solver fix
DESCRIPTION
ccTRANSCRIPT
![Page 1: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/1.jpg)
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
![Page 2: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/2.jpg)
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
![Page 3: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/3.jpg)
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
![Page 4: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/4.jpg)
Xt
![Page 5: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/5.jpg)
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
![Page 6: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/6.jpg)
0.007
![Page 7: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/7.jpg)
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
![Page 8: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/8.jpg)
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
![Page 9: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/9.jpg)
Xt
![Page 10: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/10.jpg)
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
![Page 11: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/11.jpg)
0.000
![Page 12: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/12.jpg)
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
![Page 13: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/13.jpg)
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
![Page 14: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/14.jpg)
Xt
![Page 15: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/15.jpg)
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
![Page 16: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/16.jpg)
0.000
![Page 17: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/17.jpg)
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
![Page 18: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/18.jpg)
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
![Page 19: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/19.jpg)
Xt
![Page 20: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/20.jpg)
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
![Page 21: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/21.jpg)
0.000
![Page 22: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/22.jpg)
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
![Page 23: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/23.jpg)
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
![Page 24: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/24.jpg)
Xt
![Page 25: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/25.jpg)
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
![Page 26: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/26.jpg)
0.000
![Page 27: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/27.jpg)
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
![Page 28: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/28.jpg)
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
![Page 29: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/29.jpg)
Xt
![Page 30: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/30.jpg)
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
![Page 31: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/31.jpg)
0.000
![Page 32: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/32.jpg)
R32
0
0
0
0
R03yeast
R04urea
2*(80:Bmmolase)*BMCO2
R32
0
0
0
0
0
0.00
#DIV/0!
#DIV/0!
![Page 33: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/33.jpg)
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
![Page 34: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/34.jpg)
R32
0
0
0
0
R03yeast
R04urea
2*(80:Bmmolase)*BMCO2
R32
0
0
0
0
0
0.00
#DIV/0!
#DIV/0!
![Page 35: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/35.jpg)
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
![Page 36: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/36.jpg)
Xt
![Page 37: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/37.jpg)
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
![Page 38: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/38.jpg)
0.000
![Page 39: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/39.jpg)
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
![Page 40: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/40.jpg)
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
![Page 41: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/41.jpg)
Xt
![Page 42: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/42.jpg)
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
![Page 43: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/43.jpg)
0.000
![Page 44: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/44.jpg)
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
![Page 45: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/45.jpg)
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
![Page 46: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/46.jpg)
Xt
![Page 47: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/47.jpg)
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
![Page 48: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/48.jpg)
0.000
![Page 49: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/49.jpg)
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
![Page 50: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/50.jpg)
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
![Page 51: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/51.jpg)
bar
K
C
x y0.792 0.8970.208 0.1030.000 0.000
1.0000 1.0000
![Page 52: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/52.jpg)
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
![Page 53: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/53.jpg)
Xt
![Page 54: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/54.jpg)
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
![Page 55: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/55.jpg)
0.000
![Page 56: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/56.jpg)
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
![Page 57: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/57.jpg)
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
![Page 58: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/58.jpg)
Xt
![Page 59: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/59.jpg)
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
![Page 60: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/60.jpg)
0.000
![Page 61: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/61.jpg)
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
![Page 62: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/62.jpg)
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
![Page 63: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/63.jpg)
Xt
![Page 64: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/64.jpg)
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
![Page 65: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/65.jpg)
0.000
![Page 66: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/66.jpg)
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
![Page 67: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/67.jpg)
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
![Page 68: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/68.jpg)
Xt
![Page 69: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/69.jpg)
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
![Page 70: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/70.jpg)
0.000
![Page 71: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/71.jpg)
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
![Page 72: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/72.jpg)
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
![Page 73: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/73.jpg)
Xt
![Page 74: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/74.jpg)
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
![Page 75: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/75.jpg)
0.000
![Page 76: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/76.jpg)
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
![Page 77: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/77.jpg)
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
![Page 78: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/78.jpg)
Xt
![Page 79: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/79.jpg)
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
![Page 80: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/80.jpg)
0.000
![Page 81: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/81.jpg)
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
![Page 82: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/82.jpg)
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
![Page 83: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/83.jpg)
Xt
![Page 84: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/84.jpg)
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
![Page 85: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/85.jpg)
0.000
![Page 86: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/86.jpg)
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
![Page 87: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/87.jpg)
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
![Page 88: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/88.jpg)
Xt
![Page 89: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/89.jpg)
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
![Page 90: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/90.jpg)
0.000 5.705 113.275
0.661 5.705
0.000 0.000
![Page 91: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/91.jpg)
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
![Page 92: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/92.jpg)
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
![Page 93: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/93.jpg)
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
![Page 94: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/94.jpg)
F2= 3355.6 KG B2= 1535.75 KG
F1= 7852.44 KG
B1= 4496.84 KG
2
1
![Page 95: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/95.jpg)
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
![Page 96: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/96.jpg)
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
![Page 97: Solver Fix](https://reader035.vdocuments.mx/reader035/viewer/2022062519/5695cfe21a28ab9b028ff5a2/html5/thumbnails/97.jpg)
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