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:
Jul. 07, 2020

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:
Int. Cl.
CPC ...
C10G 63/02 (2006.01); B01J 21/04 (2006.01); C10G 35/06 (2006.01); C10G 50/00 (2006.01); C10G 7/00 (2006.01); B01J 23/89 (2006.01); B01J 23/00 (2006.01); B01J 23/62 (2006.01); B01J 23/60 (2006.01);
U.S. Cl.
CPC ...
C10G 63/02 (2013.01); B01J 21/04 (2013.01); B01J 23/005 (2013.01); B01J 23/60 (2013.01); B01J 23/626 (2013.01); B01J 23/8966 (2013.01); C10G 7/00 (2013.01); C10G 35/06 (2013.01); C10G 50/00 (2013.01); B01J 2523/42 (2013.01); B01J 2523/43 (2013.01); B01J 2523/82 (2013.01); C10G 2300/1085 (2013.01); C10G 2400/20 (2013.01); C10G 2400/22 (2013.01); C10G 2400/30 (2013.01);
Abstract

Systems for reforming a feedstock comprising paraffins and naphthenes. A first reactor containing a first reforming catalyst is operable to maintain a temperature and pressure that facilitates conversion of naphthenes in the feedstock to aromatics while facilitating conversion of less than 50 wt. % of paraffins in the feedstock to olefins. A first separator receives and separates the first effluent that is produced in the first reactor to produce a first fraction enriched in aromatics and a second fraction enriched in paraffins. A second reactor containing a second reforming catalyst is operable to maintain a temperature and pressure that facilitates conversion of at least 50 wt. % of paraffins in the second fraction to olefins. The system is operable to produce a liquid hydrocarbon product suitable for use as a blend component of a liquid transportation fuel.


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