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:
Oct. 06, 2020

Filed:

Jul. 17, 2019
Applicant:

Ifp Energies Nouvelles, Rueil-Malmaison, FR;

Inventors:

Jean-Philippe Heraud, Rueil-Malmaison, FR;

Christophe Bouchy, Rueil-Malmaison, FR;

Assignee:

IFP Energies Nouvelles, Rueil-Malmaison, FR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 67/00 (2006.01); B01J 21/04 (2006.01); B01J 29/74 (2006.01); B01J 37/00 (2006.01); B01J 37/02 (2006.01); B01J 37/08 (2006.01); B01J 37/30 (2006.01);
U.S. Cl.
CPC ...
C10G 67/00 (2013.01); B01J 21/04 (2013.01); B01J 29/74 (2013.01); B01J 37/0018 (2013.01); B01J 37/0207 (2013.01); B01J 37/08 (2013.01); B01J 37/30 (2013.01); B01J 2229/186 (2013.01); C10G 2300/1022 (2013.01); C10G 2300/1085 (2013.01); C10G 2300/202 (2013.01); C10G 2300/301 (2013.01);
Abstract

A process is described for producing middle distillates from a paraffinic feedstock produced by Fischer-Tropsch synthesis and divided into a light fraction (cold condensate) and a heavy fraction (waxes). The process involves fractionation of the waxes to obtain a light fraction, the final boiling point of which is between 350° C. and 400° C., and a heavy fraction which boils above the light fraction. The light fraction is mixed with at least one portion of the cold condensate. The resultant mixture is hydrotreated in the presence of a hydrotreatment catalyst of at least one portion of the resultant effluent is hydroisomerized in the presence of a catalyst comprising at least one noble metal from Group VIII and at least one zeolite IZM-2. At least one portion of the heavy fraction is subjected to hydrocracking and hydroisomerization in the presence of a hydrocracking catalyst. The resultant effluents are fractionated to obtain at least one middle distillates fraction.


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