solver fix
DESCRIPTION
ccTRANSCRIPT
Kapasitas molase= 2000 kg C6H1206 2C2H5OH + 2CO2
pengenceran rasio tetes:air = 1:5 (massa)
BM CO2= 44
BM Etanol= 46
BM Molase= 180
molase= 95
Xmolase= 80% 80 Kg
Urea= 2.50%
Ragi= 1% dari molase
H2SO4= 27%
Komponen R01 R02 R1 R2 R05 R03 R04 R31 R32 R41 R42
Etanol 0 0 0 0 0 0 0 2*(80% MOLASE/Bmmolase)*BMetanol 0 y etanol D*(0.7*(R31-R31H2SO4)) y etanol B*(R31-R31H2SO4-R41)
Air 0 5*R01molase R02air R1air 0 0 0 R2air 0 y airl D*(0.7*(R31-R31H2S04)) y air B*(R31-R31H2SO4-R41)
Molase R01 Molase 0 R01molase R1molase 0 0 0 0.2*R2molase 0 y molaseD*(0.7*(R31-R31H2SO4)) y molase B*(R31-R31H2SO4-R41)
h2so4 0 0 0 0 0.27*R01molase 0 0 R05.H2SO4 0 0 R 31 H2SO4
Yeast 0 0 0 0 0 0.01*R01molase 0 0 R03yeast 0
Urea 0 0 0 0 0 0 0.025*R01molase 0 R04urea 0
CO2 0 0 0 0 0 0 0 0 2*(80:Bmmolase)*BMCO2 0
Komponen R01 R02 R1 R2 R05 RO3 RO4 R31 R32 R41 R42 R52 R51
Etanol 0 0 0 0 0 0 0 817.78 0 3355.60456499174 9.72877034257451
Air 0 10000 10000 10000 0 0 10000 0 4463.74013850805 23.3709774099222
Molase 2000 0 2000 2000 0 0 400 0 33.0990487750767 3332.23496992015
h2so4 0 0 0 0 540 0 0 540 0 0 540
Yeast 0 0 0 0 0 20 0 0 20 0 0
Urea 0 0 0 0 0 0 50 0 50.00 0 0
CO2 0 0 0 0 0 0 0 0 782.22 0 0
TOTAL 2000 10000 12000 12000 540 20 50 11757.78 852.22 7852.44375227486 3905.33471767264
Kondisi operasi P dan T: 1 bar, 30 C 1 bar, 30 C 1 bar, 30 C 1 bar, 30 C 1 bar, 30 C 1 bar, 30 C 1 bar, 30 C 1 bar, 38 C 1 bar, 38 C 1 bar. 96 C 1 bar, 96 C
PEMBUKTIAN MASUK=KELUAR (HINGGA UNIT FERMENTOR) PEMBUKTIAN MASUK=KELUAR ( UNIT STRIPPER)
MASUK KELUAR MASUK KELUAR
STREAM MASSA (KG) STREAM MASSA(KG) STREAM MASSA (KG) STREAM MASSA(KG)
R01 2000 R32 852.22 R31 11757.78 R42 3905.33
R02 10000 R41 11757.78 R41 7852.44
R03 20 TOTAL 11757.78 11757.78
R04 50
R05 540
R31 11757.78
TOTAL 12610 12610.00
FLASH DISTILATION
KOOFISIEN ANTOINEA B C D E F
Etanol 86.486 -7931.100 0 -10.250 6.39E-06 2
Water 65.928 -7227.530 0 -7.177 4.03E-06 2
Sorbitol 245.662 -34214.00 0 -29.400 2.62E-18 6
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
Asumsi masuk destilasi:molase,etanol dan air
Flash distillation
1. Mixing2.
FeedingTank
3. Fermentor
R03
R04R05
R32
4. Stripper
R31 R41
R42
5. Rectifier
R52
R517.
