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:
Aug. 30, 2016

Filed:

Feb. 12, 2013
Applicant:

Saudi Basic Industries Corporation, Riyadh, SA;

Inventors:

Ravichander Narayanaswamy, Bangalore, IN;

Krishna Kumar Ramamurthy, Bangalore, IN;

P. S. Sreenivasan, Bangalore, IN;

Assignee:
Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 1/10 (2006.01); C10G 1/08 (2006.01); B01J 29/80 (2006.01); B01J 29/40 (2006.01); C10G 69/04 (2006.01); C10G 69/08 (2006.01); C10G 11/18 (2006.01); B01J 29/00 (2006.01); B01J 38/12 (2006.01); B01J 29/03 (2006.01); B01J 29/08 (2006.01); B01J 29/18 (2006.01); B01J 29/82 (2006.01); B01J 29/90 (2006.01);
U.S. Cl.
CPC ...
C10G 1/10 (2013.01); B01J 29/005 (2013.01); B01J 29/40 (2013.01); B01J 29/80 (2013.01); C10G 11/18 (2013.01); C10G 69/04 (2013.01); C10G 69/08 (2013.01); B01J 29/0308 (2013.01); B01J 29/08 (2013.01); B01J 29/18 (2013.01); B01J 29/82 (2013.01); B01J 29/90 (2013.01); B01J 38/12 (2013.01); B01J 2229/42 (2013.01); C10G 2400/30 (2013.01);
Abstract

A method of producing olefins and aromatic compounds from a feedstock is accomplished by introducing a hydrocarbon feedstock and a catalyst composition within a reactor. At least a portion of the reactor is at a reactor temperature of from 470° C. to 730° C. The catalyst composition is comprised of a fluidized catalytic cracking (FCC) catalyst and a ZSM-5 zeolite catalyst, wherein the amount of ZSM-5 zeolite catalyst makes up from greater than 0 wt. % of the total weight of the FCC catalyst and the ZSM-5 zeolite catalyst. At least a portion of the feedstock is converted to products of at least one of olefins and aromatic compounds within the reactor, with at least some of the products being contained in a liquid product stream. At least a portion of the liquid product stream is directed to different downstream processes to increase production of at least one of olefins and aromatic compounds.


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