Dpa Dinda Acak2

X03

X01 X1

X02

1 Kapasitan 3000 lit/jam tetesKomponen X01 X02 X03 X04

H2O 0 (7/1)*C22 0 0Urea 0 0 0 (0,3/100)*X01TetesRagi 0 0 (0,1/100)*X01 Tetes 0Tetes 100 0 0 0Etanol 0 0 0 0kondisi operasi T.P : 30,100.3 T.P : 30, 100.3 T.P : 30, 100.3 T.P : 30, 100.3

2 KapasitasTetes 100 kg/jamH2OUREARAGI

Komponen X01 X02 X03 X04H2O 0 700 0 0Urea 0 0 0 0.3Ragi 0 0 0.1 0Tetes 100 0 0 0Etanol 0 0 0 0

TOTAL 100 700 0.1 0.3

Mixer Fermentor

X04

X2 32

X2 X2

31

X1 X2 X31 X32 X41X02 H2O X02 H2O 0 X2 H2O M2AIR/M1AIR*32H2O

0 X04 Urea X2 Urea 0 00 X03 Ragi X2 Ragi 0 0

X01 tetes 0,2*X01 Tetes 0 X2 Tetes 00 0,8*X01 Tetes 0 X2 Etanol M2/M1(ETANOL)*32ETANOL

T.P : 35, 100.3 T.P : 35, 100.3 T.P : 30, 100.3 T.P : 30, 100.3 T.P : 175, 100.3

X1 X2 X31 X32 X41700 700 0 700 988.073254162512

0 0.3 0.3 0 00 0.1 0.1 0 0

100 20 0 20 00 80 0 80 116.103107772395

800 800.4 0.4 800 1104.17636193491

Fermentor flash distillationPEMISAHAN

41 51

X32

4252

X42 51 52M3/M1*32AIR

0 0 00 0 0

M3/M1*32TETES 0 42TETESM3/M1*32ETANOL

T.P : 80, 100.3 T.P: 100, 100.3

X42 51 52110.702873173747 37.3513405969125 551.800991890502

0 0 00 0 0

60.9130051687347 0 60.91300516873476.14566825503191 50.4729554228124 0.727239246486428

177.761546597513 87.8242960197249 613.441236305723

((0.01)*(0.43)*41)/0.91 ((41*(1-0.43/0.91)-((0.01)*(0.43/0.91)*41-42tetes

((0.92)*(0.43)*41)/0.91 ((0.01)*(1-0.43/0.91)*41

flash distillation Distilasi 2

61

X42

62

D 67.16629 kgYe 0.4353866541Ya 0.5646132881Yt 6.264624E-47

F 100

M1E Ze 0.3 m,n,n,nnnnnM1A Za 0.4M1T Zt 0.3

EVAPORATOR DEHIDRASI

1

B 32.83371 kgXe 0.023046256Xa 0.0632587847Xt 0.9136950775

nnnnnnnnnnnnnnn

1

nnnnnnnn

FFFF

M2E 29.24331M2A

M3EM3AM3T

etanol air sorbitol T =a 5.33675 a 5.11564 a 245.66200b 1648.22000 b 1687.53700 b -34214.00000c 230.91800 c 230.17000 c 0.00000

d -29.39999e 2.6181E-18f 6.00000

P = 10^(a-(b/T+c))etanol P = 18.891860568 bar Ptot 103 kPaair P = 8.9254526629 bar 1 barsolbitol P = 6.856362E-47 bar

Fix B/D 0.488842 Ze 0.3Pe 18.891860568 Za 0.4Pa 8.9254526629 Zt 0.3Pt 6.856362E-47Ke 18.891860568Ka 8.9254526629Kt 6.856362E-47Ye 0.4353866541Ya 0.5646132881Yt 6.264624E-47Xe 0.023046256Xa 0.0632587847Xt 0.9136950775Jumlah =Ye+Ya+Yt 1Jumlah =Xe+Xa+Yt 1 F 100

M1E Ze 0.3M1A Za 0.4M1T Zt 0.3

note: jika ingin D besar maka yang diubah T nyaXe harus sekecil mungkin

1

175 C

12 cari Ke,Ka,Kt ---> K1=P1⁰/Pt

pt = 103 Kpa ==> 1 bar3 Trial B/D-----> Harga terserah 4 Hitung Ye = Ze (B/D +1) , Ya Yt

1+ B/(Dki)

