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. 25, 2014

Filed:

Mar. 28, 2008
Applicants:

Fabrice Giroudiere, Orlienas, FR;

Christophe Boyer, Charly, FR;

Inventors:

Fabrice Giroudiere, Orlienas, FR;

Christophe Boyer, Charly, FR;

Assignee:

IFP Energies Nouvelles, Rueil Malmaison Cedex, FR;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C01B 3/02 (2006.01); C01B 3/22 (2006.01); C01B 3/24 (2006.01); C01B 3/48 (2006.01); C01B 3/56 (2006.01); C01B 3/32 (2006.01); C01B 3/38 (2006.01);
U.S. Cl.
CPC ...
C01B 3/323 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/0833 (2013.01); C01B 3/48 (2013.01); C01B 2203/0883 (2013.01); C01B 2203/0894 (2013.01); C01B 2203/042 (2013.01); C01B 2203/0244 (2013.01); C01B 2203/025 (2013.01); C01B 2203/80 (2013.01); C01B 2203/0811 (2013.01); C01B 2203/0877 (2013.01); C01B 2203/1229 (2013.01); C01B 2203/0866 (2013.01); C01B 2203/0888 (2013.01); C01B 3/56 (2013.01); C01B 2203/148 (2013.01); C01B 2203/1294 (2013.01); C01B 2203/1614 (2013.01); C01B 2203/047 (2013.01); C01B 2203/1288 (2013.01); C01B 2203/1235 (2013.01); C01B 2203/127 (2013.01); C01B 2203/0205 (2013.01); C01B 3/382 (2013.01); C01B 2203/066 (2013.01); C01B 2203/0405 (2013.01); C01B 2203/146 (2013.01);
Abstract

A process for the production of highly thermally-integrated hydrogen by reforming a hydrocarbon feedstock wherein a stream of air or water, whose temperature is less by at least 200° C. than the combustion temperature inside a burner, is mixed with the effluent that is obtained from said burner, so as to reduce the temperature of this effluent to less than 725° C.; the mixture obtained is used to superheat at least one stream of water vapor and/or hydrocarbon feedstock in gaseous form, whereby said stream that is thus superheated by indirect heat exchange is injected directly into a reforming reactor where it is used as a fuel; and the second heat exchanger and is used to totally evaporate a stream of liquid water and/or hydrocarbon feedstock.


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