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0.0570 0.1295 0.1848 99.811 99.950 0332 77.524 0.0858 0.6605 0.6926 0.7124 0.7383 78.951 0.1046 0.1452 0.2190 100.278 0.6945 82.528 0.2694 0.3633 0.4184 100.467 0.7327 0.7752 86.762 0.2173 0.2787 100.999 101.059 99.877 99.799 96.885 0.7729 0.7876 90.088 0.7922 93.206 0.3579 0.4050 0.4779 0.5135 0.5512 0.9080 0.8959 95.017 0.9448 0.9336 96.365 0.4480 1.0000 1.0000 GE :(as a function of x1) based on the data set. a. Calculate y1, Y2, and · b. Fit the van Laar equation to the VLE data. c. Plot ln y1, In y2, and - d. Prepare a P-x-y diagram that shows both the data and model. X1X2 RT GE as function of x1 for both the data and model.

0.0570 0.1295 0.1848 99.811 99.950 0332 77.524 0.0858 0.6605 0.6926 0.7124 0.7383 78.951 0.1046 0.1452 0.2190 100.278 0.6945 82.528 0.2694 0.3633 0.4184 100.467 0.7327 0.7752 86.762 0.2173 0.2787 100.999 101.059 99.877 99.799 96.885 0.7729 0.7876 90.088 0.7922 93.206 0.3579 0.4050 0.4779 0.5135 0.5512 0.9080 0.8959 95.017 0.9448 0.9336 96.365 0.4480 1.0000 1.0000 GE :(as a function of x1) based on the data set. a. Calculate y1, Y2, and · b. Fit the van Laar equation to the VLE data. c. Plot ln y1, In y2, and - d. Prepare a P-x-y diagram that shows both the data and model. X1X2 RT GE as function of x1 for both the data and model.

Introduction to Chemical Engineering Thermodynamics
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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The following data is for the system acetone (1) / methanol (2) at 55 °C. P (kPa) P (kPa) X1 0.0000 yı 0.0000 68.728 97.646 0.5052 0.5844 72.278 0.0287 0.0647 98.462 0.5432 0.6174 75.279 0.0570 0.1295 99.811 0.6332 0.6772 77.524 0.0858 0.1848 99.950 0.6605 0.6926 78.951 0.1046 0.2190 100.278 0.6945 0.7124 82.528 0.1452 0.2694 100.467 0.7327 0.7383 86.762 0.2173 0.3633 100.999 0.7752 0.7729 90.088 0.2787 0.4184 101.059 0.7922 0.7876 93.206 0.4779 0.8959 0.3579 0.4050 99.877 0.9080 95.017 0.5135 99.799 0.9448 0.9336 96.365 0.4480 0.5512 96.885 1.0000 1.0000 a. Calculate y1, Y2, and GE :(as a function of x1) based on the data set. X1X2RT b. Fit the van Laar equation to the VLE data. c. Plot In y1, In Y 2, and GE as function of x1 for both the data and model. X,X2RT d. Prepare a P-x-y diagram that shows both the data and model.
Transcribed Image Text:The following data is for the system acetone (1) / methanol (2) at 55 °C. P (kPa) P (kPa) X1 0.0000 yı 0.0000 68.728 97.646 0.5052 0.5844 72.278 0.0287 0.0647 98.462 0.5432 0.6174 75.279 0.0570 0.1295 99.811 0.6332 0.6772 77.524 0.0858 0.1848 99.950 0.6605 0.6926 78.951 0.1046 0.2190 100.278 0.6945 0.7124 82.528 0.1452 0.2694 100.467 0.7327 0.7383 86.762 0.2173 0.3633 100.999 0.7752 0.7729 90.088 0.2787 0.4184 101.059 0.7922 0.7876 93.206 0.4779 0.8959 0.3579 0.4050 99.877 0.9080 95.017 0.5135 99.799 0.9448 0.9336 96.365 0.4480 0.5512 96.885 1.0000 1.0000 a. Calculate y1, Y2, and GE :(as a function of x1) based on the data set. X1X2RT b. Fit the van Laar equation to the VLE data. c. Plot In y1, In Y 2, and GE as function of x1 for both the data and model. X,X2RT d. Prepare a P-x-y diagram that shows both the data and model.
e. Conduct an error analysis using the residual method and integral method.
Transcribed Image Text:e. Conduct an error analysis using the residual method and integral method.
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