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A solute gas (A) is to be absorbed from an air-A mixture by using pure water in a packed tower at 1 atm. and 300 K. The total liquid flow to the top of tower is 325 kgmol/hr. The total gas flow rate to the bottom of absorption tower is 90 kgmol/hr, and concentration of solute (A) is 5 % by mole. It is necessary to absorb 95 % of solute in air. If the diameter of the tower is 0.8 m, Data: Kya=0,05 kgmol A/s.m2, equilibrium line yA=2.5XA (YA and xA are mole fractions of A.) Calculate (questions 16,17,18,19, and 20), Only one question will appear on the screen. Therefore, the data calculated from throughout the questions can be used in the next questions. You will see case C in every question. Calculate the solute composition of leaving liquid phase

A solute gas (A) is to be absorbed from an air-A mixture by using pure water in a packed tower at 1 atm. and 300 K. The total liquid flow to the top of tower is 325 kgmol/hr. The total gas flow rate to the bottom of absorption tower is 90 kgmol/hr, and concentration of solute (A) is 5 % by mole. It is necessary to absorb 95 % of solute in air. If the diameter of the tower is 0.8 m, Data: Kya=0,05 kgmol A/s.m2, equilibrium line yA=2.5XA (YA and xA are mole fractions of A.) Calculate (questions 16,17,18,19, and 20), Only one question will appear on the screen. Therefore, the data calculated from throughout the questions can be used in the next questions. You will see case C in every question. Calculate the solute composition of leaving liquid phase

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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Case C A solute gas (A) is to be absorbed from an air-A mixture by using pure water in a packed tower at 1 atm. and 300 K. The total liquid flow to the top of tower is 325 kgmol/hr. The total gas flow rate to the bottom of absorption tower is 90 kgmol/hr, and concentration of solute (A) is 5 % by mole. It is necessary to absorb 95 % of solute in air. If the diameter of the tower is 0.8 m, Data: Kya=0,05 kgmol A/s.m, equilibrium line yA=2.5XA (YA and XA are mole fractions of A.) Calculate (questions 16,17,18,19, and 20), Only one question will appear on the screen. Therefore, the data calculated from throughout the questions can be used in the next questions. You will see case C in every question. Calculate the solute composition of leaving liquid phase Lütfen birini seçin: a. 0.00262 b. 0.0201 c. 0.0325 d. 0.0125
Transcribed Image Text:Case C A solute gas (A) is to be absorbed from an air-A mixture by using pure water in a packed tower at 1 atm. and 300 K. The total liquid flow to the top of tower is 325 kgmol/hr. The total gas flow rate to the bottom of absorption tower is 90 kgmol/hr, and concentration of solute (A) is 5 % by mole. It is necessary to absorb 95 % of solute in air. If the diameter of the tower is 0.8 m, Data: Kya=0,05 kgmol A/s.m, equilibrium line yA=2.5XA (YA and XA are mole fractions of A.) Calculate (questions 16,17,18,19, and 20), Only one question will appear on the screen. Therefore, the data calculated from throughout the questions can be used in the next questions. You will see case C in every question. Calculate the solute composition of leaving liquid phase Lütfen birini seçin: a. 0.00262 b. 0.0201 c. 0.0325 d. 0.0125
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