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:
Dec. 06, 2022

Filed:

Oct. 26, 2020
Applicants:

China Petroleum & Chemical Corporation, Beijing, CN;

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

Inventors:

Youhao Xu, Beijing, CN;

Xuhui Bai, Beijing, CN;

Xinyu Xie, Beijing, CN;

Shouye Cui, Beijing, CN;

Xin Wang, Beijing, CN;

Yanfen Zuo, Beijing, CN;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/04 (2006.01); C10G 55/06 (2006.01); C10G 11/05 (2006.01); C10G 21/14 (2006.01); C10G 21/00 (2006.01); C10G 11/18 (2006.01); C10G 45/10 (2006.01);
U.S. Cl.
CPC ...
C10G 69/04 (2013.01); C10G 11/05 (2013.01); C10G 11/18 (2013.01); C10G 21/003 (2013.01); C10G 21/14 (2013.01); C10G 45/10 (2013.01); C10G 55/06 (2013.01); C10G 2300/206 (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);
Abstract

A process for producing propylene and a low-sulfur fuel oil component, comprising the steps of contacting a heavy feedstock oil with a solvent for extraction separation to obtain a deasphalted oil and a deoiled asphalt; contacting the deasphalted oil and optionally a light feedstock oil with a catalytic conversion catalyst for reaction to obtain a reaction product comprising propylene; separating the reaction product to obtain a catalytic cracking distillate oil, and subjecting the catalytic cracking distillate oil to hydrodesulfurization to obtain a low-sulfur hydrogenated distillate oil, wherein the low-sulfur hydrogenated distillate oil and/or the deoiled asphalt is suitable for use as a fuel oil component. The process allows the conversion of saturated hydrocarbons in the heavy feedstock into propylene, eliminates the use of saturated hydrocarbons in the fuel oil component, and thus has better economic and social benefits.


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