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.
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
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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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.
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