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Equilibrium data are in table 1 For the more volatile component, the feed has a mole fraction of 0.40 with a bottom product of 0.03 and an overhead product of 0.80. Calculate the outlet gas and liquid mole fractions of hydrogen sulfide

Why is this operation not practical The feed is a vapor at its dewpoint. What would an engineer do to develop a practical process

Henry's law constants [h] for h_2s in water

Calculate the outlet gas and liquid mole fracs of hydrogen sulfide What would an engineer do to develop a practical process? Minimum number of theoretical plates and minimum reflur ratio Determine the minimum reflux ratio rm and the minimum number of theoretical plates at tota reflux for the rectification of a mixture of heptane and ethyl benzene as given in prob

Rectification using a partially vaporized feed A total feed of 200. Xilb =0.011 and q line is vertical The vle data for heptane and ethyl.

Mccabe thiele efficiency (wankat 1e, 6d7)we are separating methanol and water in a distillation column with a total condenser and a partial reboiler

Reflux is a saturated liquid, and constant molal overflow can be assumed.

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