Evaporator6. Kondensor
R72
R71
8. Dehidrator R81
R82
R2R1R01
R02
R6
P OPERASI= 100 kPa= 1 bar
D 7852.44444444444 T trial= 120 C 569.631283490371 K
Ye 0.427 296.631283490371 C
Ya 0.568Yt 0.004
Komposisi Ln P P (kPa) K x y
F 11217.78 Etanol 9.60E+00 14782.100 147.821 0.003 0.427
Zfe 0.3 Air 9.01E+00 8185.502 81.855 0.007 0.568
Zfa 0.4 Tetes -8.54E-01 0.4256995579100 0.004 0.990 0.004
Zft 0.3 TOTAL 1.0000 1.0000
B 0.3D 0.7 B 3365.33333333333
b/d= 0.429 Xe 0.003Xa 0.007Xt 0.990
NM TOTAL : R 31= R 41 + R 42
NM KOMP :
ETANOL 0.003 R 42
0.3 R 31= 0.427 R 41+ 0.003 (R 31-R 41)
0.3 R 31= 0.427 R 41+
0.297 R 31= 0.424 R 41
R 41= 0.7 R 31
Destilasi
TRAY 1
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 7852.44444444444Zfe 0.427332480825866Zfa 0.568452304258722Zft 0.00421512676839046
B 0.568452304258722D 0.427332480825866 B
b/d= 1.330 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
3355.60456499174 P OPERASI= 100 kPa=
0.542 T trial= 120 C
0.4580.0000000000000239993
Komposisi Ln P P (kPa)
Etanol 5.07E+00 159.098
Air 4.25E+00 70.223
Tetes -2.18E+01 0.0000000003250
TOTAL
4496.839879452710.3410.652
0.007
1 bar
363.185776185811 K
90.1857761858107 C
K x y
1.591 0.341 0.542
0.702 0.652 0.458
0.0000000000032502 0.007 0.000
TOTAL 1.00 1.0000
TRAY 2
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 3355.60456499174Zfe 0.542333849051035Zfa 0.457666148265473Zft 0.0000000000000240
B 0.457666148265473D 0.542333849051035 B
b/d= 0.844 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
1819.85793962519 P OPERASI= 100 kPa=
0.635 T trial= 120 C
0.3650.00000000000000
Komposisi Ln P P (kPa)
Etanol 4.99E+00 146.517
Air 4.17E+00 64.466
Tetes -2.22E+01 0.0000000002173
TOTAL
1535.746625366540.4330.567
0.000
1 bar
360.948270522094 K
87.9482705220941 C
K x y
1.465 0.433 0.635
0.645 0.567 0.365
0.0000000000021733 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 3
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 1819.85793962519Zfe 0.634532358450143Zfa 0.365468224394375Zft 0.0000000000000000
B 0.365468224394375D 0.634532358450143 B
b/d= 0.576 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
1154.75875047459 P OPERASI= 100 kPa=
0.705 T trial= 120 C
0.2950.000000000
Komposisi Ln P P (kPa)
Etanol 4.93E+00 137.695
Air 4.10E+00 60.442
Tetes -2.26E+01 0.0000000001604
TOTAL
665.0991891506020.5120.488
0.000
1 bar
359.283384157904 K
86.2833841579038 C
K x y
1.377 0.512 0.705
0.604 0.488 0.295
0.0000000000016044 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 4
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 1154.75875047459Zfe 0.705075248261359Zfa 0.294925498428649Zft 0.0000000000000000
B 0.294925498428649D 0.705075248261359 B
b/d= 0.418 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
814.191812672849 P OPERASI= 100 kPa=
0.758 T trial= 120 C
0.2420.000000000
Komposisi Ln P P (kPa)
Etanol 4.88E+00 131.031
Air 4.05E+00 57.410
Tetes -2.28E+01 0.0000000001259
TOTAL
340.5669378017420.5790.421
0.000
1 bar
357.966366023604 K
84.9663660236043 C
K x y
1.310 0.579 0.758
0.574 0.421 0.242
0.0000000000012589 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 5
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 814.191812672849Zfe 0.758018631503364Zfa 0.241982447980575Zft 0.0000000000000000
B 0.241982447980575D 0.758018631503364 B
b/d= 0.319 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
617.172563623516 P OPERASI= 100 kPa=
0.798 T trial= 120 C
0.2020.000000000
Komposisi Ln P P (kPa)
Etanol 4.84E+00 125.991
Air 4.01E+00 55.122
Tetes -2.30E+01 0.0000000001039
TOTAL
197.0192490493330.6330.367
0.000
1 bar
356.933208713952 K
83.9332087139525 C
K x y
1.260 0.633 0.798
0.551 0.367 0.202
0.0000000000010392 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 6
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 617.172563623516Zfe 0.79784593327817Zfa 0.202155509021582Zft 0.0000000000000000
B 0.202155509021582D 0.79784593327817 B
b/d= 0.253 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
492.408620017885 P OPERASI= 100 kPa=
0.828 T trial= 120 C
0.1720.000000000
Komposisi Ln P P (kPa)
Etanol 4.81E+00 122.134
Air 3.98E+00 53.374
Tetes -2.31E+01 0.0000000000893
TOTAL
124.7639436056310.6780.322
0.000
R32
0
0
0
0
R03yeast
R04urea
2*(80:Bmmolase)*BMCO2
R32
0
0
0
0
0
0.00
#DIV/0!
