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:
Dec. 05, 2017

Filed:

Feb. 18, 2011
Applicants:

Alexander Rabinovich, Cherry Hill, NJ (US);

Michael Gallagher, Philadelphia, PA (US);

Alexander Fridman, Philadelphia, PA (US);

Anatoliy Polevich, Philadelphia, PA (US);

Alexander F. Gutsol, San Ramon, CA (US);

Inventors:

Alexander Rabinovich, Cherry Hill, NJ (US);

Michael Gallagher, Philadelphia, PA (US);

Alexander Fridman, Philadelphia, PA (US);

Anatoliy Polevich, Philadelphia, PA (US);

Alexander F. Gutsol, San Ramon, CA (US);

Assignee:

Drexel University, Philadelphia, PA (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C01B 3/36 (2006.01); C10J 3/72 (2006.01); C10J 3/48 (2006.01); B01J 19/08 (2006.01); C01B 3/34 (2006.01); H05H 1/48 (2006.01);
U.S. Cl.
CPC ...
C01B 3/363 (2013.01); B01J 19/088 (2013.01); C01B 3/342 (2013.01); C10J 3/487 (2013.01); C10J 3/721 (2013.01); H05H 1/48 (2013.01); B01J 2219/0809 (2013.01); B01J 2219/0847 (2013.01); B01J 2219/0869 (2013.01); B01J 2219/0877 (2013.01); B01J 2219/0884 (2013.01); B01J 2219/0894 (2013.01); C01B 2203/025 (2013.01); C01B 2203/0244 (2013.01); C01B 2203/0255 (2013.01); C01B 2203/0861 (2013.01); C01B 2203/1235 (2013.01); C01B 2203/1241 (2013.01); C01B 2203/1247 (2013.01); C01B 2203/141 (2013.01); C01B 2203/142 (2013.01); C10J 2300/0916 (2013.01); C10J 2300/0956 (2013.01); C10J 2300/1238 (2013.01); Y02P 20/145 (2015.11);
Abstract

A reactor for reforming a liquid hydrocarbon fuel, and associated processes and systems, are described herein. In one example, a two stage process is disclosed in which a first reactor is coupled to a second stage reactor having a reaction volume greater than the first reactor. In the first reactor, the liquid hydrocarbon fuel is partially reformed and thereafter is inputted into the second stage reactor for complete partial oxidation. The reaction product is at last partially synthesis gas, a mixture of carbon monoxide, hydrogen, as well as other low hydrocarbons such as methane, ethylene, ethane, and acetylene. The low hydrocarbons can be reformed further in a solid oxide fuel cell. A portion of the gaseous, rotating contents of the second stage reactor may be input into the first reactor to help generate and sustain rotation within the first reactor.


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