Beban Steam Dan Air Pendingin

Menghitung beban steamHE 312CPO M 18000 kg/jam Steam

T1 80 C 353.15 KT2 90 C 363.15 KCp CPO 460.431 Kkal/Kmol 0C 0.52 Kkal/Kg 0CPanas Masuk

QCPO 93600 Kkal 391894.2 Kj

Q steam = QCPO Data Steam :

Qsteam = m. ental phi entalphi Msteam = 144.8085 Kg

3475.403 KG / hari

HE 712CPO M 20000 kg/jam Steam


QCPO 41600 Kkal 174175.2 Kj

Q steam = QCPO

Qsteam = m. ental phiMsteam = 64.35931 Kg/jam

1544.624 KG / hari

HE 722 Dari GK BoilerCPO M 20000 kg/jam Steam


QCPO 270400 Kkal 1132139 Kj

Q steam = QCPO

Qsteam = m. ental phiMsteam = 404.0739 Kg/jam

9697.773 KG / hari

Total HE di refeneri= 14717.8 Kg/hari

Ejector systemSteam 8.5 Bar

tair 30 ctout 34 c

Bar Kj/kg 1 Kj = 0.23884 k cal1.985 2706

2 2706.292.701 2720

EntalphiBar Kj/kg

1.985 27062 2706.29

2.701 2720

EntalphiBar Kj/kg

39.73 280240 2801.81

46.88 2797

EntalphiBar Suhu Kj/kg

7.916 170 27698.5 172.776 2771.498

10.02 180 2778

CPO mixer

CPO dengan kandungan Kandungan PAFA 93.5 % H3PO4FFA 5 % H2OH2O 0.5 %Impurities dan Gum 1 %

100 %

N1 (Masuk) N2 (Masuk)Misal laju alir CPO 20000 kg/ jam Misal PA : Maka dalam cpo ada : PA dipakaiFA 18700 kg/ jam H3PO4FFA 1000 kg/ jam H2OH2O 100 kg/ jamImpurities 200 kg/ jamJumlah 20000 kg/ jam Jumlah

Neraca Massa Mixer

Zat Masuk (kg/jam) Keluar (kg/jam)N1 N2 N3

FA 18700 18700FFA 1000 1000H2O 100 1.5 101.5

Impurities 200 200H3PO4 8.5 8.5

Sub Jumlah 20000 10 20010Jumlah 20010 20010

Di BleacherBE kandungan

BEH2OPenggunaan BE 1 %

Zat

N3

N4N6

N1

FA 93,5%FFA 0,5%H2O 15% Impuritis 1%

N2

H3PO4 85%H2O 15%

N3

FA 93,5%FFA 0,5%H3PO4 0,085%H2OImpuritis 1%

Zat

FAFFAH2O

ImpuritiesH3PO4

BE

Jumlah

Kadar air yang di bpo diharapkan 0.1 %jadi = 0.1215 kg/jam

Jadi Air yang harus ditarik steam sebanyak= 121.3785 kg/jam

Maka minimum steam yang dibutuhkan :

Suhu air T 120CAhf 503.7 Kj/Kg

Q air= 61138.35045 Kj

Steam yang digunakanEntalphi

Bar Kj/kg1.985 2706

2 2706.293296092.701 2720

Maka massa steam yang digunakan :M= 22.5911768463 Kg/jamdalam 24 jam 542.188244312 Kg/hari

Vakuum bleaching

Other, similar equations have been derived for counter- and co-current deodorization [4].

- with S = Total moles of steam or any other stripping agent per mole of oil (to express the amount of steam as a percentage of the oil, the factor S has to be multiplied by a factor of 2.);

Pt = Total pressure of the gas phase = system pressure; maks 3 Torr

Pi0 = Vapor pressure of a given fatty acid i;

E = Vaporization Efficiency; di industri E=0.3-0.7,, gas ideal 1

Va = Initial amount of the volatile component in the oil (moles),

V0 = Final amount of the volatile component in the oil (moles).

