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:
Aug. 01, 2017

Filed:

Nov. 18, 2014
Applicants:

Stuart S. Shih, Gainesville, VA (US);

Gary P. Schleicher, Milford, NJ (US);

Michael B. Carroll, Center Valley, PA (US);

Timothy L. Hilbert, Middleburg, VA (US);

Stephen J. Mccarthy, Center Valley, PA (US);

William J. Novak, Bedminster, NJ (US);

Inventors:

Stuart S. Shih, Gainesville, VA (US);

Gary P. Schleicher, Milford, NJ (US);

Michael B. Carroll, Center Valley, PA (US);

Timothy L. Hilbert, Middleburg, VA (US);

Stephen J. McCarthy, Center Valley, PA (US);

William J. Novak, Bedminster, NJ (US);

Assignee:
Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 45/64 (2006.01); C10G 69/02 (2006.01); C10M 103/06 (2006.01); B01J 35/10 (2006.01); C10G 65/04 (2006.01); C10G 65/12 (2006.01); B01J 23/883 (2006.01); B01J 23/888 (2006.01); B01J 29/78 (2006.01);
U.S. Cl.
CPC ...
C10G 69/02 (2013.01); B01J 23/883 (2013.01); B01J 23/888 (2013.01); B01J 29/78 (2013.01); B01J 29/7846 (2013.01); B01J 29/7861 (2013.01); B01J 29/7884 (2013.01); B01J 29/7892 (2013.01); B01J 35/1014 (2013.01); C10G 65/043 (2013.01); C10G 65/12 (2013.01); C10M 103/06 (2013.01); B01J 2229/186 (2013.01); B01J 2229/20 (2013.01); B01J 2229/42 (2013.01); C10G 2300/1048 (2013.01); C10G 2300/203 (2013.01); C10G 2300/301 (2013.01); C10G 2300/302 (2013.01); C10G 2300/307 (2013.01); C10G 2400/04 (2013.01); C10G 2400/10 (2013.01);
Abstract

Methods are provided for processing a gas oil boiling range feedstock, such as a vacuum gas oil, in a single reaction stage and/or without performing intermediate separations. The methods are suitable for forming lubricants and distillate fuels while reducing or minimizing the production of lower boiling products such as naphtha and light ends. The methods can provide desirable yields of distillate fuels and lubricant base oils without requiring separate catalyst beds or stages for dewaxing and hydrocracking. The methods are based in part on use of a dewaxing catalyst that is tolerant of sour processing environments while still providing desirable levels of activity for both feed conversion and feed isomerization.


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