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:
Feb. 09, 2016

Filed:

Nov. 24, 2014
Applicants:

Siemens Aktiengesellschaft, München, DE;

Clariant International Ltd., Muttenz, CH;

Inventors:

Yeping Cai, Louisville, KY (US);

William M. Faris, Louisville, KY (US);

Christian Görsch, Leipzig, DE;

Frank Hannemann, Freiberg, DE;

Doris Klostermann, Freiberg, DE;

Robert Marx, München, DE;

Manfred Schingnitz, Freiburg, DE;

Justin Wang, Louisville, KY (US);

Ling Xu, München, DE;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C01B 3/38 (2006.01); B01J 8/18 (2006.01); B01J 8/00 (2006.01); B01J 8/02 (2006.01); C01B 3/16 (2006.01);
U.S. Cl.
CPC ...
B01J 8/18 (2013.01); B01J 8/0005 (2013.01); B01J 8/02 (2013.01); B01J 8/0285 (2013.01); C01B 3/16 (2013.01); B01J 2208/027 (2013.01); C01B 2203/0288 (2013.01); C01B 2203/0877 (2013.01); C01B 2203/0883 (2013.01);
Abstract

A technology for producing synthesis gas from crude gas from various gasification processes for solid or liquid fuels. To limit the temperatures in a subsequent strongly exothermic CO shift reaction to adjust the H/CO ratio, the crude gas which has been freed of dust flows through two shift reactors arranged in series. The first reactor has a specific reaction-kinetically limited catalyst and the second reactor has a conventional sour gas catalyst. The specific catalyst used in the first reactor limits the exothermic shift reaction to such an extent that the reaction temperatures in the first and second reactors remain so low to avoid thermal damage to the catalysts even without introduction of external steam, and the desired gas composition is achieved.


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