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A liq mixture of benzene-toluene is to be distilled in a fractionating tower at 101.3 kPa...

A liq mixture of benzene-toluene is to be distilled in a fractionating tower at 101.3 kPa pressure. The feed of 100 kg mol/h is liquid and it contains 45 mole % benzene and 55 mole % toluene and enters at 327.6 K (130 ◦F). A distillate containing 95 mole % benzene and 5 mole % toluene and a bottoms containing 10 mole % benzene and 90 mole % toluene are to be obtained. The average heat capacity of the feed is 159 kJ/ kg mol – K and the average latent heat 32099 kJ/ kg mol.

Calculate the following: (a) Minimum reflux ratio Rm· (b) Minimum number of theoretical plates at total reflux by using the graphical McCabe-Thiele Method. (c) Minimum number of theoretical plates at total reflux by using the Fenske eq.

The equilibrium and the vapor - pressure data are given below for the system benzene-toluene. Make a list of all the important assumptions you are making in your calculations. Note: All plots must be done either by using Excel or on a graph paper.

Mole % Benzene at 101.325 kPa
x y
1 1
0.78 0.9
0.581 0.777
0.411 0.632
0.258 0.456
0.13 0.261
0 0
Vapor Pressure
Benzene Toluene
T(K) T(°C) kPa mm Hg kPa mm Hg
353 80.1 101.3 760
358 85 116.9 877 46 345
363 90 135.5 1016 54 405
368 95 155.7 1168 63.3 475
373 100 179.2 1344 74.3 557
378 105 204.2 1532 86.0 645

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