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im data have been reported at 45 °C. X1 c. Calculate molar excess Gibbs energy a y1 0 0000 composition, ft the data to the following equation

im data have been reported at 45 °C. X1 c. Calculate molar excess Gibbs energy a y1 0 0000 composition, ft the data to the following equation

Chemistry
Chemistry
10th Edition
ISBN:9781305957404
Author:Steven S. Zumdahl, Susan A. Zumdahl, Donald J. DeCoste
Publisher:Steven S. Zumdahl, Susan A. Zumdahl, Donald J. DeCoste
Chapter1: Chemical Foundations
Section: Chapter Questions
Problem 1RQ: Define and explain the differences between the following terms. a. law and theory b. theory and...
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3. For a binary mixture of benzene (1) and acetonitrile (2), the following vapor liquid equilibrium data have been reported at 45 °C. Calculate molar excess Gibbs energy as function of Р(bar) 0,2778 0,00 0,0000 composition, fit the data to the following equation and find constant. 0,3022 0,05 0,1243 Gex 0,3351 0,15 0,3542 0,25 0,3725 X1 yi c. a 5 0,2784 | RT = x1X2 > A;(x1 – x2)'-1 i=1 0,3650 0,35 0,4392 d. Calculate fugacity of component in liquid phase at x1=0,25. 0,3715 0,50 0,5182 0,3710 0,60 0,3662 0,70 0,6260 0,5687 0,3554 0,80 0,7002 0,3350 0,90 0,8890 0,2982 1,00 1,0000
Transcribed Image Text:3. For a binary mixture of benzene (1) and acetonitrile (2), the following vapor liquid equilibrium data have been reported at 45 °C. Calculate molar excess Gibbs energy as function of Р(bar) 0,2778 0,00 0,0000 composition, fit the data to the following equation and find constant. 0,3022 0,05 0,1243 Gex 0,3351 0,15 0,3542 0,25 0,3725 X1 yi c. a 5 0,2784 | RT = x1X2 > A;(x1 – x2)'-1 i=1 0,3650 0,35 0,4392 d. Calculate fugacity of component in liquid phase at x1=0,25. 0,3715 0,50 0,5182 0,3710 0,60 0,3662 0,70 0,6260 0,5687 0,3554 0,80 0,7002 0,3350 0,90 0,8890 0,2982 1,00 1,0000
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