Xe = Ze (B/D +1) , Xa XtKi + B/D

5 Trial BenarBila Ye + Ya + Yt = 1

Xe+ Xa + Xt = 1

D 67.16629 kgYe 0.435387 M2EYa 0.564613 M2AYt 6.265E-47

B 32.83371 kgXe 0.023046 M3EXa 0.063259 M3AXt 0.913695 M3T

cari P⁰e,P⁰a,P⁰t pada 105⁰C

1


d -29.39999e 2.6181E-18f 6.00000


Fix B/D 1.320186Pe 1.5783425934 Ze 0.431Pa 0.6953727031 Za 0.569Ke 1.5783425934Ka 0.6953727031Ye 0.5445324247Ya 0.4554673667Xe 0.34500268Xa 0.6549974779

Jumlah =Ye+Ya 1 3Jumlah =Xe+Xa 1

89.83793 C etanol air sorbitola 5.33675 a 5.11564 a 245.66200b 1648.22000 b 1687.53700 b -34214.00000c 230.91800 c 230.17000 c 0.00000

d -29.39999e 2.6181E-18f 6.00000

P = 10^(a-(b/T+c))etanol P = 1.46356733397 bar Ptotair P = 0.64341220984 barsolbitol P = 2.099271E-122 bar


Jumlah =Ye+Ya 1Jumlah =Xe+Xa 0.999999

T = 87.8042 C etanol air sorbitola 5.33675 a 5.11564 ab 1648.22000 b 1687.53700 bc 230.91800 c 230.17000 c

def

P = 10^(a-(b/T+c))103 kPa etanol P = 1.37537692641 bar

1 bar air P = 0.60356488711 barsolbitol P = 2.061718E-125 bar


4 Jumlah =Ye+Ya 1Jumlah =Xe+Xa 1.000001

sorbitol T = 86.14932 C etanol air245.66200 a 5.33675 a

-34214.00000 b 1648.22000 b0.00000 c 230.91800 c

-29.399992.6181E-18

6.00000

P =Ptot 103 kPa etanol P =

1 bar air P =solbitol P =

Fix B/D 0.415527Pe 1.30891594548 ZePa 0.57358315873 ZaKe 1.30891594548Ka 0.57358315873Ye 0.75903694161Ya 0.24096329233Xe 0.57989739084Xa 0.42010175624

5 Jumlah =Ye+Ya 1Jumlah =Xe+Xa 0.999999

air sorbitol T = 84.84274 C etanol5.11564 a 245.66200 a 5.33675

1687.53700 b -34214.00000 b 1648.22000230.17000 c 0.00000 c 230.91800

d -29.39999e 2.6181E-18f 6.00000

10^(a-(b/T+c)) P1.30891594548 bar Ptot 103 kPa etanol P0.57358315873 bar 1 bar air P7.131657E-128 bar solbitol P

Fix B/D0.7064506545 Pe 1.2490213145

0.29354926039 Pa 0.5466004976Ke 1.2490213145Ka 0.5466004976Ye 0.8062217516Ya 0.1937788857Xe 0.645482781Xa 0.3545164824

6 Jumlah =Ye+YaJumlah =Xe+Xa

air sorbitol T = 83.61699 C etanola 5.11564 a 245.66200 ab 1687.53700 b -34214.00000 bc 230.17000 c 0.00000 c

d -29.39999e 2.6181E-18f 6.00000

= 10^(a-(b/T+c))= 1.249021314 bar Ptot 103 kPa etanol= 0.546600498 bar 1 bar air= 2.96257E-130 bar solbitol

0.317459 FixZe 0.759036942 PeZa 0.240963292 Pa

KeKaYeYaXeXa

1.000001 7 Jumlah0.999999 Jumlah

etanol air sorbitol T = 82.509395.33675 a 5.11564 a 245.66200

1648.22000 b 1687.53700 b -34214.00000230.91800 c 230.17000 c 0.00000

d -29.39999e 2.6181E-18f 6.00000

P = 10^(a-(b/T+c))P = 1.196883531 bar Ptot 103 kPaP = 0.523142102 bar 1 barP = 1.80492E-132 bar

B/D 0.2403541.196883531 Ze 0.80622175160.523142102 Za 0.19377888571.1968835310.523142102

0.84712779320.15287334760.70777796780.2922214576

=Ye+Ya 1.000001 8=Xe+Xa 0.999999

C etanol air sorbitola 5.33675 a 5.11564 a 245.66200b 1648.22000 b 1687.53700 b -34214.00000c 230.91800 c 230.17000 c 0.00000

d -29.39999e 2.6181E-18f 6.00000

P = 10^(a-(b/T+c))etanol P = 1.1529653838462 bar Ptot 103air P = 0.5034044057615 bar 1solbitol P = 1.88860034E-134 bar


