Background: Efficient treatment of multi-azeotropic mixtures such as tetrahydrofuran (THF)/methanol (MeOH)/methyl acetate (MeAc) remains a critical challenge. Reactive-extractive distillation (RED) has recently been developed for separating MeOH/MeAc-containing multi-azeotropes, while exhibiting high energy demands for THF-rich feeds.
Methods: Using THF/MeOH/MeAc as a case study, this study proposes a novel intensified separation strategy for MeOH/MeAc-containing multi-azeotropic systems via combining RED, preconcentration, and heat integration (HI). Two baseline processes, three-column reactive-extractive distillation (TCRED) and extractive-reactive distillation (TCERD) are initially developed. By integrating preconcentration columns (IDC) in extractive and solvent recovery sections, TCRED-IDC and TCERD-IDC configurations are respectively proposed. Subsequently, process optimizations are conducted, followed by HI implementation, yielding the final HITCRED-IDC and HITCERD-IDC as process intensification configurations. Finally, key performance evaluation is used to highlight the proposed RED processes.
Significant finding: HITCRED-IDC and HITCERD-IDC demonstrates superior performance over the corresponding baseline processes, achieving 15.9 % and 27.6 % TAC reductions, 28.4 % and 57.8 % exergy efficiency improvements, and 16.5 % and 25.6 % CO₂ emission reductions. Additionally, all proposed configurations outperform recently reported four-column extractive distillation, with 27.4 %–54.5 % TAC reductions, 22.1 %–55.7 % CO₂ emission reductions, and 295 %–753 % exergy efficiency improvement. This work successfully integrates IDC and HI within RED systems for energy-efficient processing of MeOH/MeAc-containing azeotropic mixtures.
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