High Performance Bifunctional Porous Non-Noble Metal Phosphide Catalyst for Overall Water Splitting
US-2021189574-A1 · Jun 24, 2021 · US
US11413611B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11413611-B2 |
| Application number | US-201916707005-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 9, 2019 |
| Priority date | Dec 9, 2019 |
| Publication date | Aug 16, 2022 |
| Grant date | Aug 16, 2022 |
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An electrocatalyst comprising molybdenum disulfide nanosheets with dispersed iron phosphide nanoparticles is described. The molybdenum disulfide nanosheets may have an average length in a range of 300 nm-1 μm and the iron phosphide nanoparticles may have an average diameter in a range of 5-20 nm. The electrocatalyst may have an electroactive surface area in a range of 10-50 mF·cm−2 when deposited on a working electrode for use in a hydrogen evolution reaction.
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The invention claimed is: 1. An electrocatalyst, comprising: molybdenum disulfide nanosheets having an average length in a range of 300 nm 1 μm, and iron phosphide nanoparticles having an average diameter in a range of 5-20 nm, wherein the iron phosphide nanoparticles are distributed on the molybdenum disulfide nanosheets with an average nearest neighbor distance of the nanoparticles between 12-20 nm. 2. The electrocatalyst of claim 1 , wherein the electrocatalyst consists essentially of Mo, S, Fe, and P. 3. The electrocatalyst of claim 1 , wherein the molybdenum disulfide nanosheets are crystalline with interplanar spacing in a range of 0.26-0.28 nm or 0.62-0.64 nm. 4. The electrocatalyst of claim 1 , wherein the molybdenum disulfide nanosheets have XRD peaks at 2(θ) Bragg angles of 33.2±1° and 59.1±1°. 5. The electrocatalyst of claim 1 , wherein the iron phosphide nanoparticles are crystalline with interplanar spacing in a range of 0.23-0.25 nm. 6. The electrocatalyst of claim 1 , wherein the iron phosphide nanoparticles have XRD peaks at 2(θ) Bragg angles of 37.2±1°, 48.3±1°, and 56.1±1°. 7. The electrocatalyst of claim 1 , which has an electroactive surface area in a range of 10-50 mF·cm −2 . 8. The electrocatalyst of claim 1 , wherein the iron phosphide nanoparticles have a Fe to P molar ratio in a range of 0.75-1.25. 9. The electrocatalyst of claim 8 , wherein the iron phosphide nanoparticles consist essentially of FeP. 10. The electrocatalyst of claim 1 , wherein a mass ratio of the iron phosphide nanoparticles to the molybdenum disulfide nanosheets is in a range of 0.60-0.95. 11. An electrocatalyst, comprising: molybdenum disulfide nanosheets having an average length in a range of 300 nm-1 μm, and iron phosphide nanoparticles having an average diameter in a range of 5-20 nm, and wherein the molybdenum disulfide nanosheets have an average thickness of less than 5 nm. 12. An electrocatalyst, comprising: molybdenum disulfide nanosheets having an average length in a range of 300 nm-1 μm, and iron phosphide nanoparticles having an average diameter in a range of 5-20 nm, and which has a BET surface area in a range of 10-20 m 2 /g. 13. An electrochemical cell, comprising: a working electrode comprising the electrocatalyst of claim 1 , a counter electrode, and an electrolyte solution in contact with both electrodes, the electrolyte solution comprising water and an inorganic acid. 14. The electrochemical cell of claim 13 , wherein the working electrode comprises the electrocatalyst deposited on glassy carbon, and wherein the working electrode has an overpotential in a range of 100-140 mV/cm 2 at a current density of 10 mA/cm 2 . 15. The electrochemical cell of claim 13 , wherein the inorganic acid has a concentration in a range of 0.2-1.0 M. 16. A method for producing H 2 from an acidic electrolyte solution, the method comprising: subjecting the electrodes of the electrochemical cell of claim 13 with a potential in a range of −1.0 to 1.0 V RHE . 17. The method of claim 16 , wherein the electrocatalyst has a turnover frequency in a range of 0.16-0.30 s −1 . 18. The method of claim 16 , wherein the electrocatalyst has a number of active sites per electrocatalyst mass in a range of 1.4 ×10 −4 to 1.4 ×10 −3 mol/g. 19. The method of claim 16 , further comprising separately collecting H 2 -enriched gas and O 2 -enriched gas.
Manufacture or treatment of nanostructures · CPC title
characterised by the substrate or carrier material · CPC title
with iron, cobalt or nickel · CPC title
Nanotechnology for materials or surface science, e.g. nanocomposites · CPC title
Electrodes formed of electrocatalysts on a substrate or carrier · CPC title
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