H, ннннн H3C CH3 H' H H H Acetone 1-hexene TABLE P12-22 Vapor-liquid equilib- rium of acetone(1) + 1-hexene (2) at 101.33 kPa. T[K] X, y, 336.75 331.05 0.060 0.184 327.85 0.116 0.299 326.35 0.184...








Predict the Txy behavior for a mixture of acetone
(1) + 1-hexene (2) at 101.33 kPa using the
Peng-Robinson equation of state. Compare the
predictions to the experimental data given in
Table P12-22. Determine an optimal binary interaction
value by defining an objective function in
terms of the temperature (it can be called OBJ_T).
Is the Peng-Robinson
equation of state a reasonable
model for this system at this state? Please explain.

H,<br>ннннн<br>H3C<br>CH3<br>H'<br>H H H<br>Acetone<br>1-hexene<br>TABLE P12-22 Vapor-liquid equilib-<br>rium of acetone(1) + 1-hexene (2) at<br>101.33 kPa.<br>T[K]<br>X,<br>y,<br>336.75<br>331.05<br>0.060<br>0.184<br>327.85<br>0.116<br>0.299<br>326.35<br>0.184<br>0.365<br>324.65<br>0.287<br>0.441<br>323.85<br>0.387<br>0.500<br>323.35<br>0.497<br>0.555<br>323.25<br>0.593<br>0.605<br>323.25<br>0.605<br>0.605<br>323.45<br>0.698<br>0.658<br>324.15<br>0.805<br>0.730<br>325.95<br>0.908<br>0.838<br>329.55<br>1<br>1<br>Based on data fom S. K. Ogorodnkov, V. B. Kogan and M. S.Nermtsov, J. Appl.Chem. USSR 34,313 (1961).<br>

Extracted text: H, ннннн H3C CH3 H' H H H Acetone 1-hexene TABLE P12-22 Vapor-liquid equilib- rium of acetone(1) + 1-hexene (2) at 101.33 kPa. T[K] X, y, 336.75 331.05 0.060 0.184 327.85 0.116 0.299 326.35 0.184 0.365 324.65 0.287 0.441 323.85 0.387 0.500 323.35 0.497 0.555 323.25 0.593 0.605 323.25 0.605 0.605 323.45 0.698 0.658 324.15 0.805 0.730 325.95 0.908 0.838 329.55 1 1 Based on data fom S. K. Ogorodnkov, V. B. Kogan and M. S.Nermtsov, J. Appl.Chem. USSR 34,313 (1961).

Jun 08, 2022
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