neraca massa pabrik APG

7/23/2019 neraca massa pabrik APG

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kapasitas 80000 ton/tahun dalam patii sagu

kapasitas kg per hari 242424.2 kg/hari pati 84.70%

kapasitas kg per jam 10101.01 kg/jam air 14%

basis (pati kering) 1000 kg/jam impuritis 1.30%

berat pati 1180.38 kg/jam mol pati kering 172.84

air 1!.28"3 kg/jam

impuritis 1!.3482" kg/jam 1. mi#er

berat pati 1180.38 kg/jam

mol pati$air 1$8

mol air 4"382.72 mol/jam

berat air 888888." g/jam pati sagu 1180.38

berat air total 888.888" kg/jam komp pati 1000

berat air &ang ditambah 723.!"" kg/jam air 1!.28"3

mol pati$ butanol 1$8'! impuritis 1!.3482"

mol butanol !24".14 mol/jam

berat butanol 388271 g/jam

berat butanol 3882.71 kg/jam

mol pati$ 1$ 2. butanolisis

mol 37037.04 mol/jam

berat "02"3 g/jam pati 1000

berat "02."3 kg/jam air 888.888"

pati$p*+ , 1$0.0232 butanol 3882.71

mol p*+ , 143.!802 mol/jam impuritis 1!.3482"

berat p*+ , 27311.83 g/jam

berat p*+ , 27.31183 kg/jam

pati$p*+ * 1$0'017 #-"8% reaksi note$

mol p*+ * 103.084 mol/jam 04".383 ati ,utanol

berat p*+ * 1"0".1 g/jam mula 172.83"!0173 !24".14

berat p*+ * 1".0"1 kg/jam bereaksi 04".38271 04".383

mol pati$a 1$0'082" sisa 123.4!7"01728 441".7!

mol a !11.7284 mol/jam

berat a 204".14 g/jam

berat a 20.4"14 kg/jam 3. transasetalisasi

mol air$ kasarpela 1$1

berat 22 2% dari kasar

pati 20

air ""7.7778

butanol 343!.02

p*sa 27.31183

, 1!"2.!74

impuritis 1!.3482"

283!."!1

#-4'88% reaksi note$

1

3

reaktranasi



, odeanol

04".383 37037.03703704

283!."!1 283!."!1

3213.432 34201.0803704

e - "0% 4. polishing 5lter

pati 20

air ""7.7778

butanol 344."22

p*sa 4."20"3 pati

, 84!."7!1 impuritis

impuritis 1!.3482"

odeanol 374.3"8

"88.2438



!. separat

0.10!

mol/jam

butanol 3882.71 pati

air 723.!"" air

butanol

p*sa

pati 1000 ,

air 888.888" impuritis

butanol 3882.71 odeanol

impuritis 1!.3482"

p*sa 27.31183

mol berat

pati 123.4!8 20

air 04".383 ""7.7778 . tangki n

butanol 441".7! 343!.02

p*sa 27.31183

, 04".383 1!"2.!74

impuritis 1!.3482"

dalam reaksi harus mol pati

, air air

6 6 butanol

04".383 04".383 p*sa

04".383 04".383 ,

impuritis

odeanol

p*+ 1".0"1

odeanol "02."3

#-100% reaksi

a

mol berat m !11.7284

pati 20 b 24.

air ""7.7778 s 2!.024

butanol 283!."!1 344."22

p*sa 4."20"3 e-"8% al

, 3213.432 84!."7!1 8. distilasi

impuritis 1!.3482"

odeanol 34201.0" 374.3"8

283!."!1 "88.2438

total 12"33.!" kg/jam pati

dalam reaksi harus mol air

mi#er

2

3

reaktorbutanolisis

!

4

torasetalis



,utanol total umpa 13"17.47 kg/jam butanol

6 6 ,

283!."!1 283!."!1 impuritis

283!."!1 283!."!1 odeanol

a

memisahkan pati'impuritis' a*+

total

pati 2

air ""7.7778

butanol 344."22

p*sa 4."20"3

18 , 84!."7!1

13.8134 impuritis 1.!3482"

odeanol 374.3"8

"88.2438



r memisahkan butanol dan air dengan produk atas berupa butanol 7.7% dan air

pada produk atas berupa air seban&ak kandungan air pada pati

air "77.8222 0."23

e- "8% butanol 3!72.024 0.077

2

""7.7778 pati 2

344."22 air 0.8"72"4

4."20"3 butanol 1.4!7""