N5

Kandungan Caroten dalam FA = 0.008 % 1.496 Kg/jam 0.00302

Komponen a b/t c log 10 t d t

AIR 29.8605 -3.15E+03 -7.304E+00 2.42E-09

TocoperolCaroten

jumlah

Operating system Presure50 torr 38000 mm HG

S vacuum -70288.009001 -70.28801 KmolKarena faktor S perkalian faktor 2 = maka S= -35.1440045005 Kmol

S= -633.294961098 Kg/jam-15199.0790664 kg/hari

H2O (l)

300/10000000.03 %

Kandungan PA85 %15 %

N2 (Masuk) N3 (keluar)0.05 % FA 18700 Kg/jam

10 Kg/jam FFA 1000 Kg/jam8.5 Kg/jam H2O 101.5 Kg/jam1.5 Kg/jam Impurities 200 Kg/jam

H3PO4 8.5 Kg/jamKg/jam

10 Kg/jam Jumlah 20010 Kg/jam

BE kandungan

90 %10 %

Penggunaan BE 1 % 200 Kg/jam

Masuk (kg/jam) Keluar (kg/jam) Keluar (kg/jam)

N1

FA 93,5%FFA 0,5%H2O 15% Impuritis 1%

N2

H3PO4 85%H2O 15%

N3

FA 93,5%FFA 0,5%H3PO4 0,085%H2OImpuritis 1%

N3 N4 N5 N618700 187001000 1000101.5 20 0.1215 121.3785200 2008.5 8.5

180 18020010 200 20088.6215 121.3785

20210 20210

senyawa mr (kg/kmol)FFA 256H20 18.02c14h28o2 228.3709c16h32o2 256.4241C18H3602 284.4772C18H34O2 282.4614C18H3202 280.45 WIKIPEDIAH3PO4 97.9952Karoten (F) 495.37Gum (J) 128.94BE (K) 284.18Spent Earth (L) 1186.79posfatida



Kmol

ET2 mm hg

1.81E-06 ### -1.435E+021.000E-022.710E-16 8.184E-19

### -1.435E+02

FL 621Neraca masuk

Zat Masuk (kg/jam) Keluar (kg/jam) Keluar (kg/jam)N3 N4 N5 N6

FA 18700 0 18700 0FFA 1000 0 1000 0H2O 101.5 20 0.1215 121.3785

Impurities & gum 200 0 200 0H3PO4 8.5 0 8.5 0

BE 0 180 180 020010 200 20088.6215 121.3785

Jumlah 20210 20210

ZatMasuk (kg/jam) Keluar (kg/jam)

N5 N7 N8FA 18700 18700

FFA 1000 1000H2O 0.1215 0.1215

Impurities & gum 200 200H3PO4 8.5 8.5

BE 180 180388.5 19700.1215

Jumlah 20088.6215 20088.6215

Steam yang digunakan untuk mengeringkan cake dari minyak :

Steam 4 bart 32 menitT in 120 c 393.15 KT out 50 c 323.15 K

Massa cake 388.5 kg/jam

Q= 15605825.84549 Joule

Q= 15605.82584549 Kj M steam= 5.699600900356 Kg/jam

136.7904216086 Kg/hari

N5FAFFAH2OImpuriteis n gumH3PO4BE

FL 621

EntalphiBar Suhu Kj/kg

3.613 140 27344 143.3799 2738.056

4.758 150 2746

Sio2 komponen utama Suhu CP Joule/mol KT min 100 18.033 Cp min

323.15 34.43095T max 848 72.999 Cp Max

BM BE= 60 gr/mol http://eprints.upnjatim.ac.id/4331/1/file_1.pdf60 kg/kmol

N5FAFFAH2OImpuriteis n gumH3PO4BE

N7Impuriteis n gumH3PO4BE

N8FAFFAH2O

http://eprints.upnjatim.ac.id/4331/1/file_1.pdf

Deodorized

Neraca Massa


N8 N9 N10 N11Myristic 172.04 159.9972 12.0428Palmitic 8697.37 8088.5541 608.8159Stearic 618.97 575.6421 43.3279Oleic 7401.46 6883.3578 518.1022Linoleic 1810.16 1683.4488 126.7112FFA 1000 1 999H2O 0.1215 0.0001215 0.001215 0.1201635

17392.00012 2308.001215 0.1201635Jumlah 19700.1215 19700.1215

ZatMasuk (kmol/jam) Keluar (kmol/jam)

