he data in table 10.2 are experimental values of ve for binary liquid mixtures of 1,3-dioxolane(1) and isooctane(2) at 298.15 k and 1(atm). final pdf to printer (a) determine from the data numerical values of parameters a, b, and c in the corre%02lating equation: ve = x1 x2(a + b x1 + cx1 2 ) (b) determine from the results of part (a) the maximum value of ve. at what value of x1 does this occur? (c) determine from the results of part (a) expressions for v¯ 1 e and v¯ 2 e. prepare a plot of these quantities vs. x1, and discuss its features. x1 ve /10−3 cm3·mol−1 0.02715 87.5 0.09329 265.6 0.17490 417.4 0.32760 534.5 0.40244 531.7 0.56689 421.1 0.63128 347.1 0.66233 321.7 0.69984 276.4 0.72792 252.9 0.77514 190.7 0.79243 178.1 0.82954 138.4 0.86835 98.4 0.93287 37.6 0.98233 10.0

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
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the data in table 10.2 are experimental values of ve for binary liquid mixtures of 1,3-dioxolane(1) and isooctane(2) at 298.15 k and 1(atm). final pdf to printer (a) determine from the data numerical values of parameters a, b, and c in the corre%02lating equation: ve = x1 x2(a + b x1 + cx1 2 ) (b) determine from the results of part (a) the maximum value of ve. at what value of x1 does this occur? (c) determine from the results of part (a) expressions for v¯ 1 e and v¯ 2 e. prepare a plot of these quantities vs. x1, and discuss its features. x1 ve /10−3 cm3·mol−1 0.02715 87.5 0.09329 265.6 0.17490 417.4 0.32760 534.5 0.40244 531.7 0.56689 421.1 0.63128 347.1 0.66233 321.7 0.69984 276.4 0.72792 252.9 0.77514 190.7 0.79243 178.1 0.82954 138.4 0.86835 98.4 0.93287 37.6 0.98233 10.0

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