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:
Dec. 15, 2020

Filed:

Sep. 07, 2017
Applicant:

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

Inventors:

Ashim Kumar Ghosh, Sugar Land, TX (US);

Alla Khanmamedova, Sugar Land, TX (US);

Scott A. Stevenson, Sugar Land, TX (US);

Luis Aramburo, Geleen, NL;

David L. Sullivan, Little Ferry, NJ (US);

Cong Nguyen, Sugar Land, TX (US);

Assignee:

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

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 4/06 (2006.01); B01J 23/42 (2006.01); B01J 29/22 (2006.01); B01J 29/44 (2006.01); B01J 35/00 (2006.01); B01J 35/10 (2006.01);
U.S. Cl.
CPC ...
C07C 4/06 (2013.01); B01J 23/42 (2013.01); B01J 29/22 (2013.01); B01J 29/44 (2013.01); B01J 35/0066 (2013.01); B01J 35/1057 (2013.01); B01J 35/1061 (2013.01); B01J 2229/186 (2013.01); C07C 2521/12 (2013.01); C07C 2523/10 (2013.01); C07C 2523/42 (2013.01); C07C 2523/44 (2013.01); C07C 2529/18 (2013.01); C07C 2529/40 (2013.01); C07C 2529/44 (2013.01);
Abstract

A process for hydrocracking 2,4-dimethylpentane and/or 2,2,3-trimethylbutane can comprise: contacting a hydrocracking feed stream in the presence of hydrogen with a hydrocracking catalyst, wherein the hydrocracking feed stream comprises at least 0.5 wt % of 2,4-dimethylpentane and/or 2,2,3-trimethylbutane, based upon a total weight of the hydrocracking feed stream; and wherein the hydrocracking catalyst comprises a medium pore zeolite having a pore size of 5-6 A and a silica to alumina molar ratio of 20-75; preferably the hydrocracking catalyst comprises a medium pore zeolite having a pore size of 5-6 A and a silica to alumina molar ratio of 20-75 and a large pore zeolite having a pore size of 6-8 A and a silica to alumina molar ratio of 10-80, wherein the hydrogenation metal is deposited on the medium pore zeolite and the large pore zeolite.


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