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:
Nov. 07, 2017

Filed:

Mar. 10, 2016
Applicant:

Exxonmobil Research and Engineering Company, Annandale, NJ (US);

Inventors:

Benjamin S. Umansky, Fairfax, VA (US);

Teck-Mui Hoo, Centreville, VA (US);

Richard A. Demmin, Highland Park, NJ (US);

Fengrong Chen, Spring, TX (US);

James W. Gleeson, Magnolia, TX (US);

Suisheng M. Dou, The Woodlands, TX (US);

Tomas R. Melli, The Woodlands, TX (US);

Michael C. Clark, Montgomery, TX (US);

Assignee:
Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 47/12 (2006.01); C10G 47/16 (2006.01); C10G 67/02 (2006.01); C10G 47/14 (2006.01); C10G 65/12 (2006.01); C10M 101/02 (2006.01);
U.S. Cl.
CPC ...
C10G 67/02 (2013.01); C10G 47/14 (2013.01); C10G 47/16 (2013.01); C10G 65/12 (2013.01); C10M 101/02 (2013.01); C10G 2300/301 (2013.01); C10G 2300/302 (2013.01); C10G 2300/304 (2013.01); C10G 2400/10 (2013.01);
Abstract

A process for producing high yields of higher quality (API Group II, Group III') lubricating oil basestock fractions which allows the production of two or more types of high quality lubes in continuous mode (no blocked operation mode) without transition times and feed or intermediate product tankage segregation. Two consecutive hydroprocessing steps are used: the first step processes a wide cut feed at a severity needed to match heavy oil lube properties. The second step hydroprocesses a light oil after fractionation of the liquid product from the first step at a severity higher than for the heavy oil fraction. The two hydroprocessing steps will normally be carried out in separate reactors but they may be combined in a single reactor which allows for the two fractions to be processed with different degrees of severity.


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