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. 06, 2020

Filed:

Jun. 01, 2015
Applicant:

Sabic Global Technologies B.v., Bergen op Zoom, NL;

Inventors:

Dustin Fickel, Houston, TX (US);

Stephen Hall, Cheshire, GB;

Kumar Prashant, Altrincham, GB;

Maikel van Iersel, Den Bosch, NL;

Sonia Farrokhpanah, Walton on Thames, GB;

Assignee:

SABIC GLOBAL TECHNOLOGIES B.V., Bergen op Zoom, NL;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 4/06 (2006.01); C10G 65/14 (2006.01); C10G 65/10 (2006.01); B01J 29/44 (2006.01); C10G 45/00 (2006.01); C07C 4/18 (2006.01); C07C 6/12 (2006.01); C10G 47/18 (2006.01); C10G 45/62 (2006.01); C10G 65/18 (2006.01); C07C 7/04 (2006.01); B01J 29/42 (2006.01);
U.S. Cl.
CPC ...
C07C 4/06 (2013.01); B01J 29/42 (2013.01); B01J 29/44 (2013.01); C07C 4/18 (2013.01); C07C 6/123 (2013.01); C07C 7/04 (2013.01); C10G 45/00 (2013.01); C10G 45/62 (2013.01); C10G 47/18 (2013.01); C10G 65/14 (2013.01); C10G 65/18 (2013.01); B01J 2229/18 (2013.01); B01J 2229/20 (2013.01); B01J 2229/42 (2013.01); C07C 2529/44 (2013.01); C10G 2400/30 (2013.01); Y02P 20/52 (2015.11);
Abstract

A process for producing benzene comprising the steps of: (a) separating a source feedstream comprising C5-C12 hydrocarbons including benzene and alkylbenzenes into a first feedstream comprising a higher proportion of benzene than the source feedstream and a second feedstream comprising a lower proportion of benzene than the source feedstream and subsequently,(b) contacting the first feedstream in the presence of hydrogen with a first hydrocracking catalyst, and(c) contacting the second feedstream with hydrogen under second process conditions to produce a second product stream comprising benzene, whereini) the second process conditions are suitable for hydrocracking and step (c) involves contacting the second feedstream in the presence of hydrogen with a second hydrocracking catalyst,ii) the second process conditions are suitable for toluene disproportionation and involve contacting the second feedstream with a toluene disproportionation catalyst oriii) the second process conditions are suitable for hydrodealkylation.


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