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. 15, 2021

Filed:

Sep. 04, 2017
Applicant:

Bp P.l.c., London, GB;

Inventor:

Larry Nemec, Houston, TX (US);

Assignee:

BP P.L.C., London, GB;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 47/02 (2006.01); C10G 47/10 (2006.01); C10G 47/14 (2006.01); B01J 23/42 (2006.01); B01J 23/44 (2006.01); B01J 23/882 (2006.01);
U.S. Cl.
CPC ...
C10G 47/14 (2013.01); B01J 23/42 (2013.01); B01J 23/44 (2013.01); B01J 23/882 (2013.01); C10G 47/02 (2013.01); C10G 47/10 (2013.01); B01J 2523/68 (2013.01); B01J 2523/824 (2013.01); B01J 2523/828 (2013.01); B01J 2523/845 (2013.01); C10G 2300/1022 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/703 (2013.01);
Abstract

The present invention provides a process for upgrading a Fischer-Tropsch product by hydrocracking in the presence of a hydrocracking catalyst in a reactor, wherein the process is initiated by a series of steps (i) to (iv). The hydrocracking catalyst is (i) contacted with a hydrogen-containing stream having a feed temperature of from 360° C. to 420° C.; (ii) the feed temperature of the hydrogen-containing stream is reduced to a temperature of from 220° C. to 280° C.; (iii) the catalyst is contacted with a Fischer-Tropsch product stream having a feed temperature of from 220° C. to 280° C., which is co-fed with the hydrogen-containing stream; and (iv) the catalyst is co-fed with a Fischer-Tropsch product stream and hydrogen-containing stream having feed temperatures of from 380° C. and 400° C. for at least four days and wherein the hydrocracking catalyst is not activated by sulfiding.


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