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. 27, 2020

Filed:

May. 29, 2018
Applicant:

Emerging Fuels Technology, Inc., Tulsa, OK (US);

Inventor:

Kenneth L. Agee, Tulsa, OK (US);

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 2/12 (2006.01); C10G 3/00 (2006.01); C10G 7/00 (2006.01); C10G 50/00 (2006.01); C10G 9/00 (2006.01); C10G 69/12 (2006.01); C10M 107/04 (2006.01); C10M 107/10 (2006.01); B01J 29/40 (2006.01); B01J 29/70 (2006.01); B01J 27/10 (2006.01); B01J 27/12 (2006.01); C10N 70/00 (2006.01);
U.S. Cl.
CPC ...
C07C 2/12 (2013.01); C10G 3/40 (2013.01); C10G 3/50 (2013.01); C10G 7/003 (2013.01); C10G 9/00 (2013.01); C10G 50/00 (2013.01); C10G 69/126 (2013.01); C10M 107/04 (2013.01); C10M 107/10 (2013.01); B01J 27/10 (2013.01); B01J 27/12 (2013.01); B01J 29/40 (2013.01); B01J 29/703 (2013.01); B01J 29/7046 (2013.01); C10G 2300/1085 (2013.01); C10G 2300/1092 (2013.01); C10G 2400/22 (2013.01); C10M 2205/0225 (2013.01); C10N 2070/00 (2013.01);
Abstract

A process to convert paraffinic feedstocks into renewable poly-alpha-olefins (PAO) basestocks. In a preferred embodiment of the invention, renewable feed comprising triglycerides and/or free fatty acids are hydrotreated producing an intermediate paraffin feedstock. This paraffin feedstock is thermally cracked into a mixture of olefins and paraffins comprising linear alpha olefins. The olefins are separated and the un-reacted paraffins are recycled to the thermal cracker. Light olefins preferably are oligomerized with a surface deactivated zeolite producing a mixture of slightly branched oligomers comprising internal olefins. The heavier olefins (C8-C14) are oligomerized, preferably with a BF3 catalyst and co-catalyst to produce PAO products. The oligomerized products can be hydrotreated and distilled together or separate to produce finished products that include naphtha, distillate, solvents, drilling fluid, and PAO lube basestocks.


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