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:
Jul. 14, 2026

Filed:

Jan. 21, 2025
Applicant:

Duke Technologies, Llc, Fayetteville, AR (US);

Inventors:

Michael D. Ackerson, Fayetteville, AR (US);

Michael Steven Byars, Fayetteville, AR (US);

Kyle Ackerson, Prairie Grove, AR (US);

John Coleman, Lowell, AR (US);

Assignee:

Duke Technologies, LLC, Fayetteville, AR (US);

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/02 (2006.01); B01D 17/02 (2006.01); B01D 19/00 (2006.01); C10G 3/00 (2006.01);
U.S. Cl.
CPC ...
C10G 69/02 (2013.01); B01D 17/0214 (2013.01); B01D 19/0005 (2013.01); C10G 3/40 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/1011 (2013.01); C10G 2300/202 (2013.01); C10G 2300/205 (2013.01); C10G 2300/302 (2013.01); C10G 2300/308 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4018 (2013.01); C10G 2400/04 (2013.01);
Abstract

A system for treating non-petroleum or renewable feedstocks containing oxygen and contaminants of one or more of metals, gums, and resins comprises a reactor having a heat source for heating an interior of the reactor. The reactor is configured to receive the feedstock at a flow velocity of from 20 ft/sec to 100 ft/sec within the interior to facilitate heating the feedstock to a temperature of from 700° F. to 1100° F. to form a reactor product. A heat exchanger is configured to cool the reactor product and a separator unit is configured to separate metals, water, and gases comprising Cor greater hydrocarbons from the cooled reactor product to form a final product. A reformer unit is configured to receive at least a portion of the gases for converting the at least one of Cor greater hydrocarbons to produce hydrogen gas from the Cor greater hydrocarbons.


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