OP-II-3

PL-1− braking up complex process model to simpler hierarchically connectedlevels, and studying every level separately,− emphasizing non-linear phenomena in every level,− examining process stability and parametric sensitivity,− applying mathematical methods for reactor process optimization,− examining reactor aerodynamics.In this lecture we will assess how the catalytic reactor design methodology hasevolved since 1960 s . The content of the presentation will be based on literaturereview including recent results obtained by our former colleagues in BoreskovInstitute of Catalysis.Most of the examples will be related to gas-phase fixed-bed reactor includingtubular reactors for processes of partial oxidation, adiabatic-bed reactors forexothermic reversible processes, and unsteady-state reactors for air pollution control.Intensification of the existing and development of new processes will be discussed.References[1]. M.G. Slin’ko, Theor. Found. Chem. Eng., 2007, Vol. 41, pp. 13-29.8