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:
Feb. 25, 2025

Filed:

Jul. 20, 2023
Applicant:

Phillips 66 Company, Houston, TX (US);

Inventors:

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

Matthew J. Wulfers, Owasso, OK (US);

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

Robert M. Walston, Skiatook, OK (US);

Assignee:

Phillips 66 Company, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 2/74 (2006.01); C07C 2/76 (2006.01); C07C 5/333 (2006.01); C10G 57/00 (2006.01); C10L 1/04 (2006.01);
U.S. Cl.
CPC ...
C10G 57/005 (2013.01); C07C 2/74 (2013.01); C07C 2/76 (2013.01); C07C 5/333 (2013.01); C10L 1/04 (2013.01); C07C 2529/40 (2013.01); C10G 2300/1081 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/70 (2013.01);
Abstract

The present disclosure relates generally to processes and systems for producing liquid transportation fuels by converting a feed stream that predominantly comprises isobutane. The feed stream is catalytically-activated in two separate reaction zones arranged in series in a manner that minimizes the production of C1-C3 light paraffins and is tolerant to the presence of typical catalyst poisons. The first reaction zone is selective for conversion of the feed stream to predominantly olefins and some aromatics. The second reaction zone is maintained at a lower temperature and a higher pressure and is selective for converting olefins to monocyclic aromatics which facilitates further feed stream olefination. Certain embodiments contact the activation effluent with an alkylation catalyst to provide enhanced yields of upgraded hydrocarbon products that meet specifications for a transportation fuel blend component.


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