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.

Patent No.:

US 7226574 B1

PDF
Full Text
Expired
Date of Patent:
Jun. 05, 2007

Filed:

May. 30, 2003
Applicants:

Richard Q. Long, New Albany, OH (US);

Anna Lee Tonkovich, Dublin, OH (US);

Eric Daymo, Dublin, OH (US);

Barry L. Yang, Dublin, OH (US);

Yong Wang, Richland, WA (US);

Francis P. Daly, Delaware, OH (US);

Inventors:

Richard Q. Long, New Albany, OH (US);

Anna Lee Tonkovich, Dublin, OH (US);

Eric Daymo, Dublin, OH (US);

Barry L. Yang, Dublin, OH (US);

Yong Wang, Richland, WA (US);

Francis P. Daly, Delaware, OH (US);

Assignee:

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

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 3/02 (2006.01); C01B 31/18 (2006.01);
U.S. Cl.
CPC ...
Abstract

A process is disclosed for converting a hydrocarbon reactant to a product comprising CO and H. The process comprises: (A) flowing a reactant composition comprising the hydrocarbon reactant and oxygen or a source of oxygen through a microchannel reactor in contact with a catalyst under reaction conditions to form the product, the microchannel reactor comprising at least one process microchannel with the catalyst positioned within the process microchannel, the hydrocarbon reactant comprising methane, the contact time for the reactant composition within the process microchannel being up to about 500 milliseconds, the temperature of the reactant composition and product within the process microchannel being up to about 1150° C., the conversion of the hydrocarbon reactant to carbon oxide being at least about 50%. The product formed in step (A) may be converted to a product comprising COand HO in a microchannel reactor.


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