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:
Aug. 18, 2015

Filed:

Aug. 10, 2007
Applicants:

John H. Brophy, Bristol, GB;

Frederick A. Pesa, Aurora, OH (US);

Anna Lee Tonkovich, Marysville, OH (US);

Jeffrey S. Mcdaniel, Columbus, OH (US);

Kai Tod Paul Jarosch, Bexley, OH (US);

Inventors:

John H. Brophy, Bristol, GB;

Frederick A. Pesa, Aurora, OH (US);

Anna Lee Tonkovich, Marysville, OH (US);

Jeffrey S. McDaniel, Columbus, OH (US);

Kai Tod Paul Jarosch, Bexley, OH (US);

Assignee:

Velocys, Inc., Plain City, OH (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 19/00 (2006.01); C07C 253/26 (2006.01); C07B 41/00 (2006.01); C07B 43/08 (2006.01); C07C 45/33 (2006.01); C07C 45/34 (2006.01); C07C 45/35 (2006.01); C07C 45/36 (2006.01); C07C 51/25 (2006.01); C07C 51/265 (2006.01); C07C 67/05 (2006.01); C07C 253/24 (2006.01);
U.S. Cl.
CPC ...
C07C 253/26 (2013.01); B01J 19/0093 (2013.01); C07B 41/00 (2013.01); C07B 43/08 (2013.01); C07C 45/33 (2013.01); C07C 45/34 (2013.01); C07C 45/35 (2013.01); C07C 45/36 (2013.01); C07C 51/252 (2013.01); C07C 51/265 (2013.01); C07C 67/05 (2013.01); C07C 253/24 (2013.01); B01J 2219/0086 (2013.01); B01J 2219/00783 (2013.01); B01J 2219/00804 (2013.01); B01J 2219/00835 (2013.01); B01J 2219/00873 (2013.01);
Abstract

This invention relates to a process for converting a hydrocarbon reactant to a product comprising an oxygenate or a nitrile, the process comprising: (A) flowing a reactant composition comprising the hydrocarbon reactant, and oxygen or a source of oxygen, and optionally ammonia, through a microchannel reactor in contact with a catalyst to convert the hydrocarbon reactant to the product, the hydrocarbon reactant undergoing an exothermic reaction in the microchannel reactor; (B) transferring heat from the microchannel reactor to a heat exchanger during step (A); and (C) quenching the product from step (A).


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