84!."7!1 pati 2 , 84.!"7!1

1.!3482" air 1"."!!! impuritis 1.!3482"

374.3"8 butanol 72.8"844 odeanol 127.488

"88.2438 p*sa 4."20"3 "88.2438

, 84!."7!1 a 10.02!

impuritis 1.!3482" a*+ !.23474

odeanol 374.3"8

"88.2438

etralisasi a 20.4"13!8 0.!

ir 20.4"13!8 0.!

mol berat

2 pati 2

1"."!!! air 24. 44.848 pati 2

72.8"844 butanol 72.8"844 air 44.848

4."20"3 p*sa 0 0 butanol 72.8"844

84!."7!1 , 84!."7!1 , 84!."7!1

1.!3482" impuritis 1.!3482" impuritis 1.!3482"

374.3"8 odeanol 374.3"8 odeanol 374.3"8

"88.2438 "88.2438 "88.2438

a 2!.024 10.02! a 10.02!

a*+ 24. !2.3474 a*+ !2.3474

note$ dalam reaksi harus mol

p*+ a*+ air

24. 6 6

24. 24. 24.

0 24. 24.

erdistilasi menjadi produk atas butanol 71.44047

1 odeanol 24."1

ir 43."73"

total 32.318

2

44.848

separator

tangkinetralisasi

istilasi

tapel



72.8"844

84.!"7!1 e "8% distilasi 2

1.!3482" pati 2

374.3"8 air 0.8"72"4

"88.2438 butanol 1.4!7""

10.02! , 84.!"7!1 pati 2

!.23474 impuritis 1.!3482" air 0.8"72"4

7!84.37! odeanol 127.488 butanol 1.4!7""

"88.2438 , 84.!"7!1

a 10.02! impuritis 1.!3482"

a*+ !.23474 odeanol 127.488

"88.2438

a 10.02!

a*+ !.23474



"2'3%

mol in 283!."!1 e-"0%

". elarutan air !1.04712 10. bleahing

pati 2

air !1."4441 pati 2

butanol 1.4!7"" air 0.017"4

, 84.!"7!1 butanol 0.02"1!"

impuritis 1.!3482" , 84.!"7!1

odeanol 127.488 impuritis 1.!3482"

"88.2438 odeanol 2.!4"7!"

a 10.02! "88.2438

a*+ !.23474 a 10.02!

a*+ !.23474

7.pen&aringan memisahkan , dengan e5siensi "0 %

pati 2

air 44.848

butanol 72.8"844

, 71.377 , 84.!"7!1

a*+ 47.11271 impuritis 1.!3482"

odeanol 374.3"8

"88.2438

a 10.02!

a*+ !.23474

butanol 1.42880"

gkiarutan



odeanol 124."382

ir 0.87"348

pati 2

air 0.017"4

butanol 0.02"1!"

, 84.!"7!1

impuritis 1.!3482"

odeanol 2.!4"7!"

"88.2438

a 10.02!

a*+ !.23474

istilasi



22 1".7488 0.3

air 4.1180! 0.7

total !.882"2

pati

air

butanol

,

impuritis

odeanol

a

a*+

,leahing





kapasitas !0000 ton/tahun

kapasitas kg per hari 1!1!1!.1!1!2 kg/hari

kapasitas kg per jam 313.1313131 kg/jam

basis (pati kering) 11122.2344" kg/jam

berat pati 13131.3180!kg/jam

air 1838.3"0!28 kg/jam

impuritis 170.70770347 kg/jam

berat pati 13131.3180!kg/jam

mol pati$air 1$8

mol air !4"247.!7774 mol/jam

berat air "884!.3""3 g/jam

berat air total "88.4!3""3 kg/jam

berat air &ang ditambahkan pada butanol 8048.0!74! kg/jam

mol pati$ butanol 1$8'!

