Base Metal Catalyst
US-2015360178-A1 · Dec 17, 2015 · US
US10022703B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10022703-B2 |
| Application number | US-201414785279-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 11, 2014 |
| Priority date | Apr 17, 2013 |
| Publication date | Jul 17, 2018 |
| Grant date | Jul 17, 2018 |
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The disclosure concerns an improved method of preparation of nanoparticular vanadium oxide/anatase titania catalysts having a narrow particle size distribution. In particular, the disclosure concerns preparation of nanoparticular vanadium oxide/anatase titania catalyst precursors comprising combustible crystallization seeds upon which the catalyst metal oxide is coprecipitated with the carrier metal oxide, which crystallization seeds are removed by combustion in a final calcining step.
Opening claim text (preview).
The invention claimed is: 1. A method of preparation of nano-sized particular vanadium oxide/anatase titania catalysts, the nano-sized particular vanadium oxide/anatase titania catalysts comprising an anatase titania carrier and a catalytically active vanadium oxide component, the method comprising the following steps: a) providing a solution of an ammonium salt in a first solvent; b) providing a solution of one or more hydrolysable titania precursors and one or more hydrolysable vanadium precursors in a second solvent; c) combining the solutions of step a) and b) under acidic, aqueous conditions using hydrochloric acid, sulphuric acid or nitric acid, thereby hydrolyzing the one or more hydrolysable titania precursors and the one or more hydrolysable vanadium precursors; d) aging the reaction mixture of step c) thereby allowing the hydrolytic processes to proceed substantially to completion, thereby providing nano-sized particular titania catalyst precursors comprising crystallization seeds upon which the vanadium oxide is co-precipitated with the titania carrier material; e) removing solvents and volatile reaction components by either i) drying at atmospheric pressure and temperatures between 50° C. and 120° C. for between 50 hours and 200 hours, or ii) spray drying at temperatures between 50° C. and 120° C., and f) calcining the nano-sized particular titania catalysts precursor at temperature above 380° C. 2. A method according to claim 1 wherein the aging in step d) proceeds for between 0.5 and 8 hours. 3. A method according to claim 1 wherein the temperature used in step e) i) is between 70° C. and 95° C. 4. A method according to claim 1 , wherein the step e)i) proceeds for between 100 hours and 200 hours. 5. A method according to claim 1 wherein the temperature used in step e) ii) is between 60° C. and 90° C. 6. A method according to claim 1 , wherein the calcining in step f) proceeds for between 2 and 10 hours. 7. A method according to claim 1 , wherein the first solvent comprises water, and the second solvent is selected from polar, water miscible solvents; cyclic ethers; dialkylketones; alkylnitriles, and mixtures thereof, optionally comprising water. 8. A method according to claim 7 wherein the second solvent is selected from the group of C 1 -C 4 alcohols, tetra-hydrofuran, and mixtures thereof, optionally comprising water. 9. A method according to claim 1 , wherein the ammonium salt is: wherein each R group is individually selected from the group consisting of hydrogen, C 1 -C 12 alkyl, phenyl-C 1 -C 6 alkyl, alcohol-, ether-, ester-, amine-, amide-, cyano-, and halogen-functionalized alkyl chains, such that all four R groups are identical or three R groups are identical or two R groups are identical or all four R groups are different; and wherein X − is a negatively charged ion, a halide or an oxyanion. 10. A method according to claim 9 wherein the ammonium salt is a salt selected from the group consisting of ammonium chloride, ammonium bromide, ammonium nitrate, ammonium carbonate, ammonium hydrogen sulphate, ammonium hydrogen carbonate, ammonium carbamate and ammonium sulfate. 11. A method according to claim 1 , wherein the titania carrier further comprises a metal selected from the group consisting of zirconium, cerium, tungsten, silicon, aluminum, and a mixture thereof. 12. A method according to claim 1 , wherein the catalytically active vanadium oxide component further comprises an oxide of a metal selected from the group consisting of iron, copper, platinum, palladium, chromium, manganese, molybdenum and a mixture thereof. 13. A method according to claim 1 , wherein the one or more hydrolysable titania precursors is anatase titanium dioxide and the one or more hydrolysable vanadium catalyst precursors is vanadium oxide. 14. A method according to claim 13 wherein the vanadium oxide content in the nano-sized particular vanadium oxide/anatase titania catalysts is up to 25 wt %. 15. A method according to claim 1 , wherein prior to drying the mixture in step e), an effective amount of a strong acid, is added, wherein the strong acid is selected from the group consisting of hydrochloric acid, nitric acid, sulphuric acid, methanesulphonic acid and trifluoromethanesulphonic acid. 16. A method according to claim 1 , wherein the aging in step d) proceeds for 4 hours. 17. A method according to claim 1 , wherein the temperature used in step e) i) is 85° C. 18. A method according to claim 1 , wherein the step e)i) proceeds for between 80 hours and 90 hours. 19. A method according to claim 1 , wherein the temperature used in step e) ii) is between 50° C. and 80° C. 20. A method according to claim 1 , wherein the calcining in step f) proceeds for between 4 and 5 hours. 21. A method according to claim 7 , wherein the water miscible solvent is a C 1 -C 4 alcohol. 22. A method according to claim 7 , wherein the cyclic ether is tetra-hydrofuran. 23. A method according to claim 7 , wherein the dialkylketone is acetone. 24. A method according to claim 7 , wherein the alkylnitrile is acetonitrile. 25. A method according to claim 9 , wherein the negatively charged ion is a C 1 -C 4 carboxylate. 26. A method according to claim 9 , wherein the halide is chloride. 27. A method according to claim 9 , wherein the oxyanion is carbonate. 28. A method according to claim 14 , wherein the vanadium oxide content in the nano-sized particular vanadium oxide/anatase titania catalysts is up to 20 wt %. 29. A method according to claim 15 , wherein 0.05-1 mole protons per mole metal oxide is added.
Precipitation on carriers · CPC title
Manufacture or treatment of nanostructures · CPC title
Vanadium · CPC title
Titanium; Oxides or hydroxides thereof · CPC title
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
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