Publication | Open Access
Optimal Design and Effective Control of Triple-Column Extractive Distillation for Separating Ethyl Acetate/Ethanol/Water with Multiazeotrope
156
Citations
53
References
2019
Year
Process IntegrationSolvent ExtractionEngineeringEnergy EfficiencyEnergy ConversionEthyl Acetate/ethanol/waterChemical Engineering SeparationsDistillation BoundaryChemical EngineeringSeparation ScienceTriple-column Extractive DistillationWater TreatmentSeparation TechniqueAdvanced SeparationChromatographyProcess DesignSeparation TechnologyOptimal DesignProcess IntensificationEnvironmental EngineeringProcess ControlFuel ProductionSustainable ProductionDistillationTernary Extractive Distillation
Separating the ternary nonideal EtAC/EtOH/water system is critical because it arises in n‑butanol synthesis from ethanol and is hindered by multiazeotrope formation and distillation boundaries. The study proposes a systematic conceptual design, optimization, and control approach for ternary extractive distillation of EtAC/EtOH/water multiazeotrope mixtures. The approach includes entrainer screening, conceptual design, global optimization, process evaluation, and a robust control strategy. Optimization shows that the proposed triple‑column extractive distillation markedly reduces annual cost, exergy loss, and CO₂ emissions versus existing processes, and dynamic simulations confirm that the dual‑temperature and feedforward control strategy maintains product purities under feed flow and composition disturbances.
The separation of the ternary nonideal system ethyl acetate (EtAC)/ethanol (EtOH)/water with multiazeotropes is very important since they are always generated in the production process of n-butanol synthesis from ethanol, which is much more difficult due to the formation of the multiazeotrope and distillation boundary. Herein, a systematic conceptual design, optimization, and control approach for ternary extractive distillation of multiazeotrope mixtures EtAC/EtOH/water is proposed. The procedure involves entrainer screening, conceptual design, global optimization, process evaluation, and a robust control strategy. The optimization results demonstrate that the total annual cost, exergy loss, and carbon dioxide emissions of the proposed triple-column extractive distillation are significantly reduced compared with those of the existing process. Dynamic performances illustrate that the improved dual temperature and feedforward control strategy can well handle the three product purities, while two kinds of disturbances (i.e., feed flow rate and composition) are introduced.
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