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Methyl acetate (1) / methanol (2) system Determine: 1. Bubble P, given T = 348.15 K, x₁ = 0.3 2. Dew P, given T = 348.15 K, y₁ = 0.43 3. Bubble T, given P = 0.35 bar, x₁ = 0.3 4. Dew T, given P = 0.35 bar, y₁ = 0.35 bar, y₁ = 0.5179 5. Flash, given P = 2.0 bar, T = 348.15 K, Z₁ = 0.35

Methyl acetate (1) / methanol (2) system Determine: 1. Bubble P, given T = 348.15 K, x₁ = 0.3 2. Dew P, given T = 348.15 K, y₁ = 0.43 3. Bubble T, given P = 0.35 bar, x₁ = 0.3 4. Dew T, given P = 0.35 bar, y₁ = 0.35 bar, y₁ = 0.5179 5. Flash, given P = 2.0 bar, T = 348.15 K, Z₁ = 0.35

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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Methyl acetate (1)/ methanol (2) system Determine: 1. Bubble P, given T = 348.15 K, x₁ = 0.3 2. Dew P, given T = 348.15 K, y₁ = 0.43 3. Bubble T, given P 0.35 bar, x₁ = 0.3 4. Dew T, given P = 0.35 bar, y₁ = 0.5179 5. Flash, given P = 2.0 bar, T = 348.15 K, 348.15 K, Z₁ = 0.35
Transcribed Image Text:Methyl acetate (1)/ methanol (2) system Determine: 1. Bubble P, given T = 348.15 K, x₁ = 0.3 2. Dew P, given T = 348.15 K, y₁ = 0.43 3. Bubble T, given P 0.35 bar, x₁ = 0.3 4. Dew T, given P = 0.35 bar, y₁ = 0.5179 5. Flash, given P = 2.0 bar, T = 348.15 K, 348.15 K, Z₁ = 0.35
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