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:
Dec. 03, 2019

Filed:

Dec. 01, 2015
Applicants:

Ifp Energies Nouvelles, Rueil-Malmaison, FR;

Total Raffinage Chimie, Courbevoie, FR;

Inventors:

Tiago Sozinho, Feyzin, FR;

Mahdi Yazdanpanah, Le Havre, FR;

Florent Guillou, Ternay, FR;

Ann Cloupet, Longes, FR;

Stephane Bertholin, Chaponost, FR;

Hélène Stainton, Lyons, FR;

Assignees:

IFP ENERGIES NOUVELLES, Rueil-Malmaison, FR;

TOTAL RAFFINAGE CHIME, Courbevoie, FR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 3/44 (2006.01); F23C 10/01 (2006.01); F23C 10/22 (2006.01); C01B 3/38 (2006.01); B01J 8/26 (2006.01); B01J 8/18 (2006.01); B01J 8/00 (2006.01);
U.S. Cl.
CPC ...
C01B 3/44 (2013.01); B01J 8/0055 (2013.01); B01J 8/1827 (2013.01); B01J 8/26 (2013.01); C01B 3/382 (2013.01); F23C 10/01 (2013.01); F23C 10/22 (2013.01); B01J 2208/00752 (2013.01); B01J 2208/00893 (2013.01); C01B 2203/025 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0238 (2013.01); C01B 2203/0255 (2013.01); C01B 2203/06 (2013.01); C01B 2203/1058 (2013.01); C01B 2203/1082 (2013.01); C01B 2203/1094 (2013.01); C01B 2203/1241 (2013.01); F23C 2900/99008 (2013.01); Y02E 20/346 (2013.01);
Abstract

The invention relates to a method and to a plant for chemical looping oxidation-reduction combustion (CLC) of a gaseous hydrocarbon feed, for example natural gas essentially containing methane. According to the invention, catalytic steam reforming of the feed is performed between two successive feed combustion steps on contact with an oxidation-reduction active mass in form of particles. The reforming catalyst is arranged in a fixed bed in an intermediate reforming zone () between the two reduction zones () where the two combustion steps are conducted.


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