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Komponen
Aliran Proses (Kg/jam)
F1
F2
F3
F4
F5
F6
F7
F8
F9
F10
F11
F12
F13
F14
F15
F16
F17
F18
F19
F20
F21
F22
Temperatur (oC), Tekanan (atm)
30,1
30,1
104, 1
63.1065, 5
130, vacum
130, 1
90, 1
30, 1
90, 1
90, 1
90, 1
150, 1
150, 1
90, 1
260, 1
30, 1
90, 1
90, 1
30, 1
90, 1
120, 1
120, 1
APG
-
- - - - - 5,599.5
-
5,599.5
-
5,599.5
-
5,599.5
- - 5,599
- 5,599.5
-
5,599.5
- 5,599
151
151
151
151
.5151
155
155
.5155
Air
- -
3,148.1532
3,148.1532
-
3,148.1532
- -
12.4352
-
12.4352
12.4352
- - - -
6,593.1072
6,593.1068
-
6,802.5349
6,802.5349
-
Butanol
297.6754
-
13,751.3079
12,262.9311
-
13,453.6326
- - -
- -
- - - - - - -
- - - -
Butil Glikosida
- - -
4,746.7154
- -
949.3431
-
949.3431
-
949.3431
-
949.3431
- -
949.3431
-
949.3431
-
949.3431
-
949.3431
Do
-
- - - 24,
- 21,
-
21,
-
21,
-
21,
21,
2,
- - - -
- - -
dekanol
398.1871
405.3428
405.3428
405.3428
405.3428
405.3428
992.8443
H2O2
- - - - - - -
- -
- -
- - - - - - -
271.6080
- - -
HOO-
- - - - - - -
- -
- -
- - - - - - -
-
395.5865
-
395.5865
NaOH
- - - - - - -
71.8828
44.2490
-
44.2490
-
44.2490
- -
44.2490
-
44.2490
289.1576
- - -
Pati
-
3,5
3,54
283.
- - 283.
-
283.
283
- -
- - - - - - -
- - -
41.6723
1.6723
3338
3338
3338
.3338
pTSA
-
87.9307
87.9307
87.9307
30.8946
- - - -
- -
- - -
30.8946
- - - - - - -
pTSA-Na
- - - - - - -
-
134.0239
134.0239
- - - - - - - -
- - - -
Total
297.6754
3,629.6030
20,529.0641
20,529.0641
24,429.0816
16,601.7857
28,237.5347
71.8828
28,428.2429
417.3577
28,010.8852
12.4352
27,998.4500
21,405.3428
3,023.7389
6,593.1072
6,593.1072
13,186.2144
560.7656
13,746.9801
6,802.5349
6,944.4451
