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2. Using the equilibrium diagram below, draw both an arbitrary real op-line for a stripper as well as the corresponding limiting op-line (representing infinite stages) and identify: The real inlet composition (in mol fraction) of the liquid phase. The real outlet composition (in mol fraction) of the liquid phase. The real inlet composition (in mol fraction) of the gas phase. The real outlet composition (in mol fraction) of the gas phase. The slope of the real operating line, L/V.

2. Using the equilibrium diagram below, draw both an arbitrary real op-line for a stripper as well as the corresponding limiting op-line (representing infinite stages) and identify: The real inlet composition (in mol fraction) of the liquid phase. The real outlet composition (in mol fraction) of the liquid phase. The real inlet composition (in mol fraction) of the gas phase. The real outlet composition (in mol fraction) of the gas phase. The slope of the real operating line, L/V.

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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solve for both a stripper and absorber. take the equilibrium data given to just be a y=x line

2. Using the equilibrium diagram below, draw both an arbitrary real op-line for a stripper as well as the corresponding limiting op-line (representing infinite stages) and identify: The real inlet composition (in mol fraction) of the liquid phase. The real outlet composition (in mol fraction) of the liquid phase. The real inlet composition (in mol fraction) of the gas phase. The real outlet composition (in mol fraction) of the gas phase. The slope of the real operating line, L/V.
Transcribed Image Text:2. Using the equilibrium diagram below, draw both an arbitrary real op-line for a stripper as well as the corresponding limiting op-line (representing infinite stages) and identify: The real inlet composition (in mol fraction) of the liquid phase. The real outlet composition (in mol fraction) of the liquid phase. The real inlet composition (in mol fraction) of the gas phase. The real outlet composition (in mol fraction) of the gas phase. The slope of the real operating line, L/V.
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