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:
Sep. 26, 2017

Filed:

Nov. 25, 2015
Applicant:

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

Inventors:

Renus C. Kelfkens, Longmont, CO (US);

Wayne W. Simmons, Longmont, CO (US);

Douglas S. Jack, Longmont, CO (US);

Jerrod Wayne Hohman, Louisville, CO (US);

Sidney P. White, Fort Collins, CO (US);

Assignee:

Other;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 3/00 (2006.01); C10G 2/00 (2006.01); C10J 3/46 (2006.01); C10G 45/44 (2006.01); C10K 1/08 (2006.01); C10K 1/32 (2006.01); C10K 3/02 (2006.01); C10G 45/00 (2006.01); C10L 1/04 (2006.01); C10K 3/00 (2006.01); C10J 3/84 (2006.01); C10J 3/50 (2006.01); C01B 3/38 (2006.01); C10J 3/48 (2006.01);
U.S. Cl.
CPC ...
C10J 3/466 (2013.01); C01B 3/38 (2013.01); C10G 2/32 (2013.01); C10G 2/34 (2013.01); C10G 3/00 (2013.01); C10G 45/00 (2013.01); C10G 45/44 (2013.01); C10J 3/485 (2013.01); C10J 3/506 (2013.01); C10J 3/84 (2013.01); C10K 1/08 (2013.01); C10K 1/32 (2013.01); C10K 3/008 (2013.01); C10K 3/023 (2013.01); C10L 1/04 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/062 (2013.01); C01B 2203/1241 (2013.01); C10G 2300/1011 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01); C10G 2400/08 (2013.01); C10J 2300/0916 (2013.01); C10J 2300/0976 (2013.01); C10J 2300/1659 (2013.01); C10J 2300/1807 (2013.01); C10J 2300/1853 (2013.01); C10L 2200/0492 (2013.01); C10L 2270/023 (2013.01); C10L 2270/026 (2013.01); C10L 2270/04 (2013.01); C10L 2290/04 (2013.01); C10L 2290/06 (2013.01); C10L 2290/10 (2013.01); C10L 2290/42 (2013.01); C10L 2290/541 (2013.01); C10L 2290/542 (2013.01); C10L 2290/543 (2013.01); C10L 2290/548 (2013.01); Y02E 50/32 (2013.01); Y02P 20/145 (2015.11); Y02P 20/582 (2015.11); Y02P 30/20 (2015.11);
Abstract

An integrated plant to generate chemical grade syngas from a steam biomass reforming in a multiple stage bio reforming reactor for use with either a high temperature or low temperature Fischer-Tropsch synthesis process to produce fuel from biomass is discussed. The first stage has a reactor to cause a chemical devolatilization of a biomass feedstock from the biomass feedstock supply lines into its constituent gases of CO, H2, CO2, CH4, tars, chars, and other components into a raw syngas mixture. A second stage performs further reforming of the raw syngas from the first stage into the chemical grade syngas by further applying heat and pressure to chemically crack at least the tars, reform the CH4, or a combination of both, into their corresponding syngas molecules. The second stage feeds the chemical grade syngas derived from the biomass feedstock to the downstream Fischer-Tropsch train to produce the fuel from the biomass. One or more recycle loops supply tail gas or FT product back into the plant.


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