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Alkylation of isobutane with 1-butene on zeolite beta

机译:β-沸石上异丁烷与1-丁烯的烷基化

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Alkylation of isobutane with 1butene was carried out in the liquid phase at 353 K on beta zeolite catalyst samples with varying framework Si/Al ratios and particle sizes. The specific external surface area determined with nitrogen physisorption and t-plot analysis is the key parameter to rationalize alkylation activity and stability. The catalytic activity of zeolite beta samples with specific external surface areas smaller than ca 280 m(2) g(-1) suffers from intracrystalline diffusional limitations. The critical particle size to avoid diffusional limitations is estimated at 14 nm. In the absence of diffusional limitations, the alkylate yield obtained during the catalyst lifetime is proportional to the number of Bronsted acid sites in the zeolite and amounts to ca 3 kg mole(-1), irrespective of the acid site density. The deactivation of the samples is explained by a site coverage model. (C) 1998 Academic Press. [References: 34]
机译:在353 K液相条件下,在具有不同骨架Si / Al比和粒径的β沸石催化剂样品上,异丁烷与1-丁烯进行烷基化。通过氮的物理吸附和t线图分析确定的比表面积是合理化烷基化活性和稳定性的关键参数。比表面积小于大约280 m(2)g(-1)的沸石β样品的催化活性受到晶体内扩散的限制。避免扩散限制的临界粒度估计为14 nm。在没有扩散限制的情况下,催化剂寿命期间获得的烷基化物收率与沸石中布朗斯台德酸位点的数量成正比,与酸位点密度无关,约为3 kg摩尔(-1)。站点范围模型解释了样本的停用。 (C)1998年学术出版社。 [参考:34]

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