THE ROLE OF PELLET THERMAL STABILITY IN REACTOR DESIGN FOR HETEROGENEOUSLY CATALYSED CHEMICAL REACTIONS

Abstract-For exothermic fluid-phase reactions, a reactor which is cooled at the wall can exhibit multipli-city or parametric sensitivity _ Moreover, for heterogeneously catalyaed exothermic fluid-phase reactions, each of the catalytically active pellets in the reactor can exhibit multiplicity. Both forms of multiplicity can lead to thermal instability and as such have to he taken into account in reactor design. Here the effect of both instabilities is quantiiied. To this end, simple first-order kinetics are assumed, and intraparticle resistances and reactor and particle dynamic are not considered. A one-dimensional model, consisting of microscale mass and heat balances, is chosen to describe the reactor. It is assumed that the fluid inlet temperature equals the coolant temperature. The pellet scale model is a combined mass and heat balance for the pellet and it assumes that the Chilton-Colburn analogy holds. For its incorporation in the reactor model it is assumed that for every individual pellet heat removal to neighbouring pellets via the mutual contact spots is negligible as compared to the heat transferred to the surrounding fluid. Consequently every pellet is isolated from its neighbours. In the thermally most critical region, i.e. the hot-spot region, reactor stability is determined by three parameter groups: a dimensionless adiabatic temperature rise, an Arrhenius number or dimensionless activation temperature and the ratio of the number of heat transfer units to the number of reaction units. For pellet multiplicity, a fourth parameter group becomes sign&ant in addition