4.10. Continuous, single-stage distillation. Saturated-liquid feed of F = 40 mol/h, containing 50 mol% A and B, is supplied to the apparatus in Figure 4.23. The condensate is split so that reflux/distillate = 1. (a) If heat is supplied such that W = 30 mol/h and α = 2, as defined below, what will be the composition of the overhead and the bot- toms product? PS απ Α = PB YAXB YBXA (b) If the operation is changed so that no condensate is returned to the still pot and W = 3D, compute the product compositions. Vapor V Condenser Still pot Feed F Distillate Reflux R D Heat Bottoms W
4.10. Continuous, single-stage distillation. Saturated-liquid feed of F = 40 mol/h, containing 50 mol% A and B, is supplied to the apparatus in Figure 4.23. The condensate is split so that reflux/distillate = 1. (a) If heat is supplied such that W = 30 mol/h and α = 2, as defined below, what will be the composition of the overhead and the bot- toms product? PS απ Α = PB YAXB YBXA (b) If the operation is changed so that no condensate is returned to the still pot and W = 3D, compute the product compositions. Vapor V Condenser Still pot Feed F Distillate Reflux R D Heat Bottoms W
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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