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:
Apr. 21, 2015

Filed:

Dec. 08, 2010
Applicants:

Wayne W. Simmons, Dublin, OH (US);

Christopher Perkins, Boulder, CO (US);

Zoran Jovanovic, Louisville, CO (US);

Courtland M. Hilton, Broomfield, CO (US);

Peter Popp, Broomfield, CO (US);

Bryan J. Schramm, Broomfield, CO (US);

John T. Turner, West Chester, OH (US);

Inventors:

Wayne W. Simmons, Dublin, OH (US);

Christopher Perkins, Boulder, CO (US);

Zoran Jovanovic, Louisville, CO (US);

Courtland M. Hilton, Broomfield, CO (US);

Peter Popp, Broomfield, CO (US);

Bryan J. Schramm, Broomfield, CO (US);

John T. Turner, West Chester, OH (US);

Assignee:

Sundrop Fuels, Inc., Longmont, CO (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 7/00 (2006.01); C07C 29/152 (2006.01); C01B 3/24 (2006.01); C01B 3/34 (2006.01); C10J 3/48 (2006.01); C10J 3/50 (2006.01); C10J 3/84 (2006.01); F28D 21/00 (2006.01);
U.S. Cl.
CPC ...
C07C 29/152 (2013.01); C01B 3/24 (2013.01); C01B 3/34 (2013.01); C10J 3/485 (2013.01); C10J 3/506 (2013.01); C10J 3/84 (2013.01); C01B 2203/0216 (2013.01); C01B 2203/0222 (2013.01); C01B 2203/0272 (2013.01); C01B 2203/0485 (2013.01); C01B 2203/0495 (2013.01); C01B 2203/061 (2013.01); C01B 2203/062 (2013.01); C01B 2203/0816 (2013.01); C01B 2203/0822 (2013.01); C01B 2203/0877 (2013.01); C01B 2203/0894 (2013.01); C01B 2203/1241 (2013.01); F28D 2021/0022 (2013.01); C10J 2300/0906 (2013.01); C10J 2300/0909 (2013.01); C10J 2300/0916 (2013.01); C10J 2300/0976 (2013.01); C10J 2300/0989 (2013.01); C10J 2300/1223 (2013.01); C10J 2300/1246 (2013.01); C10J 2300/1269 (2013.01); C10J 2300/1292 (2013.01); C10J 2300/1621 (2013.01); C10J 2300/1665 (2013.01); C10J 2300/1687 (2013.01); C10J 2300/1693 (2013.01); C10J 2300/1884 (2013.01); C10J 2300/1892 (2013.01); C10J 2200/152 (2013.01); Y02E 50/18 (2013.01); C10G 2300/1011 (2013.01); C10G 2400/02 (2013.01); C10G 2300/807 (2013.01);
Abstract

Various processes and apparatus are discussed for an ultra-high heat flux chemical reactor. A thermal receiver and the reactor tubes are aligned to 1) absorb and re-emit radiant energy, 2) highly reflect radiant energy, and 3) any combination of these, to maintain an operational temperature of the enclosed ultra-high heat flux chemical reactor. Particles of biomass are gasified in the presence of a steam carrier gas and methane in a simultaneous steam reformation and steam biomass gasification reaction to produce reaction products that include hydrogen and carbon monoxide gas using the ultra-high heat flux thermal energy radiated from the inner wall and then into the multiple reactor tubes. The multiple reactor tubes and cavity walls of the receiver transfer energy primarily by radiation absorption and re-radiation, rather than by convection or conduction, to the reactants in the chemical reaction to drive the endothermic chemical reaction flowing in the reactor tubes.


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