The catalytic hydrogenation of ethylene on Pt catalysts was simulated
by a Monte Carlo model. Elementary events such as adsorption, diffusio
n, and desorption of the species involved (hydrogen, ethylene, and eth
ane) and reaction on the surface were considered. Based on comparison
between experimental and calculated data no distinction has to be made
between competitive and noncompetitive hydrogen adsorption sites nor
has adsorbed hydrogen activation to be taken into consideration. Howev
er, steric hindrance caused by adsorbed ethylene and ethane has been i
ncluded in the model. Not only was the basic physical and chemical beh
avior reproduced by this very simple model, but also important experim
ental findings such as the trend of the turnover frequency versus hydr
ogen pressure (P-H2) and the magnitudes of reaction orders for hydroge
n and ethylene. In addition this model can predict some aspects of hyd
rocarbon hydrogenation not investigated experimentally so far. (C) 199
6 Academic Press, Inc.