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:
May. 31, 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);

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

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 5/327 (2006.01); C07C 5/333 (2006.01); C07C 7/12 (2006.01); C07C 2/84 (2006.01); B01J 8/02 (2006.01); C07C 2/42 (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 is a hydrocarbon conversion process that is less energy intensive than comparable processes. The hydrocarbon conversion process is particularly desirable for converting alkanes, such as methane into Colefins, such as ethylene and propylene, particularly with increasing selectivity to ethylene production. It is also desirable for effectively removing a Ccomposition (i.e., ethane, ethylene and/or acetylene) produced from the catalytic conversion of hydrocarbon comprised of Colefins. In addition, the hydrocarbon process is desirable for providing a substantially non-cryogenic separation of the desired Ccompositions from the hydrocarbons (e.g., methane) present in the reaction mixture.


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