BrazilRio de JCUEUO-21945-970 -RJ Bulk styrene homopolymerization in cylindrical molds was studied in order to simulate the reactive injection process when the reaction kinetics was much slower than the filling process. Mathematical models were built and implemented, allowjng the analysis of certain kinetic phenomena, such as the gel-effect, and the relevance of natural convection. Based on a detailed kinetic mechanism, the polymer properties (average molecular weight and polydispersity) and monomer conversion were calculated as functions of spatial coordinates and time. The results obtained show that polymer properties and monomer conversion may be very heterogeneous inside the cylindrical mold, although insensitive to variations of the diffusion coefficient, so that defects are expected to appear as a consequence of the heterogeneity of polymer properties inside the mold. Experiments confirmed the simulation results. Simulations indicate that heterogeneities may be expected to increase when the reaction rates are one order of magnitude higher, as in acrylic acid polymerizations. Gogos (2) and Lord and Williams (3) developed models for simple and arbitrary plane geometries, using Hele-Shaw approximations. Nunn and Fenner (41, Hieber and Shen (5) and Richardson and Lekakou (61, using generalized Hele-Shaw flows, studied spherical and cylindrical geometries . Hayes et aL (7) solved the complete 2D-Navier-Stokes equation. They also included reaction and fountain-flow phenomena in their model, so that this paper may be regarded as a landmark in the study of RIM. Lo et aL (8,9) developed a very detailed 2D/3D model for RIM, but their interface tracking technique was very limited. Peebles and Compio (10) proved that simplified models lead to accurate results and are fast enough to be useful for control systems. In the last few years, there have been many studies about the steps that come after the filling of the mold, specially the cure. An interesting work in this area was presented by Kamal(l1).None of these works, however, discusses the influence of diffusion or natural convection in RIM processes mostly because reactions are assumed to occur in a very viscous polymer phase. Broyer and