Electrolysis cell and electrolysis tank
US-2015027878-A1 · Jan 29, 2015 · US
US10487408B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10487408-B2 |
| Application number | US-201515527843-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 19, 2015 |
| Priority date | Nov 19, 2014 |
| Publication date | Nov 26, 2019 |
| Grant date | Nov 26, 2019 |
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A system and method for generating hydrogen gas from an aqueous solution are disclosed herein. The system comprises a compartment with a working electrode for reducing water in response to an applied voltage to generate hydrogen and a redox-active electrode capable of reversibly undergoing oxidation and reduction. The system may further comprise a second compartment with a working electrode for generating oxygen and redox-active electrode electrically connectable to the redox-active electrode in the first compartment. The method comprises applying a voltage between a working electrode and a redox-active electrode of a system described herein and/or between comprising a working electrode of one compartment and a working electrode of a second compartment of a system described herein.
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What is claimed is: 1. A system for generating hydrogen gas from an aqueous solution, the system comprising: a non-partitioned compartment comprising a working electrode and a redox-active electrode; said compartment having an inlet configured for receiving an aqueous solution, and at least one gas outlet configured for controllably evacuating a gas from the compartment, said working 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, and said redox-active electrode being capable of reversibly undergoing oxidation in the presence of hydroxide ions in said aqueous solution in response to the applied electrical bias, wherein said applied bias between the working electrode and redox-active electrode is at least 1.23V when measured at 25° C. 2. A system configured for alternate generation of hydrogen gas and oxygen gas from an aqueous solution, the system comprising: a compartment comprising a working electrode and a redox-active electrode; said compartment having an inlet for receiving an aqueous solution, and at least one gas outlet for controllably evacuating hydrogen gas or oxygen gas from the compartment, said working electrode being configured to affect reduction of water in said aqueous solution in response to applied electrical bias, to thereby generate hydrogen gas and hydroxide ions, said redox-active electrode being configured to reversibly undergo oxidation in the presence of the hydroxide ions in said aqueous solution in response to an applied electrical bias, and to undergo reduction to thereby generate oxygen gas in the absence of electrical bias, wherein said applied bias between the working electrode and redox-active electrode is of at least 1.23V when measured at 25° C. 3. The system according to claim 1 , wherein the applied electrical bias between the working and redox-active electrodes is between 1.23 and 1.8 V when measured at 25° C., between 1.23 and 1.6 V when measured at 25° C. or between 1.23 and 1.5 V when measured at 25° C. 4. The system according to claim 1 , wherein said redox-active electrode comprises nickel hydroxide (Ni(OH) 2 ). 5. The system according to claim 4 , wherein the nickel hydroxide is transformed by oxidation to a nickel oxyhydroxide (NiOOH). 6. The system according to claim 1 , further comprising a reservoir for receiving hydrogen gas from the gas outlet. 7. A method for generating hydrogen gas from an aqueous solution, in a non-partitioned cell, the method comprising applying an electrical bias of at least 1.23 V when measured at 25° C. between a working electrode and a redox-active electrode in said non-partitioned cell comprising an aqueous solution to cause reduction of water in said aqueous solution at said working electrode, to thereby generate hydrogen gas and hydroxide ions; said redox-active electrode reversibly undergoing oxidation in the presence of the hydroxide ions and optionally applying a stimulation to said cell to cause the oxidized redox-active electrode to generate oxygen gas. 8. A method for generating hydrogen gas and oxygen gas from an aqueous solution in a cell, the method comprising applying an electrical bias of at least 1.23 V when measured at 25° C. between a working electrode and a redox-active electrode, said cell comprising an aqueous solution to cause reduction of water in said aqueous solution at said working electrode, to thereby generate hydrogen gas and hydroxide ions; evacuate said hydrogen gas from the cell; said redox-active electrode reversibly undergoing oxidation in the presence of hydroxide ions to obtain an at least partially oxidized redox-active electrode causing the at least partially oxidized redox-active electrode to undergo reduction by applying a stimulation to the cell in the absence of electrical bias, to thereby regenerate the redox-active electrode and generate oxygen gas. 9. The method according to claim 8 for continuous alternate generation of hydrogen gas and oxygen gas from an aqueous solution, the method comprising applying an electrical bias of at least 1.23 V when measured at 25° C. between a working electrode and a redox-active electrode in a cell comprising an aqueous solution, to cause reduction of water in said aqueous solution and generation of hydrogen gas and hydroxide ions said redox-active electrode reversibly undergoing oxidation in the presence of the hydroxide ions to obtain an at least partially oxidized redox-active electrode and causing the at least partially oxidized redox-active electrode undergo regeneration to evolve oxygen gas; and subsequent reduction of water in said aqueous solution and generation of hydrogen gas. 10. The method according to claim 7 , wherein said stimulation comprises electric and/or thermal stimulation. 11. The method according to claim 7 , wherein the generation of hydrogen gas is achieved under applied bias between the working electrode and the redox electrode between 1.23 and 1.8 V when measured at 25° C., between 1.23 and 1.6 V when measured at 25° C. or between 1.23 and 1.5 V when measured at 25° C. 12. The method according to claim 7 , wherein the generation of oxygen gas is achieved in the absence of bias.
Operating or servicing cells · CPC title
Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features · CPC title
characterised by the material · CPC title
Process control or regulation · CPC title
by electrolysis of water · CPC title
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