mol butanol !83!7!.!!134 mol/jam

berat butanol 43184!"0.8 g/jam

berat butanol 43184.!"08 kg/jam

mol pati$ 1$

mol 411"3!.833 mol/jam

berat 777!72.!4 g/jam

berat 777.!72!4 kg/jam

pati$p*+ , 1$0.0232

mol p*+ , 1!"."373323 mol/jam

berat p*+ , 3037".41"34 g/jam

berat p*+ , 303.7"41"34 kg/jam

pati$p*+ * 1$0'017

mol p*+ * 114.!!4318! mol/jam

berat p*+ * 2180"7.!247 g/jam

berat p*+ * 218.0"7!247 kg/jam

mol pati$a 1$0'082"

mol a !"1.!780243 mol/jam

berat a 2273.120"7 g/jam

berat a 227.3120"7 kg/jam

mol air$ kasarpelarutan 1$1

berat 22 2% dari kasar







komponen ma

2

raksi

pati 0.000134

impuritis 0.000103

p*+ 0.0003

odekanol 0.8!!33

0.1321

a 0.001!!!

air 0.003283

ap*+ 0.00322

total 1

komponen ma

2

raksi

pati 0.00072"

impuritis 0.000!!"

p*+ 0.00342

odekanol 0.232282

0.72022"

a 0.00844

ap*+ 0.03433

total 1



bleahing

komponen

2

raksi

pati 0.000"3!

impuritis 0.000718

p*+ 0.004388

odekanol 0.014"03

0."2411

a 0.010838

ap*+ 0.0440!8

h2o2 0

air 0

total 1

5ltrasi

komponen ma

2

raksi

pati 0.000881

impuritis 0.371203

p*+ 0.004133

odekanol 0.014038

0.!

a 0.01020"

ap*+ 0.041!01

h2o2 0.0402!

air 0.017411

total 1

pelarutan

komponen

3

raksi



pati 0.00138!

impuritis 0.011"

p*+ 0.004"

odekanol 0.02204

0.78!8"1

a 0.0104

ap*+ 0.0!23

h2o2 0.038!3

air 0.0273

total 1



dalam patii sagu mi# point 2

pati 84.70%

komponen

masuk

1

air 14% raksi laju raksi

impuritis 1.30% air 1 8048.0 0

mol pati k 8!!."! mol/jam butanol 0 0 1

total 1 8048.0 1

mi# point 3

komponen masuk

3 4

raksi laju raksi laju raksi

air 0.1!708" 43184.!" 0.14 1838.3"1 0

butanol 0.842"11 8048.0 0 0 0

pati 0 0 0.847 11122.2 0

impuritis 0 0 0.013 170.7077 0

p*+ 0 0 0 0 1

total 1 !1232. 1 13131.3 1

reaktor butanolisis separator

komponen masuk keluar komponen

7

raksi laju raksi laju

air 0.1!2881 "88.4! 0.22!088 110"7.!! butanol

butanol 0.77"1 43184.!" 0.774"12 3820!. air

pati 0.171""1 11122.2 0.0120"4 222.44!3total

impuritis 0.0024 170.7077 0.00"281 170.7077

p*+ 0.004"7 303.7"4 0.01!1 303.7"4

, 0 0 0."2108 17"!.38

total 1 47.7" 2 7"!.!2

sentriuse

komponen masuk keluar

7 10 11

raksi laju raksi laju raksi laju



pati 0.0120"4 222.44!3 0.!!7"8 211.323 0.00017 11.1222

impuritis 0.00"281 170.7077 0.434202 12.1723 0.000474 8.!3!38!

p*+ 0.01!1 303.7"4 0 0 0.018!8 303.7"4

, 0."2108 17"!.38 0 0 0."820!1 17"!.38

total 1 183"2.31 1 373.4"!3 1 18018.81

mi# point

komponen masuk kel

" 10 11 1

raksi laju raksi laju raksi laju raksi

pati 0.00017 11.1222 0 0 0 0 0.000117

impuritis 0.000474 8.!3!38! 0 0 0 0 8."8600!

p*+ 0.018!8 303.7"4 1 218.0"7 0 0 0.00!4"3

, 0."820!1 17"!.38 0 0 0 0 0.18241

odekanol 0 0 0 0 1 777.!7 0.8080

total 1 18018.81 1 218.0"7 1 777.!7 1

reaktor transasetalisasi


14 1!


butanol 0 0 0.024788 2334.122

pati 0.000117 11.1222 0.000118 11.1222

impuritis 8."8600! 8.!3!38! ".0600! 8.!3!38!