N8 N9 N10 N11Myristic 0.75333591101143 0.700602397 0.0527335138Palmitic 33.9179117719434 31.54365795 2.374253824Stearic 2.17581584745632 2.023508738 0.1523071093Oleic 26.2034387707489 24.36919806 1.834240714Linoleic 6.45448386521662 6.002669995 0.4518138706FFA 3.90625 0.00390625 3.90234375H2O 0.00674250832408 6.74251E-06 6.742508E-05 0.00666834073

64.64355013 8.7677602067 0.00666834073Jumlah 73.4179786747007 73.4179786747007

25 298T1 256 529.15 K

Komponen a bTFFA 0.08056 0.003289 -6.836E-06 5.695E-09

AIR 92.0530 -4.00E-02 -2.110E-04 5.35E-07

formaldehyde CH2OMyristic c14h28o2 80.266 2.82E+00 -6.01E-03 5.13E-06Palmitic c16h32o2 86.29 3.5237 -7.32E-03 6.10E-06stearic acid C18H3602 99.012 3.5874 -7.25E-03 5.90E-06oleic acid C18H34O2 278.686 2.5434 -5.44E-03 4.92E-06linoleic acid C18H32O2 241.348 2.31E+00 -5.07E-03 4.75E-06

h3po4 55.20955 3001.3204 -0.095194 0.04231

ZatMasuk Q Keluar Q

N8 N9 N10 N11Myristic 3.573E+02 3.323E+02 2.501E+01 0Palmitic 1.984E+04 1.845E+04 1.389E+03 0Stearic 1.336E+03 1.242E+03 9.350E+01 0Oleic 1.669E+04 1.552E+04 1.168E+03 0Linoleic 3.630E+03 3.376E+03 2.541E+02 0FFA 2.132E+00 2.132E-03 2.130E+00 0H2O 5.269E-01 5.269E-04 5.269E-03 5.211E-01

38924.26171 2931.9184912 5.21E-01Jumlah 41856.7013075304 41856.7013075304

Beban Q= 41856.7013075304 Kj

Steam sparging 15.4664320264229 Kg/jam371.194368634149 Kg/hari

Vakuum Deo

cT2 dT3

H2O (l)


Pt = Total pressure of the gas phase = system pressure; maks 3 Torr

Pi0 = Vapor pressure of a given fatty acid i;

E = Vaporization Efficiency; di industri E=0.3-0.7,, gas ideal 1

Va = Initial amount of the volatile component in the oil (moles),

V0 = Final amount of the volatile component in the oil (moles).


Komponen a b/t c log 10 t d tFFA 34.6559 -5.26E+03 -8.86E+00 2.30E-03

AIR 29.8605 -3.15E+03 -7.304E+00 2.42E-09

Myristic c14h28o2 -79.3115 -4.69E+03 4.36E+01 -6.85E-02Palmitic c16h32o2 34.6559 -5.26E+03 -8.86E+00 2.30E-03stearic acid C18H3602 -40.3638 -4.77E+03 2.45E+01 -3.77E-02oleic acid C18H34O2 78.6973 -8.82E+03 -2.25E+01 4.84E-11linoleic acid C18H32O2 40.6453 -7.54E+03 -7.56E+00 -1.07E-02

jumlah

S vacuum -106335.663638947 -106.335664 KmolKarena faktor S perkalian faktor 2 = maka S= -53.16783182 Kmol

S= -958.0843294 Kg/jam-22994.02391 kg/hari

H2O (l)

Kandungan FA 18700 Kg/jamN8Myristic 0.92 % 172.04 Kg/jam 0.753335911011Palmitic 46.51 % 8697.37 Kg/jam 33.91791177194Stearic 3.31 % 618.97 Kg/jam 2.175815847456Oleic 39.58 % 7401.46 Kg/jam 26.20343877075Linoleic 9.68 % 1810.16 Kg/jam 6.454483865217

