Fischer-tropsch catalyst based on a metal of group viiib and an oxides support comprising alumina, silica, a spinel and phosphorus
US-2015266006-A1 · Sep 24, 2015 · US
US11110438B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11110438-B2 |
| Application number | US-201916528124-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 31, 2019 |
| Priority date | Jul 31, 2018 |
| Publication date | Sep 7, 2021 |
| Grant date | Sep 7, 2021 |
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Described herein are catalysts relating to liquid synthesis, methods of their preparation, and methods of their use. In an embodiment according to the present disclosure, a method of producing a catalyst for liquid synthesis comprises: providing a silica oxide support; pretreating the silica oxide support to remove air and moisture; impregnating the pretreated silica oxide support with cobalt from a cobalt source using a cobalt impregnation method; and calcinating the impregnated silica oxide support in an oven with a temperature ramping profile, wherein the calcinating comprises feeding air into the oven.
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Therefore, the following is claimed: 1. A method of using a liquid synthesis catalyst, comprising: impregnating a silica oxide support with cobalt; drying the impregnated silica oxide support with an inert gas at a temperature of about 90° C. to about 130° C.; after drying with the inert gas, calcinating the impregnated silica oxide support in the presence of oxygen to produce a liquid synthesis catalyst; positioning the liquid synthesis catalyst in a reactor; bedding and packing the liquid synthesis catalyst in the reactor; reducing the liquid synthesis catalyst with H 2 gas; cooling the reactor to about 110° C. to about 160° C. while purging with H 2 gas and increasing the reactor pressure to a set pressure point; activating the liquid synthesis catalyst by introducing a gas stream into the reactor, wherein the gas stream comprises H 2 gas and CO from a CO source at a molar ratio of 2:1 H 2 to CO; and collecting the reaction products in a reaction vessel. 2. The method of claim 1 , wherein the bedding and packing comprises diluting the liquid synthesis catalyst with quartz and holding the mixture in a position in the reactor. 3. The method of claim 1 , wherein the set pressure point is about 150 psig to about 300 psig. 4. The method of claim 1 , further comprising separating the collected reaction products. 5. The method of claim 1 , wherein the inert gas is nitrogen (N 2 ) gas.
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