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:
Oct. 14, 2008

Filed:

Sep. 27, 2004
Applicants:

Jun Long, Beijing, CN;

Huiping Tian, Beijing, CN;

Yujian Liu, Beijing, CN;

Yuxia Zhu, Beijing, CN;

Zhenyu Chen, Beijing, CN;

Yaoqing Guo, Beijing, CN;

Zhijian Da, Beijing, CN;

Jiushun Zhang, Beijing, CN;

Mingyuan He, Beijing, CN;

Inventors:

Jun Long, Beijing, CN;

Huiping Tian, Beijing, CN;

Yujian Liu, Beijing, CN;

Yuxia Zhu, Beijing, CN;

Zhenyu Chen, Beijing, CN;

Yaoqing Guo, Beijing, CN;

Zhijian Da, Beijing, CN;

Jiushun Zhang, Beijing, CN;

Mingyuan He, Beijing, CN;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 11/00 (2006.01); C10G 9/00 (2006.01);
U.S. Cl.
CPC ...
Abstract

This invention relates to a process for cracking hydrocarbon oils. The process comprises contacting a hydrocarbon oil with a catalyst that has been contacted with an atmosphere containing a reducing gas, separating cracked products and the catalyst, and regenerating the catalyst. The catalyst is a cracking catalyst containing a metal component, or a catalyst mixture of a cracking catalyst containing a metal component and a cracking catalyst free of metal component. The catalyst is contacted with the atmosphere containing a reducing gas at a temperature of 100 to 900° C. for at least 1 second, and the amount of the atmosphere containing a reducing gas is not less than 0.03 cubic meters of reducing gas per ton of the cracking catalyst containing a metal component per minute, at a pressure of 0.1-0.5 MPa in the reduction reactor. The process has enhanced capability for desulfurizing and cracking heavy oils.


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