Page 286 - Distillation theory

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260 Trajectories of the Finite Columns and Their Design Calculation

4. Same for split 1,2:2,3,4 with a) equal and b) optimal shares of the distributed
component in the products.
5. Same as in item 4 for split 1,2,3:3,4.
6. State the feasible splits for the equimolar mixture of acetone(1), benzene(2), chlo-
roform(3), and toluene(4). For each split, determine the necessary tray numbers
and liquid and vapor flow rates in the top and bottom sections of the column at
optimal location of the feed tray and optimal distribution of the component and
reflux excess coefficients and product purities as in item 1.

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