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- W2021586476 abstract "The process to produce TAME via reactive distillation requires a methanol-recovery section because the presence of C5/methanol azeotropes means that a significant amount of methanol is present in the distillate from the reactive column. The use of pressure-swing azeotropic distillation and extractive distillation were studied in a previous paper in which both the steady-state design and the plantwide control of the entire process were developed. This paper considers a third alternative flowsheet for the separation of the C5/methanol azeotropes that takes advantage of the heterogeneity of the azeotrope. Two stripping columns and a decanter are used. The total annual cost of this flowsheet is a factor of 4 less than that of the pressure-swing system. The system is demonstrated to be easy to control by controlling a tray temperature in each stripping column." @default.
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- W2021586476 date "2009-09-15" @default.
- W2021586476 modified "2023-10-18" @default.
- W2021586476 title "Two-Stripper/Decanter Flowsheet for Methanol Recovery in the TAME Reactive-Distillation Process" @default.
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- W2021586476 doi "https://doi.org/10.1021/ie900670f" @default.
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