Using the method of non-linear regression in Excel, prepare a plot of lnγ1, lnγ2, GE/RT and P-x-y diagram showing both the correlated and experimental values. This correlation and plotting procedures shall be executed using Wilson equations.

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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Using the method of non-linear regression in Excel, prepare a plot of lnγ1, lnγ2, GE/RT and P-x-y diagram showing both the correlated and experimental values. This correlation and plotting procedures shall be executed using Wilson equations.

. VLE data for methyl tert-butyl ether(1)/dichloromethane(2) at 308.15 K are as follows:
P/kPa
yi
P/kPa
yi
85.265
0.0000
0.0000
59.651
0.5036
0.3686
83.402
0.0330
0.0141
56.833
0.5749
0.4564
82.202
0.0579
0.0253
53.689
0.6736
0.5882
80.481
0.0924
0.0416
51.620
0.7676
0.7176
76.719
0.1665
0.0804
50.455
0.8476
0.8238
72.422
0.2482
0.1314
49.926
0.9093
0.9002
68.005
0.3322
0.1975
49.720
0.9529
0.9502
65.096
0.3880
0.2457
49.624
1.0000
1.0000
Transcribed Image Text:. VLE data for methyl tert-butyl ether(1)/dichloromethane(2) at 308.15 K are as follows: P/kPa yi P/kPa yi 85.265 0.0000 0.0000 59.651 0.5036 0.3686 83.402 0.0330 0.0141 56.833 0.5749 0.4564 82.202 0.0579 0.0253 53.689 0.6736 0.5882 80.481 0.0924 0.0416 51.620 0.7676 0.7176 76.719 0.1665 0.0804 50.455 0.8476 0.8238 72.422 0.2482 0.1314 49.926 0.9093 0.9002 68.005 0.3322 0.1975 49.720 0.9529 0.9502 65.096 0.3880 0.2457 49.624 1.0000 1.0000
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