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:
Nov. 23, 2021

Filed:

Nov. 24, 2017
Applicant:

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

Inventors:

Mao Ye, Dalian, CN;

Tao Zhang, Dalian, CN;

Zhongmin Liu, Dalian, CN;

Jinling Zhang, Dalian, CN;

Hailong Tang, Dalian, CN;

Jinming Jia, Dalian, CN;

Changqing He, Dalian, CN;

Xiangao Wang, Dalian, CN;

Cheng Zhang, Dalian, CN;

Hua Li, Dalian, CN;

Yinfeng Zhao, Dalian, CN;

Chenggong Li, Dalian, CN;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 1/24 (2006.01); C07C 2/88 (2006.01); C07C 15/08 (2006.01); B01J 8/26 (2006.01); B01J 8/34 (2006.01); B01J 8/44 (2006.01); B01J 8/00 (2006.01); B01J 8/18 (2006.01); C07C 1/22 (2006.01);
U.S. Cl.
CPC ...
C07C 2/88 (2013.01); B01J 8/0015 (2013.01); B01J 8/0055 (2013.01); B01J 8/1809 (2013.01); B01J 8/1827 (2013.01); B01J 8/1863 (2013.01); B01J 8/26 (2013.01); B01J 8/34 (2013.01); C07C 1/22 (2013.01); C07C 1/24 (2013.01); B01J 2208/00115 (2013.01); B01J 2208/00168 (2013.01); B01J 2208/00769 (2013.01); B01J 2208/00884 (2013.01); B01J 2208/00893 (2013.01); B01J 2208/00991 (2013.01); C07C 2529/40 (2013.01);
Abstract

A turbulent fluidized bed reactor, device and method for preparing para-xylene and co-producing light olefins from methanol and/or dimethyl ether and toluene, resolving or improving the competition problem between an MTO reaction and an alkylation reaction during the process of producing para-xylene and co-producing light olefins from methanol and/or dimethyl ether and toluene, and achieving a synergistic effect between the MTO reaction and the alkylation reaction. By controlling the mass transfer and reaction, competition between the MTO reaction and the alkylation reaction is coordinated and optimized to facilitate a synergistic effect of the two reactions, so that the conversion rate of toluene, the yield of para-xylene, and the selectivity of light olefins are increased. The turbulent fluidized bed reactor includes a first reactor feed distributor and a number of second reactor feed distributors and are arranged sequentially along the gas flow direction.


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