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destilasi
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alfa = 2
Xa Ya0 0
0.1 0.1818180.2 0.3333330.3 0.4615380.4 0.5714290.5 0.6666670.6 0.750.7 0.8235290.8 0.8888890.9 0.947368
1 1
0 0.2 0.4 0.6 0.8 1 1.20
0.10.20.30.40.50.60.70.80.9
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2
0 01 1
alfa = 3
Xa Ya0 0 0 0
0.1 0.25 1 10.2 0.4285710.3 0.56250.4 0.6666670.5 0.750.6 0.8181820.7 0.8750.8 0.9230770.9 0.964286
1 1
0 0.2 0.4 0.6 0.8 1 1.20
0.10.20.30.40.50.60.70.80.9
1
3
alfa = 4
Xa Ya0 0 0 0
0.1 0.307692 1 10.2 0.50.3 0.6315790.4 0.7272730.5 0.80.6 0.8571430.7 0.9032260.8 0.9411760.9 0.972973
1 1
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
0.10.20.30.40.50.60.70.80.9
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4
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
0.10.20.30.40.50.60.70.80.9
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4
Xbenzen Ytoluena1 1
0.897 0.957 0 00.773 0.907 1 10.659 0.8310.555 0.7570.459 0.678
0.37 0.5910.288 0.4960.211 0.3930.141 0.2810.075 0.1610.013 0.031
0 0
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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campuran biner A dan B dengan αAB = 3F = 100 mol/jamXf = 0.4hasil distilasi bag. atas = 0.9 A + 0.1 B
bawah = 0.1 A + 0.9 Bfeed berupa camp 0.4 uap
0.6 cair F, Xfa. Jika R= 2 berapa rate atas dan bawah
berapa jumlah rate teoritisb. Jika jumlah plate teoritis = 12
berapa rate kembali ke kolom atas
JAWABF = D + W
100 =
NM Komponen AF.Xf = D. Xd + W. Xw
40 =
Distilasi
D, Xd
W, Xw
Distilasi
C
R
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 3
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 2
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 3
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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Benzena - Toluena
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 2
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 4
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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Benzena - Toluena
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 4
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 2
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 2
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 4
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 4
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 3
Xf0.40.4
Xd0.90.9
Xw0.10.1
goa0
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0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 3
01
01
01
0.30.9
30.960.54042
1.2
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 4
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
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α = 4
