Sustainable Separation of Azeotrope <i>n</i> -Hexane/Isopropanol via Extractive Distillation: Molecular Insights, Process Optimization, and Techno-Economic–Environmental Analysis for Cleaner Production
Separation of the azeotrope n-hexane (HEX)/isopropanol (IPA) is critical for solvent recovery in electronic and pharmaceutical industries, yet conventional distillation faces challenges of energy inefficiency and high carbon footprint. This study proposes an energy-efficient extractive distillation (ED) strategy using N-methyl pyrrolidone (NMP) as an entrainer to separate HEX and IPA with a high solvent recyclability and low environmental impact. Three processes, including conventional extractive distillation (CED), dividing wall column, and vapor-phase side-stream extractive distillation (VSED), were proposed and optimized via NSGA-II and TOPSIS algorithms. The results demonstrate that the VSED process achieves the optimal performance, reducing the total annual cost by 13.62% and CO2 emissions by 6.35% compared to the CED process. This study provides a comprehensive decision-making framework with the integration of molecular interactions, MD-assisted ED optimization, and process intensification supported by NSGA-II for sustainable separation of the HEX/IPA azeotrope.
Authors
- Weizhuo Li
- Longwei Cao
- Dongmei Xu (ORCID: https://orcid.org/0000-0003-0193-7543)
- Zhishan Zhang
- Yinglong Wang
- Jun Gao
Institutions
- Qingdao University of Science and Technology (CN)
- Shandong University of Science and Technology (CN)
Publication Details
- Journal
- Industrial & Engineering Chemistry Research
- Published
- 2026-02-25
- DOI
- https://doi.org/10.1021/acs.iecr.5c04681
- Primary Topic
- Process Optimization and Integration
- Type
- article
- Field-Weighted Citation Impact
- 0.00