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:
Jul. 29, 2014

Filed:

Mar. 30, 2010
Applicants:

Youhao Xu, Beijing, CN;

Shouye Cui, Beijing, CN;

Zhigang Zhang, Beijing, CN;

Weimin LU, Beijing, CN;

Inventors:

Youhao Xu, Beijing, CN;

Shouye Cui, Beijing, CN;

Zhigang Zhang, Beijing, CN;

Weimin Lu, Beijing, CN;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 38/04 (2006.01); B01J 38/12 (2006.01); B01J 38/30 (2006.01); B01J 38/34 (2006.01); B01J 38/20 (2006.01); B01J 38/16 (2006.01); B01J 38/06 (2006.01); B01J 23/94 (2006.01); B01J 29/90 (2006.01);
U.S. Cl.
CPC ...
B01J 38/30 (2013.01); C01G 11/185 (2013.01); B01J 38/06 (2013.01); B01J 38/12 (2013.01); B01J 23/94 (2013.01); C01G 11/05 (2013.01); B01J 29/90 (2013.01); C01G 11/182 (2013.01); B01J 38/16 (2013.01); B01J 38/34 (2013.01);
Abstract

The object of the present invention is to provide a catalyst regeneration process which can improve catalyst selectivity. A first aspect of the invention is characterized in that a spent catalyst from a reactor is introduced into a first fluidized bed regenerator and contacted with an oxygen-containing gas stream and optional steam to carry out a coke combustion reaction, wherein the resultant mixture of the partially regenerated catalyst and flue gas is introduced into a second fluidized bed regenerator and contacted with steam and an optional oxygen-containing gas stream to carry out a further regeneration reaction, and then the regenerated catalyst is introduced into the reactor. A second aspect of the invention is characterized in that a spent catalyst from a reactor is introduced into a fluidized dense bed regenerator and contacted with an oxygen-containing gas stream and steam to carry out a coke combustion reaction, and then the regenerated catalyst is introduced into the reactor. The inventive processes result in a more uniform distribution of the regenerated catalyst activity; due to the exposure of the catalyst to a low temperature for a long time, a part of the heavy metals are buried by the matrix and the remaining are passivated. Thereby dry gas and coke yields decrease sharply when hydrocarbons are subjected to a catalytic cracking reaction on the regenerated catalyst.


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