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:
Oct. 13, 2015

Filed:

Oct. 30, 2012
Applicant:

Kellogg Brown & Root Llc, Houston, TX (US);

Inventors:

Siva Ariyapadi, Pearland, TX (US);

Philip Shires, Katy, TX (US);

Assignee:

KELLOGG BROWN & ROOT LLC, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10J 3/00 (2006.01); C10J 3/54 (2006.01); C10L 3/08 (2006.01); C10J 3/48 (2006.01); C10J 3/56 (2006.01); C10K 1/00 (2006.01); C10K 1/02 (2006.01); C10K 3/04 (2006.01); C10G 2/00 (2006.01); C10K 3/00 (2006.01);
U.S. Cl.
CPC ...
C10L 3/08 (2013.01); C10G 2/30 (2013.01); C10G 2/32 (2013.01); C10G 2/332 (2013.01); C10J 3/00 (2013.01); C10J 3/482 (2013.01); C10J 3/56 (2013.01); C10K 1/002 (2013.01); C10K 1/004 (2013.01); C10K 1/005 (2013.01); C10K 1/02 (2013.01); C10K 3/008 (2013.01); C10K 3/04 (2013.01); C10J 2300/093 (2013.01); C10J 2300/0956 (2013.01); C10J 2300/0959 (2013.01); C10J 2300/0973 (2013.01); C10J 2300/0983 (2013.01); C10J 2300/1662 (2013.01); C10J 2300/1671 (2013.01); C10J 2300/1675 (2013.01); C10J 2300/1678 (2013.01); C10J 2300/1687 (2013.01); C10J 2300/1884 (2013.01); C10J 2300/1892 (2013.01);
Abstract

Systems and methods for processing a hydrocarbon are provided. The method can include gasifying a feedstock within a gasifier to provide a raw syngas. The raw syngas can be processed within a purification system to provide a treated syngas. A first portion of the treated syngas can be converted into a first effluent in a first methanator. The first effluent can be mixed with a second portion of the treated syngas to provide a first mixed effluent. The first mixed effluent can be converted into a second effluent in a second methanator. The second effluent can be mixed with a third portion of the treated syngas to provide a second mixed effluent. The second mixed effluent can be converted into a third effluent in a third methanator.


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