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摘要
采用等体积浸渍法制备了Ru/Al2O3催化剂,在间歇式反应釜中研究了双酚A的加氢反应动力学。根据Langmuir-Hinshelwood反应机理建立了双酚A加氢反应的动力学模型,并确定第一步加氢是决定反应速率的控制步骤。结果表明,通过计算得到双酚A与中间体4-(2-(4-羟基环己基)丙-2-基)苯酚的两步加氢反应所需活化能分别为66.46 kJ/mol和68.07 kJ/mol,动力学模型与实验数据之间存在良好的相关性。
Abstract
Ru/Al2O3 catalyst is prepared through using the equivalent volumetric impregnation method,and the kinetics of bisphenol A hydrogenation over the catalyst is studied in a batch reactor.The kinetic model for bisphenol A hydrogenation reaction is established based on the Langmuir-Hinshelwood reaction mechanism,and the first hydrogenation step is identified as the rate-determining step.It is verified that the activation energies required for the hydrogenation of bisphenol A and 4-(2-(4-hydroxycyclohexyl) prop-2-phenol,the intermediate,are determined to be 66.46 kJ·mol-1 and 68.07 kJ·mol-1,respectively.There is a strong correlation between the kinetic model and experimental data.
关键词
双酚A
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动力学
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内外扩散
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催化加氢
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氢化双酚A
Key words
bisphenol A
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kinetics
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internal and external diffusion
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catalytic hydrogenation
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hydrogenated bisphenol A
Author summay
李志诚(1997-),男,硕士生,研究方向为催化加氢,lizhicheng20212021@163.com;陈群(1963-),男,本科,研究员,研究方向为聚合物离子交换催化材料的合成及其结构、性能与应用研究,通讯联系人,13906123032@126.com。
Ru/Al2O3催化剂上双酚A加氢反应动力学研究[J].
现代化工, 2024, 44(8): 196-202 DOI:10.16606/j.cnki.issn0253-4320.2024.08.036