Question: The stripping section operating line for a binary distillation problem y = 1 . 4 x - 0 . 0 2 . The relative volatility

The stripping section operating line for a binary distillation problem y=1.4x-0.02. The relative volatility is a 2.6. On a particular tray the liquid composition is x=0. What is the composition of the vapour leaving the tray if the Murphree tray efficiency is 0.7? bs afor
The stripping section operating line for a binary distillation problem y=1.4x-0.02.

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