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. 12, 2012

Filed:

Mar. 04, 2010
Applicants:

Detlef Abe, Angermunde, DE;

Frank Eschenroder, Schwedt, DE;

David Laban, Schwedt, DE;

Hartmut Schutter, Schwedt, DE;

Laurent Bournay, Chaussan, FR;

Thierry Chapus, Lyons, FR;

Nathalie Dupassieux, Lyons, FR;

Inventors:

Detlef Abe, Angermunde, DE;

Frank Eschenroder, Schwedt, DE;

David Laban, Schwedt, DE;

Hartmut Schutter, Schwedt, DE;

Laurent Bournay, Chaussan, FR;

Thierry Chapus, Lyons, FR;

Nathalie Dupassieux, Lyons, FR;

Assignee:

IFP Energies nouvelles, Rueil Malmaison Cedex, FR;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10L 1/19 (2006.01);
U.S. Cl.
CPC ...
Abstract

Process for the continuous hydrogenation of triglyceride containing raw materials in a fixed bed reactor system having several catalyst beds arranged in series and comprising hydrogenation catalyst. The raw material feed, hydrogen containing gas and diluting agent are passed together through the catalyst beds at hydrogenation conditions. The raw material feed stream as well as the stream of hydrogen containing gas are divided into an equal number of different partial streams. These are each passed to one catalyst bed in such a manner that the weight ratio of diluting agent to raw material feed is essentially the same at the entrance of all catalyst beds and does not exceed 4:1. The claimed process is preferably conducted at low temperatures and allows the utilization of existing units due to the low recycle ratio. Further, a sufficient excess of hydrogen is used so that no valuable product is lost through decarb-reactions.


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