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Titanium Silicalite Catalyst in a Polymer Matrix for the Co-Production of Catechol and Hydroquinone

机译:聚合物基体中的钛硅沸石催化剂用于联产邻苯二酚和对苯二酚

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摘要

A method for synthesizing new catalytical systems based on titanium silicalite (TS-1) is proposed for the liquid phase oxidation of phenol by hydrogen peroxide, allowing in turn a continuous instead of cyclical process with a yield of 90-92% on hydroquinone and catechol (1: 1) with the intermediate separation of vaporous catalyst-titanum silicalite. The method is based on encapsulating TS-1 in a polymeric matrix (polypropylene, polyethylene, polystyrene, or their copolymers). The nature of the polymeric matrix's effects on the catalytical properties of the system is shown using TS-1/polypropylene and TS-1/polystyrene sytems as examples. The catalytical properties of TS-1/polypropylene and TS-1/polystyrene systems with features of an industrial catalyst (EniChem) are compared. Use of the TS-1/polypropylene catalytical system allows us to improve the performance of current technologies and considerably lower energy consumption.
机译:提出了一种基于钛硅沸石(TS-1)的新型催化体系的合成方法,用于过氧化氢液相氧化苯酚,从而允许连续而不是循环过程,对苯二酚和邻苯二酚的收率为90-92%。 (1:1)与中间气态催化剂-钛硅沸石的分离。该方法基于将TS-1封装在聚合物基质(聚丙烯,聚乙烯,聚苯乙烯或它们的共聚物)中。以TS-1 /聚丙烯和TS-1 /聚苯乙烯体系为例,说明了聚合物基质对体系催化性能的影响。比较了具有工业催化剂(EniChem)特性的TS-1 /聚丙烯和TS-1 /聚苯乙烯体系的催化性能。 TS-1 /聚丙烯催化系统的使用使我们能够改善当前技术的性能并显着降低能耗。

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