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. 27, 2023

Filed:

Jan. 28, 2019
Applicants:

Sabic Global Technologies B.v., Bergen op Zoom, NL;

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

Inventors:

Yinfeng Zhao, Liaoning, CN;

Mao Ye, Liaoning, CN;

Zhongmin Liu, Liaoning, CN;

Hailong Tang, Liaoning, CN;

Jing Wang, Liaoning, CN;

Jinling Zhang, Liaoning, CN;

Tao Zhang, Liaoning, CN;

Talal Khaled Al-Shammari, Riyadh, SA;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 11/18 (2006.01); B01J 35/02 (2006.01); C07C 4/06 (2006.01); C10G 61/00 (2006.01); C10G 69/08 (2006.01); C10G 59/00 (2006.01); C10G 63/00 (2006.01); C10G 35/00 (2006.01); C10G 69/10 (2006.01); C10G 45/58 (2006.01); C07C 4/10 (2006.01); C07C 4/12 (2006.01);
U.S. Cl.
CPC ...
C10G 11/18 (2013.01); B01J 35/023 (2013.01); B01J 35/026 (2013.01); C07C 4/06 (2013.01); C07C 4/10 (2013.01); C07C 4/12 (2013.01); C10G 35/00 (2013.01); C10G 45/58 (2013.01); C10G 59/00 (2013.01); C10G 61/00 (2013.01); C10G 63/00 (2013.01); C10G 69/08 (2013.01); C10G 69/10 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/301 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/4018 (2013.01); C10G 2400/20 (2013.01); C10G 2400/30 (2013.01);
Abstract

Disclosed is a method for producing low carbon olefins and/or aromatics from feedstock comprising naphtha. The method can include the following steps: a) feeding feedstock comprising naphtha into a fast fluidized bed reactor; b) contacting the feedstock with a catalyst under conditions to produce a gas product and spent catalyst; c) separating the gas product to produce a stream comprising primarily one or more low carbon olefins and/or one or more aromatics; d) transporting the spent catalyst to a regenerator; e) regenerating the spent catalyst in the regenerator to form regenerated catalyst; and f) returning the regenerated catalyst to the fast fluidized bed reactor.


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