#DIV/0!
1 bar
356.119511613776 K
83.1195116137764 C
K x y
1.221 0.678 0.828
0.534 0.322 0.172
0.0000000000008927 0.000 0.000
TOTAL 1.0000 1.0000
R32
0
0
0
0
R03yeast
R04urea
2*(80:Bmmolase)*BMCO2
R32
0
0
0
0
0
0.00
#DIV/0!
#DIV/0!
TRAY 7
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 492.408620017885Zfe 0.828187955649634Zfa 0.171813709033169Zft 0.0000000000000000
B 0.171813709033169D 0.828187955649634 B
b/d= 0.207 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
407.80688835687 P OPERASI= 100 kPa=
0.852 T trial= 120 C
0.1480.000000000
Komposisi Ln P P (kPa)
Etanol 4.78E+00 119.137
Air 3.95E+00 52.017
Tetes -2.33E+01 0.0000000000791
TOTAL
84.60173166101530.7150.285
0.000
1 bar
355.472293496973 K
82.4722934969731 C
K x y
1.191 0.715 0.852
0.520 0.285 0.148
0.0000000000007905 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 8
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 407.80688835687Zfe 0.851693556448295Zfa 0.148308432393491Zft 0.0000000000000000
B 0.148308432393491D 0.851693556448295 B
b/d= 0.174 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
347.326499088775 P OPERASI= 100 kPa=
0.870 T trial= 120 C
0.1300.000000000
Komposisi Ln P P (kPa)
Etanol 4.76E+00 116.768
Air 3.93E+00 50.945
Tetes -2.34E+01 0.0000000000717
TOTAL
60.48038926809480.7450.255
0.000
1 bar
354.951033959086 K
81.9510339590864 C
K x y
1.168 0.745 0.870
0.509 0.255 0.130
0.0000000000007166 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 9
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 347.326499088775Zfe 0.870226554340023Zfa 0.129775810084359Zft 0.0000000000000000
B 0.129775810084359D 0.870226554340023 B
b/d= 0.149 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
302.252742533008 P OPERASI= 100 kPa=
0.885 T trial= 120 C
0.1150.000000000
Komposisi Ln P P (kPa)
Etanol 4.74E+00 114.861
Air 3.91E+00 50.083
Tetes -2.34E+01 0.0000000000661
TOTAL
45.07375655576720.7710.229
0.000
1 bar
354.525160248154 K
81.5251602481542 C
K x y
1.149 0.771 0.885
0.501 0.229 0.115
0.0000000000006611 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 10
ANTOINEA B C D E F
Etanol 86.486 -7931.100 0 -10.250 6.39E-06 2
Water 65.928 -7227.530 0 -7.177 4.03E-06 2
Sorbitol 245.662 -34214.00 0 -29.400 2.62E-18 6
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
D 267.520099515639 P OPERASI= 100 kPa= 1
Ye 0.897 T trial= 120 C 354.17411797508
Ya 0.103 81.1741179750804
Yt 0.000000000
F 302.252742533008 Komposisi Ln P P (kPa) K
Zfe 0.885087418144518 Etanol 4.73E+00 113.308 1.133Zfa 0.114912610786146 Air 3.90E+00 49.382 0.494Zft 0.0000000000000000 Tetes -2.35E+01 0.0000000000619 0.0000000000006185
B 0.114912610786146 TOTAL
D 0.885087418144518 B 34.7326430173682b/d= 0.130 Xe 0.792
Xa 0.208Xt 0.000
Destilasi
bar
K
C
x y0.792 0.8970.208 0.1030.000 0.000
1.0000 1.0000
TRAY 11
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 267.520099515639Zfe 0.897196460043776Zfa 0.102803586984139Zft 0.0000000000000000
