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- W2802100032 abstract "The separation of Iso-Propanol-Toluene azeotropic mixture using Acetone as an entrainer has been simulated on Aspen Plus software package using rigorous methods. Calculations of the vapor-liquid equilibrium for the binary system are done using UNIQUAC-RK model which gives a good agreement with the experimental data reported in literature. The effects of the Reflux ratio (RR), distillate-to-feed molar ratio (D/F), feed stage, solvent feed stage, Total no. of stages and solvent feed temperature on the product purities and recoveries are studied to obtain their optimum values that give the maximum purity and recovery of products. The configuration consists of 20 theoretical stages with an equimolar feed of binary mixture. The desired separation of binary mixture has been achieved at the feed stage and an entrainer feeding stage of 15 and 12 respectively with the reflux ratios of 2.5 and 4.0, and D/F ratio of 0.75 and 0.54 respectively in the two columns. The simulation results thus obtained are useful to setup the optimal column configuration of the azeotropic distillation process." @default.
- W2802100032 created "2018-05-17" @default.
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- W2802100032 date "2018-01-01" @default.
- W2802100032 modified "2023-09-26" @default.
- W2802100032 title "Separating Iso-Propanol-Toluene mixture by azeotropic distillation" @default.
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- W2802100032 doi "https://doi.org/10.1063/1.5032351" @default.
- W2802100032 hasPublicationYear "2018" @default.
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