Neraca Massa

Neraca Massa

Mixer 1
Komponen
C50H90O6
Minyak
H2O
NaHCO3
Total

Masuk
244.296
68.904
6646.8
17.4
6977.4

Keluar
244.296
68.904
6646.8

17.4
6977.4

Mixer 2
Komponen
C50H90O6
Minyak
H2O
NaHCO3
FeCl2
ZnCl2
Urea
Total

F3
244.296
68.904
6646.8
17.4
0

0
0
6977.4

Masuk
F4
0
0
0
0
0.00696
0.000696
0.348
0.355656
13757.281

F8
619.5041
174.7319
5967.533

17.4
0.00696
0.000696
0.348
6779.525

Reactor
Komponen
CH4
CO2
C50H90O6
Minyak
H2O

Masuk
F5
0
0
850.77101
4

239.96105
5
12631.037
3

Keluar

F6
89.82576
108.4048

F7
0
0

0

723.7871

0

239.9611

0

12559.79

Keluar
F5
850.771014
239.961055
12631.0373
34.8
0.01392
0.001392
0.696
13757.281

NaHCO3
FeCl2

ZnCl2
Urea
Total

34.8
0.01392
0.001392
0.696
13757.281

0
34.8
0
0.01392
0
0.001392
0
0.696
198.2306 13559.05
13757.281

Tangki sedimentasi

H2O
NaHCO3
FeCl2
ZnCl2
Urea

Masuk
F7
687.44384
2
193.89441
7
12642.200
6
34.8
0.01392
0.001392

0.696

Total

13559.050

Komponen
C50H90O6
Minyak

Keluar
F8

F9

619.5041 67.93971
174.7319 19.16248
5967.533 6674.667
17.4
17.4

0.00696 0.00696
0.000696 0.000696
0.348
0.348
6779.525 6779.525
13559.050

Absorber
Komponen
CH4
CO2
H2O
K2CO3
KHCO3
Total

Masuk

Keluar

F6
F11
F10
F12
89.82576
0
89.82576
0
108.4048 4.471699 1.084048 4.471699
0
785.393
0
741.489
0
336.597
0
0
0
0
0

487.8217
1324.692
1324.692

Stripper
Kompone
n
CH4
CO2
H2O
K2CO3
KHCO3
Total

Masuk
F12
0
4.4716992
741.48903
0
487.82173
1233.782

Keluar
F11
f13
0
0
4.471699 107.3208
785.393
0
336.597
0
0
0
1233.782

Neraca massa total
Alat
mixer 1
mixer 2
reaktor
tangki
sedimentasi
absorber
stripper
total

masuk
Keluar
6977.4
6977.4
13757.28 13757.28
13757.28 13757.28
13559.05
1324.692
1233.782
50609.49

13559.05
1324.692
1233.782
50609.49