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Selective hydrogenation of acetylene in ethylene rich feed streams at high pressure over ligand modified Pd/TiO2

机译:在配体修饰的PD/TIO2上,乙二烯富含进料流中乙炔的选择性氢化

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The selective hydrogenation of acetylene from ethylene rich streams was conducted at high pressure and in the presence of CO over two 1 wt% loaded Pd/TiO2 catalysts with differing dispersions. Although, the more poorly dispersed sample did not result in high acetylene conversion only a small proportion of the total available ethylene was hydrogenated to ethane. The more highly dispersed sample was able to remove acetylene to a level below the detection limit but this was at the expense of significant proportion (ca. 30%) of the available ethylene. Modification of the catalysts by exposure to triphenyl phosphine or diphenyl sulfide and subsequent reduction at 393 K led to improved performance with increased conversion of acetylene and decreased propensity to hydrogenate ethylene resulting in an overall net gain in ethylene. The higher dispersed sample which had been ligand modified provided the best results overall and in particular for the diphenyl sulfide treated sample which was able to completely eliminate acetylene and still obtain a net gain in ethylene. The differences observed are thought to be due to the creation of appropriate active ensembles of Pd atoms which are able to accommodate acetylene but have limited ability to adsorb ethylene. Sub-surface hydrogen formation was suppressed, but not eliminated, by exposure to modifier.
机译:从富含乙烯的流中对乙炔的选择性氢化是在高压下进行的,并且在两个1 wt%加载的PD/TIO2催化剂的CO存在下,具有不同的分散体。虽然,分散较差的样品并未导致乙炔转化率很高,只有一小部分可用乙烯被氢化为乙烷。较高的样品能够将乙炔水平降至低于检测极限的水平,但这是牺牲可用乙烯的显着比例(约30%)的代价。通过暴露于三苯基磷酸或二苯基硫化物以及随后在393 K时的降低来修饰催化剂,从而改善了性能,随着乙炔的转化和氢化乙烯的倾向降低,导致乙烯的总净增益。经过配体修饰的较高的分散样品总体上提供了最佳的结果,尤其是二苯基硫化物处理的样品,该样品能够完全消除乙炔并仍然获得乙烯的净增益。观察到的差异被认为是由于创建适当的PD原子的主动集合,这些PD原子能够容纳乙炔,但吸附乙烯的能力有限。通过暴露于修饰符,抑制了地下氢的形成,但没有消除。

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