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3) In a tower 2 components, named as A and B, are present. The components are mutually present both in the gas and liquid phases. Component A, which is the solute, diffuses from the gas phase to the liquid phase. Component B, on the other hand, is the non-diffusing stagnant component. At a certain location in the tower, the bulk concentration of A in the gas phase is 45% by mole; and the bulk concentration of A in the liquid phase is 5% by mole. The film mass-transfer coefficients in the gas phase and the liquid phase are calculated as 1.465 x 103 kg mol A/s.m².mol frac. and 1.967 x 103 kg mol A/s.m².mol frac., respectively. Considering the given information, please calculate the interface concentration and the flux of A by using both liquid and gas phase equations. YA 0.00 0.02 0.05 0.09 0.13 0.18 0.25 0.37 0.53 0.72 ХА 0.00 0.05 0.10 0.15 0.20 0.25 0.30 0.35 0.40 0.45

3) In a tower 2 components, named as A and B, are present. The components are mutually present both in the gas and liquid phases. Component A, which is the solute, diffuses from the gas phase to the liquid phase. Component B, on the other hand, is the non-diffusing stagnant component. At a certain location in the tower, the bulk concentration of A in the gas phase is 45% by mole; and the bulk concentration of A in the liquid phase is 5% by mole. The film mass-transfer coefficients in the gas phase and the liquid phase are calculated as 1.465 x 103 kg mol A/s.m².mol frac. and 1.967 x 103 kg mol A/s.m².mol frac., respectively. Considering the given information, please calculate the interface concentration and the flux of A by using both liquid and gas phase equations. YA 0.00 0.02 0.05 0.09 0.13 0.18 0.25 0.37 0.53 0.72 ХА 0.00 0.05 0.10 0.15 0.20 0.25 0.30 0.35 0.40 0.45

Introduction to Chemical Engineering Thermodynamics
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) In a tower 2 components, named as A and B, are present. The components are mutually present both in the gas and liquid phases. Component A, which is the solute, diffuses from the gas phase to the liquid phase. Component B, on the other hand, is the non-diffusing stagnant component. At a certain location in the tower, the bulk concentration of A in the gas phase is 45% by mole; and the bulk concentration of A in the liquid phase is 5% by mole. The film mass-transfer coefficients in the gas phase and the liquid phase are calculated as 1.465 x 103 kg mol A/s.m?.mol frac. and 1.967 x 103 kg mol A/s.m².mol frac., respectively. Considering the given information, please calculate the interface concentration and the flux of A by using both liquid and gas phase equations. YA 0.00 0.02 0.05 0.09 0.13 0.18 0.25 0.37 0.53 0.72 XA 0.00 0.05 0.10 0.15 0.20 0.25 0.30 0.35 0.40 0.45
Transcribed Image Text:3) In a tower 2 components, named as A and B, are present. The components are mutually present both in the gas and liquid phases. Component A, which is the solute, diffuses from the gas phase to the liquid phase. Component B, on the other hand, is the non-diffusing stagnant component. At a certain location in the tower, the bulk concentration of A in the gas phase is 45% by mole; and the bulk concentration of A in the liquid phase is 5% by mole. The film mass-transfer coefficients in the gas phase and the liquid phase are calculated as 1.465 x 103 kg mol A/s.m?.mol frac. and 1.967 x 103 kg mol A/s.m².mol frac., respectively. Considering the given information, please calculate the interface concentration and the flux of A by using both liquid and gas phase equations. YA 0.00 0.02 0.05 0.09 0.13 0.18 0.25 0.37 0.53 0.72 XA 0.00 0.05 0.10 0.15 0.20 0.25 0.30 0.35 0.40 0.45
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