Hendrik
Düdder
a,
Kevin
Kähler
a,
Bastian
Krause
b,
Katharina
Mette
c,
Stefanie
Kühl
c,
Malte
Behrens
c,
Viktor
Scherer
b and
Martin
Muhler
*a
aLaboratory of Industrial Chemistry, Ruhr-University Bochum, Bochum, Germany. E-mail: muhler@techem.rub.de
bLaboratory of Energy Plant Technology, Ruhr-University Bochum, Bochum, Germany
cDepartment of Inorganic Chemistry, Fritz-Haber-Institut der Max-Planck-Gesellschaft, Berlin, Germany
First published on 11th September 2014
Correction for ‘The role of carbonaceous deposits in the activity and stability of Ni-based catalysts applied in the dry reforming of methane’ by Hendrik Düdder et al., Catal. Sci. Technol., 2014, 4, 3317–3328.
Table 1 summarizes examples of catalyst activities in the DRM reported in the literature.14–22 For a better comparison, specific average reaction rates rCH4 were calculated for all catalysts according to eqn (2), where mcat is the catalyst mass and and
are the molar flows of methane at the entrance and the exhaust of the reactor, respectively.
The Royal Society of Chemistry apologises for these errors and any consequent inconvenience to authors and readers.
This journal is © The Royal Society of Chemistry 2014 |