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- W2348351722 abstract "Adopting UNIFAC equation,the extractive distillation separation process of benzene-cyclohexane mixture is simulated and optimized by PRO/Ⅱ.Important process parameters,such as the type,flowrate,temperature and the feed tray of the solvent,the temperature and the feed tray of the benzene-cyclohexane feed,are all optimized to a better separating effect.It concludes that,the separation achieves the best when the solvent is used about twice the flowrate than the benzene-cyclohexane mixture,feeding on the seventh tray at 298.15℃,the mixture is feeded on the twenty-fifth tray at 353.85℃,the number of the theoretical plate of T1 is 35 and the number of the theoretical plate of T2 is 10. In that condition,the purity of the product of cyclohexane is improved to 0.9953,benzene is improved to 0.9890 and the recycle of the furfural is to 0.9985." @default.
- W2348351722 created "2016-06-24" @default.
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- W2348351722 date "2010-01-01" @default.
- W2348351722 modified "2023-09-28" @default.
- W2348351722 title "Simulation and Optimization Study on Extractive Distillation of Benzene-Cyclohexane" @default.
- W2348351722 hasPublicationYear "2010" @default.
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