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:
Nov. 05, 2019

Filed:

Aug. 21, 2018
Applicant:

Phillips 66 Company, Houston, TX (US);

Inventors:

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

Sundararajan Uppili, Bartlesville, OK (US);

Clark A. Miller, Bartlesville, OK (US);

Tushar V. Choudhary, Bartlesville, OK (US);

Assignee:

Phillips 66 Company, Houston, TX (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 59/06 (2006.01); C10G 65/14 (2006.01); C10G 35/06 (2006.01); C10G 50/00 (2006.01); C10G 7/00 (2006.01); B01J 23/89 (2006.01); C10G 65/12 (2006.01); C10G 63/02 (2006.01);
U.S. Cl.
CPC ...
C10G 59/06 (2013.01); B01J 23/8966 (2013.01); C10G 7/00 (2013.01); C10G 35/06 (2013.01); C10G 50/00 (2013.01); C10G 65/12 (2013.01); C10G 65/14 (2013.01); B01J 2523/42 (2013.01); B01J 2523/43 (2013.01); B01J 2523/82 (2013.01); C10G 63/02 (2013.01); C10G 2300/1085 (2013.01); C10G 2400/20 (2013.01); C10G 2400/22 (2013.01); C10G 2400/30 (2013.01);
Abstract

Process for reforming a hydrocarbon feedstock comprising paraffins and naphthenes. A hydrocarbon feedstock is separated to produce a first fraction enriched in naphthenes and a second fraction that is enriched in paraffins. The first fraction is contacted with a first reforming catalyst in a first reactor that is maintained at a temperature and pressure that facilitates conversion of naphthenes to aromatics. The second fraction is contacted with a second reforming catalyst in a second reactor at a temperature and pressure that converts at least 50 wt. % of paraffins in the second fraction to olefins. The process produces a liquid hydrocarbon reformate product suitable for use as a blend component of a liquid transportation fuel.


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