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:
Jul. 12, 2016

Filed:

Oct. 11, 2011
Applicants:

Patrick Leroy, Saint Vigor d'Ymonville, FR;

Marc Bories, Saint Jouin de Bruneval, FR;

Michaël Echard, Montivilliers, FR;

Inventors:

Patrick Leroy, Saint Vigor d'Ymonville, FR;

Marc Bories, Saint Jouin de Bruneval, FR;

Michaël Echard, Montivilliers, FR;

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 4/06 (2006.01); B01J 38/06 (2006.01); C10G 11/18 (2006.01); C10G 51/02 (2006.01); B01J 38/14 (2006.01);
U.S. Cl.
CPC ...
C07C 4/06 (2013.01); B01J 38/06 (2013.01); B01J 38/14 (2013.01); C10G 11/18 (2013.01); C10G 11/182 (2013.01); C10G 51/026 (2013.01); C10G 2300/1011 (2013.01); C10G 2300/301 (2013.01); C10G 2300/4081 (2013.01); C10G 2300/4093 (2013.01); C10G 2300/708 (2013.01); C10G 2300/807 (2013.01); C10G 2400/20 (2013.01);
Abstract

The present invention relates to a multi staged cracking and stripping process that can be used in a fluidized-bed catalytic cracking process or FCC (fluidized catalytic cracking) process for maximizing the production of olefins, that is to say of Cand Colefins, in particular propylene and distillates. One subject of the present invention is therefore a multi-staged process for cracking and stripping a fluidized mixture of hydrocarbons and of coked catalyst particles, integrated into a conventional fluidized-bed catalytic cracking process comprising at least one cracking step and one stripping step after separation of the particles of coked catalyst from the cracked effluent during the disengaging/stripping step, characterized in that it comprises at least two steps of cracking at least one hydrocarbonaceous fluid over the separated coked catalyst particles followed by at least two steps of stripping these particles, each cracking step preceding a stripping step. The present invention also relates to a separating and stripping device that implements this process.


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