Process simulation and optimization of extractive distillation for separating isopropanol-ethanol from IBE fermentation broth as a gasoline additive

Addressing the downstream processing challenges of the bio-butanol fermentation broth (Isopropanol-Butanol-Ethanol-Water), and producing the isopropanol-ethanol mixture with a mass fraction of ≥ 0.99975 as a high-quality gasoline additive, is crucial for enhancing the overall economy and sustainability of the bio-butanol production process. To obtain the high-purity isopropanol-ethanol mixture, this paper, based on the dehydration-butanol-extractive four column distillation process, proposes a baseline extractive distillation process using a deep eutectic solvent (DES, glycerol: choline chloride = 2:1) as the extractant, termed the extractive distillation-DES basic process. With heat load as optimization target, the extractive distillation-DES basic process was optimized to determine the optimal operating parameters, termed the extractive distillation-DES sensitivity optimization process. Based on the extractive distillation-DES sensitivity optimization process, the particle swarm optimization algorithm was applied to minimize the total annual cost, resulting in the extractive distillation-DES algorithm optimization process. Compared with the extractive distillation-DES basic process, the total load of the extractive distillation-DES sensitivity optimization process is reduced from 1110.15 kW to 856.83 kW (a 22.82 % reduction) and the total annual cost is reduced from 206,744.43 $/Y to 157,726.17 $/Y (a 23.71 % reduction). The total load of the extractive distillation-DES algorithm optimization process is 874.18 kW (a 21.26 % reduction), and the total annual cost is 156,986.01 $/Y (a 24.07 % reduction). • The Deep Eutectic Solvent (DES) was selected over ethylene glycol as a more efficient and eco-friendly extractant. • An Extractive Distillation-DES Basic Process was proposed and optimized via temperature and concentration-composition curves. • After sensitivity analysis and optimization, the Extractive Distillation-DES Sensitivity Optimization Process was devoloped. • The Extractive Distillation-DES Algorithm Optimization Process was developed via particle swarm optimization for parameters. • Both optimized processesdemonstrate superior energy conservation and economy compared with the basic process.

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Journal
Industrial Crops and Products
Published
2025-09-04
DOI
https://doi.org/10.1016/j.indcrop.2025.121853
Primary Topic
Process Optimization and Integration
Type
article
Field-Weighted Citation Impact
0.00

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article

Process simulation and optimization of extractive distillation for separating isopropanol-ethanol from IBE fermentation broth as a gasoline additive

Zeqiu Li, Ying Tian, Chenhao Fang, Xiuhui Huang et al.
Industrial Crops and Products
Process Optimization and Integration
article

Process simulation and optimization of extractive distillation for separating isopropanol-ethanol from IBE fermentation broth as a gasoline additive

Zeqiu Li, Ying Tian, Chenhao Fang, Xiuhui Huang, Yi Jin, Wenkai Yang
article en

Abstract

Addressing the downstream processing challenges of the bio-butanol fermentation broth (Isopropanol-Butanol-Ethanol-Water), and producing the isopropanol-ethanol mixture with a mass fraction of ≥ 0.99975 as a high-quality gasoline additive, is crucial for enhancing the overall economy and sustainability of the bio-butanol production process. To obtain the high-purity isopropanol-ethanol mixture, this paper, based on the dehydration-butanol-extractive four column distillation process, proposes a baseline extractive distillation process using a deep eutectic solvent (DES, glycerol: choline chloride = 2:1) as the extractant, termed the extractive distillation-DES basic process. With heat load as optimization target, the extractive distillation-DES basic process was optimized to determine the optimal operating parameters, termed the extractive distillation-DES sensitivity optimization process. Based on the extractive distillation-DES sensitivity optimization process, the particle swarm optimization algorithm was applied to minimize the total annual cost, resulting in the extractive distillation-DES algorithm optimization process. Compared with the extractive distillation-DES basic process, the total load of the extractive distillation-DES sensitivity optimization process is reduced from 1110.15 kW to 856.83 kW (a 22.82 % reduction) and the total annual cost is reduced from 206,744.43 $/Y to 157,726.17 $/Y (a 23.71 % reduction). The total load of the extractive distillation-DES algorithm optimization process is 874.18 kW (a 21.26 % reduction), and the total annual cost is 156,986.01 $/Y (a 24.07 % reduction). • The Deep Eutectic Solvent (DES) was selected over ethylene glycol as a more efficient and eco-friendly extractant. • An Extractive Distillation-DES Basic Process was proposed and optimized via temperature and concentration-composition curves. • After sensitivity analysis and optimization, the Extractive Distillation-DES Sensitivity Optimization Process was devoloped. • The Extractive Distillation-DES Algorithm Optimization Process was developed via particle swarm optimization for parameters. • Both optimized processesdemonstrate superior energy conservation and economy compared with the basic process.

Industrial Crops and ProductsVol. 236
University of Shanghai for Science and Technology (CN)
National Natural Science Foundation of China
Openalex Percentile: Top 71%
Process Optimization and Integration
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