现代化工2024,Vol.44Issue(8) :196-202.DOI:10.16606/j.cnki.issn0253-4320.2024.08.036

Ru/Al2O3催化剂上双酚A加氢反应动力学研究

Reaction kinetics of bisphenol A hydrogenation over Ru/Al2O3 catalyst

李志诚 钱俊峰 孙中华 吴中 陈群
现代化工2024,Vol.44Issue(8) :196-202.DOI:10.16606/j.cnki.issn0253-4320.2024.08.036

Ru/Al2O3催化剂上双酚A加氢反应动力学研究

Reaction kinetics of bisphenol A hydrogenation over Ru/Al2O3 catalyst

李志诚 1钱俊峰 1孙中华 1吴中 1陈群1
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作者信息

  • 1. 常州大学石油化工学院,江苏省精细石油化工重点实验室,江苏 常州 213164
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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/氢化双酚A/催化加氢/内外扩散/动力学

Key words

bisphenol A/hydrogenated bisphenol A/catalytic hydrogenation/internal and external diffusion/kinetics

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出版年

2024
现代化工
中国化工信息中心

现代化工

CSTPCD北大核心
影响因子:0.553
ISSN:0253-4320
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