69.50498616638N10 Diharapkan FFA dari PFAD 99,9 % 999

Diharapkan FA 7 % 1309Myristic 0.92 % 12.0428 Kg/jamPalmitic 46.51 % 608.8159 Kg/jamStearic 3.31 % 43.3279 Kg/jamOleic 39.58 % 518.1022 Kg/jamLinoleic 9.68 % 126.7112 Kg/jamH20 1 % 0.001215 Kg/jam

N9 Diharapkan FFA dari RBDPO 0.1 % 1Diharapkan FA 93 % 17391

Myristic 0.92 % 159.9972 Kg/jamPalmitic 46.51 % 8088.5541 Kg/jamStearic 3.31 % 575.6421 Kg/jamOleic 39.58 % 6883.3578 Kg/jamLinoleic 9.68 % 1683.4488 Kg/jamH20 0.1 % 0.0001215 Kg/jam

N11H20 98.9 % 0.1201635 Kg/jam

BMsenyawa mr (kg/kmol)FFA 256H20 18.02c14h28o2 228.3709 n-tetradecanoid acidc16h32o2 256.4241 n-hexadecanoid acidC18H3602 284.4772 stearic acidC18H34O2 282.4614 oleic acidC18H3202 280.45 WIKIPEDIA linoleic acidH3PO4 97.9952Karoten (F) 495.37Gum (J) 128.94BE (K) 284.18Spent Earth (L) 1186.79

Joule/mol K

ET4 CP ZatMasuk (kmol/jam)

5.459E-01 N8

7.815E+01 Myristic 753.3359110114

0.000E+00 Palmitic 33917.911771944.743E+02 Stearic 2175.8158474565.849E+02 Oleic 26203.438770756.139E+02 Linoleic 6454.4838652176.370E+02 FFA 3906.255.624E+02 H2O 6.742508324084

0.000512 1.211E+06Jumlah 73417.9786747

Zat Masuk QN8

Myristic 3.573E+05Palmitic 1.984E+07Stearic 1.336E+06Oleic 1.669E+07Linoleic 3.630E+06FFA 2.132E+03H2O 5.269E+02

Jumlah 41856701.31

Entalphi EntalphiBar Suhu Kj/kg Bar Suhu

7.916 170 2769 39.73 2508.5 172.775665399 2771.49809886 256

10.02 180 2778 46.88 260

EntalphiBar Kj/kg

1.985 27062 2706.29329609

2.701 2720


L72

D0002:


mm hg Operating system PresureET2 3 torr

-3.61E-13 1.000E+01 3.902E+04

1.81E-06 -9.450E-01 -6.372E-020.000E+00

2.79E-05 -1.095E+01 -5.774E+02-3.61E-13 -8.542E+00 -2.028E+041.46E-05 -1.102E+01 -1.678E+032.66E-06 -1.245E+01 -2.284E+045.26E-06 -1.203E+01 -5.437E+03

-4.594E+01 -1.179E+04

senyawa mr (kg/kmol)FFA 256

Kmol/jam H20 18.02Kmol/jam c14h28o2 228.3709Kmol/jam c16h32o2 256.4241Kmol/jam C18H3602 284.4772Kmol/jam C18H34O2 282.4614Kmol/jam C18H3202 280.45 WIKIPEDIAKg/jam H3PO4 97.9952Kg/jam Karoten (F) 495.37

Gum (J) 128.94BE (K) 284.18Spent Earth (L) 1186.79posfatida

Kg/jamKg/jam

Keluar (kmol/jam)N9 N10 N11

700.6023972406 52.733513771 031543.65794791 2374.253824 02023.508738134 152.30710932 024369.1980568 1834.240714 0

6002.669994651 451.81387057 03.90625 3902.34375 0

0.006742508324 0.0674250832 6.668340732564643.55012724 8767.7602067 6.6683407325

73417.9786747007

Keluar QN9 N10 N11

3.323E+05 2.501E+04 01.845E+07 1.389E+06 01.242E+06 9.350E+04 01.552E+07 1.168E+06 03.376E+06 2.541E+05 02.132E+00 2.130E+03 05.269E-01 5.269E+00 5.211E+023.892E+07 2.932E+06 5.211E+02

