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Updated: May 13, 2026

Ethylene Polymerizations Using Parallel Pressure Reactors and a Kinetic Analysis of Chain Transfer Polymerization
Published on: November 27, 2015
Site count: is a high-pressure quenched-flow reactor suitable for kinetic studies of molecular catalysts in ethylene
Maria M Ranieri1, Jean-Pierre Broyer, Francesco Cutillo
1Université de Lyon, CPE Lyon, CNRS UMR 5265 Laboratoire de Chimie, Catalyse, Polymères et Procédés (C2P2), Bât. 308 F, B.P. 2077, 43 Bd du 11 Nov. 1918, 69616 Villeurbanne cedex, France.
Abstract:
Understanding the kinetics of olefin polymerization with Ziegler-Natta and related catalysts means identifying the main kinetic parameters such as k(p) and concentration of active sites. The high-pressure quenched-flow technique could be an absolute method for counting active sites and for activation studies of molecular catalysts. A kinetic study of metallocene catalysts and a phenoxy-imine titanium catalyst in the first instants of polymerization is presented in this paper.
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