Jumlah =Ye+Ya 1.000002 9Jumlah =Xe+Xa 1

T = 81.54469 C etanol air sorbitola 5.33675 a 5.11564 ab 1648.22000 b 1687.53700 bc 230.91800 c 230.17000 c

def

P = 10^(a-(b/T+c))kPa etanol P = 1.1170583194 barbar air P = 0.4872828626 bar

solbitol P = 3.72909E-136 bar


Jumlah =Ye+Ya 1.000003Jumlah =Xe+Xa 1

sorbitol T = 80.73289 C245.66200

-34214.000000.00000

-29.399992.6181E-18

6.00000

Ptot 103 kPa1 bar

10


d -29.39999e 2.6181E-18f 6.00000


D

Fix B/D 1.296809 YePe 1.578342593 Ze 0.435386654146 YaPa 0.695372703 Za 0.564613288093Ke 1.578342593Ka 0.695372703 F 100Ye 0.54895977Ya 0.452652236Xe 0.34780774 Ze 0.43538665415Xa 0.650949102 Za 0.56461328809

Jumlah =Ye+Ya 1.001612 3Jumlah =Xe+Xa 0.998757

KOMPOSISITRAIY 1 T 89.8379349395651 TRAIY 2 T 87.8042002431618 TRAIY 3 TY X MASSA Y X MASSA Y

ETANOL 0.54895977 0.347808 23.90097712729 0.640666 0.43774243754 15.28789 0.710693AIR 0.452652236 0.650949 8.243341494641 0.361988 0.56260654305 8.637941 0.292602

89.83793 C etanol air sorbitola 5.33675 a 5.11564 a 245.66200b 1648.22000 b 1687.53700 b -34214.00000c 230.91800 c 230.17000 c 0.00000

d -29.39999e 2.6181E-18f 6.00000


43.53867

0.54896 Fix B/D 0.8245640.452652 Pe 1.463567334 Ze 0.5489597698764

Pa 0.64341221 Za 0.4526522364748Ke 1.463567334Ka 0.64341221 F 43.538667929Ye 0.640665532

B 56.46133 Ya 0.361987919Xe 0.347808 Xe 0.437742438 Ze 0.5489597699Xa 0.650949 Xa 0.562606543 Za 0.4526522365

Jumlah =Ye+Ya 1.002653Jumlah =Xe+Xa 1.000349

86.1493177495008 TRAIY 4 T 84.842742711281 TRAIY 5 T 83.616987864377X MASSA Y X MASSA Y X MASSA0.516726 10.83625 0.763226 0.58309802 8.243341 0.8103440895282 0.648783 6.6553693561

0.48479 4.461434 0.240466 0.419234791 2.59719 0.1936254392255 0.354236 1.590248922

T = 87.8042 C etanol aira 5.33675 a 5.11564b 1648.22000 b 1687.53700c 230.91800 c 230.17000

P = 10^(a-(b/T+c))103 kPa etanol P = 1.37537692641

1 bar air P = 0.603564887113solbitol P = 2.06171768E-125

D 23.86251

Ye 0.640666 Fix B/D 0.565019Ya 0.361988 Pe 1.3753769264101 Ze 0.640665532268

Pa 0.6035648871132 Za 0.361987919136Ke 1.3753769264101Ka 0.6035648871132Ye 0.7106934792226

B 19.67616 Ya 0.2926023466714Xe 0.437742 Xe 0.5167263355781Xa 0.562607 Xa 0.4847902071821

4 Jumlah =Ye+Ya 1.003296Jumlah =Xe+Xa 1.001517

TRAIY 6 T 82.5093856172802 TRAIY 7 T 81.5446931577048 TRAIY 7 T 80.7328887539957Y X MASSA Y X MASSA Y X0.851179 0.711162 5.64251 0.885438 0.767966 4.9754918843975 0.913352 0.8176401527230.152962 0.292391 1.013995 0.118787 0.235968 0.667495366417 0.090895 0.18653447477

sorbitol T = 86.14932 C etanol aira 245.66200 a 5.33675 ab -34214.00000 b 1648.22000 bc 0.00000 c 230.91800 cd -29.39999e 2.6181E-18f 6.00000

P =bar Ptot 103 kPa etanol P =bar 1 bar air P =bar solbitol P =

D 15.24743

Ye 0.710693 Fix B/D 0.411714Ya 0.292602 Pe 1.308915945476 Ze

Pa 0.573583158728 ZaKe 1.308915945476

F 23.8625106086 Ka 0.573583158728Ye 0.763226296534

B 8.615081 Ya 0.24046601575Ze 0.64066553227 Xe 0.516726 Xe 0.58309802029Za 0.36198791914 Xa 0.48479 Xa 0.41923479114


