A 100 Ibmol/h gas stream consisting of 35 mol% ammonia (NH3) and air is scrubbed with water to make a 5 mol% liquid product stream The temperature of the absorber is 80 °F, and the pressure is 14.7 psia (1 atm). The diagram below shows the unit operation which is a single equilibrium stage. Perform a DOF to show that the system is solvable, and calculate the flow rates and compositions of all streams. Equilibrium data is provided in the Table below. Vapor pressure NH3 (5 mol% in water, T- 80 °F). Vapor pressure water (T = 80 °F) 37.2 mmHg 26.2 mmHg vapor outlet Air! water-2 Variables Stream system Constraints Flow Composition Performance Material Balances 3 그 T= 80 °F P= 14.7 psia Absorber NHs, AiR Total Total ,=100 Ibmol/h Yoea=0.35 -1 iquid outlet wH3, H2O Xeg=0.05 Oz
A 100 Ibmol/h gas stream consisting of 35 mol% ammonia (NH3) and air is scrubbed with water to make a 5 mol% liquid product stream The temperature of the absorber is 80 °F, and the pressure is 14.7 psia (1 atm). The diagram below shows the unit operation which is a single equilibrium stage. Perform a DOF to show that the system is solvable, and calculate the flow rates and compositions of all streams. Equilibrium data is provided in the Table below. Vapor pressure NH3 (5 mol% in water, T- 80 °F). Vapor pressure water (T = 80 °F) 37.2 mmHg 26.2 mmHg vapor outlet Air! water-2 Variables Stream system Constraints Flow Composition Performance Material Balances 3 그 T= 80 °F P= 14.7 psia Absorber NHs, AiR Total Total ,=100 Ibmol/h Yoea=0.35 -1 iquid outlet wH3, H2O Xeg=0.05 Oz
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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