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. 24, 2017

Filed:

Mar. 15, 2013
Applicant:

Seerstone Llc, Provo, UT (US);

Inventor:

Dallas B. Noyes, Provo, UT (US);

Assignee:

Seerstone LLC, Provo, UT (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 31/02 (2006.01); B01J 37/16 (2006.01); B01J 23/755 (2006.01); C01B 31/04 (2006.01); B01J 37/18 (2006.01); B01J 23/28 (2006.01); B01J 23/30 (2006.01); B01J 23/75 (2006.01); B01J 23/882 (2006.01); B01J 23/883 (2006.01); B01J 23/888 (2006.01); B01J 35/00 (2006.01); B01J 35/02 (2006.01); B82Y 30/00 (2011.01); B82Y 40/00 (2011.01); B01J 35/06 (2006.01); B01J 35/08 (2006.01); C01B 31/06 (2006.01);
U.S. Cl.
CPC ...
C01B 31/02 (2013.01); B01J 23/28 (2013.01); B01J 23/30 (2013.01); B01J 23/75 (2013.01); B01J 23/755 (2013.01); B01J 23/882 (2013.01); B01J 23/883 (2013.01); B01J 23/888 (2013.01); B01J 23/8885 (2013.01); B01J 35/002 (2013.01); B01J 35/02 (2013.01); B01J 35/023 (2013.01); B01J 35/026 (2013.01); B01J 35/06 (2013.01); B01J 35/08 (2013.01); B01J 37/16 (2013.01); B01J 37/18 (2013.01); B82Y 30/00 (2013.01); B82Y 40/00 (2013.01); C01B 31/0206 (2013.01); C01B 31/0213 (2013.01); C01B 31/0233 (2013.01); C01B 31/04 (2013.01); C01B 31/0438 (2013.01); C01B 31/06 (2013.01); C01B 2202/06 (2013.01); Y10T 428/24917 (2015.01); Y10T 428/2958 (2015.01); Y10T 428/2982 (2015.01); Y10T 428/31678 (2015.04);
Abstract

A method of reducing a gaseous carbon oxide includes reacting a carbon oxide with a gaseous reducing agent in the presence of a non-ferrous catalyst. The reaction proceeds under conditions adapted to produce solid carbon of various allotropes and morphologies, the selective formation of which can be controlled by means of controlling reaction gas composition and reaction conditions including temperature and pressure. A method for utilizing a non-ferrous catalyst in a reactor includes placing the catalyst in a suitable reactor and flowing reaction gases comprising a carbon oxide with at least one gaseous reducing agent through the reactor where, in the presence of the catalyst, at least a portion of the carbon in the carbon oxide is converted to solid carbon and a tail gas mixture containing water vapor.


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