10.28 Given below are values of GE /J.mol-¹, HE /J.mol-¹, and CE/J.mol-¹.K-¹ for some equimolar binary liquid mixtures at 298.15 K. Estimate values of GE, HE, and SE at 328.15 K for one of the equimolar mixtures by two procedures: (I) Use all the data; (II) Assume CE = 0. Compare and discuss your results for the two procedures. (a) Acetone/chloroform: GE = −622, HE = − 1920, CE = 4.2. == (b) Acetone/n-hexane: GE = 1095, HE = 1595, CF = 3.3. (c) Benzene/isooctane: (d) Chloroform/ethanol: GE = 407, HE = 984, CE = -2.7. GE = 632, HE = -208, CE = 23.0. (e) Ethanol/n-heptane: GE = 1445, HE = 605, C = 11.0. (f) Ethanol/water: G¹ = 734, HE = −416, C² = 11.0. (g) Ethyl acetate/n-heptane: GE = 759, H² = 1465, CE = −8.0.
10.28 Given below are values of GE /J.mol-¹, HE /J.mol-¹, and CE/J.mol-¹.K-¹ for some equimolar binary liquid mixtures at 298.15 K. Estimate values of GE, HE, and SE at 328.15 K for one of the equimolar mixtures by two procedures: (I) Use all the data; (II) Assume CE = 0. Compare and discuss your results for the two procedures. (a) Acetone/chloroform: GE = −622, HE = − 1920, CE = 4.2. == (b) Acetone/n-hexane: GE = 1095, HE = 1595, CF = 3.3. (c) Benzene/isooctane: (d) Chloroform/ethanol: GE = 407, HE = 984, CE = -2.7. GE = 632, HE = -208, CE = 23.0. (e) Ethanol/n-heptane: GE = 1445, HE = 605, C = 11.0. (f) Ethanol/water: G¹ = 734, HE = −416, C² = 11.0. (g) Ethyl acetate/n-heptane: GE = 759, H² = 1465, CE = −8.0.
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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