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首页> 外文期刊>Chemical engineering journal >Kinetic study of Amberlite IR120 catalyzed acid esterification of levulinic acid with ethanol: From batch to continuous operation
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Kinetic study of Amberlite IR120 catalyzed acid esterification of levulinic acid with ethanol: From batch to continuous operation

机译:乙酰乙酸乙酰乙酸氨苄酸IR120催化酸酯化的动力学研究:从批量到连续操作

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摘要

Levulinic acid (LA) is one of the most important platform chemicals as it is a versatile building block for a variety of high value-added products, fine chemicals and pharmaceutical intermediates. Catalytic esterification of LA with alkyl alcohols leads to levulinate esters which can be used as fragrances, flavoring agents and fuel additives. In the present work, the kinetics of the levulinic acid esterification with ethanol in the presence of Amberlite IR120 was investigated in a batch reactor. The collected experimental data were interpreted with a reliable model taking into account also for the mass transfer phenomena involved in the reaction network. The kinetic model was further validated by conducting experiments in a fixed bed reactor. The reactor was characterized in terms of fluid-dynamics and the collected kinetic data were interpreted with a reliable reactor model, considering the extent of the reaction and fluid-solid mass transfer limitation.
机译:Levulinic acid(La)是最重要的平台化学品之一,因为它是各种高附加值产品,精细化学品和药物中间体的多功能组化学品之一。 用烷基醇的La催化酯化导致剥离酯,其可用作香料,调味剂和燃料添加剂。 在本作工作中,在分批反应器中研究了在氨苄啶IR120存在下用乙醇的乙酰丙酸酯化的动力学。 收集的实验数据被解释为同时考虑到反应网络中涉及的传质现象的可靠模型。 通过在固定床反应器中进行实验进一步验证动力学模型。 反应器以流体动力学的特征在于,考虑到反应和流体固体传质限制的程度,将收集的动力学数据解释为可靠的反应器模型。

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