Methods utilizing active quantum chemistry
US-2024317612-A1 · Sep 26, 2024 · US
US2018195182A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018195182-A1 |
| Application number | US-201615741607-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 29, 2016 |
| Priority date | Sep 29, 2015 |
| Publication date | Jul 12, 2018 |
| Grant date | — |
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Provided herein are scalable photoreactors that can include a membrane-free water-splitting electrolyzer and systems that can include a plurality of membrane-free water-splitting electrolyzers. Also provided herein are methods of using the scalable photoreactors provided herein.
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1 . A membrane-free water-splitting electrolyzer comprising: a power source configured to generate about 1.4 V to about 2.2 V; a rail reactor, wherein the rail reactor is operatively coupled to the power source, and wherein the rail reactor comprises a first and a second “U” shaped channel; and an electrocatalyst element, wherein the electrocatalyst element comprises a first and a second electrocatalyst, wherein the first electrocatalyst and the second electrocatalyst are electrically coupled to the power source, wherein the first electrocatalyst is positioned within the first “U” shaped channel, and wherein the second electrocatalyst is positioned within the second “U” shaped channel. 2 . The membrane-free water-splitting electrolyzer of claim 1 , wherein the power source is a solar cell. 3 . The membrane-free water-splitting electrolyzer of claim 1 , wherein the first “U” shaped channel and the second “U” shaped channel each comprise an alkaline resistant polymer or co-polymer. 4 . The membrane-free water-splitting electrolyzer of claim 1 , wherein the first electrocatalyst and the second electrocatalyst each comprise a transition metal, a noble metal, or a transition metal and a noble metal. 5 . The membrane-free water-splitting electrolyzer of claim 1 , wherein at least one component of the membrane-free water-splitting electrolyzer is in fluidic contact with an electrolyte solution. 6 . The membrane-free water-splitting electrolyzer of claim 5 , wherein the electrolyte solution is a densely buffered electrolyte solution. 7 . The membrane-free water-splitting electrolyzer of claim 5 , wherein the electrolyte solution is an acidic buffered electrolyte solution, an alkali buffered electrolyte solution, or a neutral buffered electrolyte solution. 8 . A system comprising: a plurality of rows, wherein each row of the plurality of rows comprises a plurality of membrane-free water-splitting electrolyzers, wherein each membrane-free water-splitting electrolyzer of the plurality of membrane-free water-splitting electrolyzers comprises: a rail reactor, wherein the rail reactor is operatively coupled to a power source configured to generate about 1.4 V to about 2.2 V, and wherein the rail reactor comprises a first “U” shaped channel and a second “U” shaped channel; and an electrocatalyst element, wherein the electrocatalyst element comprises a first electrocatalyst and a second electrocatalyst, wherein the first and the second electrocatalyst are electrically coupled to the power source, wherein the first electrocatalyst is positioned within the first “U” shaped channel, and wherein the second electrocatalyst is positioned within the second “U” shaped channel. 9 . The system of claim 8 , wherein each row of the plurality of rows is coupled to at least one other row in the plurality of rows via one or more of the first “U” shaped channels or second “U” shaped channels of the membrane-free water-splitting electrolyzers. 10 . The system of claim 8 , wherein at least one component of the membrane-free water-splitting electrolyzer is in fluidic contact with an electrolyte solution. 11 . The system of claim 10 , wherein the electrolyte solution is a densely buffered electrolyte solution. 12 . The system of claim 10 , wherein the electrolyte solution is an acidic buffered electrolyte solution, an alkali buffered electrolyte solution, or a neutral buffered electrolyte solution. 13 . A method of water-splitting comprising: applying a voltage to a membrane-free rail reactor, wherein the rail reactor comprises a first “U” shaped channel and a second “U” shaped channel; and an electrocatalyst element, wherein the electrocatalyst element comprises a first electrocatalyst and a second electrocatalyst, wherein the first electrocatalyst is positioned within the first “U” shaped channel, wherein the second electrocatalyst is positioned with in the second “U” shaped channel. 14 . The method of claim 13 , wherein the voltage is about 1.4 V to about 2.2 V 15 . The method of claim 13 , wherein the electrocatalyst element is in fluidic contact with an electrolyte solution. 16 . The method of claim 15 , wherein the electrolyte solution is a densely buffered electrolyte solution. 17 . The method of claim 15 , wherein the electrolyte solution is an acidic buffered electrolyte solution, an alkali buffered electrolyte solution, or a neutral buffered electrolyte solution. 18 . The method of claim 13 , further comprising generating the voltage, wherein the voltage is generated by a solar cell. 19 . The method of claim 13 , wherein the first “U” shaped channel and the second “U” shaped channel each comprise an alkaline resistant polymer or co-polymer. 20 . The method of claim 13 , wherein the first electrocatalyst and the second electrocatalyst each contain a transition metal, a noble metal, or a transition metal and a noble metal.
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