A model is developed to predict the viscoelastic behavior of polyolefins produced in catalytic polymerization reactors. The approach is based on the solution of different sub‐models (e.g., a kinetic model, a single particle model, a macroscopic reactor model and a rheological model). From the calculated rheological curve, the polymer melt index is determined. The ability of the proposed model to predict the viscoelastic behavior of linear polymer melts quantitatively is examined for the operation of a catalytic olefin polymerization cascade‐loop reactor process. In addition, the transient rheological properties of polyolefins produced in a Ziegler‐Natta gas‐phase olefin polymerization fluidized‐bed reactor are calculated.
