Alternative low cost electrodes for hybrid flow batteries
US-2024047707-A1 · Feb 8, 2024 · US
US2018358642A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018358642-A1 |
| Application number | US-201816005783-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 12, 2018 |
| Priority date | Jun 12, 2017 |
| Publication date | Dec 13, 2018 |
| Grant date | — |
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Anode half-cells for the electrocatalytic oxidation of a liquid or gaseous fuel or other reductant are disclosed, along with electrochemical cells that include such half-cells. The anode half-cells include redox mediator/heterogeneous redox catalyst pairs within an electrolyte solution that is also in contact with an electrode. The electrode is not in direct contact with the heterogeneous catalyst. The redox mediator must include at least one carbon atom and be capable of transferring or accepting electrons and protons while undergoing reduction or oxidation. In operation, the fuel or other reductant is oxidized and the redox mediator is reduced at the heterogeneous catalyst. The reduced form of the redox mediator can then migrate to the electrode, where it is converted back to its oxidized form, which can then migrate back to the heterogeneous catalyst, where the cycle is repeated. The disclosed anode half-cells can be used in electrochemical cells, such as in fuel cells that produce electricity, or in electrosynthetic cells that produce one or more desired chemical products.
Opening claim text (preview).
1 . An anode half-cell for oxidizing a fuel or other reductant, the anode half-cell comprising: an electrolyte solution (anolyte) that is in contact with an electrode (anode) and a heterogeneous redox catalyst, wherein the electrode is not in direct contact with the heterogeneous redox catalyst; and a redox mediator comprising at least one carbon atom, wherein the redox mediator is capable of transferring or accepting electrons and protons while undergoing reduction or oxidation. 2 . The anode half-cell of claim 1 , wherein the redox mediator is dissolved within the electrolyte solution and is capable of moving between the electrode and the heterogeneous redox catalyst. 3 . The anode half-cell of claim 1 , further comprising a fuel or other reductant. 4 .- 7 . (canceled) 8 . The anode half-cell of claim 1 , wherein the reduced form of the redox mediator is selected from the group consisting of substituted dihydroxybenzenes, substituted hydrazines, substituted hydroxylamines, and substituted heterocycles, such as dihydropyridines, dihydroflavins, or dihydroindigos. 9 . The anode half-cell of claim 8 , wherein the substituted dihydroxybenzene is a 1,2-dihydroxybenzene or a 1,4-dihydroxybenzene. 10 . The anode half-cell of claim 8 , wherein the substituted dihydroxybenzene has one or more dihydroxybenzene hydrogen atoms on the ring substituted with a substituent group that is independently selected from the group consisting of an alkyl with less than ten carbons, an aryl, a fused aryl, a heterocycle, an alkenyl, an alkynyl, a cycloalkyl, an amine, a protonated amine, a quaternary amine, sulfate, a sulfonate, a mercaptoalkylsulfonate, sulfonic acid, phosphate, a phosphonate, a phosphinate, a ketone, an aldehyde, an oxime, a hydrazine, a nitrone, an ether, an ester, a halide, a nitrile, a carboxylate, an amide, a thioether, a fluoroalkyl, a perfluoroalkyl, a pentafluorosulfanyl, a sulfonamide, a sulfonic ester, an imide, carbonate, a carbamate, a urea, a sulfonylurea, an azide, a sulfone, a sulfoxide, an amine oxide, phosphine oxide, a quaternary phosphonium, a quaternary borate, a siloxane, a nitro, and combinations of two or more of the foregoing; and wherein at least one of the substituent groups is charged to increase the aqueous solubility of the substituted dihydroxybenzene. 11 . The anode half-cell of claim 10 , wherein the fused aryl is selected from the group consisting of naphthohydroquinone, anthrahydroquinone, and derivatives thereof. 