Reaction/distillation matrix algorithm development to cover sequences containing reactive dividing wall column: Validation in process of cumene production
{"title":"Reaction/distillation matrix algorithm development to cover sequences containing reactive dividing wall column: Validation in process of cumene production","authors":"Maedeh Jamshidi , Ali Mallahzadeh , Amirhossein Khalili-Garakani , Norollah Kasiri","doi":"10.1016/j.cep.2025.110289","DOIUrl":null,"url":null,"abstract":"<div><div>The Reactive Dividing Wall Column (RDWC) offers a powerful approach to process intensification by combining chemical reactions and multi-component separations within a single unit, delivering significant economic and operational benefits. This study investigates various RDWC configurations for Cumene production generated through a modified Reaction/Distillation matrix-based algorithm. Rigorous simulations of both the conventional Reactive Distillation Column (RDC) and RDWC setups were conducted in Aspen Plus, while the Teaching-Learning-Based Optimization (TLBO) algorithm in MATLAB minimized total annual costs (TAC) and met product specifications. TLBO was chosen for its parameter-free nature, computational efficiency, and strong optimization performance, making it a robust tool for this case study. Comparative analysis revealed that the optimized RDWC configuration substantially outperformed the conventional RDC, reducing TAC by 27.62 % and total energy consumption by 27.98 %. Furthermore, the optimized RDWC configuration led to a 57.66 % decrease in capital costs and a 29.13 % reduction in operating costs by minimizing the required number of columns, condensers, and reboilers. These results demonstrate that the RDWC is a highly efficient and economically viable option for energy-intensive processes such as Cumene production, achieving substantial cost savings and enhanced operational efficiency.</div></div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"213 ","pages":"Article 110289"},"PeriodicalIF":3.8000,"publicationDate":"2025-03-30","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/S0255270125001382","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
The Reactive Dividing Wall Column (RDWC) offers a powerful approach to process intensification by combining chemical reactions and multi-component separations within a single unit, delivering significant economic and operational benefits. This study investigates various RDWC configurations for Cumene production generated through a modified Reaction/Distillation matrix-based algorithm. Rigorous simulations of both the conventional Reactive Distillation Column (RDC) and RDWC setups were conducted in Aspen Plus, while the Teaching-Learning-Based Optimization (TLBO) algorithm in MATLAB minimized total annual costs (TAC) and met product specifications. TLBO was chosen for its parameter-free nature, computational efficiency, and strong optimization performance, making it a robust tool for this case study. Comparative analysis revealed that the optimized RDWC configuration substantially outperformed the conventional RDC, reducing TAC by 27.62 % and total energy consumption by 27.98 %. Furthermore, the optimized RDWC configuration led to a 57.66 % decrease in capital costs and a 29.13 % reduction in operating costs by minimizing the required number of columns, condensers, and reboilers. These results demonstrate that the RDWC is a highly efficient and economically viable option for energy-intensive processes such as Cumene production, achieving substantial cost savings and enhanced operational efficiency.
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.