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Isomerization of cyclohexane, n-hexane and their mixtures on zeolite catalyst

机译:沸石催化剂上环己烷,正己烷及其混合物的异构化

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The skeletal rearrangement of cyclohexane, n-hexane and their mixtures has beeninvestigated on platinum/hydrogen-mordenite at 180-270℃, 5-40 bar total pressure andhydrogen to hydrocarbon molar ratio 1-20. The apparent activation energy for cyclohexaneisomerization is 114 kJ/mol, for n-hexane isomerization 123 kJ/mol. The reaction order up to4 bar in cyclohexane is 0.18, in n-hexane 0.39. The reaction orders in hydrogen up to 36 barare –0.57 and –0.65 in the case of cyclohexane and n-hexane, respectively. Rate equationswere derived and parameters involved determined for the isomerization of pure paraffins andtheir binary mixtures. The rate of single paraffins can be described with sufficient accuracypresuming rate determining skeletal rearrangement of the carbenium ion, while in binarymixtures rate determining transport in the micropores is to be assumed. At high conversionsof cyclohexane hydroisomerization products of higher molecular weight than the feed areformed through alkylation and disproportination reactions.
机译:研究了环己烷,正己烷及其混合物在180-270℃,总压力5-40 bar和氢碳氢化合物摩尔比为1-20的条件下在骨架上的骨架重排。环己烷异构化的表观活化能为114 kJ / mol,正己烷异构化的表观活化能为123 kJ / mol。在环己烷中至多4 bar的反应顺序为0.18,在正己烷中的反应顺序为0.39。在环己烷和正己烷中,氢的反应顺序分别高达36 barare –0.57和–0.65。推导了速率方程,并确定了用于纯链烷烃及其二元混合物异构化的参数。可以足够准确地描述单链烷烃的速率,假定速率决定了碳正离子的骨架重排,而在二元混合物中,速率决定了微孔中的迁移。在高转化率下,通过烷基化和歧化反应形成分子量比进料高的环己烷加氢异构化产物。

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  • 会议地点 Montpellier(FR);Montpellier(FR)
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    University of Veszprém Veszprém P.O.Box 158 H-8201 Hungary MOL-Hungarian Oil and Gas Co. Százhalombatta P.O.Box 1 H-2443 Hungary;

    University of Veszprém Veszprém P.O.Box 158 H-8201 Hungary;

    Chemical Research Center Institute of Chemistry Hungarian Academy of Sciences Budapest P.O.Box 17 H-1525 Hungary;

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