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:
Jun. 04, 2024

Filed:

Dec. 10, 2019
Applicant:

Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian, CN;

Inventors:

Feng Jiao, Dalian, CN;

Na Li, Dalian, CN;

Xiulian Pan, Dalian, CN;

Xinhe Bao, Dalian, CN;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
B01J 29/70 (2006.01); B01J 29/72 (2006.01); B01J 29/76 (2006.01); B01J 29/78 (2006.01); B01J 35/61 (2024.01); B01J 37/00 (2006.01); C10G 2/00 (2006.01);
U.S. Cl.
CPC ...
C10G 2/334 (2013.01); B01J 29/703 (2013.01); B01J 29/7042 (2013.01); B01J 29/7046 (2013.01); B01J 29/7261 (2013.01); B01J 29/7284 (2013.01); B01J 29/7292 (2013.01); B01J 29/7661 (2013.01); B01J 29/7684 (2013.01); B01J 29/7692 (2013.01); B01J 29/7861 (2013.01); B01J 29/7884 (2013.01); B01J 29/7892 (2013.01); B01J 35/612 (2024.01); B01J 35/613 (2024.01); B01J 35/615 (2024.01); B01J 37/0018 (2013.01); B01J 2229/18 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/4018 (2013.01); C10G 2400/30 (2013.01);
Abstract

A method for preparing liquid fuel by direct conversion of syngas uses the syngas as reaction raw material and conducts a catalytic conversion reaction on a fixed bed or a moving bed. The catalyst is a composite catalyst formed by compounding component I and component II in a mechanical mixing mode. The active ingredient of the component I is a metal oxide, and the component II is at least one of zeolites with one-dimensional ten-membered ring porous channels; and a weight ratio of the active ingredient in the component I to that in the component II is 0.1-20. The reaction process has high product yield and selectivity. The selectivity for liquid fuel composed of C-Ccan reach 50-80%. The selectivity for aromatic hydrocarbon is less than 40% in C-C, while the selectivity for methane side product is less than 15%.


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