12 . The anode half-cell of claim 8 , wherein the substituted hydrazine has one or more hydrazine hydrogen atoms substituted with a substituent group that is independently selected from the group consisting of an alkyl with less than ten carbons, an aryl, a heterocycle, an alkenyl, an alkynyl, a cycloalkyl, an amine, a protonated amine, a quaternary amine, sulfate, a sulfonate, a mercaptoalkylsulfonate, sulfonic acid, phosphate, a phosphonate, a phosphinate, a ketone, an aldehyde, an oxime, a hydrazine, a nitrone, an ether, an ester, a halide, a nitrile, a carboxylate, an amide, a thioether, a fluoroalkyl, a perfluoroalkyl, a pentafluorosulfanyl, a sulfonamide, a sulfonic ester, an imide, carbonate, a carbamate, a urea, a sulfonylurea, an azide, a sulfone, a sulfoxide, an amine oxide, phosphine oxide, a quaternary phosphonium, a quaternary borate, a siloxane, a nitro, and combinations of two or more of the foregoing; and wherein at least one of the substituent groups is charged to increase the aqueous solubility of the substituted hydrazine. 13 . The anode half-cell of claim 8 , wherein the substituted hydroxylamine has one or more nitrogen-bound hydroxylamine hydrogen atoms substituted with a substituent group that is independently selected from the group consisting of an alkyl with less than ten carbons, an aryl, a cycloalkyl, and a bicycloalkyl. 14 . (canceled) 15 . The anode half-cell of claim 13 , wherein one or more of the substituent groups further comprises an alkyl with less than ten carbons, an aryl, a heterocycle, an alkenyl, an alkynyl, a cycloalkyl, an amine, a protonated amine, a quaternary amine, sulfate, a sulfonate, a mercaptoalkylsulfonate, sulfonic acid, phosphate, a phosphonate, a phosphinate, a ketone, an aldehyde, an oxime, a hydrazine, a nitrone, an ether, an ester, a halide, a nitrile, a carboxylate, an amide, a thioether, a fluoroalkyl, a perfluoroalkyl, a pentafluorosulfanyl, a sulfonamide, a sulfonic ester, an imide, carbonate, a carbamate, a urea, a sulfonylurea, an azide, a sulfone, a sulfoxide, an amine oxide, phosphine oxide, a quaternary phosphonium, a quaternary borate, a siloxane, a nitro, and combinations of two or more thereof on the same or on different positions on the substituent; and wherein at least one of the substituents is charged to increase the aqueous solubility of the substituted hydroxylamine. 16 . The anode half-cell of claim 8 , wherein the substituted heterocycle, such as a dihydropyridine, dihydroflavin, or dihydroindigo, has one or more heterocycle hydrogen atoms substituted with a substituent group that is selected from the group consisting of an alkyl with less than ten carbons, an aryl, a heterocycle, an alkenyl, an alkynyl, a cycloalkyl, an amine, a protonated amine, a quaternary amine, sulfate, a sulfonate, a mercaptoalkylsulfonate, sulfonic acid, phosphate, a phosphonate, a phosphinate, a ketone, an aldehyde, an oxime, a hydrazine, a nitrone, an ether, an ester, a halide, a nitrile, a carboxylate, an amide, a thioether, a fluoroalkyl, a perfluoroalkyl, a pentafluorosulfanyl, a sulfonamide, a sulfonic ester, an imide, carbonate, a carbamate, a urea, a sulfonylurea, an azide, a sulfone, a sulfoxide, an amine oxide, phosphine oxide, a quaternary phosphonium, a quaternary borate, a siloxane, a nitro, and combinations of two or more thereof on the same or on different positions on the substituent; and wherein at least one of the substituents is charged to increase the aqueous solubility of the substituted heterocycle. 17 . The anode half-cell of claim 1 , wherein the heterogeneous redox catalyst comprises one or more metals selected from the group consisting of Pt, Pd, Ru, Co, Mn, Fe, Cu, V, Mo, Rh, Ag, Au, W, Os, Ni, Cr, and Ir. 18 .- 20 . (canceled) 21 . The anode half-cell of claim 1 , further comprising an anode flow reactor containing the heterogeneous redox catalyst, wherein the anode flow reactor is configured to facilitate contact of the heterogeneous redox catalyst with a flowing fluid comprising the electrolyte solution, the redox mediator, and a fuel or other reductant. 22 .- 23 . (canceled) 24 . An electrochemical cell comprising the anode half-cell of claim 1 in fluid communication with a cathode half-cell. 25 . The electrochemical cell of claim 24 , wherein the electrochemical cell is a fuel cell or an electrosynthetic cell. 26 . The electrochemical cell of claim 24 , further comprising: a cathode inlet configured to allow O 2 or air to flow into the cathode half-cell, whereby O 2 can be reduced; an anode inlet configured to allow a gaseous or liquid fuel or other reductant to be delivered to the anode half-cell, whereby the fuel or other reductant can be oxidized; a semi-permeable membrane separating the anode half-cell and the cathode half-cell; and an external electrical circuit connecting the anode half-cell and the cathode half-cell. 27 . (canceled) 28 . The electrochemical cell of claim 26 , wherein the cathode half-cell comprises: an electrolyte solu
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