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Long -chain branching in ethylene polymerization using combined metallocene catalyst systems.

机译:使用组合的茂金属催化剂体系在乙烯聚合中的长链支化。

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摘要

The development of homogeneous and supported metallocene catalysts has revolutionized the polyolefin industry. These single-site catalysts produce ethylene homo- and copolymers with properties that are different from the ones of traditional polyethylenes synthesized with free radical initiators or Ziegler-Natta catalysts. With the advent of monocyclopentadienyl metallocenes (constrained geometry catalysts, CGC), the production of polyolefins with long-chain branches became possible. These catalyst systems can produce polyethylenes with both excellent physical properties and improved melt behavior. The improved processability is believed to be the result of significant amounts of long-chain branching in the polymer.;The concept of combining two metallocene catalysts to manipulate long-chain branching (LCB) in ethylene polymerization was introduced. Using mathematical modeling the feasibility of the idea was investigated and the characteristics of an efficient system were predicted. Polymerization experiments were performed to evaluate the model predictions and to examine the effects of different reaction components on the microstructure of the synthesized polymer. Excellent agreement between experimental data and model predictions was observed. The structure of the branches in CGC polymerization systems was also investigated using a Monte-Carlo model.;The precipitation mechanism in Crystallization Analysis Fractionation (CRYSTAF) was investigated and a mechanism for the separation was proposed. Copolymer chains were simulated using a Monte-Carlo model and the precipitation was simulated according to the proposed mechanism. Good agreement between experimental and simulated CRYSTAF curves verifies the validity of the proposed fractionation mechanism.;A general model for the polymerization of vinylic monomers with free-radical initiators was developed. In this model transfer to polymer as the source of branching with the potential of gelation was considered. The results of this simulation provided information about the distribution of branching and time variations of average molecular weights as well as amounts and molecular weights of chains with different branching contents before, during, and after gelation.
机译:均相和负载型茂金属催化剂的发展彻底改变了聚烯烃工业。这些单中心催化剂生产的乙烯均聚物和共聚物的性能与传统的由自由基引发剂或齐格勒-纳塔催化剂合成的聚乙烯不同。随着单环戊二烯基茂金属(几何尺寸受限的催化剂,CGC)的出现,具有长链分支的聚烯烃的生产成为可能。这些催化剂体系可以生产具有优异的物理性能和改善的熔融行为的聚乙烯。认为加工性的改善是由于聚合物中大量长链支化的结果。引入了将两种茂金属催化剂组合以控制乙烯聚合中的长链支化(LCB)的概念。使用数学模型研究了该想法的可行性,并预测了有效系统的特征。进行聚合实验以评估模型预测并检查不同反应组分对合成聚合物的微观结构的影响。观察到实验数据和模型预测之间的极好的一致性。还使用蒙特卡洛模型研究了CGC聚合体系中支链的结构。;研究了结晶分析分馏(CRYSTAF)中的沉淀机理,并提出了分离机理。使用蒙特卡洛模型模拟共聚物链,并根据所提出的机理模拟沉淀。实验和模拟的CRYSTAF曲线之间的良好一致性验证了所提出的分馏机理的有效性。;建立了乙烯基单体与自由基引发剂聚合的通用模型。在该模型中,考虑了转移到聚合物作为支化的来源以及潜在的胶凝作用。该模拟的结果提供了关于凝胶化之前,之中和之后平均分子量的分支分布和时间变化以及具有不同分支含量的链的数量和分子量的信息。

著录项

  • 作者

    Beigzadeh, Daryoosh.;

  • 作者单位

    University of Waterloo (Canada).;

  • 授予单位 University of Waterloo (Canada).;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 2000
  • 页码 208 p.
  • 总页数 208
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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