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:
Oct. 29, 2019

Filed:

Mar. 24, 2017
Applicant:

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

Inventors:

Ajit B. Dandekar, Clinton, NJ (US);

Bradley R. Fingland, Mason, MI (US);

Kendall S. Fruchey, Easton, PA (US);

Scott J. Weigel, Allentown, PA (US);

Assignee:
Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 65/12 (2006.01); C10M 101/02 (2006.01); C10G 69/02 (2006.01); C10G 47/18 (2006.01);
U.S. Cl.
CPC ...
C10G 65/12 (2013.01); C10G 47/18 (2013.01); C10G 69/02 (2013.01); C10M 101/02 (2013.01); C10G 2300/202 (2013.01); C10G 2300/302 (2013.01); C10G 2400/10 (2013.01); C10M 2203/1006 (2013.01); C10M 2203/1025 (2013.01); C10M 2203/1045 (2013.01); C10M 2203/1065 (2013.01); C10N 2220/02 (2013.01); C10N 2220/022 (2013.01); C10N 2220/025 (2013.01); C10N 2230/02 (2013.01); C10N 2230/08 (2013.01); C10N 2230/10 (2013.01); C10N 2240/10 (2013.01); C10N 2240/12 (2013.01);
Abstract

Systems and methods are provided for producing lubricant basestocks having a reduced or minimized aromatics content. A first processing stage can perform an initial amount of hydrotreating and/or hydrocracking. A first separation stage can then be used to remove fuels boiling range (and lower boiling range) compounds. The remaining lubricant boiling range fraction can then be exposed under hydrocracking conditions to a USY catalyst including a supported noble metal, such as Pt and/or Pd. The USY catalyst can have a desirable combination of catalyst properties, such as a unit cell size of 24.30 or less (or 24.24 or less), a silica to alumina ratio of at least 50 (or at least 80), and an alpha value of 20 or less (or 10 or less). In some aspects, the effluent from the second (hydrocracking) stage can be dewaxed without further separation. In such aspects, a portion of the dewaxed effluent can be used as a recycle quench stream to cool the hydrocracking effluent prior to entering the dewaxing reactor.


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