solver fix

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

R04R05

4. Stripper

R31 R41

5. Rectifier

Evaporator6. Kondensor

8. Dehidrator R81

R2R1R01

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

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

-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

4496.839879452710.3410.652

363.185776185811 K

90.1857761858107 C

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

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

-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

Etanol 4.99E+00 146.517

Air 4.17E+00 64.466

Tetes -2.22E+01 0.0000000002173

1535.746625366540.4330.567

360.948270522094 K

87.9482705220941 C

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

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

-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

Etanol 4.93E+00 137.695

Air 4.10E+00 60.442

Tetes -2.26E+01 0.0000000001604

665.0991891506020.5120.488

359.283384157904 K

86.2833841579038 C

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

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

-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

Etanol 4.88E+00 131.031

Air 4.05E+00 57.410

Tetes -2.28E+01 0.0000000001259

340.5669378017420.5790.421

357.966366023604 K

84.9663660236043 C

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

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

-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

Etanol 4.84E+00 125.991

Air 4.01E+00 55.122

Tetes -2.30E+01 0.0000000001039

197.0192490493330.6330.367

356.933208713952 K

83.9332087139525 C

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

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

-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

Etanol 4.81E+00 122.134

Air 3.98E+00 53.374

Tetes -2.31E+01 0.0000000000893

124.7639436056310.6780.322

R03yeast

R04urea

2*(80:Bmmolase)*BMCO2

#DIV/0!

356.119511613776 K

83.1195116137764 C

1.221 0.678 0.828

0.534 0.322 0.172

0.0000000000008927 0.000 0.000

TOTAL 1.0000 1.0000

R03yeast

R04urea

2*(80:Bmmolase)*BMCO2

#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

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

-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

Etanol 4.78E+00 119.137

Air 3.95E+00 52.017

Tetes -2.33E+01 0.0000000000791

84.60173166101530.7150.285

355.472293496973 K

82.4722934969731 C

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

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

-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

Etanol 4.76E+00 116.768

Air 3.93E+00 50.945

Tetes -2.34E+01 0.0000000000717

60.48038926809480.7450.255

354.951033959086 K

81.9510339590864 C

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

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

-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

Etanol 4.74E+00 114.861

Air 3.91E+00 50.083

Tetes -2.34E+01 0.0000000000661

45.07375655576720.7710.229

354.525160248154 K

81.5251602481542 C

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

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

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

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

-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

Etanol 4.70E+00 110.054

Air 3.87E+00 47.914

Tetes -2.36E+01 0.0000000000536

80.25602985469180.8380.162

353.425231708289 K

80.4252317082892 C

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

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

-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

Etanol 4.69E+00 109.266

Air 3.86E+00 47.559

Tetes -2.37E+01 0.0000000000518

14.51704151021820.8500.150

353.241249743434 K

80.2412497434341 C

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

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

-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

Etanol 4.69E+00 108.586

Air 3.86E+00 47.252

Tetes -2.37E+01 0.0000000000502

12.33707470004220.8600.140

353.081315600933 K

80.0813156009326 C

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

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

-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

Etanol 4.68E+00 107.992

Air 3.85E+00 46.984

Tetes -2.37E+01 0.0000000000489

10.61011285787560.8690.131

352.941202912735 K

79.941202912735 C

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

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

-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

Etanol 4.68E+00 107.471

Air 3.84E+00 46.750

Tetes -2.38E+01 0.0000000000478

9.220178865118640.8770.123

352.817618517751 K

79.8176185177509 C

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

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

-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

Etanol 4.67E+00 107.010

Air 3.84E+00 46.542

Tetes -2.38E+01 0.0000000000468

8.085788232357430.8840.116

352.70789991722 K

79.7078999172196 C

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

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

-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

Etanol 4.67E+00 106.599

Air 3.84E+00 46.357

Tetes -2.38E+01 0.0000000000459

7.148451232835730.8900.110

352.60992872398 K

79.6099287239798 C

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

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

-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

Etanol 4.67E+00 106.232

Air 3.83E+00 46.192

Tetes -2.38E+01 0.0000000000451

6.365361057787140.8960.104 R52 R51

0.000 5.705 113.275

0.661 5.705

0.000 0.000

352.521980437166 K

79.5219804371663 C

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

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

F2= 3355.6 KG B2= 1535.75 KG

F1= 7852.44 KG

B1= 4496.84 KG

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

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

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

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

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

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

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

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

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

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

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

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