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:
Apr. 24, 2018

Filed:

Jun. 12, 2015
Applicant:

Exxonmobil Chemical Patents Inc., Baytown, TX (US);

Inventors:

Juan D. Henao, Houston, TX (US);

Paul F. Keusenkothen, Houston, TX (US);

Abhimanyu O. Patil, Westfield, NJ (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 2/76 (2006.01); C07C 2/82 (2006.01); C07C 2/84 (2006.01); B01J 29/78 (2006.01); B01J 29/72 (2006.01); B01J 29/70 (2006.01); B01J 29/48 (2006.01); B01J 29/42 (2006.01); B01J 29/40 (2006.01);
U.S. Cl.
CPC ...
C07C 2/84 (2013.01); B01J 29/405 (2013.01); B01J 29/42 (2013.01); B01J 29/48 (2013.01); B01J 29/7088 (2013.01); B01J 29/7276 (2013.01); B01J 29/7876 (2013.01); C07C 2523/02 (2013.01); C07C 2523/04 (2013.01); C07C 2523/06 (2013.01); C07C 2523/08 (2013.01); C07C 2523/10 (2013.01); C07C 2523/14 (2013.01); C07C 2523/18 (2013.01); C07C 2523/28 (2013.01); C07C 2523/30 (2013.01); C07C 2523/36 (2013.01); C07C 2523/42 (2013.01); C07C 2523/44 (2013.01); C07C 2523/50 (2013.01); C07C 2523/72 (2013.01); C07C 2523/745 (2013.01); C07C 2523/755 (2013.01); C07C 2529/40 (2013.01); C07C 2529/42 (2013.01); C07C 2529/48 (2013.01); C07C 2529/70 (2013.01); C07C 2529/72 (2013.01); C07C 2529/78 (2013.01); Y02P 20/52 (2015.11);
Abstract

A process and catalyst for use therein for the production of aromatics via the oxidative coupling of methane and methane co-aromatization with higher hydrocarbons in a single reaction stage. First, methane is partially converted to ethane and ethylene on an OCM catalyst component, and the OCM intermediate mixture containing methane, ethane and ethylene is subsequently converted into aromatics on an aromatization catalyst component. The reaction may be conducted at 550-850° C. and at about 50 psig. The claimed process and catalyst used therein achieves high methane conversion at lower temperatures (less than 800° C.), higher methane conversion into the aromatic products and significant reductions in production cost when compared to the traditional two (or more) step processes.


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