A binary distillation is performed so that a distillate 94% and bottoms 8% in of the more volatile Component A. The column operates with a 600 kgmoles/hr of feed consisting that is 40% Component A and 60% Component B. The rectification, stripping and q-lines are all provided on the x-y diagram below. Several specific points on the figure are also indicated for convenience. Y, Mole Fraction 1.00 0.90 0.80 0.70 0.60 0.50 0.40 0.30 0.20 0.188 " 0.30 10.00 cno 0.10 (0.169, 0.323) 0.20 (0.169, 0.32) 0.30 0.40 050 , Mole Fraction 0.60
A binary distillation is performed so that a distillate 94% and bottoms 8% in of the more volatile Component A. The column operates with a 600 kgmoles/hr of feed consisting that is 40% Component A and 60% Component B. The rectification, stripping and q-lines are all provided on the x-y diagram below. Several specific points on the figure are also indicated for convenience. Y, Mole Fraction 1.00 0.90 0.80 0.70 0.60 0.50 0.40 0.30 0.20 0.188 " 0.30 10.00 cno 0.10 (0.169, 0.323) 0.20 (0.169, 0.32) 0.30 0.40 050 , Mole Fraction 0.60
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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