80.7328887539957MASSA4.5252520.450345

air sorbitol T = 84.84274 C etanol5.11564 a 245.66200 a

1687.53700 b -34214.00000 b230.17000 c 0.00000 c

d -29.39999e 2.6181E-18f 6.00000

10^(a-(b/T+c))1.30891594547644 bar Ptot 103 kPa etanol0.57358315872772 bar 1 bar air

7.13165653E-128 bar solbitol

D 10.80065

Ye 0.763226 Fix0.71069347922258 Ya 0.240466 Pe0.29260234667142 Pa

KeF 15.24742974646 Ka

YeB 4.446778 Ya

Ze 0.710693479223 Xe 0.583098 XeZa 0.292602346671 Xa 0.419235 Xa

6 JumlahJumlah

etanol air sorbitol T = 83.616995.33675 a 5.11564 a 245.66200

1648.22000 b 1687.53700 b -34214.00000230.91800 c 230.17000 c 0.00000

d -29.39999e 2.6181E-18f 6.00000

P = 10^(a-(b/T+c))P = 1.2490213145 bar Ptot 103 kPaP = 0.5466004976 bar 1 barP = 2.962569E-130 bar

D 8.213016

B/D 0.315065 Ye1.24902131446045 Ze 0.7632262965 Ya

0.546600497584711 Za 0.24046601581.24902131446045

0.546600497584711 F 10.80065182770.8103440895281580.193625439225494 B0.648783235439189 Ze 0.76322629653 Xe0.354235753683131 Za 0.24046601575 Xa

=Ye+Ya 1.00397 7=Xe+Xa 1.003019

C etanol air sorbitola 5.33675 a 5.11564 a 245.66200b 1648.22000 b 1687.53700 b -34214.00000c 230.91800 c 230.17000 c 0.00000

d -29.39999e 2.6181E-18f 6.00000


0.810344 Fix B/D 0.2389420.193625 Pe 1.19688353101 Ze 0.8103440895

Pa 0.52314210197 Za 0.1936254392Ke 1.19688353101Ka 0.52314210197Ye 0.8511785645 F 8.21301647302773

2.587635 Ya 0.152962181040.648783 Xe 0.71116240005 Ze 0.8103440895281580.354236 Xa 0.29239126514 Za 0.193625439225494

Jumlah =Ye+Ya 1.004141Jumlah =Xe+Xa 1.003554

T = 82.50939 C etanol aira 5.33675 a 5.11564b 1648.22000 b 1687.53700c 230.91800 c 230.17000

P = 10^(a-(b/T+c))103 kPa etanol P = 1.15296538385

1 bar air P = 0.50340440576solbitol P = 1.8886E-134

D 6.629055

Ye 0.851179 Fix B/D 0.179706Ya 0.152962 Pe 1.15296538384623 Ze 0.8511785645

Pa 0.503404405761544 Za 0.15296218104Ke 1.15296538384623Ka 0.503404405761544Ye 0.885438299158896

B 1.583961 Ya 0.118787443667654Xe 0.711162 Xe 0.767966073886035Xa 0.292391 Xa 0.235968224171486


sorbitol T = 81.54469 C etanola 245.66200 a 5.33675b -34214.00000 b 1648.22000c 0.00000 c 230.91800d -29.39999e 2.6181E-18f 6.00000

Pbar Ptot 103 kPa etanol Pbar 1 bar air Pbar solbitol P

D 5.619242

Fix B/DYe 0.885438 Pe 1.11705831940112Ya 0.118787 Pa 0.487282862608904

Ke 1.11705831940112F 6.62905513116272 Ka 0.487282862608904

Ye 0.913351734876179Ya 0.0908950528409747

Ze 0.85117856449597 B 1.009813 Xe 0.817640152723495Za 0.1529621810435 Xe 0.767966 Xa 0.186534474769591

9 Xa 0.235968 Jumlah =Ye+YaJumlah =Xe+Xa

air sorbitol T = 80.73289 Ca 5.11564 a 245.66200b 1687.53700 b -34214.00000c 230.17000 c 0.00000

d -29.39999e 2.6181E-18f 6.00000

= 10^(a-(b/T+c))= 1.117058319401 bar Ptot 103 kPa= 0.487282862609 bar 1 bar= 3.72908888E-136 bar

