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Kinetic modeling of pore mouth catalysis in the hydroconversion of n-octane on Pt-H-ZSM-22

机译:Pt-H-ZSM-22上正辛烷加氢转化中孔口催化的动力学模型

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摘要

A microkinetic model based on the single-event theory was developed to describe the hydroconversion of n-octane on Pt-H-ZSM-22 zeolite.In the model,alkene protonation and subsequent acid-catalyzed reactions,i.e.,skeletal isomerization and cracking,occur in the pore mouths of ZSM-22.In contrast to USY,in these pore mouths,the molecules are physisorbed according to different modes,each with a specific enthalpy and enropy loss.Moreover after protonation of the physisorbed alkenes,the stability of the resulting carbenium ions increases with the number of carbon atoms entering the pore mouth.The reaction network is based on transformations of alkylcarbenium ions that can be obtained by protonation of physisorbed alkenes in pore mouths.Reactions that are sterically hindered or that lead to alkylcarbenium ions with charged carbon atoms outside the poe were discarded.In particular,methyl shifts as well as branching and beta-scission reactions involving tertiary alkylcarbenium ions were excluded.The composite activation energy,DELTAE_(act)~(comp),i.e.,the sum of the protonation enthalpy and the real activation energy for the allowed reactions,was taken from data on a reference ultrastable Y zeolite (CBV760).This pore mouth catalysis model adequately describes the conversion of n-octane on Pt-H-ZSM-22.The difference in composite activation energy DELTAE_(act)~(comp) of -8.9 (+-0.3) kJ mol~(-1) between the reference USY zeolite and the ZSM-22 corresponds to the higher average acid streth in ZSM-22.Further,the yield pattern of individual isomers of octane is described well using three parameters:(i) h_(cd) with a value of -1.1 (+-0.2) kJ mol~(-1) accounting for differences in carbenium ion stability proportional to the number of carbon atoms entering the pore mouth:(ii) DELTAE_(pcp);and (iii) DELTAE_(beta) with values of -4.0(+-0.2) and -16.7 (+-0.21) kJ mol~(-1).
机译:建立了基于单事件理论的微动力学模型,描述了正辛烷在Pt-H-ZSM-22分子筛上的加氢转化。与USY相比,在这些孔中,分子根据不同的模式进行物理吸附,每个分子都有特定的焓和取代度。此外,对物理吸附的烯烃进行质子化后,生成的碳正离子随进入孔口的碳原子数增加而增加。反应网络基于烷基碳原子离子的转化,该转化可通过对孔口中的物理吸附的烯烃进行质子化而获得。除去在poe外的带电碳原子。特别是,不包括甲基转移以及涉及叔烷基碳鎓离子的支化和β断裂反应d。复合活化能DELTAE_(act)〜(comp),即质子化焓和允许反应的实际活化能之和,是从参考超稳定Y型沸石(CBV760)的数据中得出的。口催化模型充分描述了Pt-H-ZSM-22上正辛烷的转化。复合活化能DELTAE_(act)〜(comp)的差为-8.9(+ -0.3)kJ mol〜(-1)。参考USY沸石和ZSM-22对应于ZSM-22中较高的平均酸碱度。此外,使用三个参数很好地描述了辛烷的各个异构体的产率模式:(i)h_(cd)的值为- 1.1(+ -0.2)kJ mol〜(-1)解释了碳正离子稳定性的差异与进入孔口的碳原子数成正比:(ii)DELTAE_(pcp);和(iii)DELTAE_β的值-4.0(+-0.2)和-16.7(+ -0.21)kJ mol〜(-1)。

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