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:
Feb. 16, 2016

Filed:

Sep. 14, 2012
Applicants:

Yongcan Gao, Beijing, CN;

Chaogang Xie, Beijing, CN;

Chuanfeng Niu, Beijing, CN;

Jiushun Zhang, Beijing, CN;

Lishun Dai, Beijing, CN;

Hong Nie, Beijing, CN;

Dadong LI, Beijing, CN;

Jun Long, Beijing, CN;

Jianguo MA, Beijing, CN;

Yan Cui, Beijing, CN;

Inventors:

Yongcan Gao, Beijing, CN;

Chaogang Xie, Beijing, CN;

Chuanfeng Niu, Beijing, CN;

Jiushun Zhang, Beijing, CN;

Lishun Dai, Beijing, CN;

Hong Nie, Beijing, CN;

Dadong Li, Beijing, CN;

Jun Long, Beijing, CN;

Jianguo Ma, Beijing, CN;

Yan Cui, Beijing, CN;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 11/00 (2006.01); C10G 11/18 (2006.01); C10G 51/06 (2006.01); C10G 69/04 (2006.01);
U.S. Cl.
CPC ...
C10G 11/18 (2013.01); C10G 11/182 (2013.01); C10G 51/06 (2013.01); C10G 69/04 (2013.01); C10G 2300/107 (2013.01); C10G 2300/1037 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/301 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/70 (2013.01); C10G 2300/807 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01); C10G 2400/28 (2013.01);
Abstract

Disclosed is a combination process for improved hydrotreating and catalytic cracking of hydrocarbon oils, including: contacting residual oil, catalytic cracking cycle oil, and optional distillate oil with a hydrotreating catalyst under hydrotreating conditions in the presence of hydrogen followed by separation of the reaction products to obtain hydrogenated tail oil and other products; contacting the hydrogenated tail oil and optional normal catalytic cracking feedstock oil with a cracking catalyst under catalytic cracking conditions followed by separation of the reaction products; wherein the hydrogenated tail oil and/or normal catalytic cracking feedstock oil are separated into at least two fractions prior to contacting the hydrogenated tail oil and/or normal catalytic cracking feedstock oil with the cracking catalyst.


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