300 F 280 F 260 F 30 Saturated vapor 20 Saturated liquid 10 140 F 120°F 100 F P-1 atm 1.0 0.8 0.6 0.2 Mole fraction of a-hexane, x Of y 0.4 Enthalpy. Btulbmolx 10 220 F .081 4. 09 3. 007

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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Figure shows  an enthalpy-concentration diagram for n-hexan(H), and n-octane (O) at 101 kPa. Use this diagram to determine the: (a) mole-fraction composition of the vapor when a liquid containing 30 mol% H is heated from Point A to the bubble-point temperature at Point B; (b) energy required to vaporize 60 mol% of amixture initially at 100oF and containing 20 mol% H (Point G); and (c) compositions of the equilibrium vapor and liquid resulting from part (b).

300 F
280 F
260 F
30
Saturated vapor
20
Saturated liquid
10
140 F
120°F
100 F
P-1 atm
1.0
0.8
0.6
0.2
Mole fraction of a-hexane, x Of y
0.4
Enthalpy. Btulbmolx 10
220 F
.081
4. 09
3. 007
Transcribed Image Text:300 F 280 F 260 F 30 Saturated vapor 20 Saturated liquid 10 140 F 120°F 100 F P-1 atm 1.0 0.8 0.6 0.2 Mole fraction of a-hexane, x Of y 0.4 Enthalpy. Btulbmolx 10 220 F .081 4. 09 3. 007
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