Question: Consider the separation by distillation of a chlorination effluent to recover C2H5Cl. The feed is a bubble-point liquid at the column pressure of 240 psia

Consider the separation by distillation of a chlorination effluent to recover C2H5Cl. The feed is a bubble-point liquid at the column pressure of 240 psia with the following composition and K-values for the column conditions:

Component Mole Fraction C;H4 0.05 5.1 0.05 3.8 3.4 - C;H,CI 0.10

Calculate the product distribution, the minimum theoretical stages, the minimum reflux and the theoretical stages at 1.5 times minimum L/D and locate the feed stage. The column is to have a partial condenser and a partial reboiler.

Component Mole Fraction C;H4 0.05 5.1 0.05 3.8 3.4 - C;H,CI 0.10 0.80 0.15 Specifications are: (xp/xa) for C;H$CI = 0.01 (xp/xa) for C;H6 = 75

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Subject Use of the FUG method for the distillation of a chlorination effluent Given Bubblepoint liquid feed with the following composition and average ... View full answer

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