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methanol by using wa Tower has a packed bed tower air sectional area of 0.2 m? and system operates at 313.1 K and 101.32 kPa. The inlet a contains 10 mol% methanol and at outlet the concentration of methanol drops to 2 mol9 The gas flow is 20 kg mol inert air/h. The pure inlet flow is 50 kg mol water/h. Filr coefficients for the given flows in the tower are k',a= 0.07 kg mol/s.m.mol frac and k',a 0.04 kg mol/s.m³.mol frac. Equilibrium data is given below. Calculate the tower height. Equilibrium data for methanol-water system at 313.1 K Mole fraction Methanol Partial in Liquid, xA of pressure methanol in vapor pA (mmHg) 0.05 25.0 0.10 46.0 0.15 66.5

methanol by using wa Tower has a packed bed tower air sectional area of 0.2 m? and system operates at 313.1 K and 101.32 kPa. The inlet a contains 10 mol% methanol and at outlet the concentration of methanol drops to 2 mol9 The gas flow is 20 kg mol inert air/h. The pure inlet flow is 50 kg mol water/h. Filr coefficients for the given flows in the tower are k',a= 0.07 kg mol/s.m.mol frac and k',a 0.04 kg mol/s.m³.mol frac. Equilibrium data is given below. Calculate the tower height. Equilibrium data for methanol-water system at 313.1 K Mole fraction Methanol Partial in Liquid, xA of pressure methanol in vapor pA (mmHg) 0.05 25.0 0.10 46.0 0.15 66.5

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
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In a packed bed tower air is purified from methanol by using water. Tower has a cross sectional area of 0.2 m? and system operates at 313.1 K and 101.32 kPa. The inlet air contains 10 mol% methanol and at outlet the concentration of methanol drops to 2 mol%. The gas flow is 20 kg mol inert air/h. The pure inlet flow is 50 kg mol water/h. Film coefficients for the given flows in the tower are k',a= 0.07 kg mol/s.m³.mol frac and k',a= 0.04 kg mol/s.m³.mol frac. Equilibrium data is given below. Calculate the tower height. Equilibrium data for methanol-water system at 313.1 K Mole fraction Methanol Partial pressure of in Liquid, xA methanol in vapor pA (mmHg) 0.05 25.0 0.10 46.0 0.15 66.5
Transcribed Image Text:In a packed bed tower air is purified from methanol by using water. Tower has a cross sectional area of 0.2 m? and system operates at 313.1 K and 101.32 kPa. The inlet air contains 10 mol% methanol and at outlet the concentration of methanol drops to 2 mol%. The gas flow is 20 kg mol inert air/h. The pure inlet flow is 50 kg mol water/h. Film coefficients for the given flows in the tower are k',a= 0.07 kg mol/s.m³.mol frac and k',a= 0.04 kg mol/s.m³.mol frac. Equilibrium data is given below. Calculate the tower height. Equilibrium data for methanol-water system at 313.1 K Mole fraction Methanol Partial pressure of in Liquid, xA methanol in vapor pA (mmHg) 0.05 25.0 0.10 46.0 0.15 66.5
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