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:
Feb. 28, 2023

Filed:

Aug. 24, 2021
Applicant:

Advanced Energy Materials, Llc, Louisville, KY (US);

Inventors:

Mahendra Sunkara, Louisville, KY (US);

Sivakumar Vasireddy, Louisville, KY (US);

Vivekanand Kumar, Louisville, KY (US);

Juan He, Louisville, KY (US);

Tu Nguyen, Louisville, KY (US);

Veerendra Atla, Louisville, KY (US);

Assignee:

Advanced Energy Materials, LLC, Louisville, KS (US);

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C01B 32/40 (2017.01); C07C 1/12 (2006.01); C01B 3/04 (2006.01);
U.S. Cl.
CPC ...
C01B 32/40 (2017.08); C01B 3/04 (2013.01); C07C 1/12 (2013.01); C01B 2203/061 (2013.01); C01B 2203/062 (2013.01); C01B 2203/0861 (2013.01); C01B 2203/1076 (2013.01); C01B 2203/1082 (2013.01); C01B 2203/148 (2013.01); C07C 2521/06 (2013.01); C07C 2523/80 (2013.01);
Abstract

The present development is a process to produce commodity chemicals such as methanol and syngas using an integrated plasma catalysis technology. The method comprises providing a fixed or fluidized bed reactor having a microwave plasma flame and a catalyst bed with a catalyst, wherein the catalyst is an alloyed bimetallic nanowire. In the process, the plasma flame fluidizes the catalyst thereby producing a more effective catalyst than the non-fluidized catalyst. It is anticipated that the reactor can have a throughput capacity of up to 30 Lpm/kW and can be effective for the conversion of CO, CH, air, water, and combinations thereof, through reactions such as pure COsplitting, reverse water gas shift (RWGS) for CO production, methanol synthesis, and plasma reforming of methane, thereby making a system that would be attractive for small GTL units.


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