 4. The system according to claim 1 , wherein the control unit is further configured to operate the two or more cells in accordance with a predetermined operational pattern, wherein the operational pattern provides for each cell in the two or more cells an output in a form of at least one of mode selector and operational parameter selector. 5. The system according to claim 1 , wherein the control unit is further configured to operate the two or more cells in accordance with a predetermined operational pattern, wherein the operational pattern provides an output comprising at least one of (i) applied bias, (ii) timing for operation, and (iii) duration of operation of each of the two or more cells. 6. The system according to claim 5 , wherein the operational pattern further provides a temperature value for each of the two or more cells. 7. The system according to claim 1 , wherein the two or more cells are separated, having essentially no fluid or gas communication. 8. The system according to claim 1 , further comprising at least one inlet and at least one outlet configured to allow circulation of the aqueous solution and of the gas in the system. 9. The system according to claim 8 , wherein the at least one inlet is for receiving an aqueous solution into the two or more cells and at least one outlet for evacuating an aqueous solution and/or a gas from the two or more cells. 10. The system according to claim 1 , wherein the electrode assembly is selected from mono-polar assembly, bi-polar assembly, flat assembly and rolled assembly. 11. The system according to claim 1 , comprising at least one reservoir. 12. The system according to claim 1 , comprising at least one phase separator configured to extract the gas. 13. The system according to claim 1 , wherein the applied electric bias between the cathode and the anode electrodes in each of the at least one electrode assembly is at least 1.23V when measured at 25° C. 14. A method of generating hydrogen gas and/or oxygen gas, the method comprising: in a system comprising two or more electrochemical thermally activated chemical (E-TAC) cells, each cell containing an aqueous solution, each cell comprising an electrode assembly having a cathode electrode and an anode electrode and at least two of said two or more cells are non-partitioned cells, wherein the method is operable in a continuous mode comprising two or more operation cycles, wherein in a first operation cycle, generation of hydrogen gas in at least one of the two or more cells, in parallel to generation of oxygen gas in at least one different cell of the two or more cells and in a second operation cycle, generation of hydrogen gas in the at least one different cell of the two or more cells, in parallel to generation of oxygen gas in the at least one of the two or more cells, wherein hydrogen gas is generated by applying an electrical bias between the anode and cathode electrodes of at least one of the two or more cells and oxygen gas is generated by discontinuing the bias applied between the anode and cathode within the at least one of the two or more cells.
Renewable energy sources, e.g. sunlight · CPC title
Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title
Hydrogen or oxygen · CPC title
Assemblies comprising two or more cells · CPC title
by electrolysis of water · CPC title
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