Develop the feasible product composition regions for the system of Figure 11 10 if the feed is 50 mol chloroform, 25 mol methanol, and 25 mol acetone Chloroform (61 8C) (53 9C) Methanol (64 5C) 1 3 A (65 5C) B (57 6C) D Azeotrope 2 (55 3C) Acetone (56 1C) Figure 11 10 Comparison of residue curves t...

To develop the feasibleproductcomposition regions for the system in Figure 1110 we must first unders ...

Develop the feasible-product-composition regions for the system of Figure 11.10 if the feed is 50 mol% chloroform,

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Develop the feasible-product-composition regions for the system of Figure 11.10 if the feed is 50 mol% chloroform, 25 mol% methanol, and 25 mol% acetone.

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Develop the feasible-product-composition regions for the system of Figure 11.10 if the feed is 50 mol% chloroform,

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Chloroform (61.8°C) (53.9°C) Methanol (64.5°C) 1 3 A (65.5°C) B (57.6°C) D ■ Azeotrope 2 (55.3°C) Acetone (56.1°C) Figure 11.10 Comparison of residue curves to distillation curves. [From Z.T. Fidkowski, M.F. Malone, and M.F. Doherty, AIChE J., 39, 1303 (1993) with permission.]

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Separation Process Principles Chemical And Biochemical Principles

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