Solar powered CO2 conversion
US-9528192-B1 · Dec 27, 2016 · US
US10597787B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10597787-B2 |
| Application number | US-201615260982-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 9, 2016 |
| Priority date | May 20, 2014 |
| Publication date | Mar 24, 2020 |
| Grant date | Mar 24, 2020 |
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An electrochemical reaction device includes: an electrolytic solution tank to store an electrolytic solution; an oxidation electrode disposed in the electrolytic solution tank; a reduction electrode disposed in the electrolytic solution tank; and a generator connected to the oxidation electrode and the reduction electrode. At least one of the oxidation electrode or the reduction electrode has a porous structure containing fine pores.
Opening claim text (preview).
What is claimed is: 1. An electrochemical reaction device, comprising: an electrolytic solution tank; an oxidation electrode disposed in the electrolytic solution tank; a reduction electrode disposed in the electrolytic solution tank; and a generator connected to the oxidation electrode and the reduction electrode, wherein the reduction electrode has a carbon porous layer having a porous structure with a pore distribution of 5 μm or more and 10 μm or less, and a metal porous layer disposed on the carbon porous layer, the metal porous layer having a porous structure with a pore distribution of 5 nm or more and 100 nm or less and containing particles of a reduction catalyst of 100 nm or less, the reduction catalyst being at least one selected from the group consisting of Au, Ag, Cu, Pt, Ni, Zn and Pd, wherein the generator has a photovoltaic body having a first face connected to the oxidation electrode and a second face connected to the reduction electrode, and is configured to perform charge separation by energy of light irradiated on the first face or the second face, wherein the oxidation electrode is in contact with the first face of the photovoltaic body, and has a first through hole which is capable of passing an electrolytic solution through, wherein the reduction electrode is in contact with the second face of the photovoltaic body, and has a second through hole which is capable of passing the electrolytic solution through, and wherein the photovoltaic body has a third through hole which is capable of passing the electrolytic solution through and communicated with the first through hole and the second through hole. 2. The device of claim 1 , wherein the particles of the reduction catalyst have a particle size of 5 nm or less for 25% or more of a total number of particles. 3. The device of claim 1 , wherein the metal porous layer has three pieces or more of voids each having a width of 300 nm or more in a range of 40 micrometers in width, or five pieces or more of voids each having a width of 100 nm or more in the range of 40 micrometers in width. 4. The device of claim 3 , wherein the metal porous layer is formed by applying a high frequency having a minimum potential of a reduction potential of the metal porous layer or less and a maximum potential of an oxidation potential of the metal porous layer or more. 5. The device of claim 1 , wherein the reduction electrode contains a surface active agent. 6. The device of claim 5 , wherein the surface active agent has polyvinylpyrrolidone or polyvinyl alcohol. 7. The reaction device of claim 1 , wherein the reduction electrode has an ion exchange resin. 8. The device of claim 1 , further comprising: an ion exchange membrane provided to block at least one of the first through hole to the third through hole to allow permeation of a part of ions contained in the electrolytic solution. 9. The device of claim 1 , further comprising: a stirrer disposed in the electrolytic solution tank; a pH sensor disposed in the electrolytic solution tank and configured to measure a pH value of an electrolytic solution; and a supply flow path connected to with the electrolytic solution tank, wherein a reactant for adjusting the pH value of the electrolytic solution is supplied to the electrolytic solution tank through the supply flow path when the pH value of the electrolytic solution measured by the pH sensor is out of a reference range. 10. The device of claim 1 , wherein the reduction catalyst is at least one selected from the group consisting of Au, Ag, Pt, Ni, Zn, and Pd.
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