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:
Dec. 15, 2020

Filed:

Apr. 22, 2020
Applicant:

Phillips 66 Company, Houston, TX (US);

Inventors:

Anthony O. Baldridge, Bartlesville, OK (US);

Neal D. McDaniel, Ochelata, OK (US);

James A. Suttil, Bartlesville, OK (US);

Jianhua Yao, Bartlesville, OK (US);

Edward C. Weintrob, Owasso, OK (US);

Matthew J. Wülfers, Collinsville, OK (US);

Bruce B. Randolph, Bartlesville, OK (US);

Maziar Sardashti, Timnath, CO (US);

Assignee:

Phillips 66 Company, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 5/27 (2006.01); C07C 2/84 (2006.01); B01J 29/40 (2006.01); C10L 1/06 (2006.01);
U.S. Cl.
CPC ...
C07C 5/2708 (2013.01); B01J 29/40 (2013.01); C07C 2/84 (2013.01); C10L 1/06 (2013.01); C07C 2529/40 (2013.01); C10L 2200/0423 (2013.01); C10L 2270/023 (2013.01); C10L 2290/30 (2013.01);
Abstract

Processes for producing liquid transportation fuels by converting a hydrocarbon feed stream comprising both isopentane and n-pentane. The hydrocarbon feed stream is separated into a first fraction that predominantly comprises isopentane and a second fraction that predominantly comprises n-pentane and some C6 paraffins. The first fraction is catalytically activated to produce an activation effluent comprising olefins and aromatics, while the second fraction is isomerized to convert at least a portion of the n-pentane to isopentane, then combined with the hydrocarbon feed stream to allow the newly-produced isopentane to be separated into the first fraction. Finally, the activation effluent is oligomerized. The process produced increased yields of products that meet specifications for a blend component of liquid transportation fuels.


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