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. 12, 2021

Filed:

Dec. 23, 2016
Applicant:

Shell Oil Company, Houston, TX (US);

Inventors:

Diederik De Jonge, Amsterdam, NL;

Edward Julius Creyghton, Amsterdam, NL;

Eduard Philip Kieffer, Amsterdam, NL;

Duurt Renkema, Amsterdam, NL;

Assignee:

SHELL OIL COMPANY, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/02 (2006.01); C10M 171/02 (2006.01); C10G 65/04 (2006.01); C10G 65/12 (2006.01); C10M 107/02 (2006.01); C10M 105/02 (2006.01); C10N 20/02 (2006.01); C10N 20/00 (2006.01); C10N 30/02 (2006.01); C10N 70/00 (2006.01);
U.S. Cl.
CPC ...
C10G 69/02 (2013.01); C10G 65/043 (2013.01); C10G 65/12 (2013.01); C10M 105/02 (2013.01); C10M 107/02 (2013.01); C10M 171/02 (2013.01); C10G 2300/1022 (2013.01); C10G 2300/304 (2013.01); C10G 2400/10 (2013.01); C10M 2205/173 (2013.01); C10N 2020/011 (2020.05); C10N 2020/02 (2013.01); C10N 2030/02 (2013.01); C10N 2070/00 (2013.01);
Abstract

The present invention relates to a process for preparing a residual base oil from a hydrocarbon feed which is derived from a Fischer-Tropsch process, the process comprises the steps of: (a) providing a hydrocarbon feed which is derived from a Fischer-Tropsch process; (b) subjecting the hydrocarbon feed of step (a) to a hydrocracking/hydroisomerisation step to obtain an at least partially isomerised product; (c) separating at least part of the at least partially isomerised product as obtained in step (b) into one or more lower boiling fractions and a hydrowax residue fraction; (d) catalytic dewaxing of the hydrowax residue fraction of step (c) to obtain a highly isomerised product; (e) separating the highly isomerised product of step (d) into one or more light fractions and a isomerised residual fraction; (f) mixing of the isomerised residual fraction of step (e) with a diluent to obtain a diluted isomerised residual fraction; (g) cooling the diluted isomerised residual fraction of step (f) to a temperature between 0° C. and −60° C.; (i) subjecting the mixture of step (g) to a centrifuging step at a temperature between 0° C. and −60° C. to isolate the wax from the diluted isomerised residual fraction; (j) separating the diluent from the diluted isomerised residual fraction to obtain a residual base oil.


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