D 4.954555

0.134157 Ye 0.913352Ze 0.885438299159 Ya 0.090895Za 0.118787443668

F 5.61924178017

B 0.664687Ze 0.88543829916 Xe 0.81764Za 0.11878744367 Xa 0.186534

1.004247 101.004175

D 4.954555 B 0.664687Ye 0.913352 Xe 0.81764Ya 0.090895 Xa 0.186534De 4.525252 Be 0.543474Da 0.450345 Ba 0.123987





10

8

7

9




F 100 B 56.46133Ye 0.435387 Xe 0.347808Ya 0.564613 Xa 0.650949

5

6

4

3

61.41589

benzene toluena xylene T =a 3.9852 a 4.0504 a 4.0979b 1184.2400 b 1327.6200 b 1458.7060c 217.5720 c 217.6250 c 212.0410 log pv

benzene P = 0.4440754109 2.780195979 Ptot 103 kPatoluena P = 0.0811647335 1.2054931129 1 barxylene P = -0.3373362604 0.4599003495

Fix B/D 0.704518 Zb 0.3Pe 2.780195979 Zt 0.3Pa 1.2054931129 Zx 0.4Pt 0.4599003495Ke 2.780195979Ka 1.2054931129Kt 0.4599003495Ye 0.4079726954Ya 0.3227391727Yt 0.2692875668Xe 0.1467424234Xa 0.2677237798Xt 0.5855345991Jumlah =Ye+Ya+Yt 1.000 0.9999994348Jumlah =Xe+Xa+Yt 1.000 F 100

M1E Ze 0.3M1A Za 0.3M1T Zt 0.4

1

390 k117 c

41.33238A-(B/(T+C-273.15)) 58.66762



1+ B/(Dki)



Xe+ Xa + Xt = 1

D 58.66762 kgYe 0.407973 M2EYa 0.322739 M2AYt 0.269288


cari P⁰e,P⁰a,P⁰t

1

X03

X01 X1

X02

420 420 420.18 420.72

Kapasitan Komponen X01 X02 X03 X04

H2O 0 1200 0 0Urea 0 0 0 2Ragi 0 0 3 0Tetes 60 0 0 0Etanol 0 0 0 0kondisi operasi T.P : 30,100.3 T.P : 30, 100.3 T.P : 30, 100.3 T.P : 30, 100.3

Komponen X01 X02 X03 X04H2O 0 360 0 0Urea 0 0 0 0.06Ragi 0 0 0.12 0Tetes 60 0 0 0Etanol 0 0 0 0CO2 0 0 0 0SludgeTOTAL 60 360 0.12 0.06

FERMENTASI

C6H12O6 (LR) yield 0.8MASSA 9.6 KGMR 180MOL tetes total 0.053 KGMOLmol tetes reaksi 0.043 KGMOLmol tetes sisa 0.011 KGMOL 1.92 KGC2H5OH (2LR)MOL 0.085 KGMOLMR 46MASSA 3.925 KGCO2 (2LR)MOL 0.085 KGMOLMR 44MASSA 3.755 KG

Mixer Fermentor

X04

X2 X32

X2 X2

X31

420.72 420.72 317.2264 317.22640

X1 X2 X31 X32 X41X02 H2O X02 H2O 0 X2 H2O M2AIR/M1AIR*32H2O

0 X04 Urea X2 Urea 0 00 X03 Ragi X2 Ragi 0 0

X01 tetes 0,2*X01 Tetes 0 X2 Tetes 00 0,8*X01 Tetes 0 X2 Etanol M2/M1(ETANOL)*32ETANOL

T.P : 35, 100.3 T.P : 35, 100.3 T.P : 30, 100.3 T.P : 30, 100.3 T.P : 175, 100.3

X1 X2 X31 X32 X41360 360 72 288 279.04133416382

0 0.6 0.6 0 00 0.12 0.12 0 0

60 12 2.4 9.6 19.62639999862830 24.533 4.9066 19.626 8.958660718289470 23.47 23.467 0

