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. 09, 2017

Filed:

Feb. 26, 2013
Applicant:

Ifp Energies Nouvelles, Rueil-Malmaison, FR;

Inventors:

Antoine Daudin, Corbas, FR;

Alain Quignard, Roussillon, FR;

Olivier Thinon, Roanne, FR;

Assignee:

IFP Energies nouvelles, Rueil-Malmaison, FR;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 65/02 (2006.01); C10G 65/12 (2006.01); C10G 65/04 (2006.01); C08H 8/00 (2010.01); C10G 3/00 (2006.01); C10G 45/00 (2006.01); C10G 47/00 (2006.01); B01J 37/20 (2006.01); B01J 21/04 (2006.01); B01J 21/18 (2006.01); B01J 23/86 (2006.01); B01J 23/883 (2006.01); B01J 37/00 (2006.01); C10G 1/00 (2006.01);
U.S. Cl.
CPC ...
C10G 65/043 (2013.01); B01J 21/04 (2013.01); B01J 21/18 (2013.01); B01J 23/866 (2013.01); B01J 23/883 (2013.01); B01J 37/0009 (2013.01); B01J 37/20 (2013.01); C08H 8/00 (2013.01); C10G 1/002 (2013.01); C10G 3/46 (2013.01); C10G 3/48 (2013.01); C10G 3/50 (2013.01); C10G 45/00 (2013.01); C10G 47/00 (2013.01); C10G 65/12 (2013.01); C10G 2300/4081 (2013.01); Y02P 30/20 (2015.11);
Abstract

A process for the production of hydrocarbon products from a feed comprising at least one non-pre-treated bio-oil, comprising a first step for hydroreforming in the presence of hydrogen and a hydroreforming catalyst, used alone or as a mixture, to obtain at least one liquid effluent comprising at least one aqueous phase and at least one organic phase, a second step in which at least a portion of the organic phase of the effluent obtained from the first hydroreforming step is recycled to the first hydroreforming step with a recycle ratio equal to the ratio of the mass flow rate of said organic phase to the mass flow rate of the non-pre-treated bio-oil in the range 0.05 to 2 and in which the hydrocarbon effluent obtained from the hydrotreatment and/or hydrocracking step is not recycled to said first hydroreforming step.


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