41856701.31

Kj/kg280227992797

Operating system Presure2280 mm HG


N8 N9 N10 N11Myristic 172.04 159.9972 12.0428 0Palmitic 8697.37 8088.5541 608.8159 0Stearic 618.97 575.6421 43.3279 0Oleic 7401.46 6883.3578 518.1022 0Linoleic 1810.16 1683.4488 126.7112 0FFA 1000 1 999 0H2O 0.1215 0.0001215 0.001215 0.1201635

0 17392.0001215 2308.001215 0.1201635Jumlah 19700.1215 19700.1215 0 0


N8 N9 N10 N11Myristic 0.753335911011429 0.700602397241 0.0527335138 0Palmitic 33.9179117719434 31.54365794791 2.374253824 0Stearic 2.17581584745632 2.023508738134 0.1523071093 0Oleic 26.2034387707489 24.3691980568 1.834240714 0Linoleic 6.45448386521662 6.002669994651 0.4518138706 0FFA 3.90625 0.00390625 3.90234375 0H2O 0.00674250832408435 6.742508324E-06 6.7425083E-05 0.0066683407

0 64.64355012724 8.7677602067 0.0066683407Jumlah 73.4179786747007 73.4179786747 0 0

T minyak masuk 65 C 338.15 K 10Tminyak keluar 55 C 328.15 K

Komponen a bT ET4FFA 0.08056 0.003289 -6.836E-06 5.695E-09

92.0530 -4.00E-02 -2.110E-04 5.35E-07

c14h28o2 80.266 2.82E+00 -6.01E-03 5.13E-06c16h32o2 86.29 3.5237 -7.32E-03 6.10E-06C18H3602 99.012 3.5874 -7.25E-03 5.90E-06C18H34O2 278.686 2.5434 -5.44E-03 4.92E-06C18H32O2 241.348 2.31E+00 -5.07E-03 4.75E-06

Jumlah massa masuk HE 742

Zat N9 CP Q (Kj/Kmol K)

Myristic 0.700602397240629 1.128E-01 0.0790084001Palmitic 31.5436579479074 9.163E+01 2890.4369077Stearic 2.02350873813437 1.079E+02 218.27615044Oleic 24.3691980567964 1.208E+02 2943.8217911Linoleic 6.00266999465145 1.342E+02 805.36060634FFA 0.00390625 3.036E+02 1.1858647422H2O 6.7425083240844E-06 2.639E+02 0.0017794229

cT2 dT3

H2O (l)

Jumlah 64.6435501272386 6859.1621081

Maka jumlah air pendingin yang di butuhkanT air pendingin masuk 30 C 303.15 KT air pendingin keluar 60 C 333.15 K

Komponen a bT ET4

92.0530 -4.00E-02 -2.110E-04 5.35E-07

Maka Jumlah air pendingin yang di perlukan : 75.64 Kmol1363.07 Kg/jam

32713.782218 Kg/hari

cT2 dT3

H2O (l)

CP1.128E-01

9.163E+011.079E+021.208E+021.342E+023.036E+022.639E+02

CP

9.068E+01


N8 N9 N10 N11Myristic 172.04 159.9972 12.0428 0Palmitic 8697.37 8088.5541 608.8159 0Stearic 618.97 575.6421 43.3279 0Oleic 7401.46 6883.3578 518.1022 0Linoleic 1810.16 1683.4488 126.7112 0FFA 1000 1 999 0H2O 0.1215 0.0001215 0.001215 0.1201635

0 17392.0001215 2308.001215 0.1201635Jumlah 19700.1215 19700.1215 0 0


N8 N9 N10 N11Myristic 0.753335911011429 0.700602397241 0.0527335138 0Palmitic 33.9179117719434 31.54365794791 2.374253824 0Stearic 2.17581584745632 2.023508738134 0.1523071093 0Oleic 26.2034387707489 24.3691980568 1.834240714 0Linoleic 6.45448386521662 6.002669994651 0.4518138706 0FFA 3.90625 0.00390625 3.90234375 0H2O 0.00674250832408435 6.742508324E-06 6.7425083E-05 0.0066683407

0 64.64355012724 8.7677602067 0.0066683407Jumlah 73.4179786747007 73.4179786747 0 0