B 0.3D 0.7 B
b/d= 0.429 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
187.264069660947 P OPERASI= 100 kPa=
0.922 T trial= 120 C
0.0780.000000000
Komposisi Ln P P (kPa)
Etanol 4.70E+00 110.054
Air 3.87E+00 47.914
Tetes -2.36E+01 0.0000000000536
TOTAL
80.25602985469180.8380.162
0.000
1 bar
353.425231708289 K
80.4252317082892 C
K x y
1.101 0.838 0.922
0.479 0.162 0.078
0.0000000000005364 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 12
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 187.264069660947Zfe 0.922478233349825Zfa 0.0775218516637586Zft 0.0000000000000000
B 0.0775218516637586D 0.922478233349825 B
b/d= 0.084 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
172.747028150729 P OPERASI= 100 kPa=
0.929 T trial= 120 C
0.0710.000000000
Komposisi Ln P P (kPa)
Etanol 4.69E+00 109.266
Air 3.86E+00 47.559
Tetes -2.37E+01 0.0000000000518
TOTAL
14.51704151021820.8500.150
0.000
1 bar
353.241249743434 K
80.2412497434341 C
K x y
1.093 0.850 0.929
0.476 0.150 0.071
0.0000000000005179 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 13
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 172.747028150729Zfe 0.928582998896644Zfa 0.071417090920197Zft 0.0000000000000000
B 0.071417090920197D 0.928582998896644 B
b/d= 0.077 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
160.409953450687 P OPERASI= 100 kPa=
0.934 T trial= 120 C
0.0660.000000000
Komposisi Ln P P (kPa)
Etanol 4.69E+00 108.586
Air 3.86E+00 47.252
Tetes -2.37E+01 0.0000000000502
TOTAL
12.33707470004220.8600.140
0.000
1 bar
353.081315600933 K
80.0813156009326 C
K x y
1.086 0.860 0.934
0.473 0.140 0.066
0.0000000000005023 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 14
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 160.409953450687Zfe 0.93385626870631Zfa 0.0661438328555165Zft 0.0000000000000000
B 0.0661438328555165D 0.93385626870631 B
b/d= 0.071 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
149.799840592812 P OPERASI= 100 kPa=
0.938 T trial= 120 C
0.0620.000000000
Komposisi Ln P P (kPa)
Etanol 4.68E+00 107.992
Air 3.85E+00 46.984
Tetes -2.37E+01 0.0000000000489
TOTAL
10.61011285787560.8690.131
0.000
1 bar
352.941202912735 K
79.941202912735 C
K x y
1.080 0.869 0.938
0.470 0.131 0.062
0.0000000000004890 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 15
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 149.799840592812Zfe 0.938450008834248Zfa 0.061550083203945Zft 0.0000000000000000
B 0.061550083203945D 0.938450008834248 B
b/d= 0.066 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
140.579661727693 P OPERASI= 100 kPa=
0.942 T trial= 120 C
0.0580.000000000
Komposisi Ln P P (kPa)
Etanol 4.68E+00 107.471
Air 3.84E+00 46.750
Tetes -2.38E+01 0.0000000000478
TOTAL
9.220178865118640.8770.123
0.000
1 bar
352.817618517751 K
79.8176185177509 C
K x y
1.075 0.877 0.942
0.467 0.123 0.058