p*+ 0.00!4"3 !21.87 0.00!!42 !21.87

, 0.18241 17"!.38 0.0""823 "3"".788

odekanol 0.8080 777.!7 0.7!2"12 708"7.74

0 0 0.1172 10""1.!1

total 1 "!013.48 1 "414.8

pemisahan




1! 1 17


butanol 0.024788 2334.122 0.027!3 2334.122 0 0

pati 0.000118 11.1222 0.000131 11.1222 0 0

impuritis ".0600! 8.!3!38! 0.000101 8.!3!38! 0 0

p*+ 0.00!!42 !21.87 0.001!7 !21.87 0 0

, 0.0""823 "3"".788 0 0 1 "3"".788

odekanol 0.7!2"12 708"7.74 0.8340! 708"7.74 0 0

0.1172 10""1.!1 0.12"71 10""1.!1 0 0

total 1 "414.8 1 8474.8" 1 "3"".788

separator


1 18 1"


butanol 0.027!3 2334.122 1 2334.122 0 0

pati 0.000131 11.1222 0 0 0.00013! 11.1222

impuritis 0.000101 8.!3!38! 0 0 0.000104 8.!3!38!

p*+ 0.001!7 !21.87 0 0 0.00331 !21.87

odekanol 0.8340! 708"7.74 0 0 0.80088 708"7.74

0.12"71 10""1.!1 0 0 0.133342 10""1.!1

total 1 8474.8" 1 2334.122 1 82430.77

mi# point 7


1" 20 21


pati 0.00013! 11.1222 0 0 0.000134 11.1222

impuritis 0.000104 8.!3!38! 0 0 0.000103 8.!3!38!

p*+ 0.00331 !21.87 0 0 0.002" !21.87

odekanol 0.80088 708"7.74 0 a 0.8!!33 708"7.74

0.133342 10""1.!1 0 0 0.1321 10""1.!1

a 0 0 0.! 227.31 0.002747 227.31

air 0 0 0.! 227.31 0.002747 227.31

total 1 82430.77 1 4!!.322 1 8288.1

reaktor netralisasi


21 22




pati 0.000134 11.1222 0.000134 11.1222

impuritis 0.000103 8.!3!38! 0.000103 8.!3!38!

p*+ 0.002" !21.87 0.0003 !2.187

odekanol 0.8!!33 708"7.74 0.8!!33 708"7.74

0.1321 10""1.!1 0.1321 10""1.!1

a 0.002747 227.31 0.001!!! 128.8"74

air 0.002747 227.31 0.003283 272.1077

ap*+ 0 0 0.00322 !24.0014

total 1 8288.1 1 8288.1

distliasi 1

suk keluar

2 23 24

laju raksi laju raksi laju

11.1222 0 0 0.00072" 11.1222

8.!3!38! 0 0 0.000!!" 8.!3!38!

!2.187 0 0 0.00342 !2.187

708"7.74 0.""!"7 73!2.8! 0.232282 3!44.887

10""1.!1 0 0 0.72022" 10""1.!1

128.8"74 0 0 0.00844 128.8"74

272.1077 0.004024 272.1077 0 0

!24.0014 0 0 0.03433 !24.0014

8288.1 1 724." 1 1!21.14

distilasi 2

suk keluar

4 2! 2


11.1222 0 0 0.000"3! 11.1222

8.!3!38! 0 0 0.000718 8.!3!38!

!2.187 0 0 0.004388 !2.187

3!44.887 1 337.43 0.014"03 177.2443

10""1.!1 0 0 0."2411 10""1.!1

128.8"74 0 0 0.010838 128.8"74

!24.0014 0 0 0.0440!8 !24.0014

1!21.14 1 337.43 1 118"3.4"



