The kinetics of propylene polymerization with Et(H(4)Ind)(2)ZrCl2/meth
ylalumoxane (MAO) catalysts have been investigated at 0-50 degrees C a
nd 1 atm of propylene pressure. The effects of polymerization temperat
ure, catalyst concentration, and catalyst/cocatalyst mole ratio on the
catalyst activity and on the properties of the polypropylene products
were studied. By assuming the coexistence of two dynamic equilibria b
etween catalytically active species and two inactive species, which ar
e the products of zirconocene dimerization and excessive zirconocene-M
AO complexation, a kinetic model has been developed. This model could
satisfactorily explain most of experimental results.