4. Reaktor 2 RE-202
Gambar 4.4. Reaktor RE-202 Tabel 4.4 Data hasil perhitungan neraca massa reaktor RE-202
Komponen Input kgjam
Output kgjam F
6
F
G
F
K
F
7
C
2
H
4
O 744,833
692,695 196,748
H
2
SO
4
5,621 5,621
H
2
O 32,253
11,243 H
3
PO
4
11,243 32,253
C
6
H
12
O
3
2.066,119 692,695
2.614,204
Total 2.860,069
692,695 692,695
2.860,069 2.860,069
5. Netralizer NE-301
Gambar 4.5. Netralizer NE-301
Tabel 4.5 Data hasil perhitungan neraca massa Netralizer NE-301
Komponen Input kgjam
Konsumsi kgjam
Generasi kgjam
Output kgjam
F
7
F
8
F
9
C
2
H
4
O 196,748
196,748 H
2
SO
4
5,621 5,621
H
2
O 32,253
9,116 6,153
47,522 H
3
PO
4
11,243 11,243
Na
2
SO
4
8,145 8,145
Na
2
HPO
4
16,126 16,126
C
6
H
12
O
3
2.614,204 2.614,204
NaOH 13,674
13,674
Total 22,790
30,538 30,425 2.882,746
2.860,070 2.882,746
6. Dekanter DE-301
Tabel 4.6 Data hasil perhitungan neraca massa Dekanter DE-301
Komponen Input kgjam
Output kgjam F
9
F
10
F
11
C
2
H
4
O 196,748
196,748 H
2
O 47,522
5,345 42,177
Na
2
SO
4
8,145 8,145
Na
2
HPO
4
16,126 16,126
C
6
H
12
O
3
2.614,204 2.614,204
Total 2.882,746
29,616 2.853,130
2.882,746
7. Distilasi
Gambar 4.6. Menara Distilasi-1 DC-301
Tabel 4.7 Data hasil perhitungan neraca massa menara distilasi-1 DC-301
Komponen Input
Output F
11
F
13
F
12
kmolja m
kgjam kmoljam
kgjam kmolja
m kgjam
C
2
H
4
O 4,471
196,748 4,471
196,748 0,000
0,000 C
6
H
12
O
3
19,804 2.614,203
0,000 0,000
19,804 2614,203
H
2
O 1,836
42,177 0,000
0,000 1,836
42,177
Total 26,112
2.853,129 4,471
196,748 21,641
2656,381 26,112 kmoljam
2.853,129 kgjam
8. Condenser-1 CD-301
Tabel 4.8 Data hasil perhitungan neraca massa Condenser-1 CD-301
Komponen Input kgjam
Output kgjam V
L D
C
2
H
4
O 212,83
16,08 196,74
C
6
H
12
O
3
0,00 0,00
0,00 H
2
O 0,00
0,00 0,00
Total
212,83 16,08
196,74 212,83
9. Reboiler-1 RB-301
Tabel 4.9 Data hasil perhitungan neraca massa Reboiler-1 RB-301
Komponen Input kgjam
Output Bottom
kgjam Vapor
kgjam
C
2
H
4
O 0,00
0,00 0,00
C
6
H
12
O
3
3.198,504 2.614,20
584,30 H
2
O 40,45
33,06 7,39
Total 3.238,95
2.647,26 591,68
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