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- W2092855549 abstract "The design and synthesis of distillation cascades using side-stream columns with less than N − 1 columns (two or one) for separations of relatively ideal four-component mixtures are studied. Condenser and reboiler heat duties are used to compare operating costs of cascades with less than N − 1 columns to base cases with three columns. A dimensionless volume index, ∑(VjNj/FT), is used to compare capital costs. Quaternary feeds containing four of the five components n-butane, n-pentane, n-hexane, n-heptane, and n-octane were simulated using the commercially available software package Aspen Plus version 11.1. Columns were operated at L/D = 1.15(L/D)min and with optimum feed and product withdrawal locations. For systems with low concentrations of one component in the feed, side-stream cascades often show significantly lower operating and capital costs compared to the base cases. Low purity requirements (sloppy separations) also favor side-stream cascades. Tentative heuristics are developed to predict which cascade will have the lowest energy consumption and capital cost." @default.
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- W2092855549 date "2004-04-02" @default.
- W2092855549 modified "2023-09-26" @default.
- W2092855549 title "Quaternary Distillation Systems with Less than <i>N</i> − 1 Columns" @default.
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- W2092855549 doi "https://doi.org/10.1021/ie030640l" @default.
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