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Kinetics of n-Butylbenzene Dehydrocyclization over Chromia-Alumina

机译:铬-氧化铝上正丁基苯脱氢动力学

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摘要

The kinetics of dehydrogenation, cyclization, and isomerization steps in n-butylbenzene dehydrocyclization over precoked chromia—alumina has been investigated at 683—783 K. Apparent kinetic parameters of a pseudohomogeneous model were calculated from the initial-rate and integral-rate data measured with n-butylbenzene and 4-phenyl-1-butene in an isothermal fixed-bed reactor. Dehydrocyclization was shown to proceed by dehydrogenation of n-butylbenzene to n-butenylbenzenes, by their cyclization, and by dehydrogenation of the cyclic products to methylindenes and naphthalene. Direct cyclization of n-butylbenzene was of little importance over the precoked catalyst. According to the initial-rate data, dehydrogenation to n-butenylbenzenes followed an apparent order of 0.5 and the kinetic parameters seemed to be applicable also at higher conversions. The primary dehydrogenation products were 1-phenyl-1-butenes, and a surface model based on hydrogen abstraction from the α-carbon has been discussed. The initial cyclization rates measured with 4-phenyl-1-butene were appreciably lower than those observed in integral-rate experiments. The discrepancy was tentatively explained by the higher reactivity of 1-phenyl-1-butenes, which are the main constituents of the n-butenylbenzene fraction at longer contact times. High conversion runs with n-butylbenzene also showed that methylindenes and -indans were partly dealkylated and probably polymerized. The apparent orders ranged from 1 to 1.5 for 1,6-cyclization and from 0.5 to 0.8 for 1,5-cyclization. Skeletal isomerization of n-butylbenzene to sec-butyl- and sec-butenylbenzenes was rapidly subsided during coking, and on the coked catalyst at 783 K the reaction followed an apparent order of -0.5.
机译:研究了在预焦氧化铬-氧化铝上正丁基苯脱氢环化反应中的脱氢,环化和异构化步骤的动力学。研究了拟均质模型的表观动力学参数,该模型由初始速率和积分速率数据计算得出。等温固定床反应器中的正丁基苯和4-苯基-1-丁烯。通过正丁基苯的脱氢,正丁基环的环化以及环状产物的脱氢为甲基茚和萘的反应,显示出脱氢环化的过程。与预焦化催化剂相比,正丁基苯的直接环化意义不大。根据初始速率数据,脱氢为正丁烯基苯的表观顺序为0.5,动力学参数似乎也适用于更高的转化率。主要的脱氢产物是1-苯基-1-丁烯,并且已经讨论了基于从α-碳中提取氢的表面模型。用4-苯基-1-丁烯测得的初始环化率明显低于积分速率实验中观察到的环化率。暂时用1-苯基-1-丁烯的较高反应活性来解释该差异,1-苯基-1-丁烯是较长接触时间下正丁烯基苯馏分的主要成分。用正丁基苯进行的高转化率试验还表明,甲基茚和-茚满部分脱烷基并可能聚合。 1,6-环化的表观阶数为1至1.5,1,5-环化的表观阶数为0.5至0.8。在焦化过程中,正丁基苯向异构体的仲丁基苯和仲丁烯基苯的骨架异构化迅速消失,并且在783 K的焦化催化剂上,反应遵循-0.5的明显顺序。

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