Literature correlations for the apparent wall heat transfer coefficient (h(w)) in fixed bed catalytic reactors are compared. At low to moderate values of the Reynolds number (Re), different correlations can produce estimates of the dimensionless wall Nusselt number (Nu(w) = h(w)d(p)/k(f)) that differ by an order of magnitude or more. Some correlations give Nu, as a function of Re only, others allow for the effects of tube-to-particle diameter ratio and particle and fluid thermal conductivities. The value of Nu, that is used in a simulation of a fixed bed catalytic reactor can have a strong effect on the predicted behavior. Two examples of fixed bed reactors are simulated and show that the more general correlations for Nu, are to be preferred.