T minyak masuk 72 C 345.15 KTminyak keluar 58 C 331.15 K

Komponen a bT ET4FFA 0.08056 0.003289 -6.836E-06 5.695E-09

92.0530 -4.00E-02 -2.110E-04 5.35E-07

c14h28o2 80.266 2.82E+00 -6.01E-03 5.13E-06c16h32o2 86.29 3.5237 -7.32E-03 6.10E-06C18H3602 99.012 3.5874 -7.25E-03 5.90E-06C18H34O2 278.686 2.5434 -5.44E-03 4.92E-06C18H32O2 241.348 2.31E+00 -5.07E-03 4.75E-06

Jumlah massa masuk HE 742

Zat N10 CP Q (Kj/Kmol K)

Myristic 0.0527335137708001 1.253E-01 6.607E-03Palmitic 2.37425382403604 9.145E+01 217.13444726Stearic 0.152307109321942 1.186E+02 18.060899373Oleic 1.83424071395242 1.342E+02 246.16149701Linoleic 0.451813870565163 1.478E+02 66.792147266FFA 3.90234375 3.132E+02 1222.3769988H2O 6.7425083240844E-05 2.727E+02 0.0183840578

cT2 dT3

H2O (l)

Jumlah 8.76776020672961 1770.5509804

Maka jumlah air pendingin yang di butuhkanT air pendingin masuk 30 C 303.15 KT air pendingin keluar 34 C 307.15 K

Komponen a bT ET4

92.0530 -4.00E-02 -2.110E-04 5.35E-07

Maka Jumlah air pendingin yang di perlukan : 19.27 Kmol347.21 Kg/jam

8333.1066868 Kg/hari

cT2 dT3

H2O (l)

CP1.253E-01

9.145E+011.186E+021.342E+021.478E+023.132E+022.727E+02

CP

9.189E+01

ZatMasuk (kg/jam) Masuk (kg/jam)Minyak CPO N1 Minyak rbdpo N9

Myristic 172.04 159.9972Palmitic 8697.37 8088.5541Stearic 618.97 575.6421Oleic 7401.46 6883.3578Linoleic 1810.16 1683.4488FFA 1000 1H2O 100 0.0001215Impurities 200Jumlah 20000 17392.0001215

ZatMasuk (kmol/jam) Masuk (kmol/jam)

Minyak CPO N1 Minyak rbdpo N9Myristic 0.753335911011429 0.70060239724063Palmitic 33.9179117719434 31.5436579479074Stearic 2.17581584745632 2.02350873813437Oleic 26.2034387707489 24.3691980567964Linoleic 6.45448386521662 6.00266999465145FFA 3.90625 0.00390625H2O 5.54938956714761 6.74250832408E-06Impurities 1.55110904296572Jumlah 80.51173477649 64.6435501272386



92.0530 -4.00E-02 -2.110E-04 5.35E-07

FFA 99.012 3.5874 -7.25E-03 5.90E-06c14h28o2 80.266 2.82E+00 -6.01E-03 5.13E-06c16h32o2 86.29 3.5237 -7.32E-03 6.10E-06C18H3602 99.012 3.5874 -7.25E-03 5.90E-06C18H34O2 278.686 2.5434 -5.44E-03 4.92E-06C18H32O2 241.348 2.31E+00 -5.07E-03 4.75E-06

Gum

Jumlah panas masuk minyak cpoHE 311

ZatMasuk (kmol/jam)

CP Q (Kj/Kmol )Minyak CPO N1

Myristic 0.753335911011429 3.028E-01 2.281E-01Palmitic 33.9179117719434 8.778E+01 2977.3118967Stearic 2.17581584745632 2.700E+02 587.53230871Oleic 26.2034387707489 3.245E+02 8501.7154359Linoleic 6.45448386521662 3.426E+02 2211.5439038

cT2 dT3

H2O (l)

FFA 3.90625 4.499E+02 1757.3901875H2O 5.54938956714761 3.959E+02 2196.8592764Jumlah 78.9606257335242 18232.581153



92.0530 -4.00E-02 -2.110E-04 5.35E-07


Jumlah panas masuk minyak rbdpko HE 311

ZatMasuk (kmol/jam)


