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. 19, 2023

Filed:

May. 09, 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);

Soumen Kundu, Pearland, TX (US);

Bruce B Randolph, Sachse, TX (US);

Assignee:

Phillips 66 Company, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 6/10 (2006.01); C07C 7/09 (2006.01); B01J 8/04 (2006.01); B01D 3/14 (2006.01); B01D 5/00 (2006.01);
U.S. Cl.
CPC ...
C07C 6/10 (2013.01); B01D 3/14 (2013.01); B01D 5/006 (2013.01); B01J 8/0492 (2013.01); C07C 7/09 (2013.01); B01J 2208/00017 (2013.01); B01J 2208/00539 (2013.01); C07C 2529/40 (2013.01);
Abstract

The present disclosure relates generally to processes and systems for producing liquid transportation fuels by converting a feed stream that comprises both isopentane and n-pentane, and optionally, some C6+ hydrocarbons. Isopentane and smaller hydrocarbons are separated to form a first fraction while n-pentane and larger components of the feed stock form a second fraction. Each fraction is then catalytically-activated in a separate reaction zone with a separate catalyst, where the conditions maintained in each zone maximize the conversion of each fraction to olefins and aromatics, while minimizing the production of C1-C4 light paraffins. In certain embodiments, the first fraction is activated at a lower temperature than the second fraction. Certain embodiments additionally comprise mixing at least a portion of the two effluents and contacting with either an oligomerization catalyst or alkylation catalyst to provide enhanced yields of upgraded hydrocarbon products that are suitable for use as a blend component of liquid transportation fuels or other value-added chemical products.


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