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:
Dec. 30, 2014

Filed:

Aug. 17, 2011
Applicants:

Erling Rytter, Trondheim, NO;

Sigrid Eri, Ranheim, NO;

Torild Hulsund Skagseth, Ranheim, NO;

Oyvind Borg, Trondheim, NO;

Inventors:

Erling Rytter, Trondheim, NO;

Sigrid Eri, Ranheim, NO;

Torild Hulsund Skagseth, Ranheim, NO;

Oyvind Borg, Trondheim, NO;

Assignee:

GTLFI AG, Zurich, DE;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 38/12 (2006.01); C10G 3/00 (2006.01); B01J 23/94 (2006.01); B01J 33/00 (2006.01); B01J 35/02 (2006.01); B01J 35/10 (2006.01); B01J 38/10 (2006.01); C07C 1/04 (2006.01); C10G 2/00 (2006.01); B01J 23/00 (2006.01); B01J 23/75 (2006.01);
U.S. Cl.
CPC ...
C10G 3/62 (2013.01); B01J 23/94 (2013.01); B01J 33/00 (2013.01); B01J 35/023 (2013.01); B01J 35/1014 (2013.01); B01J 35/1038 (2013.01); B01J 38/10 (2013.01); B01J 38/12 (2013.01); C07C 1/045 (2013.01); C10G 2/332 (2013.01); B01J 23/005 (2013.01); B01J 23/75 (2013.01); C07C 2521/04 (2013.01); C07C 2523/36 (2013.01); C07C 2523/42 (2013.01); C07C 2523/75 (2013.01); C07C 2523/889 (2013.01); C07C 2523/89 (2013.01); Y10S 502/514 (2013.01); Y10S 502/518 (2013.01);
Abstract

A process for the regeneration of deactivated catalyst from a Fischer-Tropsch synthesis reactor, the catalyst being a supported cobalt catalyst. The process comprises the following steps: a withdrawal step, in which a portion of deactivated catalyst together with liquid hydrocarbon is withdrawn from the reactor; a concentration step, in which the concentration of the catalyst in the liquid hydrocarbon is increased; a calcination step, in which the deactivated catalyst composition is subjected to an oxidizing gas to oxidize carbonaceous material contained in the deactivated catalyst in to gaseous oxides of the components of the carbonaceous material; and a reactivation step, in which the deactivated catalyst composition is reactivated to produced a regenerated catalyst.


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