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:
Jan. 13, 2015

Filed:

Oct. 20, 2010
Applicants:

Youhao Xu, Beijing, CN;

Jianhong Gong, Beijing, CN;

Congli Cheng, Beijing, CN;

Shouye Cui, Beijing, CN;

Zhihai HU, Beijing, CN;

Yun Chen, Beijing, CN;

Inventors:

Youhao Xu, Beijing, CN;

Jianhong Gong, Beijing, CN;

Congli Cheng, Beijing, CN;

Shouye Cui, Beijing, CN;

Zhihai Hu, Beijing, CN;

Yun Chen, Beijing, CN;

Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 11/05 (2006.01); C10G 51/02 (2006.01); C10G 69/04 (2006.01); C10L 1/08 (2006.01); C10G 45/08 (2006.01); C10G 45/12 (2006.01); C10G 69/00 (2006.01); C10L 1/06 (2006.01); C10G 11/18 (2006.01);
U.S. Cl.
CPC ...
C10G 11/05 (2013.01); C10G 69/04 (2013.01); C10L 1/08 (2013.01); C10G 45/08 (2013.01); C10G 45/12 (2013.01); C10G 51/026 (2013.01); C10G 69/00 (2013.01); C10L 1/06 (2013.01); C10G 11/18 (2013.01); C10G 2300/307 (2013.01); C10G 2300/4081 (2013.01); C10G 2300/1037 (2013.01); C10G 2300/107 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/301 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01);
Abstract

A catalytic conversion process uses a catalytic cracking catalyst having a relatively homogeneous activity containing mainly large pore zeolites in a catalytic conversion reactor. The reaction temperature, residence time of oil vapors and weight ratio of the catalyst/feedstock oil are sufficient to obtain a reaction product containing from about 12 to about 60% by weight of a fluid catalytic cracking gas oil relative to the weight of the feed stock oil and containing a diesel. The reaction temperature ranges from about 420° C. to about 550° C. The residence time of oil vapors ranges from about 0.1 to about 5 seconds. The weight ratio of the catalytic cracking catalyst/feedstock is about 1-about 10.


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