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首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >High performance gas-phase ethylene polymerization metallocene catalyst investigation in a pilot-plant fluidized bed reactor (1) experimental analysis
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High performance gas-phase ethylene polymerization metallocene catalyst investigation in a pilot-plant fluidized bed reactor (1) experimental analysis

机译:高性能气相乙烯聚合茂金属催化剂在先导植物流化床反应器中进行(1)实验分析

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摘要

This work aims to explore the scaling up process of lab developed heterogeneous metallocene catalyst in a pilot plant scale fluidized bed reactor in comparison of benchmark catalyst producing polyethylene. The catalyst performance has been evaluated through copolymerization behaviors and polymerization kinetics. The produced polymers are analyzed in revealing the scale up effect of the catalyst. It was found that the catalyst particle size distribution shows very similar size distribution compared to the industrial catalyst and good particle morphology, which will benefit the gas phase fluidized bed operation. Compared to the benchmark HP-100, PME-18 shows better catalytic parameters in the ethylene/1-hexene polymerization behavior and reaction kinetics. The final product demonstrates very similar particle size distribution and polymer properties, which will obviously influence the product quality and production state. (C) 2018 Elsevier B.V. All rights reserved.
机译:该工作旨在探讨实验室在试验厂规模流化床反应器中开发的非均相茂金属催化剂的缩放过程,并在生产聚乙烯的基准催化剂的比较中。 通过共聚行为和聚合动力学评估催化剂性能。 分析产生的聚合物揭示催化剂的扩展效果。 结果发现,与工业催化剂和良好的颗粒形态相比,催化剂粒度分布显示非常相似的尺寸分布,其将有利于气相流化床操作。 与基准HP-100相比,PME-18在乙烯/ 1-己烯聚合行为和反应动力学中显示出更好的催化参数。 最终产品显示出非常相似的粒度分布和聚合物性能,这显然会影响产品质量和生产状态。 (c)2018 Elsevier B.v.保留所有权利。

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