A 2000 kmol/h of an ethanol-propanol mixture containing 65 mole percent ethanol is to be separated in a continuous plate column operating at 1.2 atm total pressure. The desired terminal composition in terms of mole fraction of ethanol is xD =0.92 and xW = 0.07. The feed is saturated liquid. Reflux ratio is 4. Relative volatility of ethanol propanol system may be taken as 2.1. Find the actual number of theoretical plates required for the each of the section of the column to attain the required separation.

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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A 2000 kmol/h of an ethanol-propanol mixture containing 65 mole percent ethanol is to be separated in a continuous plate column operating at 1.2 atm total pressure. The desired terminal composition in terms of mole fraction of ethanol is xD =0.92 and xW = 0.07. The feed is saturated liquid. Reflux ratio is 4. Relative volatility of ethanol propanol system may be taken as 2.1. Find the actual number of theoretical plates required for the each of the section of the column to attain the required separation.
propanol mixture containing
65 mole percent ethanol is to
be separated in a continuous
plate column operating at 1.2
atm total pressure. The
desired terminal composition
in terms of mole fraction of
ethanol is xp =0.92 and xw =
0.07. The feed is saturated
liquid. Reflux ratio is 4. Relative
volatility of ethanol propanol
system may be taken as 2.1.
Find the actual number of
theoretical plates required for
the each of the section of the
column to attain the required
separation.
Transcribed Image Text:propanol mixture containing 65 mole percent ethanol is to be separated in a continuous plate column operating at 1.2 atm total pressure. The desired terminal composition in terms of mole fraction of ethanol is xp =0.92 and xw = 0.07. The feed is saturated liquid. Reflux ratio is 4. Relative volatility of ethanol propanol system may be taken as 2.1. Find the actual number of theoretical plates required for the each of the section of the column to attain the required separation.
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