Equilibrium Curve 1.000 1.000 0.780 0.900 0.581 0.777 0.411 0.632 0.258 0.456 0.130 0.261

Equilibrium Curve<br>1.000<br>1.000<br>0.780<br>0.900<br>0.581<br>0.777<br>0.411<br>0.632<br>0.258<br>0.456<br>0.130<br>0.261<br>

Extracted text: Equilibrium Curve 1.000 1.000 0.780 0.900 0.581 0.777 0.411 0.632 0.258 0.456 0.130 0.261

The following are known information for the separation of a benzene-toluene system at 1 atm using<br>distillation with reflux:<br>Feed (F):<br>450 Ibmol/h<br>60 mol% benzene<br>40 mol% toluene<br>%molar vaporization due to preheating is equal to the D/F ratio<br>Tops (D):<br>95% benzene<br>Bottoms (B):<br>5% benzene<br>Using the McCabe-Thiele Method, determine the ff:<br>A) Minimum reflux ratio<br>B) Minimum number of stages<br>(For C-E, use a different equilibrium diagram)<br>c) Number of equilibrium stages for a reflux to minimum reflux ratio of 1.3<br>D) Optimal feed stage location<br>E) Actual Number of Trays if efficiency is 80%<br>

Extracted text: The following are known information for the separation of a benzene-toluene system at 1 atm using distillation with reflux: Feed (F): 450 Ibmol/h 60 mol% benzene 40 mol% toluene %molar vaporization due to preheating is equal to the D/F ratio Tops (D): 95% benzene Bottoms (B): 5% benzene Using the McCabe-Thiele Method, determine the ff: A) Minimum reflux ratio B) Minimum number of stages (For C-E, use a different equilibrium diagram) c) Number of equilibrium stages for a reflux to minimum reflux ratio of 1.3 D) Optimal feed stage location E) Actual Number of Trays if efficiency is 80%

Jun 09, 2022

SOLUTION.PDF

Equilibrium Curve 1.000 1.000 0.780 0.900 0.581 0.777 0.411 0.632 0.258 0.456 0.130 0.261

Get Answer To This Question

Related Questions & Answers

Submit New Assignment