7.14. Calculation of products. A mixture of 54.5 mol% benzene in chlorobenzene at its bubble point is fed continuously to the bottom stage of a column containing two equilibrium stages, with a partial reboiler and a total condenser. Sufficient heat is supplied to the reboiler to give V/F = 0.855, and the reflux ratio LD in the top of the column is constant at 0.50. Under these conditions using the equilibrium data in the table, what are the compositions of the expected products? x EQUILIBRIUM DATA AT COLUMN PRESSURE, MOLE-FRACTION BENZENE: 0.100 0.200 0.300 0.300 0.400 0.500 0.600 0.600 0.700 0.800 y 0.314 0.508 0.640 0.734 0.806 0.862 0.905 0.943
7.14. Calculation of products. A mixture of 54.5 mol% benzene in chlorobenzene at its bubble point is fed continuously to the bottom stage of a column containing two equilibrium stages, with a partial reboiler and a total condenser. Sufficient heat is supplied to the reboiler to give V/F = 0.855, and the reflux ratio LD in the top of the column is constant at 0.50. Under these conditions using the equilibrium data in the table, what are the compositions of the expected products? x EQUILIBRIUM DATA AT COLUMN PRESSURE, MOLE-FRACTION BENZENE: 0.100 0.200 0.300 0.300 0.400 0.500 0.600 0.600 0.700 0.800 y 0.314 0.508 0.640 0.734 0.806 0.862 0.905 0.943
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
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