Murielk Sebrian Valvassore, Caliane Bastos Borba Costa
{"title":"Analysis of novel configurations of an intensified process for ethyl lactate production","authors":"Murielk Sebrian Valvassore, Caliane Bastos Borba Costa","doi":"10.1016/j.cep.2024.110146","DOIUrl":null,"url":null,"abstract":"<div><div>Ethyl lactate is a biodegradable and non-toxic ester with market growth potential. It is used in different industries. In this work, aiming to reduce the production cost of this solvent, seeking to make it even more competitive in the market, an intensified process was proposed and evaluated with a reactive distillation column followed by extractive distillation for recovery and reuse of compounds present in the process. An optimization study was developed using Aspen Plus and MATLAB® in order to find a configuration with the minimum total annualized cost (TAC). An economically competitive structure was found. Based on this structure, simulation studies were developed by applying the vapor recompression technique in the extractive distillation column and keeping the reactive distillation column. In economic terms, an even more competitive structure, was found, with a reduction of around 48 % in the TAC compared to the results reported in the literature.</div></div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"208 ","pages":"Article 110146"},"PeriodicalIF":3.8000,"publicationDate":"2025-02-01","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/S0255270124004847","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
Ethyl lactate is a biodegradable and non-toxic ester with market growth potential. It is used in different industries. In this work, aiming to reduce the production cost of this solvent, seeking to make it even more competitive in the market, an intensified process was proposed and evaluated with a reactive distillation column followed by extractive distillation for recovery and reuse of compounds present in the process. An optimization study was developed using Aspen Plus and MATLAB® in order to find a configuration with the minimum total annualized cost (TAC). An economically competitive structure was found. Based on this structure, simulation studies were developed by applying the vapor recompression technique in the extractive distillation column and keeping the reactive distillation column. In economic terms, an even more competitive structure, was found, with a reduction of around 48 % in the TAC compared to the results reported in the literature.
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.