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With the assumed chemical model, reaction is confined to a thin reaction zone.

One of the reasons to use the 4-NP to 4-AP reduction reaction as a model reaction is that the reaction progress can be followed directly by UV-visible spectrophotometry.

The model reaction is chosen to allow investigation of the position of chemical reactions (gas phase, surface, liquid phase) and the behavior of typical products (alcohols and aldehydes).

The oxidation of ethylene on supported Pt catalyst, that is employed here as a model reaction, is a complex reaction characterized by self-inhibition (expressed by Langmuir Hinshelwood kinetics), by strong activation energy and by strong thermal effects that lead to a wide domain of steady-state multiplicity.

The standard deviation of the observed conversion degree of the individually prepared single-bead catalysts in CO oxidation as model reaction is quantified to be in the range of 5 7%, while it is in the range of 3 6% for conventionally prepared catalysts.

Also, the effect of the catalyst load on the model reaction was studied.

To study the catalyst reusability, the model reaction was carried out using 0.015 g of Fe3O4/camphor.

Meanwhile, the model reaction was studied with 10 mol % of SnO2 NPs under various temperatures.

Accordingly, a model reaction was performed by using PNC4.0 as the photo-catalyst with a definite amount of reactants for 50 h.

The selected model reaction was performed over a 4 wt.% palladium/alumina catalyst using 30% (v/v) isopropanol/water solvent.

In the present study, the enzymatic esterification of dihydrocaffeic acid (DHCA) with 1- hexanol (Fig. 1) as a model reaction was carried out in ionic liquid [1-butyl-3-methylimidazoliumbis (trifluoromethylsulfonyl) imide].