0.0000000000004775 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 16
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 140.579661727693Zfe 0.942482517506552Zfa 0.0575175816618918Zft 0.0000000000000000
B 0.0575175816618918D 0.942482517506552 B
b/d= 0.061 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
132.493873495335 P OPERASI= 100 kPa=
0.946 T trial= 120 C
0.0540.000000000
Komposisi Ln P P (kPa)
Etanol 4.67E+00 107.010
Air 3.84E+00 46.542
Tetes -2.38E+01 0.0000000000468
TOTAL
8.085788232357430.8840.116
0.000
1 bar
352.70789991722 K
79.7078999172196 C
K x y
1.070 0.884 0.946
0.465 0.116 0.054
0.0000000000004676 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 17
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 132.493873495335Zfe 0.946046929988145Zfa 0.0539531771629736Zft 0.0000000000000000
B 0.0539531771629736D 0.946046929988145 B
b/d= 0.057 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
125.3454222625 P OPERASI= 100 kPa=
0.949 T trial= 120 C
0.0510.000000000
Komposisi Ln P P (kPa)
Etanol 4.67E+00 106.599
Air 3.84E+00 46.357
Tetes -2.38E+01 0.0000000000459
TOTAL
7.148451232835730.8900.110
0.000
1 bar
352.60992872398 K
79.6099287239798 C
K x y
1.066 0.890 0.949
0.464 0.110 0.051
0.0000000000004589 0.000 0.000
TOTAL 1.0000 1.0000
TRAY 18
ANTOINEA B C
Etanol 86.486 -7931.100 0
Water 65.928 -7227.530 0
Sorbitol 245.662 -34214.00 0
(P dalam kPa) lnP=a+b/(T+c)+d*ln(T)+e*T^f(T dalam K)T min = 91.5C
T max = 594.85C
DYeYaYt
F 125.3454222625Zfe 0.949217442943734Zfa 0.0507826733486467Zft 0.0000000000000000
B 0.0507826733486467D 0.949217442943734 B
b/d= 0.053 XeXa
Destilasi
Xt
D E F
-10.250 6.39E-06 2
-7.177 4.03E-06 2
-29.400 2.62E-18 6
118.980061204713 P OPERASI= 100 kPa=
0.952 T trial= 120 C
0.0480.000000000
Komposisi Ln P P (kPa)
Etanol 4.67E+00 106.232
Air 3.83E+00 46.192
Tetes -2.38E+01 0.0000000000451
TOTAL
6.365361057787140.8960.104 R52 R51
0.000 5.705 113.275
0.661 5.705
0.000 0.000
1 bar
352.521980437166 K
79.5219804371663 C
K x y
1.062 0.896 0.952
0.462 0.104 0.048
0.0000000000004512 0.000 0.000
TOTAL 1.0000 1.0000
B19= 118. 98 KG
F18= 125.34 KG B18= 6.37 KG
F17= 132.49 KG B17= 7.15 KG
F16= 140.58 KG B16= 8.09 KG
F15= 149.8 KG B15= 9.22 KG
F14= 160.4 KG B14 10.61 KG
F13= 172.75 KG B13= 12.34 KG
F12= 187.26 KG B12= 14.52 KG
18
17
16
15
14
1313
12
11
F11= 267.52 KG B11= 80.26 KG
F10= 302.25 KG B10= 34.73 KG
F9= 347.33 KG B9= 45.07 KG
F8= 407.8 KG B8= 60.48 KG
F7= 492.4 KG B7= 84.6 KG
F6= 617.173 KG B6= 124.76 KG
F5= 814.19 KG B5= 197.02 KG
F4= 1154.76 KG B4= 340.57 KG
F3= 1819.86 KG B3= 665.09 KG
10
9
8
7
6
5
3
4
F2= 3355.6 KG B2= 1535.75 KG
F1= 7852.44 KG
B1= 4496.84 KG
2
1
0
TRAY 1 TRAY 2
Y X MASSA UAP (KG) MASSA CAIR (KG) Y X
0 0.54233385 0.340881 1819.8579396252 1532.8850876469 0.634532 0.433079
0 0.45766615 0.651735 1535.7466163618 2930.7501742546 0.365468 0.566921
0 2.3999E-14 0.007384 8.053220876E-11 33.203932259661 1.14E-25 5.24E-14
