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:
Nov. 10, 2015

Filed:

May. 07, 2012
Applicants:

Larry L. Iaccino, Seabrook, TX (US);

James R. Lattner, LaPorte, TX (US);

Glenn C. Wood, Houston, TX (US);

Surbhi Jain, Houston, TX (US);

Stephen M. Davis, Humble, TX (US);

Inventors:

Larry L. Iaccino, Seabrook, TX (US);

James R. Lattner, LaPorte, TX (US);

Glenn C. Wood, Houston, TX (US);

Surbhi Jain, Houston, TX (US);

Stephen M. Davis, Humble, TX (US);

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 1/24 (2006.01); C07C 2/86 (2006.01); C10G 29/20 (2006.01); C10G 35/00 (2006.01); C10G 57/00 (2006.01); C10G 9/00 (2006.01); C10G 9/36 (2006.01); C10G 11/00 (2006.01);
U.S. Cl.
CPC ...
C07C 2/864 (2013.01); C10G 9/005 (2013.01); C10G 9/36 (2013.01); C10G 11/00 (2013.01); C10G 29/205 (2013.01); C10G 35/00 (2013.01); C10G 57/005 (2013.01); C10G 2300/1092 (2013.01); C10G 2300/1096 (2013.01); C10G 2400/30 (2013.01);
Abstract

In a hydrocarbon upgrading process, a hydrocarbon feed is treated in at least one of a steam cracker, catalytic cracker, coker, hydrocracker, and reformer under suitable conditions to produce a first stream comprising olefinic and aromatic hydrocarbons. A second stream composed mainly of Cto Colefinic and aromatic hydrocarbons is recovered from the first stream and at least part of the second stream is contacted with a catalyst in the absence of added hydrogen under reaction conditions including a temperature of about 450° C. to about 70° C. effective to dealkylate, transalkylate, crack and aromatize components of the second stream to produce a third stream having an increased benzene and/or toluene content compared with the second stream and a C− olefin by-product. The C− olefin by-product and a fourth stream comprising toluene are then recovered from the third stream.


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