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:
Aug. 30, 2022

Filed:

Oct. 22, 2018
Applicants:

China Petroleum & Chemical Corporation, Beijing, CN;

Research Institute of Petroleum Processing, Sinopec, Beijing, CN;

Inventors:

Youhao Xu, Beijing, CN;

Xin Wang, Beijing, CN;

Yuying Zhang, Beijing, CN;

Tao Liu, Beijing, CN;

Xuhui Bai, Beijing, CN;

Lishun Dai, Beijing, CN;

Zhigang Zhang, Beijing, CN;

Jialin Liang, Beijing, CN;

Nan Jiang, Beijing, CN;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/04 (2006.01); C07C 4/06 (2006.01); C10G 11/05 (2006.01); C10G 11/18 (2006.01); C07C 9/12 (2006.01);
U.S. Cl.
CPC ...
C10G 69/04 (2013.01); C07C 4/06 (2013.01); C10G 11/05 (2013.01); C10G 11/182 (2013.01); C07C 9/12 (2013.01); C10G 2300/1096 (2013.01); C10G 2400/28 (2013.01); C10G 2400/30 (2013.01);
Abstract

Disclosed is a catalytic cracking process for producing isobutane and/or light aromatics in high yield, comprising the steps of: a) providing a catalytic cracking feedstock oil having a polycyclic naphthene content of greater than about 25 wt %; b) subjecting the catalytic cracking feedstock oil to a first catalytic cracking reaction and a second catalytic cracking reaction sequentially under different reaction conditions to obtain a catalytic cracking product; c) separating the resulting catalytic cracking product to obtain a liquefied gas fraction comprising isobutane and a gasoline fraction comprising light aromatics; and d) optionally, recovering isobutane from the liquefied gas fraction and/or recovering light aromatics from the gasoline fraction. The process can enable the production of isobutane and/or light aromatics in high yield.


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