Temperature effect on the kinetic profile of Ziegler-Natta catalyst in propene polymerization

Temperature effect on the kinetic profile of Ziegler-Natta catalyst in propene polymerization

WoS Article

Propene polymerization kinetic profiles with a diether-based Ziegler-Natta MgCl2-supported catalyst were investigated in a stainless-steel batch reactor. The initial 10 min period characterizes various temperature levels with a constant volume of liquid propene. The lowest temperature level corresponds to the usual prepolymerization temperature (10 degrees C), and the highest level corresponds to the usual main polymerization temperature (70 degrees C). The effects of the starting temperature levels were evaluated through polymerization kinetic patterns computed namely from the second polymerization period carried out at 70 degrees C for the next 90 min. Based on the heat transfer data, the kinetic profiles were fitted to suitable semi-empirical equations derived from fundamental kinetic approaches using the first and second orders of the catalyst active sites decay. Both approaches adequately describe the dependence of the initial activities and deceleration constants on the temperature during the initial period.

Propene polymerization kinetic profiles with a diether-based Ziegler-Natta MgCl2-supported catalyst were investigated in a stainless-steel batch reactor. The initial 10 min period characterizes various temperature levels with a constant volume of liquid propene. The lowest temperature level corresponds to the usual prepolymerization temperature (10 degrees C), and the highest level corresponds to the usual main polymerization temperature (70 degrees C). The effects of the starting temperature levels were evaluated through polymerization kinetic patterns computed namely from the second polymerization period carried out at 70 degrees C for the next 90 min. Based on the heat transfer data, the kinetic profiles were fitted to suitable semi-empirical equations derived from fundamental kinetic approaches using the first and second orders of the catalyst active sites decay. Both approaches adequately describe the dependence of the initial activities and deceleration constants on the temperature during the initial period.

Propene polymerization; Ziegler-Natta catalyst; Polymerization kinetics; Effect of temperature; Batch reactor; Second order of deceleration

Propene polymerization; Ziegler-Natta catalyst; Polymerization kinetics; Effect of temperature; Batch reactor; Second order of deceleration

KOLOMAZNÍK, V.; CEJPEK, I.; SKOUMAL. M.

2025

10.09.2024

SPringer Nature

CHAM

2585-7290

CHEMICAL PAPERS

78

15

Slovak Republic

8397

8408

12

https://link.springer.com/article/10.1007/s11696-024-03679-w

http://hdl.handle.net/11012/250716

s11696-024-03679-w