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:
Mar. 22, 2016

Filed:

Nov. 27, 2012
Applicants:

Raymond F. Drnevich, Clarence Center, NY (US);

Shrikar Chakravarti, East Amherst, NY (US);

Minish M. Shah, East Amherst, NY (US);

Inventors:

Raymond F. Drnevich, Clarence Center, NY (US);

Shrikar Chakravarti, East Amherst, NY (US);

Minish M. Shah, East Amherst, NY (US);

Assignee:

PRAXAIR TECHNOLOGY, INC., Danbury, CT (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 27/00 (2006.01); C07C 1/12 (2006.01); C07C 29/151 (2006.01); C10K 3/06 (2006.01); C10G 2/00 (2006.01); C10K 1/00 (2006.01); C01B 3/38 (2006.01); C10J 3/72 (2006.01); C10K 3/04 (2006.01);
U.S. Cl.
CPC ...
C07C 1/12 (2013.01); C01B 3/382 (2013.01); C07C 29/1518 (2013.01); C10G 2/30 (2013.01); C10K 1/003 (2013.01); C10K 1/005 (2013.01); C10K 3/06 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0244 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/043 (2013.01); C01B 2203/0475 (2013.01); C01B 2203/062 (2013.01); C01B 2203/0811 (2013.01); C01B 2203/1241 (2013.01); C01B 2203/1258 (2013.01); C01B 2203/142 (2013.01); C01B 2203/148 (2013.01); C10J 3/721 (2013.01); C10J 2300/1659 (2013.01); C10J 2300/1665 (2013.01); C10J 2300/1678 (2013.01); C10J 2300/1815 (2013.01); C10J 2300/1838 (2013.01); C10K 3/04 (2013.01);
Abstract

A hybrid plant and method for producing liquid fuel product from hydrogen and carbon monoxide containing streams produced by gasifying solid carbonaceous feedstock and steam reforming of light fossil fuels. When a gasification unit in the hybrid plant is operating at reduced capacity or is not operational, oxygen that would have been used in the gasification unit is diverted to a light fossil fuel conversion unit containing an autothermal reformer to increase H-rich syngas flow to a liquid fuel production unit and maintain liquid fuel production at near nameplate capacity.


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