3.6 Pompa P-201
Tabel 3.6 Neraca Massa pompa P-201
Komponen Masuk kgjam
Keluar kgjam Alur 14
Alur 15
H
2
O 3061,5275 3061,5275
Total 3061,5275 3061,5275
3.7 Steam Boiler E-201
Tabel 3.7 Neraca Massa Steam Boiler E-201
Komponen Masuk kgjam
Keluar kgjam Alur 13
Alur 15 Alur 18
Alur 16
O
2
86,912 - 86,912 - N
2
1243,0852 - 1243,0852 - CO
2
2185,144 - 2185,144 - H
2
O 158,6335 3061,5275
158,6335 3061,5275
SO
2
0,0583 - 0,0583 - Total
3673,833 3061,5275 3673,833 3061,5275 6735,3605 6735,3605
3.8 Turbin T-201
Tabel 3.8 Neraca Massa Turbin T-201
Komponen Masuk kgjam
Keluar kgjam Alur 16
Alur 17
H
2
O 3061,5275 3061,5275 Total 3061,5275 3061,5275
Universitas Sumatera Utara
3.9 Fluidized Bed Scrubber R-201
Tabel 3.9 Neraca Massa Fluidized Bed Scrubber R-201
Komponen Masuk kgjam
Keluar kgjam Alur 18
Alur 19 Alur 20
Alur 21
O
2
86,912 - 86,8731 - N
2
1243,0852 - 1243,0852 - CO
2
2185,144 - 2185,144 - H
2
O 158,6335 - 158,6335 -
SO
2
0,0583 -
- -
CaO - 0,14575
- 0,0769
CaSO
4
- - - 0,166
Total 3673,833 0,14575 3673,7358 0,2429
3673,9787 3673,9787
Universitas Sumatera Utara
IV-1
BAB IV NERACA PANAS
Basis perhitungan : 1 jam operasi
Satuan operasi : kJjam
Temperatur basis : 25
o
C
4.1 Bucket Elevator I BE-101
Tabel 4.1 Neraca Panas Bucket Elevator I M-101
Alur masuk kJjam Alur keluar kJjam
Umpan 8043,123
- Produk
- 8043,123
Total 8043,123
8043,123
4.2 Burner B-101
Tabel 4.2 Neraca Panas Burner B-101
Alur masuk kJjam Alur keluar kJjam
Umpan 9064,5106 -
Produk - 3666371,8557
ΔHr 3657307,3451 -
Total 3666371,8557 3666371,8557
4.3 Fluidized Bed Preheater H-101
Tabel 4.3 Neraca Panas Fluidized Bed Preheater H-101
Alur masuk kJjam Alur keluar kJjam
Umpan 3674414,9787 -
Produk - 8072849,1
Beban Panas 4398434,1213 -
Total 8072849,1 8072849,1
Universitas Sumatera Utara
4.4 Reduction Furnace R-101
Tabel 4.4 Neraca Panas Reduction Furnace R-101
Alur masuk kJjam Alur keluar kJjam
Umpan 4409851,0244 -
Produk - 7578397,4513
ΔHr - 587357,1399
Panas listrik 3755903,5668 -
Total 8165754,5912 8165754,5912
4.5 Mixing Point M-101