Electrocatalytic hydrogen evolution and biomass upgrading
US-2018023199-A1 · Jan 25, 2018 · US
US12180601B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12180601-B2 |
| Application number | US-201917277063-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 24, 2019 |
| Priority date | Sep 24, 2018 |
| Publication date | Dec 31, 2024 |
| Grant date | Dec 31, 2024 |
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A system and method for oxidizing organic molecules as an oxygen-atom source using an electrochemical process is described.
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What is claimed is: 1. A method of generating an oxidized substrate comprising: contacting an anode including an oxygen atom transfer epoxidation catalyst composition with a substrate, the oxygen atom transfer epoxidation catalyst composition including single atoms of one element of Re, Ir, Pt, Au, Ru, Rh, or Pd supported on a nanostructured material containing an oxide or metal nanoparticle including Ti, Cr, Mn, Co, Ni, Cu, or Zn; contacting the anode with a direct oxygen atom source; applying a voltage to the anode and a cathode to produce an oxidized substrate; wherein the cathode includes a hydrogen generation catalyst; and generating an epoxide and hydrogen gas. 2. The method of claim 1 , wherein the oxygen atom transfer epoxidation catalyst composition includes a metal oxide, metal hydroxide, metal phosphate, metal borate, metal sulfide, metal phosphide, or metal nitride, or combinations thereof. 3. The method of claim 1 , wherein the oxygen atom transfer epoxidation catalyst composition includes a manganese oxide, a titanium oxide, a copper oxide, a zinc oxide, a cobalt oxide, a cobalt phosphide, an iron oxide, a nickel oxide, an iridium oxide, a platinum oxide, or a chromium oxide. 4. The method of claim 1 , wherein the oxidized substrate is produced at a Faradaic yield of at least 20%. 5. The method of claim 1 , wherein the oxygen atom source is water without the need to generate a soluble oxidant from the water. 6. The method of claim 1 , wherein hydrogen gas is produced at the cathode. 7. The method of claim 6 , wherein hydrogen gas is produced at a Faradaic yield of at least 70%. 8. The method of claim 1 , wherein the cathode includes an oxygen reduction catalyst. 9. The method of claim 1 , wherein oxygen is introduced at the cathode and water is produced. 10. The method of claim 1 , wherein a hydrogenation reaction of an organic substrate is conducted at the cathode. 11. The method of claim 1 , wherein the substrate is an olefin that is oxidized to form the epoxide. 12. The method of claim 1 , wherein the substrate contains a C—H bond oxidized to form a product containing a carbon-oxygen bond. 13. The method of claim 1 , wherein the substrate is supplied to the anode at a concentration of 5 mM, 10 mM, 15 mM, 20 mM, 25 mM, 30 mM, 35 mM, 40 mM, 50 mM, 60 mM, 70 mM, 80 mM, 90 mM, 100 mM, 200 mM, 250 mM, 300 mM, 350 mM, 400 mM, 450 mM, 500 mM, 1 M, 2 M, 4 M, 6 M, 8 M, or 10 M. 14. The method of claim 1 , wherein the oxygen atom source is supplied at a concentration of 0.1 M, 0.25 M, 0.5 M, 1 M, 2 M, 4 M, 6 M, 8 M, 10 M, 12 M, 14 M, 16 M, 18 M or 20 M. 15. The method of claim 1 , wherein the voltage is between about 0.2V and 9.0V. 16. The method of claim 1 , wherein the voltage is 0.5V, 0.6V, 0.7V, 0.8V, 0.9V, 1.0V, 1.1V, 1.2V, 1.3V, 1.4V, 1.6V, 1.7V, 1.8V or 1.9V. 17. The method of claim 1 , wherein the cathode includes a noble metal, nickel-molybdenum-zinc alloys, cobalt phosphide, or nickel phosphide. 18. The method of claim 1 , wherein the method is carried out substantially at room temperature.
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