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:
Apr. 20, 2021

Filed:

Oct. 04, 2019
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);

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

Jianhua Yao, Bartlesville, OK (US);

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

Maziar Sardashti, Timnath, CO (US);

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

Steven E. Lusk, Ponca City, OK (US);

Assignee:

Phillips 66 Company, Houston, TX (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 5/27 (2006.01); C07C 5/333 (2006.01); C07C 4/02 (2006.01); C07C 2/76 (2006.01); C10L 1/06 (2006.01); C10G 63/02 (2006.01); C10G 63/04 (2006.01);
U.S. Cl.
CPC ...
C07C 5/2737 (2013.01); C07C 2/76 (2013.01); C07C 4/02 (2013.01); C07C 5/333 (2013.01); C10G 63/02 (2013.01); C10G 63/04 (2013.01); C10L 1/06 (2013.01); C07C 2521/04 (2013.01); C07C 2529/40 (2013.01); C10G 2300/1081 (2013.01); C10G 2300/802 (2013.01); C10G 2400/02 (2013.01); C10L 2270/023 (2013.01);
Abstract

The present disclosure relates to processes that catalytically convert a hydrocarbon feed stream predominantly comprising both isopentane and n-pentane to yield upgraded hydrocarbon products that are suitable for use either as a blend component of liquid transportation fuels or as an intermediate in the production of other value-added chemicals. The hydrocarbon feed stream is isomerized in a first reaction zone to convert at least a portion of the n-pentane to isopentane, followed by catalytic-activation of the isomerization effluent in a second reaction zone with an activation catalyst to produce an activation effluent. The process increases the conversion of the hydrocarbon feed stream to olefins and aromatics, while minimizing the production of C1-C4 light paraffins. Certain embodiments provide for further upgrading of at least a portion of the activation effluent by either oligomerization or alkylation.


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