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
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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