Effect of Prepolymerization on the Kinetics of Ethylene Polymerization and Ethylene/1-Hexene Copolymerization with a Ziegler-Natta Catalyst in Slurry Reactors

被引:9
|
作者
Chen, Keran [1 ]
Liu, Boping [1 ]
Soares, Joao B. P. [2 ]
机构
[1] East China Univ Sci & Technol, State Key Lab Chem Engn, Meilong Rd 130, Shanghai 200237, Peoples R China
[2] Univ Alberta, Dept Chem & Mat Engn, Edmonton, AB T6G 1H9, Canada
关键词
polyethylene; polymerization kinetics; polyolefin reaction engineering; prepolymerization; Ziegler-Natta; ACTIVE-CENTER DISTRIBUTION; MASS-TRANSFER RESISTANCE; PROPYLENE POLYMERIZATION; GAS-PHASE; HETEROGENEOUS CATALYSIS; OLEFIN POLYMERIZATION; MONOMER CONCENTRATION; LIQUID PROPYLENE; HYDROGEN; TEMPERATURE;
D O I
10.1002/mren.201500066
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effect of prepolymerization on ethylene homopolymerization and ethylene/1-hexene copolymerization with a commercial TiCl4/MgCl2 catalyst was investigated and the apparent homo- and copolymerization rate constants were estimated by varying polymerization temperature, pressure, time, and 1-hexene/ethylene molar ratio during the prepolymerization. The apparent rate constants for activation, propagation, and deactivation depend on the prepolymerization conditions, showing that the prepolymerization stage strongly regulates the behavior of the catalyst in the main polymerization. Interestingly, the surface morphology of the prepolymer particles correlates to and explains these changes in polymerization kinetics behavior.
引用
收藏
页码:463 / 478
页数:16
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