A kinetic model of the cycloaddition reactions between cyclopentadiene and 1,3-butadiene for synthesis of 5-vinyl-2-norbornene

IF 1.6 4区 工程技术 Q3 ENGINEERING, CHEMICAL
Hao Li, Xue Liu, Yan Zhang, Yang Xiao, Kun Cao
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引用次数: 0

Abstract

Under high temperature and pressure, a continuous tubular reactor was successfully utilized to investigate the kinetics of 5-vinyl-2-norbornene (VNB) production. The process involved multiple cycloaddition reactions between cyclopentadiene (CPD) and 1,3-butadiene (BD). The results, spanning a wide range of operating conditions, indicate that higher temperature (180°C) and proper residence time (72 min) were conducive to efficient synthesis of VNB. The apparent kinetic parameters, including activation energies and pre-exponential factors, were acquired by fitting experimental data under integral operating conditions. The kinetic model was proven effective from a practical point of view in predicting the concentration changes of each product in the range 140 to 180°C and 30 to 80 wt.% concentration. This work provides a solid basis for the optimization of the VNB synthesis process.

Abstract Image

用于合成 5-乙烯基-2-降冰片烯的环戊二烯和 1,3-丁二烯环化反应动力学模型
在高温高压条件下,成功利用连续管式反应器研究了 5-乙烯基-2-降冰片烯(VNB)的生产动力学。该过程涉及环戊二烯(CPD)和 1,3-丁二烯(BD)之间的多个环加成反应。结果表明,较高的温度(180°C)和适当的停留时间(72 分钟)有利于 VNB 的高效合成。表观动力学参数,包括活化能和前指数,是在整体操作条件下通过拟合实验数据获得的。从实用的角度来看,该动力学模型在预测 140 至 180°C 和 30 至 80 wt.% 浓度范围内每种产物的浓度变化方面被证明是有效的。这项工作为优化 VNB 合成工艺提供了坚实的基础。
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来源期刊
Canadian Journal of Chemical Engineering
Canadian Journal of Chemical Engineering 工程技术-工程:化工
CiteScore
3.60
自引率
14.30%
发文量
448
审稿时长
3.2 months
期刊介绍: The Canadian Journal of Chemical Engineering (CJChE) publishes original research articles, new theoretical interpretation or experimental findings and critical reviews in the science or industrial practice of chemical and biochemical processes. Preference is given to papers having a clearly indicated scope and applicability in any of the following areas: Fluid mechanics, heat and mass transfer, multiphase flows, separations processes, thermodynamics, process systems engineering, reactors and reaction kinetics, catalysis, interfacial phenomena, electrochemical phenomena, bioengineering, minerals processing and natural products and environmental and energy engineering. Papers that merely describe or present a conventional or routine analysis of existing processes will not be considered.
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