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:
Jul. 19, 2016

Filed:

Aug. 26, 2014
Applicant:

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

Inventors:

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

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

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 5/327 (2006.01); C07C 5/333 (2006.01); C07C 2/42 (2006.01); C07C 2/84 (2006.01); C07C 7/12 (2006.01); B01J 8/02 (2006.01); B01J 19/24 (2006.01); C07C 2/08 (2006.01); C07C 5/48 (2006.01); C07C 7/00 (2006.01); B01J 15/00 (2006.01); C07C 2/78 (2006.01); B01D 53/04 (2006.01);
U.S. Cl.
CPC ...
C07C 2/84 (2013.01); B01J 8/0207 (2013.01); B01J 15/005 (2013.01); B01J 19/24 (2013.01); B01J 19/245 (2013.01); C07C 2/08 (2013.01); C07C 2/42 (2013.01); C07C 2/78 (2013.01); C07C 5/48 (2013.01); C07C 7/005 (2013.01); C07C 7/12 (2013.01); B01D 53/04 (2013.01); B01D 2256/24 (2013.01); B01D 2257/7022 (2013.01); B01D 2259/4009 (2013.01); B01J 2208/0053 (2013.01); B01J 2208/00309 (2013.01); B01J 2208/00548 (2013.01); B01J 2208/00557 (2013.01); B01J 2208/00566 (2013.01); B01J 2219/24 (2013.01); B01J 2219/2402 (2013.01); Y02P 20/51 (2015.11);
Abstract

Disclosed are reactors and reaction processes for contacting hydrocarbon reactant in the presence of oxygen stored and released within a thermal mass region of the reactor, and catalytically converting at least a portion of alkane, e.g., methane, in the hydrocarbon reactant to produce a reaction mixture comprising a Ccomposition. Oxygen storage and release for carrying out the catalytic conversion is achieved by including an oxygen storage material in a thermal mass region of the reactor. Flow-through reactors can be used to carry out oxygen storage and the hydrocarbon conversion reactions. Reverse-flow reactors are examples of flow-through reactors, which can be used to carry out oxygen storage and the hydrocarbon conversion reactions.


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