masuk keluar

27 28


11.1222 0 0 0.000881 11.1222

8.!3!38! 0 0 0.371203 48."12

!2.187 0 0 0.004133 !2.187

177.2443 0 0 0.014038 177.2443

10""1.!1 0 0 0.! 313.131

128.8"74 0 0 0.01020" 128.8"74

!24.0014 0 0 0.041!01 !24.0014

0 0.3 21".8301 0.0402! !12."37

0 0.7 !12."37 0.017411 21".8301

118"3.4" 1 732.771 1 122.2

suk keluar e

8 2" 30


11.1222 0 0 0.00138! 11.1222 pati

48."12 1 4!"3.173 0.011" "3.73823 impuritis

!2.187 0 0 0.004" !2.187 p*+

177.2443 0 0 0.02204 177.2443 odekanol

313.131 0 0 0.78!8"1 313.131

128.8"74 0 0 0.0104 128.8"74 a

!24.0014 0 0 0.0!23 !24.0014 ap*+

!12."37 0.038!3 !12."37 h2o2

21".8301 0.0273 21".8301 air

122.2 1 4!"3.173 1 8033.088 total

masuk keluar

0 31 32 laju air




11.1222 0 0 0.000884 11.1222

"3.73823 0 0 0.0074!2 "3.73823 pati

!2.187 0 0 0.00414" !2.187 impuritis

177.2443 0 0 0.0140"1 177.2443 p*+

313.131 0 0 0.!018"7 313.131 odekanol

128.8"74 0 0 0.010247 128.8"74

!24.0014 0 0 0.041!8 !24.0014 a

!12."37 0 0 0.04077" !12."37 ap*+

21".8301 1 4!4!.4!4 0.378842 47!.284 h2o2

8033.088 1 4!4!.4!4 1 12!78.!4 air

total



keluar raksi 1 raksi

3

laju raksi laju air 8048.0 butanol

0 0.1!708" 8048.0

43184.!" 0.842"11 43184.!"

43184.!" 1 !1232.

butanol

air

total

keluar raksi berat

,utanol 0.842"11 43184.!" ati

laju raksi laju ir 0.1!708" 8048.0 ir

0 0.1!2881 "88.4! total 1 !1232. 9mpuritis

0 0.77"1 43184.!" total

0 0.171""1 11122.2 raksi berat

0 0.0024 170.7077 p*+ 1 303.7"4

303.7"4 0.004"7 303.7"4

303.7"4 1 47.7"

masuk keluar

7 8 "

raksi laju raksi laju raksi laju raksi

0.22!088 110"7.!! 1 3820!. 0 0 air 0.1!2881

0.774"12 3820!. 0 0 1 110"7.!! butanol 0.77"1

1 4"303.21 1 3820!. 1 110"7.!! pati 0.171""1

impuritis 0.0024

p*+ 0.004"7

total 1

m

b

s

e "!%

raksi laju

1

3

2

!

4

3

7



pati 0.0120"4 222.44!3

impuritis 0.00"281 170.7077

p*+ 0.01!1 303.7"4

, 0."2108 17"!.38

total 1 183"2.31

raksi

p*+ 1

uar

2 raksi laju

laju

pati 0.00017 11.1222

11.1222 impuritis 0.000474 8.!3!38!

8.!3!38! p*+ 0.018!8 303.7"4

!21.87 , 0."820!1 17"!.38

17"!.38 total 1 18018.81

777.!7

"!013.48

raksi

pati 0.000117

impuritis 8."8600!

p*+ 0.00!4"3

, 0.18241

odekanol 0.8080

total 1

reaksi # 4.88%

, odeanol

7282.83 411"3!.7

31!42.1" 31!42.1"

3!740.4 3803"3.!

"3"".788 708"7.74

1



e 100%

raksi laju

butanol 0.024788 2334.122

pati 0.000118 11.1222

impuritis ".0600! 8.!3!38!

p*+ 0.00!!42 !21.87 ,

, 0.0""823 "3"".788

odekanol 0.7!2"12 708"7.74

0.1172 10""1.!1

total 1 "414.8

raksi laju

butanol 0.027!3 2334.122

pati 0.000131 11.1222

impuritis 0.000101 8.!3!38!

p*+ 0.001!7 !21.87

odekanol 0.8340! 708"7.74

0.12"71 10""1.!1

total 1 8474.8"

raksi laju

pati 0.00013! 11.1222

impuritis 0.000104 8.!3!38!

p*+ 0.00331 !21.87

odekanol 0.80088 708"7.74

0.133342 10""1.!1

total 1 82430.77

pati

impuritis

p*+

odekanol

a

air

total

raksi laju

pati 0.000134 11.1222

1!

1

1"

18

201"

21

21



impuritis 0.000103 8.!3!38!

p*+ 0.002" !21.87

4".803 odekanol 0.8!!33 708"7.74

".10!2! 0.1321 10""1.!1

a 0.002747 227.31

air 0.002747 227.31

total 1 8288.1

reaksi # "0%

p*+ a ap*+ air

2743.4"2 !"1.!78 0 0

24".142 24".142 24".142 24".142

274.34"2 3222.43 24".142 24".142

!2.187 128.8"74 !24.0014 44.444!

raksi laju

pati 0.000134 11.1222

impuritis 0.000103 8.!3!38!

