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A liquid feed of 100kmol/hr is fed to a distillation tower operating at 405.3 kPa. The composition in mole fractions is as follows: n-butane (xA = 0.40), n-pentane (xB = 0.25), n-hexane (xc = 0.20), n-heptane (xD = 0.15).the feed is fractionioned such that 90% of pentane is to be recovered in the distillate and 90% of hexane is recovered in the bottoms  what are the vapor and liquid flow rates of the resulting stream

A liquid feed of 100kmol/hr is fed to a distillation tower operating at 405.3 kPa. The composition in mole fractions is as follows: n-butane (xA = 0.40), n-pentane (xB = 0.25), n-hexane (xc = 0.20), n-heptane (xD = 0.15).the feed is fractionioned such that 90% of pentane is to be recovered in the distillate and 90% of hexane is recovered in the bottoms  what are the vapor and liquid flow rates of the resulting stream

Introduction to Chemical Engineering Thermodynamics
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 liquid feed of 100kmol/hr is fed to a distillation tower operating at 405.3 kPa. The composition in mole fractions is as follows: n-butane (xA = 0.40), n-pentane (xB = 0.25), n-hexane (xc = 0.20), n-heptane (xD = 0.15).the feed is fractionioned such that 90% of pentane is to be recovered in the distillate and 90% of hexane is recovered in the bottoms 

what are the vapor and liquid flow rates of the resulting streams 

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