Butadiene polymerization in the gas phase is modeled by a polymeric mu
ltilayer model. Intraparticle mass and heat transfer effects are studi
ed. The effects of catalyst size and diffusivity of butadiene on the r
adial profile of monomer concentration in polymeric particles and on t
he rate of particle growth are significant. Intraparticle temperature
gradients do appear to be negligible under normal reaction conditions.
External boundary layer heat effects are studied for various operatio
n conditions. The model predicts that there is no significant temperat
ure rise of the polymeric particles, even in the case of large catalys
t particles. The effect of deactivation of active sites on the rate of
particle growth is also studied. (C) 1997 John Wiley & Sons, Inc.