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Combined activity and stability studies, ideally following the evolution of the active site as a function of catalyst treatment in real time are recommended.
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The conditions of occurrence of the main adsorbed species, i.e. nitrites and nitrates, are studied semi-quantitatively as a function of catalyst pre-treatment and/or type of adsorbed NOx molecule.
Cobalt reducibility was relatively low in monometallic cobalt alumina-supported catalysts and decreased as a function of catalyst calcination temperature.
Decline in conversion due to catalyst fouling was measured as a function of catalyst sulphur content.
After training, the NN can map catalyst activity as a function of catalyst composition and parameters for catalyst preparation.
This depth increases significantly as a function of catalyst age.
A reaction-engineering model is presented, which describes catalyst performance as a function of the catalyst activity profile, the reaction kinetics, and the degree of catalyst deactivation.
CO2 catalytic hydrogenation activity is represented as a function of the catalyst composition and reaction condition.
Resulting catalysts were composed by CNF coaxially coated by Ni-decorated MoS2 slabs, with different lengths and stacking degrees as a function of the functionalisation treatment, as TEM study revealed.
The evolution of different surface species is monitored as a function of thermal treatments.
and X-ray diffraction (WAXS) using syncrotron radiation, as a function of temperature and thermal treatment.
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