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- W2492556215 abstract "Abstract Isoamyl acetate (iAAc) - isoamyl alcohol (iAA) mixture has not been widely studied or reported in the open literature and a complete topological description is still lacking: e.g., its vapor-liquid equilibrium (VLE) data and its azeotropy. VLE experimental data of the mixture was measured in our laboratory at pressures of 50.00, 101.31, 250.00 and 350.00 kPa in a dynamic recirculation cell Fischer Labodest® model 602. It was determined the existence of an azeotrope of minimum boiling point. The data was regressed in order to obtain the adjusted aij parameters for the NTRL model at each system pressure. For the design of the separation strategy of this mixture two different arrangements were proposed: the first corresponds to a pressure swing distillation system that uses two columns, and the second is an extractive distillation system. These two arrangements were simulated in Aspen Plus® platform and an economic assessment of the process through a total annual cost (TAC) and the market price of the iAAc and the iAA were taken into account for the comparison of the two alternatives. It was found that the PSD distillation has better results in terms of TAC than the extractive distillation process." @default.
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- W2492556215 date "2016-01-01" @default.
- W2492556215 modified "2023-09-27" @default.
- W2492556215 title "Conceptual Design for the Separation of a Mixture of Isoamyl Acetate and Isoamyl Alcohol" @default.
- W2492556215 cites W2017773481 @default.
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- W2492556215 doi "https://doi.org/10.1016/b978-0-444-63428-3.50171-5" @default.
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