Abstract

The process of coupled multicomponent diffusion and surface reaction is described by combining the Maxwell–Stefan (M–S) and Langmuir–Hinshelwood (L–H) formulations. Five different systems are investigated: epoxidation of ethene C2H4+12O2⇄C2H4O, oxidation of carbon monoxide CO+12O2⇄CO2, hydrogenation of ethene H2+C2H4⇄C2H6, CO methanation CO+3H2⇄CH4+H2O, and chemical vapor deposition WF6+2SiH4→W(s)+2SiHF3+3H2. For isothermal, isobaric operations under steady-state conditions, multiplicity of solutions are found for all five reaction systems. The origin of the multiplicities is traceable to the non-linear characteristics of the L–H kinetics. Application of the Prigogine principle of minimum entropy production indicates that the low-conversion steady-state is the stable one that can be realized in practice. The reported results have important consequences for modelling and design of chemical vapor deposition processes and micro-channel reaction devices consisting of thin catalyst coatings on the walls.

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