The present work focuses on the transfer and reaction phenomenon in a catal
yst pellet for Fischer-Tropsch synthesis. It is considered that the pores o
f catalyst pellets are filled with liquid wax under Fischer-Tropsch synthes
is conditions. The reactants in the bulk gas phase dissolve in the wax at t
he external surface of the pellet, and the dissolved components diffuse thr
ough the wax inside the pellet and react on the internal surface of the pel
let. The thermodynamic equilibrium between the gases in the bulk and the li
quid wax in the pores is correlated by a modified SRK equation of sate (MSR
K EOS). On the basis of the phenomena observed from experiments, a comprehe
nsive pellet model is suggested for catalyst design simulation, in which de
tailed Fischer-Tropsch mechanistic kinetics is properly imbedded. The react
ion and diffusion interaction in a catalyst pellet and its effect on the pr
oduct selectivity are further investigated. The potential of using eggshell
-type catalyst pellets is explored as a means of decoupling the severe tran
sport restriction and, hence, enhancing the overall selectivity of desired
products.