3.7 Product Blow Tank V-202
Tabel 3.7 Neraca Massa Product Blow Tank V-202
Alur Input kgjam
Output kgjam 21
23 = 24 22
C
2
H
4
530,170955 -
530,17095 1-C
4
H
8
30,295480 -
30,295480 H
2
5,45320 -
5,45320 N
2
868,50483 883,83838
1752,34321 TiCl
3
30,48386 -
30,48386 AlC
2
H
5 3
60,82698 -
60,82698 LLDPE
22095,95959 -
22095,95959 Total
23621,69489 883,83838
24505,53327 24505,53327
24505,53327
3.8 Product Purge Bin R-301 Tabel 3.8 Neraca Massa Product Purge Bin R-301
Alur Input kgjam
Output kgjam 22
25 27
28 32
C
2
H
4
530,17095 -
- -
530,17095
1-C
4
H
8
30,295480 -
- -
30,295480
H
2
5,45320 -
- -
5,65236
N
2
1752,34321 339,55177
28,22310 19,10016
2101,01793
TiCl
3
30,48386 -
- -
-
AlC
2
H
5 3
60,82698 -
- -
-
LLDPE
22095,95959 -
- 22095,95959
-
H
2
O
- -
46,69598 10,77600
TiO
2
- -
- 15,78728
-
C
2
H
6
- -
- -
48,06690
HCl
- -
- -
21,61691
AlOH
3
- -
- 41,56058
-
Total
24505,53327 339,55177
74,91908 22172,40761
2747,59653 24920,00412
24920,00412
Universitas Sumatera Utara
3.9 Mixing Tank M-301
Tabel 3.9 Neraca Massa Mixing Tank M-301
Alur Input kgjam
Output kgjam 28
29
N
2
19,10016 19,10016
LLDPE
22095,95959 22095,95959
TiO
2
15,78728 15,78728
AlOH
3
41,56058 41,56058
Total
22172,40761 22172,40761
3.10 Pelletizer PE-301
Tabel 3.10 Neraca Massa Pelletizer PE-301
Alur Input kgjam
Output kgjam 29
31 30
N
2
19,10016 -
19,10016
LLDPE
22095,95959 22095,95959
-
TiO
2
15,78728 15,78728
-
AlOH
3
41,56058 41,56058
-
Total
22172,40761 22153,30745
19,10016 22172,40761
22172,40761
3.11 Scrubber V-301
Tabel 3.11 Neraca Massa Scrubber V-301
Alur Input kgjam
Output kgjam 32
39 33
34 = 35 = 36 C
2
H
4
530,17095 -
- 530,17095
1-C
4
H
8
30,295480 -
- 30,295480
H
2
5,65236 -
- 5,65236
N
2
2101,01793 -
- 2101,01793
H
2
O
10,77600 46,03643
56,81243 -
C
2
H
6
48,06690 -
- 48,06690
HCl
21,61691 -
21,61319 0,00372
Total
2747,59653 46,03643
78,42562 2715,20734
2793,63296 2793,63296
Universitas Sumatera Utara
3.12 Flash Drum V-302
Tabel 3.12 Neraca Massa Flash Drum V-302
Alur Input kgjam
Output kgjam 36
37 38
C
2
H
4
530,17095 530,17095
-
C
4
H
8
30,295480 30,295480
-
H
2
5,65236 -
5,65236
N
2
2101,01793 -
2101,01793
C
2
H
6
48,06690 48,06690
-
HCl
0,00372 0,00372
-
Total
2715,20734 608,53705
2106,67029 2715,20734
2715,20734
Universitas Sumatera Utara
BAB IV NERACA ENERGI
Basis perhitungan : 1 jam
Satuan operasi : kiloJoulejam kJjam
Temperatur Basis : 25
o
C 298,15 K
4.1 Heater E-101