In: Other
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 |