Manufacture of n-Propyl Propionate Using Ion Exchange Resins: Reaction Kinetics and Feasibility of Reactive Distillation

被引:1
作者
Devale, Reshma R. [1 ]
Deogharkar, Bipin S. [1 ]
Mahajan, Yogesh S. [1 ]
机构
[1] Dr Babasaheb Ambedkar Technol Univ, Dept Chem Engn, Lonere 402103, Maharashtra, India
关键词
Ion exchange resins; Intrinsic kinetics; Effect of parameters; Regression; Feasibility of Reactive Distil-lation; ACETIC-ACID; ESTERIFICATION; METHANOL; ETHANOL;
D O I
10.9767/bcrec.17.4.15928.811-820
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Reaction kinetics of esterification of propionic acid with 1-propanol to produce n-propyl propionate using Amber-lyst-15 as a catalyst was investigated in this work. Effect of various parameters was studied. Initially, the efficacy of different catalysts was investigated which revealed that Amberlyst-15 can be suitably used for the reaction. This was followed by mass transfer exclusion which included effect of agitation speed, catalyst size and calculation of Weisz-Prater Criterion. Parameters selected for kinetic study were mole ratio of propionic acid to 1-propanol, temperature, catalyst loading and initial water concentration. Catalyst reusability was also verified. Aspen Custom Modeler (ACM) was used to regress kinetic parameters and a good match was obtained. Reactive Distilla-tion (RD) runs in the batch mode were performed which showed that RD is a better option for process intensifica-tion (PI) for this reaction.Copyright (c) 2022 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0).
引用
收藏
页码:811 / 820
页数:10
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