p*+ 0.0003 !2.187

odekanol 0.8!!33 708"7.74

0.1321 10""1.!1

a 0.001!!! 128.8"74 pati

air 0.003283 272.1077 impuritis

ap*+ 0.00322 !24.0014 p*+

total 1 8288.1 odekanol

1!21.14 a

ap*+

total

dodeanol

raksi laju

pati 0.00072" 11.1222

impuritis 0.000!!" 8.!3!38!

p*+ 0.00342 !2.187

odekanol 0.232282 3!44.887 raksi

0.72022" 10""1.!1 pati 0.000"3!

a 0.00844 128.8"74 impuritis 0.000718

ap*+ 0.03433 !24.0014 p*+ 0.004388

22

24

23

24

2

2!



total 1 1!21.14 odekanol 0.014"03

0."2411

a 0.010838

ap*+ 0.0440!8

total 1

raksi laju

h2o2 0.3 21".8301

air 0.7 !12."37

total 1 732.771

raksi laju

pati 0.000"3! 11.1222

impuritis 0.000718 8.!3!38!

p*+ 0.004388 !2.187 raksi laju

odekanol 0.014"03 177.2443 pati 0.000881 11.1222

0."2411 10""1.!1 impuritis 0.0007 8.!3!38!

a 0.010838 128.8"74 impuritis 2 0.370!27 478.37

ap*+ 0.0440!8 !24.0014 p*+ 0.004133 !2.187

total 1 118"3.4" odekanol 0.014038 177.2443

0.! 313.131

a 0.01020" 128.8"74

ap*+ 0.041!01 !24.0014

air 0.0402! !12."37

h2o2 0.017411 21".8301

1 122.2

"8%

raksi

raksi laju pati 0.00138!

0.000881 11.1222 impuritis 0.011"

0.371203 48."12 p*+ 0.004"

0.004133 !2.187 odekanol 0.02204

0.014038 177.2443 raksi laju 0.78!8"1

0.! 313.131 impuritis 1 4!"3.173 a 0.0104

0.01020" 128.8"74 ap*+ 0.0!23

0.041!01 !24.0014 h2o2 0.038!3

0.0402! !12."37 air 0.0273

0.017411 21".8301 total 1

1 122.2

raksi laju

air 1 4!4!.4!4

72%

2

28

27

28 30

2"

30

31



raksi laju

0.00138! 11.1222

0.011" "3.73823

0.004" !2.187 raksi laju

0.02204 177.2443 pati 0.000884 11.1222

0.78!8"1 313.131 impuritis 0.0074!2 "3.73823

0.0104 128.8"74 p*+ 0.00414" !2.187

0.0!23 !24.0014 odekanol 0.0140"1 177.2443

0.038!3 !12."37 0.!018"7 313.131

0.0273 21".8301 a 0.010247 128.8"74

1 8033.088 ap*+ 0.041!8 !24.0014

h2o2 0.04077" !12."37

air 0.378842 47!.284

total 1 12!78.!4

32



1

43184.!"

berat raksi

43184.!" 0.842"11

8048.0 0.1!708"

!1232. 1

raksi berat

0.847 11122.2

0.14 1838.3"1

0.013 170.7077

1 13131.3

laju raksi

air "88.4! 0.1!2881

butanol 43184.!" 0.77"1

pati 11122.2 0.171""1

impuritis 170.7077 0.0024 air 0.22!088 110"7.!!

p*+ 303.7"4 0.004"7 butanol 0.774"12 3820!.

total 47.7" 1 total 1 4"303.21

raksi laju

laju

"88.4!

43184.!" pati 0.0120"4 222.44!3

11122.2 impuritis 0.00"281 170.7077

170.7077 p*+ 0.01!1 303.7"4

303.7"4 , 0."2108 17"!.38

47.7" total 1 183"2.31

reaksi #-"8 %

pati butanol , air

8!!."! !83!7!. 0 0

7282.83 7282.83 7282.83 7282.83

1373.11" !12"2.7 7282.83 7282.83 mol 4""3.732

222.44!3 3820!. 17"!.38 1211.0"1 kg/jam 108"".82

raksi laju

7

11



raksi laju pati 0.00017 11.1222

pati 0.!!7"8 211.323 impuritis 0.000474 8.!3!38!

impuritis 0.434202 12.1723p*+ 0.018!8 303.7"4

total 1 373.4"!3 , 0."820!1 17"!.38

total 1 18018.81

laju

218.0"7 raksi laju

odekanol 1 777.!7

raksi laju

pati 0.000117 11.1222

impuritis 8."8600! 8.!3!38!

p*+ 0.00!4"3 !21.87

, 0.18241 17"!.38

odekanol 0.8080 777.!7

total 1 "!013.48

laju raksi laju

butanol 0.024788 2334.122

11.1222 pati 0.000118 11.1222

8.!3!38! impuritis ".0600! 8.!3!38!

