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On the production of polyolefins with bimodal molecular weight and copolymer composition distributions in catalytic gas-phase fluidized-bed reactors

机译:催化气相流化床反应器中双峰分子量和共聚物组成分布的聚烯烃的生产

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摘要

A comprehensive mathematical model is developed for the dynamic calculation of the molecular distributed properties (i.e. MWD and CCD) in a gas-phase, catalytic, ethylene-1-butene copolymerization, FBR, taking into account the various kinetic, micro- and macroscopic phenomena in the reactor. The effects of the two single-site catalyst mass fractions and reactor operating conditions on the production of polyolefins with 'tailor-made' bimodal molecular properties are investigated. It is shown that PE grades with either a bimodal MWD or CCD can be produced in a single FBR, using a mixture of two single-site catalysts under properly selected operating conditions.
机译:考虑到各种动力学,微观和宏观现象,开发了用于数学计算气相,催化,乙烯-1-丁烯共聚,FBR中分子分布特性(即MWD和CCD)的综合数学模型。在反应堆中研究了两个单中心催化剂的质量分数和反应器操作条件对具有“量身定制的”双峰分子性质的聚烯烃生产的影响。结果表明,在适当选择的操作条件下,使用两种单中心催化剂的混合物,可以在单个FBR中生产具有双峰MWD或CCD的PE牌号。

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