Design and multi-objective optimization of hybrid extractive distillation process for separating the toluene-methanol-water ternary azeotrope

• Published in: Separation and purification technology 2024-05, Vol.336, p.126335, Article 126335
• Main Authors: Shan, Baoming, Wang, Shangkun, Xu, Qilei, Wang, Yinglong, Cui, Peizhe, Zhang, Fangkun
• Format: Article
• Language: English
• Subjects: Energy-saving; Extractive distillation; Multi-objective optimization; Ternary azeotrope
• ISSN: 1383-5866; 1873-3794
• DOI: 10.1016/j.seppur.2024.126335

[Display omitted] •A efficient and environmentally friendly extractant for separating toluene-methanol-water azeotrope.•Three feasible schemes were designed by changing solvent and optimized by multi-objective genetic algorithm.•The proposed double-column extractive distillation process with a decanter presents superior performance.•The TAC and CO2 emissions were reduced by 33.1 % and 50.5 %, respectively, compared with the existing process. Cleaner production and sustainable development are still hot topics for modern industry. Developing green technology with low energy consumption, low pollution, and low cost has always been the common pursuit of chemical, petroleum, pharmaceutical, and other industries. This article proposes an environmentally friendly and efficient solvent, glycerol, for the separation of the ternary azeotrope of toluene-methanol-water. Three feasible extractive distillation schemes were designed and optimized, while the double-column extractive distillation process with a decanter demonstrated superior performance when glycerol was used as the solvent. Additionally, the multi-objective genetic algorithm was employed to optimize these separation processes and determine the optimal operating conditions, taking total annual cost (TAC), CO2 emissions (ECO2), and separation efficiency (Eext) as target performance indicators to achieve the objectives of energy conservation, consumption reduction, and emission reduction. Results demonstrated that the newly proposed scheme can significantly reduce the total annual cost by up to 33.1 % and CO2 emissions by 50.5 % compared with the existing separation process. This work provides a new insight to separate and purify the multiple systems by extractive distillation in industry.