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. 29, 2018

Filed:

Nov. 27, 2014
Applicant:

Ifp Energies Nouvelles, Rueil-Malmaison, FR;

Inventors:

Jerome Majcher, Lyons, FR;

Isabelle Merdrignac, Chaponnay, FR;

Frederic Feugnet, Lyons, FR;

Assignee:

IFP Energies nouvelles, Rueil-Malmaison, FR;

Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 67/00 (2006.01); C10G 67/04 (2006.01); C10G 45/08 (2006.01); C10G 45/20 (2006.01); C10G 47/00 (2006.01); C10G 49/04 (2006.01); C10G 49/16 (2006.01); C10G 53/06 (2006.01); C10G 67/14 (2006.01); C10G 21/00 (2006.01); C10G 21/14 (2006.01);
U.S. Cl.
CPC ...
C10G 67/0463 (2013.01); C10G 21/003 (2013.01); C10G 21/14 (2013.01); C10G 45/08 (2013.01); C10G 45/20 (2013.01); C10G 47/00 (2013.01); C10G 49/04 (2013.01); C10G 49/16 (2013.01); C10G 53/06 (2013.01); C10G 67/00 (2013.01); C10G 67/14 (2013.01); C10G 2300/1014 (2013.01); C10G 2300/1074 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/202 (2013.01); C10G 2300/205 (2013.01); C10G 2300/206 (2013.01); Y02P 30/20 (2015.11);
Abstract

Process for converting a heavy hydrocarbon feedstock with initial boiling point of at least 300° C. comprising: a) hydroconverting at least part of said feedstock; b) separating the effluent from stage a) to obtain light and heavy liquid fractions; c) at least two stages of deasphalting in series at least part of the heavy liquid fraction originating from stage b), allowing to separate at least one fraction of asphalt, at least one fraction of heavy deasphalted oil (heavy DAO) and at least one fraction of light deasphalted oil (light DAO), at least one deasphalting stage being carried out using a mixture of at least one polar solvent and at least one apolar solvent, said deasphalting stages being under subcritical conditions of the mixture of solvents; d) recycling at least part of said heavy deasphalted oil cut from stage c) upstream of hydroconverting a) and/or of the inlet of separating b).


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