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:
Mar. 08, 2016

Filed:

Nov. 07, 2012
Applicants:

Holger Schlichting, Hofheim, DE;

Ulrich Wolf, Egelsbach, DE;

Sven Pohl, Frankfurt am Main, DE;

Dieter Ulber, Steinbach, DE;

Udo Zolnowski, Linden, DE;

Antonio Coscia, Hadamar, DE;

Julien Cances, Nantes, FR;

Frederic Camy-peyret, Paris, FR;

Fabrice Mathey, St-remy les chevreuse, FR;

Inventors:

Holger Schlichting, Hofheim, DE;

Ulrich Wolf, Egelsbach, DE;

Sven Pohl, Frankfurt am Main, DE;

Dieter Ulber, Steinbach, DE;

Udo Zolnowski, Linden, DE;

Antonio Coscia, Hadamar, DE;

Julien Cances, Nantes, FR;

Frederic Camy-Peyret, Paris, FR;

Fabrice Mathey, St-remy les chevreuse, FR;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C01B 3/38 (2006.01); B01J 8/06 (2006.01); B01J 8/00 (2006.01);
U.S. Cl.
CPC ...
B01J 8/062 (2013.01); B01J 8/0005 (2013.01); B01J 8/065 (2013.01); B01J 8/067 (2013.01); C01B 3/384 (2013.01); C01B 3/388 (2013.01); B01J 2208/0053 (2013.01); B01J 2208/00141 (2013.01); B01J 2208/027 (2013.01); B01J 2208/065 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0816 (2013.01); C01B 2203/0866 (2013.01); C01B 2203/0883 (2013.01); C01B 2203/1235 (2013.01);
Abstract

A reformer tube for producing synthesis gas by steam reforming of hydrocarbon-containing feed gases, preferably natural gas, includes one or more helically coiled heat exchanger tubes which are arranged within a catalyst bed of a reforming catalyst and are helically coiled over part of their length located within the catalyst bed and are otherwise straight are present, where the straight proportion of the heat exchanger tubes and/or the helix pitch of the helically coiled part alters within the catalyst bed and matching to requirements of the pressure drop, the heat exchange properties, and the corrosion resistance.


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