!21.87 p*+ 0.00!!42 !21.87

17"!.38 , 0.0""823 "3"".788

777.!7 odekanol 0.7!2"12 708"7.74

"!013.48 0.1172 10""1.!1

total 1 "414.8

,utanol

0 0

31!42.1" 31!42.1"

31!42.1" 31!42.1"mol

10""1.!1 2334.122kg/jam

1

12

14

13

1!14



raksi laju

butanol 0.027!3 2334.122

pati 0.000131 11.1222

impuritis 0.000101 8.!3!38!

1 "3"".788 p*+ 0.001!7 !21.87

odekanol 0.8340! 708"7.74

0.12"71 10""1.!1

total 1 8474.8"

raksi laju

,utanol 1 2334.122

raksi laju

pati 0.00013! 11.1222

impuritis 0.000104 8.!3!38!

p*+ 0.00331 !21.87

odekanol 0.80088 708"7.74

0.133342 10""1.!1

total 1 82430.77

raksi laju tangki berpengaduk

a 0.! 227.31

air 0.! 227.31

total 1 4!!.322

raksi laju

a 1 227.31

raksi laju

0.000134 11.1222

0.000103 8.!3!38!

0.002" !21.87

0.8!!33 708"7.74

0.1321 10""1.!1

0.002747 227.31

0.002747 227.31

1 8288.1

1

17

22

33



raksi laju

pati 0.000134 11.1222

impuritis 0.000103 8.!3!38!

p*+ 0.0003 !2.187

odekanol 0.8!!33 708"7.74

0.1321 10""1.!1

a 0.001!!! 128.8"74

air 0.003283 272.1077

ap*+ 0.00322 !24.0014

total 1 8288.1

mol

kg/jam

raksi laju

dodeanol 0.""!"7 73!2.8!

air 0.004024 272.1077

total 1 724."

raksi laju

0.00072" 11.1222

0.000!!" 8.!3!38!

0.00342 !2.187

0.232282 3!44.887

0.72022" 10""1.!1

0.00844 128.8"74

0.03433 !24.0014

1 1!21.14

raksi laju

1 337.43

laju

11.1222

8.!3!38!

!2.187



177.2443

10""1.!1

128.8"74

!24.0014

118"3.4"

laju

11.1222

"3.73823

!2.187

177.2443

313.131

128.8"74

!24.0014

!12."37

21".8301

8033.088



1000 !7.121

11122.2 313.131



air 110"7.!! 0.13"33

butanol 3820!. 0.!437!

pati 222.44!3 0.00328

impuritis 170.7077 0.002!22

p*+ 303.7"4 0.004487

, 17"!.38 0.213"7

total 7"!.!2 1

raksi

butanol 1

separator

raksi laju

air 0.22!088 110"7.!!

butanol 0.774"12 3820!.

total 1 4"303.21 raksi

air 1

7

"

8





raksi laju

ir 1 227.31

raksi laju

a 0.! 227.31

ir 0.! 227.31

4!!.322


33 3! 3!


a 1 227.31 0 0 0.! 227.31

air 0 0 1 227.31 0.! 227.31

total 1 227.31 1 227.31 1 4!!.322

3!

34









laju

3820!.

laju

110"7.!!













:omponen1 2 3 4 !

*ekanan (atm)

; (k</ kg)

aju lir (kg/jam)

,utanol 6 43184.!" 43184.!" 6 6 43184.!"

ir 8048.0 6 8048.0 1838.3"1 6 "88.4!

ati 6 6 6 11122.2 6 11122.2

9mpurities 6 6 6 170.7077 6 170.7077

p*+ 6 6 6 6 303.7"4 303.7"4

,util likosida 6 6 6 6 6 6

odekanol 6 6 6 6 6 6

lkil oliglikosida 6 6 6 6 6 6

+odium idroksida 6 6 6 6 6 6

a*+ 6 6 6 6 6 6idrogen eroksida 6 6 6 6 6 6

*otal 8048.0 43184.!" !1232. 13131.3 303.7"4 47.7"

