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:
Nov. 21, 2017

Filed:

Mar. 16, 2015
Applicant:

Shell Oil Company, Houston, TX (US);

Inventors:

Gerrit Leendert Bezemer, Amsterdam, NL;

Carolus Matthias Anna Maria Mesters, Sugar Land, TX (US);

Johan Peter Den Breejen, Amsterdam, NL;

Assignee:

SHELL OIL COMPANY, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 2/00 (2006.01); C07C 1/04 (2006.01); B01J 37/18 (2006.01); B01J 23/75 (2006.01); B01J 8/06 (2006.01); B01J 8/00 (2006.01); B01J 8/02 (2006.01); B01J 23/94 (2006.01);
U.S. Cl.
CPC ...
C10G 2/332 (2013.01); B01J 8/001 (2013.01); B01J 8/02 (2013.01); B01J 8/065 (2013.01); B01J 8/067 (2013.01); B01J 23/75 (2013.01); B01J 23/94 (2013.01); B01J 37/18 (2013.01); C07C 1/04 (2013.01); C07C 1/045 (2013.01); C07C 1/047 (2013.01); C07C 1/048 (2013.01); C07C 1/0455 (2013.01); C10G 2/341 (2013.01); B01J 2208/00061 (2013.01); B01J 2208/00628 (2013.01); B01J 2208/00646 (2013.01); B01J 2208/00716 (2013.01); B01J 2219/002 (2013.01); B01J 2219/00213 (2013.01); B01J 2219/00231 (2013.01);
Abstract

The invention relates to a method for start-up and operation of a Fischer-Tropsch reactor comprising the steps of: (a) providing a reactor with a fixed bed of reduced Fischer-Tropsch catalyst that comprises cobalt as catalytically active metal; (b) supplying a gaseous feed stream comprising carbon monoxide and hydrogen to the reactor, wherein the gaseous feed stream initially comprises a nitrogen-containing compound other than molecular nitrogen in an initial concentration in the range of from 0.1 to 50 ppmv based on the volume of the gaseous feed stream; (c) converting carbon monoxide and hydrogen supplied with the gaseous feed stream to the reactor into hydrocarbons at an initial reaction temperature, wherein the initial reaction temperature is set at a value of at least 200° C. and hydrocarbons are produced at a first yield; (d) maintaining the initial reaction temperature at the set value and maintaining the first yield by decreasing the concentration of the nitrogen-containing compound in the gaseous feed stream supplied to the reactor; (e) optionally increasing the reaction temperature after the concentration of the nitrogen-containing compound in the gaseous feed stream has decreased to a value below 100 ppbv.


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