An experiment on vapor-liquid equilibrium for methanol (1 and dimethylcarbonate (2) system at 337 K provides the following information. X1=0 y1=0 P=41.02 kPa X1=0.2 y1=0.51 P=68.23 kPa X1=1.0 y1=1.0 P=99.91 kPa Use this information to estimate the system press Vapor phase mole fraction when x, =0.1 Hint: The compounds do not have similar chemical structure a. 83 kPa; 0.65 O b. 45 kPa; 0.22 OC. 55 kPa: 0.32 65 kPa: 0.24

Introduction to Chemical Engineering Thermodynamics
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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Soru 3
An experiment on vapor-liquid equilibrium for methanol (1) and dimethylcarbonate (2) system at 337 K provides the following
information.
X1=0 y1=0 P=41.02 kPa
X1=0.2 y1=0.51 P368.23 kPa
X1=1.0 y1=1.0 P=99.91 kPa
Use this information to estimate the system presSu
Vapor phase mole fraction when x- =0.1
Hint: The compounds do not have similar chemical str
O a.
83 kPa; 0.65
O b.
45 kPa; 0.22
c.
55 kPa; 0.32
d.
65 kPa: 0.24
Transcribed Image Text:Soru 3 An experiment on vapor-liquid equilibrium for methanol (1) and dimethylcarbonate (2) system at 337 K provides the following information. X1=0 y1=0 P=41.02 kPa X1=0.2 y1=0.51 P368.23 kPa X1=1.0 y1=1.0 P=99.91 kPa Use this information to estimate the system presSu Vapor phase mole fraction when x- =0.1 Hint: The compounds do not have similar chemical str O a. 83 kPa; 0.65 O b. 45 kPa; 0.22 c. 55 kPa; 0.32 d. 65 kPa: 0.24
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