Neraca Massa
Mixer 1
Komponen Masuk Keluar C50H90O6 244.296 244.296
Minyak 68.904 68.904 H2O 6646.8 6646.8
NaHCO3 17.4 17.4
Total 6977.4 6977.4
Mixer 2
Komponen Masuk Keluar
F3 F4 F8 F5
C50H90O6 244.296 0 619.5041 850.771014 Minyak 68.904 0 174.7319 239.961055 H2O 6646.8 0 5967.533 12631.0373
NaHCO3 17.4 0 17.4 34.8
FeCl2 0 0.00696 0.00696 0.01392 ZnCl2 0 0.000696 0.000696 0.001392
Urea 0 0.348 0.348 0.696
Total 6977.4 0.355656 6779.525 13757.281 13757.281
Reactor
Komponen Masuk Keluar
F5 F6 F7
CH4 0 89.82576 0
CO2 0 108.4048 0
C50H90O6
850.77101
4 0 723.7871
Minyak
239.96105
5 0 239.9611
NaHCO3 34.8 0 34.8
FeCl2 0.01392 0 0.01392
ZnCl2 0.001392 0 0.001392
Urea 0.696 0 0.696
Total 13757.281
198.2306 13559.05 13757.281
Tangki sedimentasi
Komponen Masuk Keluar
F7 F8 F9
C50H90O6
687.44384
2 619.5041 67.93971 Minyak
193.89441
7 174.7319 19.16248 H2O 12642.2006 5967.533 6674.667
NaHCO3 34.8 17.4 17.4
FeCl2 0.01392 0.00696 0.00696 ZnCl2 0.001392 0.000696 0.000696
Urea 0.696 0.348 0.348
Total 13559.050 6779.525 6779.525 13559.050
Absorber
Komponen Masuk Keluar
F6 F11 F10 F12
CH4 89.82576 0 89.82576 0
CO2 108.4048 4.471699 1.084048 4.471699
H2O 0 785.393 0 741.489
K2CO3 0 336.597 0 0
KHCO3 0 0 0 487.8217
Stripper Kompone
n
Masuk Keluar
F12 F11 f13
CH4 0 0 0
CO2 4.4716992 4.471699 107.3208
H2O 741.48903 785.393 0
K2CO3 0 336.597 0
KHCO3 487.82173 0 0
Total 1233.782 1233.782
Neraca massa total
Alat masuk Keluar
mixer 1 6977.4 6977.4
mixer 2 13757.28 13757.28 reaktor 13757.28 13757.28 tangki
