The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
May. 18, 2021

Filed:

Jun. 21, 2018
Applicants:

China Energy Investment Corporation Limited, Beijing, CN;

National Institute of Clean-and-low-carbon Energy, Beijing, CN;

Inventors:

Peng Wang, Beijing, CN;

Kui Zhagn, Beijing, CN;

Yijun Lv, Beijing, CN;

Quan Lin, Beijing, CN;

Bo Feng, Beijing, CN;

Zhuowu Men, Beijing, CN;

Fengbo Zhang, Beijing, CN;

Qi Sun, Beijing, CN;

Ping Miao, Beijing, CN;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 27/22 (2006.01); B01J 21/08 (2006.01); B01J 21/04 (2006.01); B01J 21/06 (2006.01); B01J 35/02 (2006.01); B01J 37/02 (2006.01); B01J 37/08 (2006.01); B01J 37/18 (2006.01); C07C 1/04 (2006.01); C10G 2/00 (2006.01);
U.S. Cl.
CPC ...
B01J 27/22 (2013.01); B01J 21/04 (2013.01); B01J 21/063 (2013.01); B01J 21/08 (2013.01); B01J 35/026 (2013.01); B01J 37/0221 (2013.01); B01J 37/0236 (2013.01); B01J 37/088 (2013.01); B01J 37/18 (2013.01); C07C 1/044 (2013.01); C10G 2/32 (2013.01); C07C 2521/04 (2013.01); C07C 2521/06 (2013.01); C07C 2521/08 (2013.01); C07C 2523/745 (2013.01);
Abstract

The present disclosure relates to the technical field of Fischer-Tropsch synthesis reaction catalysts, and discloses a supported ε/ε' iron carbide catalyst for Fischer-Tropsch synthesis reaction, preparation method thereof and Fischer-Tropsch synthesis process, wherein the method comprises the following steps: (1) dipping a catalyst carrier in a ferric salt aqueous solution, drying and roasting the dipped carrier to obtain a catalyst precursor; (2) subjecting the catalyst precursor and Hto a precursor reduction at the temperature of 300-550° C.; (3) pretreating the material obtained in the step (2) with Hand CO at the temperature of 90-185° C., wherein the molar ratio of H/CO is 1.2-2.8:1; (4) preparing carbide with the material obtained in the step (3), Hand CO at the temperature of 200-300° C., wherein the molar ratio of H/CO is 1.0-3.2:1. The preparation method has the advantages of simple and easily obtained raw materials, simple and convenient operation steps, being capable of preparing the catalyst with 100% pure phase ε/ε′ iron carbide as the active phase, the catalyst has lower selectivity of COand CHand higher selectivity of effective products.


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