Equilibrium Stage Contact for Gas-Liquid System. A gas mixture at 2.026 × 105 Pa total pressure containing air and SO2 is contacted in a single-stage equilibrium mixer with pure water at 293 K. The partial pressure of SO, in the original gas is 1.52 x 10 Pa. The inlet gas contains 5.70 total kg mol and the inlet water 2.20 total kg mol. The exit gas and liquid leaving are in equilibrium. Calculate the amounts and compositions of the outlet phases. Use equilibrium data from Fig. 10.2-1. equil: PA(partial pressure of S02 in the vapor) = 29.6 xд(mole fraction of S02 in liquid)
Equilibrium Stage Contact for Gas-Liquid System. A gas mixture at 2.026 × 105 Pa total pressure containing air and SO2 is contacted in a single-stage equilibrium mixer with pure water at 293 K. The partial pressure of SO, in the original gas is 1.52 x 10 Pa. The inlet gas contains 5.70 total kg mol and the inlet water 2.20 total kg mol. The exit gas and liquid leaving are in equilibrium. Calculate the amounts and compositions of the outlet phases. Use equilibrium data from Fig. 10.2-1. equil: PA(partial pressure of S02 in the vapor) = 29.6 xд(mole fraction of S02 in liquid)
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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Transcribed Image Text:Equilibrium Stage Contact for Gas-Liquid System. A gas mixture at 2.026
× 105 Pa total pressure containing air and SO2 is contacted in a single-stage
equilibrium mixer with pure water at 293 K. The partial pressure of SO, in the
original gas is 1.52 x 10 Pa. The inlet gas contains 5.70 total kg mol and the
inlet water 2.20 total kg mol. The exit gas and liquid leaving are in equilibrium.
Calculate the amounts and compositions of the outlet phases. Use equilibrium
data from Fig. 10.2-1.
equil: PA(partial pressure of S02 in the vapor) = 29.6 xд(mole fraction of S02 in liquid)
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