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:
Apr. 17, 2018

Filed:

Jul. 03, 2013
Applicant:

David Bradin, Chapel Hill, NC (US);

Inventor:

David Bradin, Chapel Hill, NC (US);

Assignee:

Other;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C07C 1/00 (2006.01); C10G 1/00 (2006.01); C10L 1/04 (2006.01); C10L 1/10 (2006.01); C10G 50/00 (2006.01); C10G 69/12 (2006.01); C10G 3/00 (2006.01); C10G 45/02 (2006.01); C10G 45/58 (2006.01); C07C 1/20 (2006.01); C07C 29/136 (2006.01); C07C 41/09 (2006.01); C10G 57/02 (2006.01);
U.S. Cl.
CPC ...
C10L 1/04 (2013.01); C07C 1/20 (2013.01); C07C 29/136 (2013.01); C07C 41/09 (2013.01); C10G 3/42 (2013.01); C10G 3/49 (2013.01); C10G 45/02 (2013.01); C10G 45/58 (2013.01); C10G 50/00 (2013.01); C10G 57/02 (2013.01); C10G 69/126 (2013.01); C07C 2529/44 (2013.01); C07C 2529/85 (2013.01); C10G 2300/1011 (2013.01); C10G 2400/08 (2013.01); C10G 2400/20 (2013.01); C10G 2400/30 (2013.01); C10L 2200/0492 (2013.01); C10L 2270/04 (2013.01); C10L 2290/04 (2013.01); C10L 2290/24 (2013.01);
Abstract

Processes for producing jet fuel are disclosed. In one embodiment, syngas is converted to methanol, and a first portion of the methanol is converted to olefins using a methanol-to-olefins catalyst. The olefins are then oligomerized under conditions that provide olefins in the jet fuel range. The olefins can then optionally be isomerized and/or hydrotreated. A second portion of the methanol is converted to dimethyl ether, which is then reacted over a catalyst to form jet fuel-range hydrocarbons and aromatics. All or part of the two separate product streams can be combined, to provide jet fuel components which include isoparaffins and aromatics in the jet fuel range. The syngas is preferably derived from biomass or another renewable carbon-containing feedstock, thereby providing a biorefining process for the production of renewable jet fuel. In another embodiment, the process starts with methanol, rather than producing the methanol from syngas.


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