420 420.72 103.494 317.2264 307.626394880738

Fermentor flash distillationPEMISAHAN

X41 41 X51

X32

X42X52

307.626394880738 191.859605026795

X42 X51 X52M3/M1*32AIR

0 0 00 0 0

M3/M1*32TETES 0 42TETESM3/M1*32ETANOL

T.P : 80, 100.3 T.P: 100, 100.3

X42 X51 X528.95866583617953 13.3250075302948 178.476718507342

0 0 00 0 0

1.3717078516E-09 0 1.37170785155153E-090.64133928171053 O 0.0578789877867016

9.60000511926177 13.3250075302948 178.5345974965

((0.1)*(0.425)*41)/0.89 ((41*(1-0.425/0.89)-((0.01)*(1-0.425/0.89)*41-42tetes

((0.90)*(0.425)*41)/0.89 ((0.01)*(1-0.425/0.89)*41

flash distillation Distilasi 2

KomponenH2OUreaRagiTetesEtanol

D 67.16629 kgYe

YaYt

F 100

M1E Ze 0.3 m,n,n,nnnnnM1A Za 0.4M1T Zt 0.3

B 32.83371 kgXeXaXt

1

0.435387 M2E

0.564613 M2A6.265E-47

0.023046 M3E0.063259 M3A0.913695 M3T

etanol air sorbitol T =a = 86.486 a = 65.9278 a = 245.662b = -7931.1 b = -7227.53 b = -34214c = 0 c = 0 c = 0d = -10.2498 d = -7.17695 d = -29.3999e = 6.38949E-06 e = 0.0000040313 e = 2.6181E-18f = 2 f = 2 f = 6

etanol P = 236.28401754 bar Ptot 103 kPaair P = 105.96547581 bar 1 barsolbitol P = 0.000000002 bar

Fix B/D 32.04442 Ze 0.030262Pe 236.2840175 Za 0.907869Pa 105.9654758 Zt 0.061869Pt 0.000000002Ke 2.294019588Ka 1.028791027Kt 2.239615E-09Ye 0.06681Ya 0.93319Yt 1.428862E-10Xe 0.029121885Xa 0.907078632Xt 0.063799466Jumlah =Ye+Ya+Yt 1.000001Jumlah =Xe+Xa+Yt 1 F 317.2264

H2O 288 M1E Ze 0.030262etanol 9.6 M1A Za 0.907869tetes 19.6264 M1T Zt 0.061869

317.2264

1

101.408 C = 374.408 K



1+ B/(Dki)



Xe+ Xa + Xt = 1

D 9.6 kgYe 0.066806 M2E 0.6413392817Ya 0.933194 M2A 8.9586658362Yt 1.429E-10 1.3717079E-09

B 307.6264 kgXe 0.029122 M3E 8.9586607183Xa 0.907079 M3A 279.04133416Xt 0.063799 M3T 19.626399999


1


etanol P = 214.08394374 bar Ptot 103 kPaair P = 95.617564754 bar 1 barsolbitol P = 1.3843197E-09 bar

Fix B/D 13.96868 Ze 0.067Pe 214.084 Za 0.933Pa 95.618 Zt 0.000Pt 0.000Ke 2.078484891Ka 0.928325871Kt 1.344E-11Ye 0.129523531Ya 0.870476544Yt 2.057869E-21Xe 0.062316321Xa 0.937684245Xt 1.531153E-10Jumlah =Ye+Ya+Yt 1Jumlah =Xe+Xa+Yt 1.000001 F 9.6000

etanol 0.641 M1E Ze 0.067air 8.959 M1A Za 0.933tetes 0.000 M1T Zt 0.000

9.600005119

1

98.53145 C = 371.5314 K



1+ B/(Dki)



Xe+ Xa + Xt = 1

D 0.641339 kgYe 0.12952 M2E 0.0830684843Ya 0.87048 M2A 0.5582705037Yt 0.00000 1.3197914E-21



1


etanol P = 202.18298189 bar Ptot 103 kPaair P = 90.091512891 bar 1 barsolbitol P = 1.047276E-09 bar

Fix B/D 6.720605 Ze 0.130Pe 202.183 Za 0.870Pa 90.092 Zt 0.000Pt 0.000Ke 1.9629415718Ka 0.8746748824Kt 1.016772E-11Ye 0.2260529859Ya 0.7739471042Yt 1.669003E-21Xe 0.1151603232Xa 0.8848397498Xt 1.641472E-10Jumlah =Ye+Ya+Yt 1Jumlah =Xe+Xa+Yt 1 F 0.6413


0.6413389882

1

96.88792 C = 369.8879 K



1+ B/(Dki)



Xe+ Xa + Xt = 1

D 0.083068 kgYe 0.22605 M2E 0.0187778775Ya 0.77395 M2A 0.064290608Yt 0.00000 1.386415E-22



1

etanol air sorbitol T = 94.70038a = 86.486 a = 65.9278 a = 245.662b = -7931.1 b = -7227.53 b = -34214c = 0 c = 0 c = 0d = -10.2498 d = -7.17695 d = -29.3999e = 0.00000638949 e = 4.0313E-06 e = 2.6181E-18f = 2 f = 2 f = 6

12

etanol P = 187.18514 bar Ptot 103 kPaair P = 83.1499104 bar 1 bar 3solbitol P = 7.1896E-10 bar 4

