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Separation Process Engineering: Includes Mass Transfer Analysis, Third Edition by Phillip C. Wankat

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C. Deriviations

C1. Derive the relationships among the different NTU terms for binary distillation.

C2. Derive Eq. (16-94).

C3. Derive the following equation to determine nOG for distillation at total reflux for systems with constant relative volatility:

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C4. If a mixer-settler is used for an extraction, we can often estimate the stage efficiency of the mixer EMD and of the settler ESD separately (see Example 16-5 and Problem 16.D21) where,

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Of course, we are really most interested in the overall stage efficiency of the mixer-settler combination ...

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