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Mass fractions
F= W+D
F×Xf= W×Xw+D×Xd
F=1537.3 kmole/h
D=23.24 kmole/h
W=1514.1 kmole/h
X= msolute/mtotal
Xf=0.033
Xd=0.84
Xw=0.02
The number of theoretical trays is 4.83
The Actual Number of Trays: 6.46
Effectiveness: 0.60
The Feed enters on Tray: 4
a=(Y_A ⁄ X_A )/((1-Y_A) ⁄ (1-X_A ))
a=10,94
R_min=1/(X_F×(a-1))=3.05
R=R_min×1.3=3.97
Y_(n+1)=(R/(R+1))×X_n+X_D/(R+1)
Y_(n+1)=0,8×X_n+0,17
Enriching Operating Line
Equilibrium Line
Stripped Operating Line
q Line
y=x
Distillation: Seperation Process
Suma: Intermediate Product
%92-94
Grape mash: Feed Stock
%8-9
Eda BAYRAM
Büşra UYSUN
Şule UYSAL
Arzu SARUKAN
Rabia ÖZDEMİR
Feed Stock: Grape mash
Product: Suma
Equipment: 800 €
Capacity: 10000000 L/y = 23.24 kmole/h
Total Direct: 1885.12 €
Total Indirect: 626.7 €
Feed(F)=1537.3 knole/h
Distilled(D)=1514.1 kmole/h
Total capital: 4315.4 €
General Material Balance
General Alcohol Balance
Relative volatility
Rmin, R
Enriching Equation
Eriching Operation Line
q Line
Equilibrium Line
Stripped Operation Line
Number of Trays
Efficiency