{"title":"Next-generation pervaporation-assisted distillation: Recent advances in process intensification","authors":"Maria Polyakova , Mirko Skiborowski","doi":"10.1016/j.cep.2025.110416","DOIUrl":null,"url":null,"abstract":"<div><div>Pervaporation is a well-established membrane separation process that effectively overcomes limitations of distillation due to azeotropes and distillation boundaries. The selective mass transfer of pervaporation membranes has enabled successful implementation in a variety of industries, with applications in the chemical industry, as well as the food and pharma industry, including membrane bioreactors in fermentation processes. Yet, the majority of applications in separation processes remain focused on the dehydration of aqueous-organic process streams, including biofuel and bioethanol production. Pervaporation-assisted distillation processes leverage the benefits of both technologies and exploit the resulting synergies to provide energy and cost-efficient separations, especially for azeotropic mixtures, which otherwise require rather energy intensive distillation processes, such as pressure-swing, extractive or hetero-azeotropic distillation. The current review provides an overview of recent developments that enable further process intensification of pervaporation-assisted distillation processes and provides some perspective on emerging trends that may result in a wider application of these interesting hybrid separation processes.</div></div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"216 ","pages":"Article 110416"},"PeriodicalIF":3.8000,"publicationDate":"2025-06-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering and Processing - Process Intensification","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S025527012500265X","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0
Abstract
Pervaporation is a well-established membrane separation process that effectively overcomes limitations of distillation due to azeotropes and distillation boundaries. The selective mass transfer of pervaporation membranes has enabled successful implementation in a variety of industries, with applications in the chemical industry, as well as the food and pharma industry, including membrane bioreactors in fermentation processes. Yet, the majority of applications in separation processes remain focused on the dehydration of aqueous-organic process streams, including biofuel and bioethanol production. Pervaporation-assisted distillation processes leverage the benefits of both technologies and exploit the resulting synergies to provide energy and cost-efficient separations, especially for azeotropic mixtures, which otherwise require rather energy intensive distillation processes, such as pressure-swing, extractive or hetero-azeotropic distillation. The current review provides an overview of recent developments that enable further process intensification of pervaporation-assisted distillation processes and provides some perspective on emerging trends that may result in a wider application of these interesting hybrid separation processes.
期刊介绍:
Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.