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n-Heptane isomerization over molybdenum oxide supported catalysts

机译:氧化钼负载型催化剂上的正庚烷异构化

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摘要

Concern over the negative effects of fuel and oil usage on the environment has caused changes in regulations with severe impacts on gasoline, other jet fuels and lubricating oils. In order to improve the octane quality of a gasoline fraction, the refinery industry uses some high-octane rating components that are paraffinic in nature. The octane index is improved by increasing the degree of iso-alkane branching. Since the highly branched isomers have a relatively low environmental impact, the skeletal isomerization of n-alkane can be a key technology for production of high quality gasoline [1]. However, the practical application of this process has only been confined to short chain alkanes, because the isomerization of long-chain alkanes is usually accompanied by undesirable cracking. Thus, catalysts with a sufficiently good balance of metal and acid functions under suitable reaction conditions are generally needed to suppress cracking in order to achieve high isomerization selectivity for long-chain alkanes [2]. Molybdenum oxide (MoO3) supported catalysts have been extensively studied in recent years due to their possible potential to catalyze the isomerization of linear alkanes [3]. Based on previous study, catalyst support is one of the crucial factors that influence the catalyst acidity [4]. Therefore, in this study, a series of MoO3 catalyst supported by HZSM-5, MCM-41, SiO2and ZrO2was prepared by impregnation method. Their structural property was characterized using nitrogen physisorption analysis and the acidic property was determined by pyridine adsorbed IR spectroscopy. The catalytic property of all catalyst was evaluated over n-heptane isomerization at 623 K. The result showed that MoO3-ZrO2catalyst exhibits the highest catalytic activity with 33.9 % conversion. The result was attributed from the Lewis acid property of the catalyst which was crucial in the n-heptane isomerization. Comparison between all the catalyst acidic property and their catalytic activity is discussed.
机译:对燃料和油的使用对环境的负面影响的担忧已导致法规变更,对汽油,其他喷气燃料和润滑油造成严重影响。为了提高汽油馏分的辛烷值,炼油行业使用了一些具有高辛烷值的链烷烃成分。通过增加异烷烃的支化度可以提高辛烷值。由于高度支化的异构体对环境的影响相对较小,正构烷烃的骨架异构化可能是生产高质量汽油的关键技术[1]。然而,该方法的实际应用仅限于短链烷烃,因为长链烷烃的异构化通常伴随着不希望的裂化。因此,为了达到长链烷烃的高异构化选择性[2],通常需要在合适的反应条件下具有足够好的金属和酸官能平衡的催化剂来抑制裂解。近年来,由于氧化钼(MoO3)负载的催化剂可能催化线性烷烃的异构化[3],因此对其进行了广泛的研究。根据以前的研究,催化剂载体是影响催化剂酸度的关键因素之一[4]。因此,本研究采用浸渍法制备了一系列以HZSM-5,MCM-41,SiO2和ZrO2为载体的MoO3催化剂。通过氮物理吸附分析表征了它们的结构性质,并通过吡啶吸附红外光谱法测定了其酸性性质。在623 K下正庚烷异构化过程中评估了所有催化剂的催化性能。结果表明MoO3-ZrO2催化剂具有最高的催化活性,转化率为33.9%。该结果归因于催化剂的路易斯酸性质,这对正庚烷异构化至关重要。讨论了所有催化剂的酸性和催化活性之间的比较。

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