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:
Jan. 12, 2016

Filed:

Mar. 04, 2015
Applicant:

Greatpoint Energy, Inc., Cambridge, MA (US);

Inventors:

Francis S. Lau, Darien, IL (US);

Earl T. Robinson, Lakeland, FL (US);

Assignee:

GreatPoint Energy, Inc., Cambridge, MA (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10J 3/46 (2006.01); C10J 3/54 (2006.01); C10J 3/82 (2006.01); C10J 3/72 (2006.01); C10K 1/00 (2006.01); C10K 1/10 (2006.01); C10K 1/12 (2006.01); C10K 1/14 (2006.01); C10K 1/16 (2006.01); C10K 3/02 (2006.01); C10L 3/08 (2006.01); C10L 3/10 (2006.01);
U.S. Cl.
CPC ...
C10J 3/82 (2013.01); C10J 3/463 (2013.01); C10J 3/721 (2013.01); C10K 1/004 (2013.01); C10K 1/101 (2013.01); C10K 1/122 (2013.01); C10K 1/143 (2013.01); C10K 1/16 (2013.01); C10K 1/165 (2013.01); C10K 3/02 (2013.01); C10L 3/08 (2013.01); C10L 3/102 (2013.01); C10J 2300/0903 (2013.01); C10J 2300/093 (2013.01); C10J 2300/094 (2013.01); C10J 2300/0943 (2013.01); C10J 2300/0959 (2013.01); C10J 2300/0973 (2013.01); C10J 2300/0986 (2013.01); C10J 2300/1807 (2013.01); C10J 2300/1823 (2013.01); C10J 2300/1846 (2013.01); C10J 2300/1853 (2013.01); C10J 2300/1884 (2013.01);
Abstract

Steam generating gasification reactors for providing high-pressure and high-temperature steam for catalytic gasification of a carbonaceous feedstock can be based on oxygen blown gasification reactors adapted for processing a slurry feedstock comprising at least 40% water. The exhaust from the slurry gasifier comprises at least steam, carbon monoxide and hydrogen. The slurry composition and the oxygen to fuel ratio can be varied to control the ratio of carbonaceous gases in the generator exhaust. By directing substantially all of exhaust gases produced from the slurry gasification reactor through the catalytic gasifier and subsequent gas separation and sequestration processes, a greatly higher energy efficiency and decreased carbon footprint can be realized. The subsequent gas separation process produces a syngas stream which is recycled and directed into the slurry gasifier.


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