Myristic 0.700602397240629 2.695E-01 1.888E-01Palmitic 31.5436579479074 8.865E+01 2796.3634638Stearic 2.02350873813437 3.059E+02 618.99861215Oleic 24.3691980567964 2.417E+02 5889.5786312Linoleic 6.00266999465145 2.887E+02 1733.0586414FFA 0.00390625 3.059E+02 1.1949359462H2O 6.7425083240844E-06 4.243E+02 0.0028607721Jumlah 64.6435501272386 11039.385953

Jumlah panas acc= 7193.19520006954 Kj/Kmol

cT2 dT3

H2O (l)

senyawa mr (kg/kmol)FFA 256H20 18.02c14h28o2 228.3709c16h32o2 256.4241C18H3602 284.4772C18H34O2 282.4614C18H3202 280.45H3PO4 97.9952Karoten (F) 495.37Gum (J) 128.94BE (K) 284.18Spent Earth (L) 1186.79posfatida

ET4 CP3.028E-01

8.778E+013.426E+022.700E+023.245E+023.426E+024.499E+023.959E+02

ET4 CP2.695E-01

8.865E+013.059E+022.417E+022.887E+023.059E+024.243E+023.729E+02

ZatMasuk (kg/jam) Masuk (kg/jam)Minyak BPO N8 Minyak rbdpo N9

Myristic 172.04 159.9972Palmitic 8697.37 8088.5541Stearic 618.97 575.6421Oleic 7401.46 6883.3578Linoleic 1810.16 1683.4488FFA 1000 1H2O 0.1215 0.0001215

Jumlah 19700.1215 17392.0001215

ZatMasuk (kmol/jam) Masuk (kmol/jam)

Minyak CPO N8 Minyak rbdpo N9Myristic 0.753335911011429 0.70060239724063Palmitic 33.9179117719434 31.5436579479074Stearic 2.17581584745632 2.02350873813437Oleic 26.2034387707489 24.3691980567964Linoleic 6.45448386521662 6.00266999465145FFA 3.90625 0.00390625H2O 0.00674250832408435 6.74250832408E-06Impurities 0Jumlah 73.4179786747007 64.6435501272386



92.0530 -4.00E-02 -2.110E-04 5.35E-07


Gum

Jumlah panas masuk minyak cpoHE 721

ZatMasuk (kmol/jam)


Myristic 0.753335911011429 3.530E-01 2.659E-01Palmitic 33.9179117719434 8.628E+01 2926.5491509Stearic 2.17581584745632 3.126E+02 680.09800192Oleic 26.2034387707489 3.782E+02 9910.6889463Linoleic 6.45448386521662 3.981E+02 2569.3159847

cT2 dT3

H2O (l)

FFA 3.90625 4.884E+02 1907.7014385H2O 0.00674250832408435 4.304E+02 2.9016794505Jumlah 73.4179786747007 17997.52115



92.0530 -4.00E-02 -2.110E-04 5.35E-07


Jumlah panas masuk minyak rbdpko HE 721

ZatMasuk (kmol/jam)


Myristic 0.700602397240629 3.904E-01 2.735E-01Palmitic 31.5436579479074 8.501E+01 2681.4847008Stearic 2.02350873813437 4.395E+02 889.35125925Oleic 24.3691980567964 3.442E+02 8387.1049474Linoleic 6.00266999465145 4.183E+02 2510.8092404FFA 0.00390625 4.395E+02 1.7168338792H2O 6.7425083240844E-06 5.170E+02 0.003486012Jumlah 64.6435501272386 14470.743991

Jumlah panas acc= 3526.77715816583 Kj/Kmol

cT2 dT3

H2O (l)

senyawa mr (kg/kmol)FFA 256H20 18.02c14h28o2 228.3709c16h32o2 256.4241C18H3602 284.4772C18H34O2 282.4614C18H3202 280.45H3PO4 97.9952Karoten (F) 495.37Gum (J) 128.94BE (K) 284.18Spent Earth (L) 1186.79posfatida

ET4 CP3.530E-01

8.628E+013.981E+023.126E+023.782E+023.981E+024.884E+024.304E+02

ET4 CP3.904E-01

8.501E+014.395E+023.442E+024.183E+024.395E+025.170E+024.560E+02

Beban Steam Dan Air Pendingin

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