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. 26, 2020

Filed:

Mar. 22, 2017
Applicant:

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

Inventors:

Xinhe Bao, Dalian, CN;

Xiaoguang Guo, Dalian, CN;

Guangzong Fang, Dalian, CN;

Xiulian Pan, Dalian, CN;

Jingheng Meng, Dalian, CN;

Qinqin Yu, Dalian, CN;

Dali Tan, Dalian, CN;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
B01J 7/00 (2006.01); C07C 2/84 (2006.01); B01J 15/00 (2006.01); B01J 12/00 (2006.01); B01J 10/00 (2006.01); B01J 19/00 (2006.01); B01J 19/02 (2006.01); B01J 19/24 (2006.01); C07C 2/76 (2006.01); C23C 16/40 (2006.01);
U.S. Cl.
CPC ...
B01J 7/00 (2013.01); B01J 10/007 (2013.01); B01J 12/007 (2013.01); B01J 15/00 (2013.01); B01J 19/0013 (2013.01); B01J 19/02 (2013.01); B01J 19/2415 (2013.01); C07C 2/76 (2013.01); C07C 2/84 (2013.01); C23C 16/402 (2013.01); B01J 2219/0093 (2013.01); B01J 2219/00159 (2013.01); B01J 2219/00835 (2013.01); C07C 2521/08 (2013.01); C07C 2521/18 (2013.01); Y02P 20/52 (2015.11);
Abstract

A reactor configuration comprises an inlet section I, a preheating section II, a transition section III, a reaction section IV and an outlet section V; except for the preheating section II and the reaction section IV, the existence of the inlet section I, the transition section III and the outlet section V depends on reaction conditions; and the process realizes no coke deposition synthesis of methane and high selectivity synthesis of ethylene. The methane conversion rate is 20-90%; ethylene selectivity is 65-95%; propylene and butylene selectivity is 5-25%; aromatic hydrocarbon selectivity is 0-30%; and coke deposition is zero.


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