A method for decreasing feed impurities
US-2024350942-A1 · Oct 24, 2024 · US
US10815429B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10815429-B2 |
| Application number | US-201916281093-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 21, 2019 |
| Priority date | Sep 3, 2018 |
| Publication date | Oct 27, 2020 |
| Grant date | Oct 27, 2020 |
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Provided is a method for deoxygenating an oxygenated hydrocarbon compound using a hydrogenation catalyst of immersing a metal in a carrier comprising a metal oxide and a hydrodeoxygenation catalyst of immersing a metal in a carrier comprising a metal oxide. It is possible to increase deoxygenation efficiency by combining the hydrogenation catalyst and the hydrodeoxygenation catalyst.
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What is claimed is: 1. A method comprising: adding hydrogen and a mixture of oxygenated hydrocarbon compounds obtained by decomposition of biomass to a reactor, and subjecting the mixture to a hydrogenation reaction in the presence of a hydrogenation catalyst comprising at least one metal selected from the group consisting of nickel (Ni), palladium (Pd), and cobalt (Co) to provide a hydrogenated mixture, wherein the at least one metal of the hydrogenation catalyst is immersed in a carrier comprising a cerium oxide; and subjecting the hydrogenated mixture to a hydrodeoxygenation reaction in the presence of a hydrodeoxygenation catalyst comprising nickel (Ni) immersed in a mixed oxide carrier comprising tungsten and zirconium. 2. The method of claim 1 , wherein the carrier of the hydrogenation catalyst further comprises zirconia (zirconium oxide, ZrO 2 ). 3. The method of claim 1 , wherein the mixed oxide carrier of the hydrodeoxygenation catalyst is tungstate zirconia. 4. The method of claim 1 , wherein the at least one metal of the hydrogenation catalyst is nickel. 5. The method of claim 3 , wherein the content of the tungsten comprised in the tungstate zirconia is 5 wt % to 25 wt % based on the total weight of the mixed oxide carrier. 6. The method of claim 1 , wherein the content of the at least one metal immersed in the carrier of the hydrogenation catalyst is 1 wt % to 50 wt % based on the total weight of the hydrogenation catalyst. 7. The method of claim 1 , wherein the content of the at least one metal immersed in the carrier of the hydrodeoxygenation catalyst is 1 wt % to 50 wt % based on the total weight of the hydrodeoxygenation catalyst. 8. The method of claim 1 , wherein the reactor is a two or more step continuous reactor connecting the hydrogenation hydrodeoxygenation reactions. 9. The method of claim 1 , wherein the hydrogenation and hydrodeoxygenation reactions are carried out continuously in the reactor. 10. The method of claim 1 , wherein the hydrogenation reaction is carried out at 50° C. to 250° C. 11. The method of claim 1 , wherein the hydrodeoxygenation reaction is carried out at 200° C. to 400° C. 12. The method of claim 1 , wherein the hydrogenation reaction is carried out before the hydrodeoxygenation reaction to increase an oil yield. 13. The method of claim 1 , wherein the hydrogenation reaction is carried out before the hydrodeoxygenation reaction to suppress deactivation of the hydrodeoxygenation catalyst. 14. The method of claim 1 , wherein the mixture of oxygenated hydrocarbon compounds comprises at least one of guaiacol, diphenyl ether, or benzyl phenyl ether. 15. The method of claim 3 , wherein the content of tungsten in the tungstate zirconia is 5 wt % to 16 wt % based on the total weight of the mixed oxide carrier, and the at least one metal of the hydrodeoxygenation catalyst further comprises ruthenium.
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