停留时间和载气对氧化铝支撑铬催化剂上正己烷脱氢反应的影响

Xiuyi Li, Chunyi Li
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引用次数: 0

摘要

采用初湿浸渍法制备了 CrOx/γ-Al2O3 催化剂,并研究了停留时间和载气对正己烷脱氢的影响。研究发现,以 H2 为载气的 CrOx/γ-Al2O3 催化剂与以 N2 稀释正己烷的催化行为完全不同。用 N2 稀释进料时,脱氢产物的选择性得到提高,而裂化反应则随着停留时间的缩短而进行。然而,当使用 H2 作为载气时,脱氢产物的选择性明显降低,而正己烷的异构化却得到了促进。据推测,H2 在脱氢活性位点上发生解离,并进一步促进烯烃脱氢产物形成碳位,从而在 γ-Al2O3 表面的酸性位点上进行异构化反应。因此,当使用 H2 作为载气时,正己烷的异构化会因脱氢产物的选择性而得到促进。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Effect of Residence Time and Carrier Gas on the Dehydrogenation of n-Hexane over Alumina-supported Chromium Catalyst
CrOx/γ-Al2O3 catalyst was prepared by incipient wetness impregnation method, and the influence of residence time and carrier gas on the dehydrogenation of n-hexane were studied. It is found that n-hexane dehydrogenation over CrOx/γ-Al2O3 catalyst with H2 as carrier gas exhibits totally different catalytic behaviors with that of diluting n-hexane with N2. When diluting feed with N2, the selectivity to dehydrogenation product is promoted while the cracking reaction is exhibited with reducing residence time. However, the selectivity to dehydrogenation product is significantly decreased while the isomerization of n-hexane is promoted when using H2 as carrier gas. It is proposed that H2 undergoes dissociation on the dehydrogenation active site, and further facilitates the olefinic dehydrogenation products to form carbocation, which performing isomerization reaction on the acid site on the γ-Al2O3 surface. Therefore, the isomerization of n-hexane is promoted in cost of the selectivity to dehydrogenation product when using H2 as carrier gas.  
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