3. The following feed of 100 mol/h at the boiling point and 405.3 kPa pressure is fed to a fractionating tower: n-butane (xA =0.40), n-pentane (xB = 0.25), n-hexane (xC =0.20_ and n- heptane (xD = 0.15). The feed is distilled so that 95% of the n-pentane is recovered in the distillate and 95% of n-hexane in the bottoms. Calculate the following a). Moles per hour and composition of the distillate and bottoms b). The top and bottom temperature of the tower
3. The following feed of 100 mol/h at the boiling point and 405.3 kPa pressure is fed to a fractionating tower: n-butane (xA =0.40), n-pentane (xB = 0.25), n-hexane (xC =0.20_ and n- heptane (xD = 0.15). The feed is distilled so that 95% of the n-pentane is recovered in the distillate and 95% of n-hexane in the bottoms. Calculate the following a). Moles per hour and composition of the distillate and bottoms b). The top and bottom temperature of the tower
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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3. The following feed of 100 mol/h at the boiling point and 405.3 kPa pressure is fed to a fractionating tower: n-butane (xA =0.40), n-pentane (xB = 0.25), n-hexane (xC =0.20_ and n- heptane (xD = 0.15). The feed is distilled so that 95% of the n-pentane is recovered in the distillate and 95% of n-hexane in the bottoms. Calculate the following
a). Moles per hour and composition of the distillate and bottoms b). The top and bottom temperature of the tower
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