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:
Apr. 27, 2021

Filed:

Dec. 23, 2013
Applicant:

Basf SE, Ludwigshafen, DE;

Inventors:

Stephan Schunk, Heidelberg, DE;

Andrian Milanov, Mannheim, DE;

Andreas Strasser, Neckarsteinach, DE;

Guido Wasserschaff, Neckargemuend, DE;

Thomas Roussiere, Mannheim, DE;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 23/83 (2006.01); B01J 23/78 (2006.01); C01B 3/26 (2006.01); C01B 3/40 (2006.01); B01J 37/08 (2006.01); B01J 35/00 (2006.01); B01J 23/00 (2006.01); B01J 35/02 (2006.01); B01J 35/10 (2006.01); B01J 37/00 (2006.01); B01J 37/02 (2006.01);
U.S. Cl.
CPC ...
B01J 23/83 (2013.01); B01J 23/002 (2013.01); B01J 23/78 (2013.01); B01J 35/002 (2013.01); B01J 35/0006 (2013.01); B01J 35/023 (2013.01); B01J 35/1009 (2013.01); B01J 35/1014 (2013.01); B01J 37/0027 (2013.01); B01J 37/0036 (2013.01); B01J 37/0072 (2013.01); B01J 37/0201 (2013.01); B01J 37/08 (2013.01); C01B 3/26 (2013.01); C01B 3/40 (2013.01); C01B 2203/0238 (2013.01); C01B 2203/1041 (2013.01); C01B 2203/1052 (2013.01); C01B 2203/1241 (2013.01); Y02A 50/20 (2018.01); Y02P 20/141 (2015.11); Y02P 20/52 (2015.11);
Abstract

A hexaaluminate-containing catalyst containing a hexaaluminate-containing phase which includes cobalt and at least one further element of La, Ba or Sr. The catalyst contains 2 to 15 mol % Co, 70 to 90 mol % Al, and 2 to 25 mol % of the further element of La, Ba or Sr. In addition to the hexaaluminate-containing phase, the catalyst can include 0 to 50% by weight of an oxidic secondary phase. The process of preparing the catalyst includes contacting an aluminum oxide source with cobalt species and at least with an element from the group of La, Ba and Sr. The molded and dried material is preferably calcined at a temperature greater than or equal to 800° C. In the reforming process for reacting hydrocarbons in the presence of CO, the catalyst is used at a process temperature of greater than 700° C., with the process pressure being greater than 5 bar.


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