2013
DOI: 10.1002/aic.14204
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Synthesis of ethylene/1‐octene copolymers with controlled block structures by semibatch living copolymerization

Abstract: A kinetic model was developed for the living copolymerization of ethylene/1-octene using the fluorinated FI-Ti catalyst system, bis[N-(3-methylsalicylidene)-2,3,4,5,6-pentafluoroanilinato] TiCl 2 /dried methylaluminoxane is presented. The model was first validated by batch polymerization experiments. Kinetic parameters were estimated from the model correlations with online ethylene consumption rates and end-of-batch copolymer molecular weight. The model was then used to calculate the microstructural properties… Show more

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Cited by 24 publications
(36 citation statements)
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“…The reaction mechanism for living ethylene/α‐olefin copolymerization consists of four elementary reactions: initiation, propagation, chain transfer to cocatalyst, and deactivation (Table ) . We adopted the following modeling assumptions: (1) polymerization takes place in a semibatch well‐mixed reactor, where solvent, catalysts, and cocatalysts are fed into the reactor at the beginning of the polymerization, while ethylene is fed continuously to keep the pressure constant throughout the polymerization, and (2) all reaction rate constants are independent of chain length.…”
Section: Dynamic Monte Carlo Simulation Of Living Ethylene/α‐olefin Cmentioning
confidence: 99%
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“…The reaction mechanism for living ethylene/α‐olefin copolymerization consists of four elementary reactions: initiation, propagation, chain transfer to cocatalyst, and deactivation (Table ) . We adopted the following modeling assumptions: (1) polymerization takes place in a semibatch well‐mixed reactor, where solvent, catalysts, and cocatalysts are fed into the reactor at the beginning of the polymerization, while ethylene is fed continuously to keep the pressure constant throughout the polymerization, and (2) all reaction rate constants are independent of chain length.…”
Section: Dynamic Monte Carlo Simulation Of Living Ethylene/α‐olefin Cmentioning
confidence: 99%
“…During 0– t 1 min, f 2 = f 2,stage 1 to start making living random copolymer chains; the comonomer fraction in the reactor is increased to f 2,stage 2 from t 1 to t 2 min to produce diblock chains, and to f 2,stage 3 from t 2 to t 3 min to make triblock chains. Comonomer fractions in each stage were considered to be approximately constant as reported by the experiment performed with three injection steps and later verified by the method of moment . The chain segments produced during the first, second, and third stages will be referred to as B 1 (thick solid line), B 2 (dotted thin line), and B 3 (thin solid line), respectively.…”
Section: Dynamic Monte Carlo Simulation Of Living Ethylene/α‐olefin Cmentioning
confidence: 99%
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“…The prepolymerization temperature greatly influenced the polymerization reaction rate constant and half-life of the initiator [20][21], which would greatly influence the distribution of the chain segment of the copolymer and the resulting properties of the copolymer foam [22]. The distribution of the chain segment and the conversion ratio of the monomer were also greatly influenced by feeding method of the monomer, which would reduce the implosion possibility of bulk polymerization [23][24][25][26]. Different feeding methods were employed to adjust the conversion ratio of the monomer and further adjust the composition of the copolymer in this study.…”
Section: Introductionmentioning
confidence: 99%