*emperatur (o>)



7 8 " 10 11 12 13 14

43184.!" 3820!. 3820!. 6 6 3820!. 6 6

"88.4! 110"7.!! 110"7.!! 6 6 6 110"7.!! 6

11122.2 222.44!3 6 222.44!3 222.44!3 6 6 211.323

170.7077 170.7077 6 170.7077 170.7077 6 6 12.1723

303.7"4 303.7"4 6 303.7"4 303.7"4 6 6 6

6 17"!.38 6 17"!.38 17"!.38 6 6 6

6 6 6 6 6 6 6 6

6 6 6 6 6 6 6 6

6 6 6 6 6 6 6 6

6 6 6 6 6 6 6 66 6 6 6 6 6 6 6

47.7" 7"!.!2 4"303.21 183"2.31 183"2.31 3820!. 110"7.!! 373.4"!3



liran rose

1! 1 17 18 1" 20 21 22

eraa =assa :omponen (kg/jam)6 6 6 6 6 2334.122 6 2334.122

6 6 6 6 6 6 6 6

11.1222 6 6 11.1222 11.1222 11.1222 6 11.1222

8.!3!38! 6 6 8.!3!38! 8.!3!38! 8.!3!38! 6 8.!3!38!

303.7"4 218.0"7 6 !21.87 !21.87 !21.87 6 !21.87

17"!.38 6 6 17"!.38 17"!.38 "3"".788 "3"".788 6

6 6 777.!7 777.!7 777.!7 708"7.74 6 708"7.74

6 6 6 6 6 10""1.!1 6 10""1.!1

6 6 6 6 6 6 6 6

6 6 6 6 6 6 6 66 6 6 6 6 6 6 6

18018.81 218.0"7 777.!7 "!013.48 "!013.48 "414.8 "3"".788 8474.8"



s

23 24 2! 2 27 28 2" 30

2334.122 6 6 6 6 6 6 6

6 6 6 6 227.31 227.31 227.31 272.1077

6 11.1222 11.1222 6 6 6 11.1222 11.1222

6 8.!3!38! 8.!3!38! 6 6 6 8.!3!38! 8.!3!38!

6 !21.87 !21.87 6 6 6 !21.87 !2.187

6 6 6 6 6 6 6 6

6 708"7.74 708"7.74 6 6 6 708"7.74 708"7.74

6 10""1.!1 10""1.!1 6 6 6 10""1.!1 10""1.!1

6 6 6 227.31 6 227.31 227.31 128.8"74

6 6 6 6 6 6 6 !24.00146 6 6 6 6 6 6 6

2334.122 82430.77 82430.77 227.31 227.31 4!!.322 8288.1 8288.1



31 32 33 34 3! 3 37 38

6 6 6 6 6 6 6 6

272.1077 272.1077 6 6 6 6 !12."37 !12."37

11.1222 6 11.1222 6 11.1222 11.1222 6 11.1222

8.!3!38! 6 8.!3!38! 6 8.!3!38! 8.!3!38! 6 48."12

!2.187 6 !2.187 6 !2.187 !2.187 6 !2.187

6 6 6 6 6 6 6 6

708"7.74 73!2.8! 3!44.887 337.43 177.2443 177.2443 6 177.2443

10""1.!1 6 10""1.!1 6 10""1.!1 10""1.!1 6 313.131

128.8"74 6 128.8"74 6 128.8"74 128.8"74 6 128.8"74

!24.0014 6 !24.0014 6 !24.0014 !24.0014 6 !24.00146 6 6 6 6 6 21".8301 21".8301

8288.1 724." 1!21.14 337.43 118"3.4" 118"3.4" 732.771 122.2



3" 40 41 42 43

6 6 6 6 6

!12."37 6 21".8301 4!4!.4!4 47!.284

11.1222 6 11.1222 6 11.1222

48."12 4!"3.173 "3.73823 6 "3.73823

!2.187 6 !2.187 6 !2.187

6 6 6 6 6

177.2443 6 177.2443 6 177.2443

313.131 6 313.131 6 313.131

128.8"74 6 128.8"74 6 128.8"74

!24.0014 6 !24.0014 6 !24.001421".8301 6 !12."37 6 !12."37

122.2 4!"3.173 8033.088 4!4!.4!4 12!78.!4

neraca massa pabrik APG

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