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:
Nov. 01, 2022

Filed:

Dec. 07, 2018
Applicant:

Ifp Energies Nouvelles, Rueil-Malmaison, FR;

Inventors:

Joao Marques, Chasse sur Rhone, FR;

Matthieu Dreillard, Lyons, FR;

Frederic Feugnet, Lyons, FR;

Jean-Francois Le Coz, Saint Germain en Laye, FR;

Assignee:

IFP ENERGIES NOUVELLES, Rueil-Malmaison, FR;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 11/04 (2006.01); C10G 11/05 (2006.01); C10G 11/18 (2006.01); C10G 69/04 (2006.01); C10G 47/30 (2006.01); C10G 67/04 (2006.01); C10G 47/02 (2006.01);
U.S. Cl.
CPC ...
C10G 67/049 (2013.01); C10G 47/02 (2013.01); C10G 47/30 (2013.01); C10G 67/0463 (2013.01); C10G 69/04 (2013.01); C10G 2300/206 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/4018 (2013.01);
Abstract

The invention concerns a method for converting heavy hydrocarbon feedstocks of which at least 50% by weight boils at a temperature of at least 300° C., and in particular vacuum residues. The feedstocks are subjected to a first step a) of deep hydroconversion, optionally followed by a step b) of separating a light fraction, and a heavy residual fraction is obtained from step b) of which at least 80% by weight has a boiling temperature of at least 250° C. Said fraction from step b) or the effluent from step a) is then subjected to a second step c) of deep hydroconversion. The overall hourly space velocity for steps a) to c) is less than 0.1 h. The effluent from step c) is fractionated to separate a light fraction. The heavy fraction obtained, of which 80% by weight boils at a temperature of at least 300° C., is sent to a deasphalting step e). The deasphalted fraction DAO is then preferably converted in a step f) chosen from ebullated bed hydroconversion, fluidised bed catalytic cracking and fixed bed hydrocracking.


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