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Preparation of MFI Zeolite Catalyst Supported on Silicalite Foam and Its Catalytic Property in the Cracking of n-Octane

机译:硅沸石泡沫负载的MFI沸石催化剂的制备及其在正辛烷裂解中的催化性能

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摘要

Foam-type MFI zeolite catalyst was prepared by dispersing fine(-0.2 murn)particles of MFI zeolite on sil-icalite foam.Catalytic cracking of n-octane was investigated over the foam-type catalyst and Delplot method was employed to interpret product compositions for deducing reaction mechanism.The Si/Al molar ratio of dispersed MFI zeolite was estimated 25 and its dispersed amount of silicalite foam was 25 wt%.Since the apparent density of the foam type catalyst was very low 0.11 gcentre dotcm~(-3),the catalyst loading amount could be varied from 0.02 g to 0.5 g without concerning pressure drop,providing a wide variance in the residence time of the reactants and products.The conversion and olefin yield in the catalytic cracking of n-octane increased with the catalyst loading.The product composition was very simple and could be explained by applying the protolytic cracking mechanism when the catalyst loading was small.Higher loading of the catalyst brought about further reactions of cracked products,accumulating lower olefin and paraffin with low reactivity in product stream and resulting in complex product composition.
机译:将MFI沸石的细小(-0.2微米)颗粒分散在硅沸石泡沫上,制备了泡沫型MFI沸石催化剂。估计分散的MFI沸石的Si / Al摩尔比为25,硅沸石泡沫的分散量为25 wt%。由于泡沫型催化剂的表观密度非常低,为0.11 gcentpoint·cm〜(-3),催化剂的负载量可以在0.02 g至0.5 g的范围内变化,而无需考虑压降,这提供了反应物和产物的停留时间的宽泛变化。正辛烷催化裂化的转化率和烯烃产率随催化剂负载量的增加而增加。产物组成非常简单,可以通过在催化剂负载量较小时应用蛋白水解裂化机理来解释,较高的催化剂负载量会导致进一步的裂化反应d。产物,在产物流中积聚低反应性的低级烯烃和石蜡,并导致复杂的产物组成。

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