For supported niobia and tantala catalysts, as well as to be expected for supported dubnia catalysts, the active surface sites were exclusively acidic sites.
For supported NPs, this emission will be suppressed since the substrate will prevent ejection.
For supported nickel catalysts, large packed-bed reactors may be optimal, while micro-reactors in parallel may be best for supported platinum catalysts.
For supported vanadia catalysts, the active surface sites were essentially redox sites, with the exception of supported V2O5/Al2O3 that also contained strong acidic sites.
For supported WO3/Al2O3, the surface WOx monolayer was more active than the crystalline WO3 phases and, consequently, the TOF decreased with increasing surface W/nm2 density.
For supported clades, bayesian posterior probabilities and ML bootstrap are indicated at nodes, respectively.
R 2 variance explained; values of standardized path coefficient at p < .001 in parenthesis; solid line for supported hypothesis and dotted line for non-supported hypothesis.
To determine the crystallinity nature of fly ash-supported CaO catalysts, X-ray diffraction (XRD) patterns for supported catalysts samples were analyzed using Cu-Kα procedure.
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