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Enhancement of esterification conversion using pervaporation membrane reactor

机译:使用全蒸发膜反应器提高酯化转化率

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In the present study, the esterification reaction of propionic acid with isobutyl alcohol to produce isobutyl propionate and water was studied. The performance of esterification reaction was compared by using the batch process and the pervaporation assisted hybrid process which performs the reaction and separation simultaneously. A polyvinyl alcohol–polyethersulphone (PVA–PES) hydrophilic polymeric membrane was used in the study to separate water and also to shift the equilibrium. The influence of process parameters such as catalyst loading, molar ratio of acid to alcohol, reaction temperature and ratio of membrane area to initial reaction volume (S/V) was studied. The results showed that the pervaporation assisted esterification process gave more conversion than the batch process of esterification. The membrane showed high selectivity to the removal of water in the propionic acid, isobutyl alcohol, isobutyl propionate and water mixture. Moreover, the conversion of propionic acid was enhanced by enhancing the catalyst amount, molar ratio of acid to alcohol, reaction temperature and S/V ratio.
机译:在本研究中,研究了丙酸与异丁醇的酯化反应,生成丙酸异丁酯和水。通过使用分批工艺和同时进行反应和分离的全蒸发辅助混合工艺对酯化反应的性能进行了比较。研究中使用了聚乙烯醇-聚醚砜(PVA-PES)亲水性聚合物膜来分离水并改变平衡。研究了工艺参数的影响,如催化剂的加入量,酸与醇的摩尔比,反应温度以及膜面积与初始反应体积的比(S / V)。结果表明,全蒸发辅助酯化过程比分批酯化过程具有更高的转化率。该膜显示出对除去丙酸,异丁醇,丙酸异丁酯和水混合物中的水的高选择性。此外,通过提高催化剂量,酸与醇的摩尔比,反应温度和S / V比,可以提高丙酸的转化率。

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