Process for the production of a carbon supported catalyst
US-9873107-B2 · Jan 23, 2018 · US
US11110433B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11110433-B2 |
| Application number | US-201716084263-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 17, 2017 |
| Priority date | Mar 18, 2016 |
| Publication date | Sep 7, 2021 |
| Grant date | Sep 7, 2021 |
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The present invention relates to a metal-doped tin oxide which has a BET surface area of at least 30 m 2/g, and comprises at least one metal dopant which is Sb, Nb, Ta, Bi, W, or In, or any mixture thereof, wherein the metal dopant is present in an amount of from 2.5 at % to 25 at %, based on the total amount of tin and metal dopant atoms, and is in a mixed valence state containing atoms of oxidation state OS1 and atoms of oxidation state OS2, wherein the oxidation state OS1 is >0 and the oxidation state OS2 is >OS1 and the atomic ratio of the atoms of OS2 to the atoms of OS1 is from 1.5 to 12.0.
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The invention claimed is: 1. A metal-doped tin oxide which has a BET surface area of at least 30 m 2 /g, and comprises a dopant which is Sb, wherein the metal dopant is present in an amount of from 2.5 at % to 25 at %, based on the total amount of tin and metal dopant atoms, and is in a mixed valence state containing Sb 3+ atoms and Sb 5+ atoms, wherein the atomic ratio of Sb 5+ to Sb 3+ , measured by X-ray photoelectron spectroscopy, is from 5.0 to 9.0. 2. The metal-doped tin oxide according to claim 1 , wherein the amount of the metal dopant is from 2.5 at % to 10.0 at %. 3. The metal-doped tin oxide according to claim 1 , wherein the BET surface area of the metal-doped tin oxide is from 30 m 2 /g to 150 m 2 /g and/or the electrical conductivity of the metal doped tin oxide is at least 0.02 S/cm. 4. The metal-doped tin oxide according to claim 1 , wherein the amount of the metal dopant is from 5.0 at % to 7.5 at %. 5. The metal-doped tin oxide according to claim 1 , wherein the BET surface area of the metal-doped tin oxide is from 35 m 2 /g to 110 m 2 /g; and/or the electrical conductivity of the metal doped tin oxide is at least 0.03 S/cm. 6. The metal-doped tin oxide according to claim 1 , wherein the atomic ratio of the Sb 5+ atoms to the Sb 3+ atoms is from 5.0 to 8.0. 7. A process for preparing the metal-doped tin oxide according to claim 1 , comprising preparing a metal-doped precursor solid by a wet chemical synthesis from a reaction mixture comprising a tin-containing molecular precursor compound and a metal-dopant-containing molecular precursor compound, subjecting the metal-doped precursor solid to a thermal treatment. 8. The process according to claim 7 , wherein the wet chemical synthesis is a sol-gel process, a chemical precipitation process, a hydrothermal synthesis process, a spray drying process, or any combination thereof. 9. The process according to claim 7 , wherein the tin-containing molecular precursor compound and the metal-dopant-containing molecular precursor compound are mixed at acidic pH, and the pH is subsequently raised by adding a base until the metal-doped precursor solid precipitates; and/or wherein the wet chemical synthesis is carried out in an alcoholic solvent. 10. The process according to claim 7 , wherein the tin-containing molecular precursor compound is a tin salt such as a tin halide or a tin nitrate, or a tin alkoxide, or a mixture thereof; and/or the metal-dopant-containing molecular precursor compound is a metal halide, a metal carboxylate or a metal alkoxide or any mixture thereof. 11. The process according to claim 7 , wherein the wet chemical synthesis is carried out in the presence of a solid additive having a BET surface area of at least 40 m 2 /g. 12. The process according to claim 11 , wherein the solid additive is carbon black or activated carbon, which has a BET surface area of at least 200 m 2 /g. 13. The process according to claim 7 , wherein the thermal treatment includes heating to a temperature of from 400 to 800° C. 14. The process according to claim 11 , wherein the solid additive is carbon black or activated carbon, which has a BET surface area of at least 500 m 2 /g. 15. A composite material, comprising the metal-doped tin oxide according to claim 1 , and an electrocatalyst which is supported on the metal-doped tin oxide. 16. An electrochemical device, comprising the composite material according to claim 15 . 17. The electrochemical device according to claim 16 , wherein the electrochemical device is a polymer electrolyte membrane PEM water electrolyzer or a PEM fuel cell. 18. A catalyst support in an electrochemical device, comprising the metal-doped tin oxide according claim 1 , wherein the electrochemical device is a polymer electrolyte membrane PEM water electrolyzer or a PEM fuel cell.
Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title
supported on carriers, e.g. powder carriers · CPC title
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
by electrolysis of water · CPC title
of germanium, tin or lead · CPC title
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