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V1 Vapor 90 90 bpB 80 80 L2 70 70 V3 Liquid L3 60 60 50 L5 V5 L4 50 100% A 80 60 40 20 0% 0% 20 40 60 80 100% B Figure 15.3 Phase diagram for a fractional distillation of an ideal two-component system. Temperature (°C)

V1 Vapor 90 90 bpB 80 80 L2 70 70 V3 Liquid L3 60 60 50 L5 V5 L4 50 100% A 80 60 40 20 0% 0% 20 40 60 80 100% B Figure 15.3 Phase diagram for a fractional distillation of an ideal two-component system. Temperature (°C)

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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2. Estimate how many theoretical plates are needed to separate a mixture that has a mole fraction of B equal to 0.70 (70% B) in Figure 15.3.
Transcribed Image Text:2. Estimate how many theoretical plates are needed to separate a mixture that has a mole fraction of B equal to 0.70 (70% B) in Figure 15.3.
V1 Vapor 90 bpB 90 80 80 L2 70 70 V3 Liquid L3 60 60 50 L5 V5 L4 50 20 80 100% A 80 60 40 0% 0% 20 40 60 100% B Figure 15.3 Phase diagram for a fractional distillation of an ideal two-component system. Temperature (°C)
Transcribed Image Text:V1 Vapor 90 bpB 90 80 80 L2 70 70 V3 Liquid L3 60 60 50 L5 V5 L4 50 20 80 100% A 80 60 40 0% 0% 20 40 60 100% B Figure 15.3 Phase diagram for a fractional distillation of an ideal two-component system. Temperature (°C)
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