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:
Nov. 30, 2021

Filed:

Jul. 03, 2019
Applicant:

The Texas A&m University System, College Station, TX (US);

Inventors:

Sergio C. Capareda, College Station, TX (US);

Calvin B. Parnell, Jr., College Station, TX (US);

David B. Carney, College Station, TX (US);

Assignee:

The Texas A&M University System, College Station, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10B 53/02 (2006.01); C10B 49/22 (2006.01); C10J 3/46 (2006.01); C10B 53/00 (2006.01); C10J 3/48 (2006.01); C10K 1/02 (2006.01); B04C 5/26 (2006.01); F23C 10/20 (2006.01); F23C 10/10 (2006.01); C10J 3/84 (2006.01); C10J 3/50 (2006.01); F23G 5/027 (2006.01); B01J 8/44 (2006.01); F23G 5/30 (2006.01); F23G 7/10 (2006.01); C10J 3/54 (2006.01); F16L 41/02 (2006.01); G01F 1/76 (2006.01);
U.S. Cl.
CPC ...
C10B 53/00 (2013.01); B01J 8/44 (2013.01); B04C 5/26 (2013.01); C10B 49/22 (2013.01); C10B 53/02 (2013.01); C10J 3/463 (2013.01); C10J 3/482 (2013.01); C10J 3/503 (2013.01); C10J 3/54 (2013.01); C10J 3/84 (2013.01); C10K 1/026 (2013.01); F16L 41/02 (2013.01); F23C 10/10 (2013.01); F23C 10/20 (2013.01); F23G 5/027 (2013.01); F23G 5/30 (2013.01); F23G 7/10 (2013.01); G01F 1/76 (2013.01); C10J 2200/15 (2013.01); C10J 2300/0916 (2013.01); C10J 2300/0956 (2013.01); F23G 2201/40 (2013.01); F23G 2203/501 (2013.01); F23J 2217/40 (2013.01); Y02P 20/145 (2015.11); Y10T 137/85938 (2015.04);
Abstract

A pyrolysis and gasification system produce a synthesis gas and bio-char from a biomass feedstock. The system includes a feed hopper that has a flow measurement device. The system also includes a reactor that is operable in a gasification mode or a pyrolysis mode. The reactor is configured to receive the biomass feedstock from the feed hopper. The reactor is operable to provide heat to the biomass feedstock from the feed hopper to produce the synthesis gas and bio-char. The system also includes a cyclone assembly. The produced synthesis gas including the bio-char is fed to the cyclone assembly. The cyclone assembly removes a portion of the bio-char from the synthesis gas.


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