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:
Apr. 11, 2023

Filed:

Jul. 15, 2019
Applicants:

China Petroleum & Chemical Corporation, Beijing, CN;

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

Inventors:

Jianhong Gong, Beijing, CN;

Zhigang Zhang, Beijing, CN;

Xiaoli Wei, Beijing, CN;

Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 11/18 (2006.01); B01J 8/00 (2006.01); B01J 8/18 (2006.01); B01J 8/24 (2006.01);
U.S. Cl.
CPC ...
C10G 11/18 (2013.01); B01J 8/004 (2013.01); B01J 8/0055 (2013.01); B01J 8/1809 (2013.01); B01J 8/1872 (2013.01); B01J 8/1881 (2013.01); B01J 8/24 (2013.01); B01J 2208/00008 (2013.01); B01J 2208/00539 (2013.01); B01J 2208/00548 (2013.01); B01J 2208/00584 (2013.01); B01J 2208/00628 (2013.01); C10G 2300/202 (2013.01); C10G 2300/205 (2013.01); C10G 2300/301 (2013.01); C10G 2300/308 (2013.01); C10G 2300/4018 (2013.01); C10G 2400/04 (2013.01); C10G 2400/20 (2013.01); C10G 2400/30 (2013.01);
Abstract

A process for the catalytic cracking of hydrocarbon oils includes the step of contacting a hydrocarbon oil feedstock with a catalytic cracking catalyst in a reactor having one or more fast fluidized reaction zones for reaction. At least one of the fast fluidized reaction zones of the reactor is a full dense-phase reaction zone, and the axial solid fraction ε of the catalyst is controlled within a range of about 0.1 to about 0.2 throughout the full dense-phase reaction zone. When used for catalytic cracking of hydrocarbon oils, particularly heavy feedstock oils, the process, reactor and system show a high contact efficiency between oil and catalyst, a selectivity of the catalytic reaction, an effectively reduced yield of dry gas and coke, and an improved yield of high value-added products such as ethylene and propylene.


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