Fix B/D 3.423742 Ze 0.226Pe 187.185 Za 0.774 5Pa 83.150 Zt 0.000Pt 0.000Ke 1.8173314555Ka 0.8072806837Kt 6.9801934E-12Ye 0.3467479766 DYa 0.6532512916Yt 1.2886845E-21Xe 0.1908006245Xa 0.8091997056Xt 1.8462017E-10Jumlah =Ye+Ya+Yt 0.999999Jumlah =Xe+Xa+Yt 1 F 0.0831


0.0830684856

B

11

C = 367.7004 K

cari Ke,Ka,Kt ---> K1=P1⁰/Pt pt = 103 Kpa ==> 1 barTrial B/D-----> Harga terserah Hitung Ye = Ze (B/D +1) , Ya Yt

1+ B/(Dki)


Trial BenarBila Ye + Ya + Yt = 1

Xe+ Xa + Xt = 1

0.018778 kgYe 0.34675 M2E 0.006511Ya 0.65325 M2A 0.012267Yt 0.00000 2.42E-23

0.064291 kgXe 0.191 M3EXa 0.809 M3AXt 0.000 M3T


etanol air sorbitol T = 92.29842a = 86.486 a = 65.9278 a = 245.662b = -7931.1 b = -7227.53 b = -34214c = 0 c = 0 c = 0d = -10.2498 d = -7.17695 d = -29.3999e = 6.38949E-06 e = 4.0313E-06 e = 2.6181E-18f = 2 f = 2 f = 6

12




0.018777862

B

111

C = 365.2984 K


1+ B/(Dki)



Xe+ Xa + Xt = 1

0.006511 kgYe 0.46956 M2E 0.003057Ya 0.53043 M2A 0.003454Yt 0.00000 6.536E-24

0.012267 kgXe 0.282 M3EXa 0.718 M3AXt 0.000 M3T


etanol air sorbitol T = 90.04027a = 86.486 a = 65.9278 a = 245.662b = -7931.1 b = -7227.53 b = -34214c = 0 c = 0 c = 0d = -10.2498 d = -7.17695 d = -29.3999e = 6.3895E-06 e = 4.0313E-06 e = 2.6181E-18f = 2 f = 2 f = 6

12


Fix B/D 1.129633 Ze 0.470Pe 158.254 Za 0.530 5Pa 69.836 Zt 0.000Pt 0.000Ke 1.53644364Ka 0.67801635Kt 3.0746E-12Ye 0.5762927 DYa 0.42370382Yt 8.2823E-22Xe 0.37508223Xa 0.62491682Xt 2.6938E-10Jumlah =Ye+Ya+Yt 0.999997Jumlah =Xe+Xa+Yt 0.999999 F 0.0065


0.00651118

B

1111

C = 363.0403 K


1+ B/(Dki)



Xe+ Xa + Xt = 1

0.003057 kgYe 0.57629 M2E 0.001762Ya 0.42370 M2A 0.001295Yt 0.00000 2.532E-24

0.003454 kgXe 0.375 M3EXa 0.625 M3AXt 0.000 M3T


etanol air sorbitol T = 88.12157 Ca = 86.486 a = 65.9278 a = 245.662b = -7931.1 b = -7227.53 b = -34214c = 0 c = 0 c = 0d = -10.2498 d = -7.17695 d = -29.3999e = 6.389E-06 e = 4.031E-06 e = 2.618E-18f = 2 f = 2 f = 6


etanol P = 147.4609 bar Ptot 103 kPa pt =air P = 64.89683 bar 1 bar 3 Trial B/D-----> Harga terserah solbitol P = 2.243E-10 bar 4 Hitung

Fix B/D 0.735223 Ze 0.576Pe 147.461 Za 0.424 5 Trial BenarPa 64.897 Zt 0.000 Bila Pt 0.000Ke 1.431659Ka 0.630066Kt 2.177E-12Ye 0.660698 D 0.001762Ya 0.339296Yt 7.342E-22Xe 0.461491Xa 0.538509Xt 3.372E-10Jumlah =Ye+Ya+Yt 0.999994Jumlah =Xe+Xa+Yt 1 F 0.0031


0.003057

B 0.001295


1111

= 361.1216 K

cari Ke,Ka,Kt ---> K1=P1⁰/Pt 103 Kpa ==> 1 bar

Trial B/D-----> Harga terserah Ye = Ze (B/D +1) , Ya Yt

1+ B/(Dki)


