Ni-based catalysts are the most widely used materials
to produce
H2 in large-scale methane steam reformers under stationary
conditions. For domestic applications such as fuel cells, H2 production involves the exposure of the catalysts to more dynamic
conditions due to the daily startup and shutdown operation mode, making
Ni-based catalysts susceptible to oxidation and deactivation. In this
context, we report a systematic investigation of the structural changes
occurring for monometallic Ni/MgAlO
x
and
bimetallic NiPt/MgAlO
x
catalysts during
methane steam reforming under transient conditions, comprising catalyst
activation, operation, and deactivation processes. Besides extensive
catalytic tests, the samples prepared by incipient wetness impregnation
were characterized by complementary methods, including N2-physisorption, X-ray diffraction, H2-temperature-programmed
reduction, and electron microscopy. Next, the structure of the Ni
and Pt species was monitored under reaction conditions using time
and spatially resolved in situ/operando X-ray absorption spectroscopy. The results obtained show that before
catalyst activation by H2-reduction, nickel diffuses into
the support lattice and forms mixed oxides with magnesium. In the
activated catalysts, Ni is present in the metallic state or alloyed
with Pt. A clear beneficial effect of the noble metal addition was
identified on both the activity and stability of the bimetallic NiPt/MgAlO
x
catalyst. In contrast, the pronounced oxidation
and reincorporation of Ni into the support lattice were observed for
the monometallic sample, and these catalyst deactivation effects are
hindered in the bimetallic Ni–Pt catalyst. Overall, the outcome
of our study not only helps in understanding the catalyst activation/deactivation
processes at an atomic level but also provides the basis for the rational
development of improved methane steam reforming catalysts.