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Kinetics of the catalytic cracking of naphtha over ZSM-5 zeolite: effect of reduced crystal size on the reaction of naphthenes

机译:ZSM-5沸石上石脑油催化裂化的动力学:减小的晶体尺寸对环烷烃反应的影响

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摘要

The catalytic cracking of model naphthenes (cyclohexane and methylcyclohexane) over ZSM-5 zeolites of different crystal sizes (macro-and nano-ZSM-5) was examined at reaction temperatures ranging from 748 to 923 K under atmospheric pressure, focusing on the associated reaction rate constants and activation energies. The catalytic cracking was found to follow first-order kinetics with respect to the naphthene concentrations and the activation energies for cyclohexane and methylcyclohexane cracking over nano-ZSM- 5 were determined to be 119 and 116 kJ mol(-1), respectively. In order to elucidate the rate-limiting step in the cracking process, the Thiele modulus and the effectiveness factor obtained from cracking over the two ZSM-5 zeolites were evaluated. Cracking with nano-ZSM-5 proceeded under reaction-limiting conditions, whereas the reaction over macro-ZSM-5 at 923 K took place under transition conditions between reaction-and diffusion-limiting. Nano-ZSM-5 was applied to the catalytic cracking of a model naphtha and the results demonstrated that this catalyst was both effective and stable and generated a high yield of light olefins.
机译:在大气压下,在748至923 K的反应温度下,研究了不同晶体尺寸的ZSM-5分子筛上模型环烷烃(环己烷和甲基环己烷)的催化裂解反应。速率常数和活化能。发现催化裂化遵循环烷烃浓度的一级动力学,在纳米ZSM-5上环己烷和甲基环己烷的裂化活化能分别确定为119和116 kJ mol(-1)。为了阐明裂解过程中的限速步骤,评估了在两种ZSM-5沸石上裂解得到的Thiele模量和有效因子。纳米ZSM-5的裂解是在反应限制条件下进行的,而宏ZSM-5在923 K的反应是在反应限制和扩散限制之间的过渡条件下发生的。将纳米ZSM-5应用于模型石脑油的催化裂化,结果表明该催化剂既有效又稳定,并产生了高产率的轻质烯烃。

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