Trial BenarYe + Ya + Yt = 1Xe+ Xa + Xt = 1

kgYe 0.66070 M2E 0.001164Ya 0.33930 M2A 0.000598Yt 0.00000 1.294E-24

kgXe 0.461 M3EXa 0.539 M3AXt 0.000 M3T







0.001762

B 0.000598


1111

= 359.577 K



1+ B/(Dki)



kgYe 0.72466 M2E 0.000844Ya 0.27533 M2A 0.000321Yt 0.00000 8.058E-25

kgXe 0.536 M3EXa 0.464 M3AXt 0.000 M3T





Fix B/D 0.379937 Ze 0.725Pe 128.946 Za 0.275 5 Trial BenarPa 56.463 Zt 0.000 Bila Pt 0.000Ke 1.251902Ka 0.548187Kt 1.13E-12Ye 0.767165 D 0.000844Ya 0.224404Yt 5.864E-22Xe 0.6128Xa 0.409357Xt 5.19E-10Jumlah =Ye+Ya+Yt 0.99157Jumlah =Xe+Xa+Yt 1.022157 F 0.0012


0.001164

B 0.000321


1111

= 357.543 K



1+ B/(Dki)



kgYe 0.76717 M2E 0.000647Ya 0.22440 M2A 0.000189Yt 0.00000 4.947E-25

kgXe 0.613 M3EXa 0.409 M3AXt 0.000 M3T







0.000837

B 0.000191


1111

= 357.0926 K



1+ B/(Dki)



kgYe 0.80115 M2E 0.000523Ya 0.18796 M2A 0.000123Yt 0.00000 4.283E-25

kgXe 0.651 M3EXa 0.349 M3AXt 0.000 M3T







0.000646

B 0.000124


1111

= 356.2703 K



1+ B/(Dki)



kgYe 0.82652 M2E 0.000437Ya 0.16003 M2A 8.46E-05Yt 0.00000 3.544E-25

kgXe 0.693 M3EXa 0.307 M3AXt 0.000 M3T







0.000522

B 8.576E-05


1111

= 355.5986 K



1+ B/(Dki)



kgYe 0.84567 M2E 0.000375Ya 0.13827 M2A 6.124E-05Yt 0.00000 3.066E-25

kgXe 0.728 M3EXa 0.272 M3AXt 0.000 M3T







0.000436

B 6.224E-05


1111

= 355.0417 K



1+ B/(Dki)



kgYe 0.86030 M2E 0.000327Ya 0.12102 M2A 4.607E-05Yt 0.00000 2.739E-25

kgXe 0.756 M3EXa 0.244 M3AXt 0.000 M3T







0.000374

B 4.695E-05


1111

= 354.5728 K



1+ B/(Dki)



kgYe 0.87158 M2E 0.000291Ya 0.10711 M2A 3.575E-05Yt 0.00000 2.504E-25

kgXe 0.780 M3EXa 0.220 M3AXt 0.000 M3T





Fix B/D 0.122897 Ze 0.872Pe 113.300 Za 0.107 5 Trial BenarPa 49.379 Zt 0.000 Bila Pt 0.000Ke 1.100002Ka 0.479404Kt 6E-13Ye 0.880334 D 0.000297Ya 0.095735Yt 7.837E-22Xe 0.800303Xa 0.199697Xt 1.306E-09Jumlah =Ye+Ya+Yt 0.97607Jumlah =Xe+Xa+Yt 1 F 0.0003


0.000327

B 3.652E-05


1111

= 354.1723 K



1+ B/(Dki)



kgYe 0.88033 M2E 0.000262Ya 0.09574 M2A 2.845E-05Yt 0.00000 2.329E-25

kgXe 0.800 M3EXa 0.200 M3AXt 0.000 M3T







0.00029

B 2.915E-05


1111

= 353.8255 K



1+ B/(Dki)



kgYe 0.88717 M2E 0.000238Ya 0.08630 M2A 2.313E-05Yt 0.00000 2.195E-25

kgXe 0.817 M3EXa 0.183 M3AXt 0.000 M3T


etanol air sorbitol T = 80.52136a = 86.486 a = 65.9278 a = 245.662b = -7931.1 b = -7227.53 b = -34214c = 0 c = 0 c = 0d = -10.2498 d = -7.17695 d = -29.3999e = 0.00000638949 e = 4.031E-06 e = 2.618E-18f = 2 f = 2 f = 6

12




0.000260937625

B

1111

C = 353.5214 K


1+ B/(Dki)



Xe+ Xa + Xt = 1

0.000244 kgYe 0.89252 M2E 0.000218Ya 0.07837 M2A 1.914E-05Yt 0.00000 2.088E-25

2.376E-05 kgXe 0.832 M3EXa 0.168 M3AXt 0.000 M3T


Documents

Dpa Dinda Acak2