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. 12, 2019

Filed:

Dec. 01, 2015
Applicants:

Ifp Energies Nouvelles, Rueil-Malmaison, FR;

Total Raffinage Chimie, Courbevoie, FR;

Inventors:

Florent Guillou, Ternay, FR;

Beatrice Fischer, Lyons, FR;

Tiago Sozinho, Feyzin, FR;

Ann Cloupet, Longes, FR;

Stephane Bertholin, Chaponost, FR;

Mahdi Yazdanpanah, Le Havre, FR;

Hélène Stainton, Lyons, FR;

Assignees:

IFP ENERGIES NOUVELLES, Rueil-Malmaison, FR;

TOTAL RAFFINAGE CHIMIE, Courbevoie, FR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F23D 3/40 (2006.01); F23C 10/01 (2006.01); B01J 8/24 (2006.01); F23C 10/00 (2006.01); F23C 10/20 (2006.01); B01J 8/06 (2006.01); C01B 3/40 (2006.01); F23C 10/04 (2006.01); F23C 10/22 (2006.01);
U.S. Cl.
CPC ...
F23C 10/01 (2013.01); B01J 8/065 (2013.01); B01J 8/067 (2013.01); B01J 8/24 (2013.01); C01B 3/40 (2013.01); F23C 10/005 (2013.01); F23C 10/04 (2013.01); F23C 10/20 (2013.01); F23C 10/22 (2013.01); B01J 2208/00495 (2013.01); B01J 2208/00504 (2013.01); B01J 2208/00911 (2013.01); B01J 2208/065 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0238 (2013.01); C01B 2203/0822 (2013.01); C01B 2203/1058 (2013.01); C01B 2203/1241 (2013.01); F23C 2900/99008 (2013.01); Y02E 20/346 (2013.01);
Abstract

The invention relates to a plant and to a method for chemical looping oxidation-reduction combustion of a gaseous hydrocarbon feed, for example natural gas essentially containing methane. According to the invention, catalytic pre-reforming of the feed is performed in a pre-reforming zone comprising a fixed reforming catalyst, while benefiting from a heat transfer between the reduction or oxidation zone of the chemical loop and the pre-reforming zone adjoining the reduction or oxidation zone. Pre-reforming zone () and oxidation zone () or pre-reforming zone () and reduction zone () are thus thermally integrated within the same reactor () while being separated by at least one thermally conductive separation wall ().


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