BAB IV NERACA PANAS
Basis perhitungan : 1 jam
Satuan operasi : kiloJoulejam kJjam
Temperatur basis : 25
o
C 298,15 K
4.1 Reaktor Deprotonasi R-101
Tabel 4.1 Neraca Panas R-101 Alur masuk kJjam
Alur keluar kJjam Umpan
- Produk
- 19.511,9011
∆Hr -
-17.745,5803 Saturated steam
1.766,3208 -
Total 1.766,3208
1.766,3208
4.2 Cooler E-101
Tabel 4.2 Neraca Panas E-101 Alur masuk kJjam
Alur keluar kJjam Umpan
19.511,9011 -
Produk -
Air Pendingin -
19.511,9011 Total
19.511,9011 19.511,9011
4.3 Reaktor Polimerisasi R-102
Tabel 4.3 Neraca Panas R-102 Alur masuk kJjam
Alur keluar kJjam Umpan
- Produk
- ∆Hr
1.096,0819 -
Air Pendingin -
1.096,0819 Total
1.096,0819 1.096,0819
Universitas Sumatera Utara
4.4 Washer W-101
Tabel 4.4 Neraca Panas W-101 Alur masuk kJjam
Alur keluar kJjam Umpan
- Produk
- 1.250.832,9136
Air Pemanas 1.250.832,9136
- Total
1.250.832,9136 1.250.832,9136
4.5 Heater E-104
Tabel 4.6 Neraca Panas E-104 Alur masuk kJjam
Alur keluar kJjam Umpan
1.250.832,9137 -
Produk -
3.268.692,0320
Saturated steam 2.017.859,1183
- Total
3.268.692,0320 3.268.692,0320
4.6 Heater E-103
Tabel 4.4 Neraca Panas E-103 Alur masuk kJjam
Alur keluar kJjam Umpan
- Produk
-
1.250.832,9136
Saturated steam
1.250.832,9136
- Total
1.250.832,9136 1.250.832,9136
4.7 Condenser E-102
Tabel 4.7 Neraca Panas E-102 Alur masuk kJjam
Alur keluar kJjam Umpan
2.128.964,9497 -
Produk -
Air Pendingin -
2.128.964,9497 Total
2.128.964,9497 2.128.964,9497
4.8 Evaporator I FE-101
Tabel 4.9 Neraca Panas FE-101 Alur masuk kJjam
Alur keluar kJjam Umpan
888.755,7372 -
Produk -
4.167.620,5840 Saturated steam
3.278.864,8486 -
Total 4.167.620,5840
4.167.620,5840
Universitas Sumatera Utara
4.9 Evaporator II FE-102
Tabel 4.10 Neraca Panas FE-102 Alur masuk kJjam
Alur keluar kJjam Umpan
747.924,7010 -
Produk -
500.067,3532 Uap Air
- 247.857,3478
Total 747.924,7010
747.924,7010
4.10 Evaporator III FE-103
Tabel 4.11 Neraca Panas FE-103 Alur masuk kJjam
Alur keluar kJjam Umpan
359.782,4404 -
Produk -
143.939,0605 Uap Air
- 215.843,3799
Total 359.782,4404
359.782,4404
4.11 Condenser E-105
Tabel 4.8 Neraca Panas E-105 Alur masuk kJjam
Alur keluar kJjam Umpan
1.427.792,9018 -
Produk -
Air Pendingin -
1.427.792,9018 Total
1.427.792,9018 1.427.792,9018
Universitas Sumatera Utara
BAB V SPESIFIKASI PERALATAN
5.1 Tangki Penyimpanan Metilen Klorida CH