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:
May. 10, 2016

Filed:

Jan. 23, 2006
Applicants:

Focco Cornelis Bijlsma, Amsterdam, NL;

Jan Lodewijk Maria Dierickx, Amsterdam, NL;

Arend Hoek, Amsterdam, NL;

Frans Joris Antonius Kellendonk, De Bilt, NL;

Anna Elisabeth Maria Oud, Amsterdam, NL;

Inventors:

Focco Cornelis Bijlsma, Amsterdam, NL;

Jan Lodewijk Maria Dierickx, Amsterdam, NL;

Arend Hoek, Amsterdam, NL;

Frans Joris Antonius Kellendonk, De Bilt, NL;

Anna Elisabeth Maria Oud, Amsterdam, NL;

Assignee:

Shell Oil Company, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 21/00 (2006.01); B01J 23/00 (2006.01); B01J 25/00 (2006.01); B01J 29/00 (2006.01); B01J 23/755 (2006.01); B01J 21/04 (2006.01); B01J 35/10 (2006.01); B01J 37/02 (2006.01); C10G 45/00 (2006.01); C10G 3/00 (2006.01); C10G 45/06 (2006.01); C10G 45/12 (2006.01); C10G 2/00 (2006.01);
U.S. Cl.
CPC ...
B01J 23/755 (2013.01); B01J 21/04 (2013.01); B01J 35/10 (2013.01); B01J 37/0205 (2013.01); C10G 3/45 (2013.01); C10G 3/50 (2013.01); C10G 45/00 (2013.01); C10G 45/06 (2013.01); C10G 45/12 (2013.01); B01J 35/1061 (2013.01); B01J 35/1085 (2013.01); C10G 2/332 (2013.01); C10G 2300/1022 (2013.01); C10G 2300/4018 (2013.01); Y02P 30/20 (2015.11);
Abstract

A hydrogenation catalyst particularly suitable for hydrogenating oxygenates in a hydrogenation unit of a Fischer-Tropsch plant is disclosed. A preferred embodiment comprises more than 5% and less than 20% nickel based on a wide pore alumina support. The catalyst successfully hydrogenates oxygenates which otherwise tend to poison a catalyst in a hydroconversion unit downstream. Moreover, the temperature at which the unwanted hydrogenolysis of long chain paraffins to methane occurs is higher for one catalyst disclosed herein than a comparable known catalyst. This allows the hydrogenation plant to operate at a higher temperature.


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