KOMPONEN
TRAY 4 TRAY 5
Y X MASSA UAP (KG) MASSA CAIR (KG) Y X
ETANOL 0.75801863 0.578504 617.17256362352 197.01935818493 0.797846 0.633258
AIR 0.24198245 0.421496 197.02012795632 143.54756295733 0.202156 0.366742
MOLASE 0 0 0 0 0 0
KOMPONEN
TRAY 7 TRAY 8
Y X MASSA UAP (KG) MASSA CAIR (KG) Y X
ETANOL 0.85169356 0.714885 347.32649908877 60.480482143259 0.870227 0.745264
AIR 0.14830843 0.285115 60.481200331475 24.121258159819 0.129776 0.254736
MOLASE 0 0 0 0 0 0
KOMPONEN
TRAY 10 TRAY 11
Y X MASSA UAP (KG) MASSA CAIR (KG) Y X
ETANOL 0.89719646 0.79182 240.01808627599 27.502014055211 0.922478 0.838206
AIR 0.10280359 0.20818 27.502025820561 7.2306251256186 0.077522 0.161794
MOLASE 0 0 0 0 0 0
KOMPONEN
TRAY 13 TRAY 14
Y X MASSA UAP (KG) MASSA CAIR (KG) Y X
ETANOL 0.934 0.860 149.79984059281 10.610113921693 0.93845 0.868999
AIR 0.066 0.140 10.610129149403 1.7269600024164 0.06155 0.131001
MOLASE 0.00000000 0.000 0 0 0 0
KOMPONEN
TRAY 16 TRAY 17
Y X MASSA UAP (KG) MASSA CAIR (KG) Y X
ETANOL 0.94604693 0.884076 125.3454222625 7.1484520470836 0.949217 0.890453
AIR 0.05395318 0.115924 7.1484654297024 0.9373359294752 0.050783 0.109547
MOLASE 0 0 0 0 0 0
TRAY 2 TRAY 3
MASSA UAP (KG) MASSA CAIR (KG) Y X MASSA UAP (KG) MASSA CAIR (KG)
1154.758750475 665.09918816679 0.705075 0.512055 814.1918126728 340.56706771324
665.1002498448 870.64636750079 0.294925 0.487946 340.5678000486 324.53231988506
2.07394674E-22 8.0532209013E-11 5E-37 3.12E-25 5.77712659E-34 2.073944637E-22
TRAY 5 TRAY 6
MASSA UAP (KG) MASSA CAIR (KG) Y X MASSA UAP (KG) MASSA CAIR (KG)
492.4086200179 124.76405325845 0.828188 0.678095 407.8068883569 84.601838256822
124.7648337535 72.255184551028 0.171814 0.321905 84.60255136518 40.162175793264
0 0 0 0 0 0
TRAY 8 TRAY 9
MASSA UAP (KG) MASSA CAIR (KG) Y X MASSA UAP (KG) MASSA CAIR (KG)
302.252742533 45.07384287707 0.885087 0.770575 267.5200995156 34.732724853668
45.07457778301 15.406536228911 0.114913 0.229443 34.73265176174 10.341844172108
0 0 0 0 0 0
TRAY 11 TRAY 12
MASSA UAP (KG) MASSA CAIR (KG) Y X MASSA UAP (KG) MASSA CAIR (KG)
172.7470281507 67.271058125261 0.928583 0.849834 160.4099534507 12.337075856537
14.51705743021 12.984968390354 0.071417 0.150166 12.33709021563 2.1799660580792
0 0 0 0 0 0
TRAY 14 TRAY 15
MASSA UAP (KG) MASSA CAIR (KG) Y X MASSA UAP (KG) MASSA CAIR (KG)
140.5796617277 9.2201799217389 0.942483 0.876967 132.4938734953 8.0857890800478
9.220192652425 1.3899354403558 0.057518 0.123033 8.085802173424 1.1343896313127
0 0 0 0 0 0
TRAY 17 TRAY 18
MASSA UAP (KG) MASSA CAIR (KG) Y X MASSA UAP (KG) MASSA CAIR (KG)
118.9800612047 6.3653618470428 0.952054 0.896201 113.2754163918 5.7046455856925
6.365375634505 0.7830890059444 0.047946 0.103799 5.704659909661 0.660714952047
0 0 0 0 0 0
y= -0.1414 x4 + 1.485 x3 + -2.355 x2 + -2.284 x
x y0 0 y 0.95 0.95
0.95 trial x 0.1 0.1-0.95 y hitung 0
y trial-yhitung 0.95