Electrolytic cell equipped with concentric electrode pairs
US-9222181-B2 · Dec 29, 2015 · US
US9447511B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9447511-B2 |
| Application number | US-201314046472-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 4, 2013 |
| Priority date | Oct 4, 2013 |
| Publication date | Sep 20, 2016 |
| Grant date | Sep 20, 2016 |
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The present invention relates to catalysts for the production of CO gas through electrochemical CO 2 reduction. In particular, the present invention relates to an electrochemical cell comprising an iron porphyrin as the catalyst for the CO 2 reduction into CO, a method of performing electrochemical reduction of CO 2 using said electrochemical cell thereby producing CO gas, and a method of performing electrochemical reduction of CO 2 using said iron porphyrin catalyst thereby producing CO gas.
Opening claim text (preview).
The invention claimed is: 1. Method comprising performing electrochemical reduction of CO 2 thereby producing CO gas, using the porphyrin of formula (I): wherein R1 represents OH, or C 1 -C 4 -alcohol, R2, R3, R4, R5, R6 and R7 independently represent H, OH, or C 1 -C 4 -alcohol, and Fe represents either Fe(0), Fe(I), Fe(II) or Fe(III); as a catalyst in an electrochemical cell for said electrochemical reduction of CO 2 into CO. 2. The method of claim 1 , wherein the potential applied to the cathode is between −2.5 and −0.5 V versus NHE. 3. The method of claim 1 , wherein the intensity applied to the cathode is between 2.0 and 5.0 A/m 2 . 4. The method of claim 1 , wherein R1 represents OH. 5. The method of claim 1 , wherein R2 represents OH. 6. The method of claim 1 , wherein R1, R2 and R3 represents OH. 7. The method of claim 1 , wherein said porphyrin is 8. The method of claim 1 , wherein the CO 2 is being reduced by the porphyrin of formula (I) with iron transition metal in the state Fe(0). 9. The method of claim 1 , wherein the electrochemical reduction of CO 2 into CO is carried out at 1 bar of CO 2 . 10. The method of claim 1 , wherein the faradic yield in CO is of between 84% and 99%. 11. The method of claim 1 , wherein no formation of formic acid or formate is observed.
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