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:
Jun. 01, 2010

Filed:

Mar. 01, 2005
Applicants:

Nicholas James Adams, Rosehill, AU;

Harmannus Julius Hegge, Rotterdam, NL;

Laurent Georges Huve, Amsterdam, NL;

Kevin John Anthony Polder, Petit Couronne, FR;

Wiecher Derk Evert Steenge, Amsterdam, NL;

Inventors:

Nicholas James Adams, Rosehill, AU;

Harmannus Julius Hegge, Rotterdam, NL;

Laurent Georges Huve, Amsterdam, NL;

Kevin John Anthony Polder, Petit Couronne, FR;

Wiecher Derk Evert Steenge, Amsterdam, NL;

Assignee:

Shell Oil Company, Houston, TX (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 65/00 (2006.01); C10G 69/00 (2006.01);
U.S. Cl.
CPC ...
Abstract

Process to prepare simultaneously two or more base oil grades and middle distillates from a mineral crude derived feed, in particular a de-asphalted oil or a vacuum distillate feed or their mixtures, by performing the following steps: (a) hydrocracking the mineral crude derived feed, thereby obtaining an effluent; (b) distillation of the effluent as obtained in step (a) into one or more middle distillates and a full range residue boiling substantially above 340° C., (c) catalytically dewaxing the full range residue by contacting the residue with a dewaxing catalyst comprising a zeolite of the MTW type and a Group VIII metal, thereby obtaining a dewaxed oil; (d) isolating by means of distillation two or more base oil grades from the dewaxed oil obtained in step (c); and (e) isolating a dewaxed gas oil from the dewaxed-oil obtained in step (c); wherein the dewaxed oil as obtained in step (c) comprises between 10 and 40 wt % of a dewaxed heavy gas oil boiling for more than 70 wt % between 370 and 400° C.


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