commit to user 38
PRARANCANGAN PABRIK PARAXYLENE PROSES SELECTIVE TOLUENE DISPROPORTIONATION
KAPASITAS 200.000 TONTAHUN
BAB II DESKRIPSI PROSES
2.4.2 Neraca Panas
Basis : 1 jam operasi Satuan : kilojoule
Tabel 2.12 Neraca Panas PadaVaporizer V–01 Komponen
Input Output
Q heating 0,0000
6.355.690,301 Q vap
0,0000 101.942.305,597
Q pemanas 108.297.995,898
0,0000
Total 108.297.995,898
108.297.995,898
Tabel 2.13 Neraca Panas PadaFurnace F–01 Komponen
Input Output
Q umpan 64.950.057,737
171.449.547,703 Q beban pemanas
108.499.489,966
Total 171.449.547,703
171.449.547,703
Tabel 2.14 Neraca Panas PadaReaktor R–01 Komponen
Input Output
Q umpan 188.625.211,457
Q2 188.579.832,155
Q beban pemanas
345.112,925 Qr
390.492,227
Total 188.970.324,382
Total 188.970.324,382
commit to user 39
PRARANCANGAN PABRIK PARAXYLENE PROSES SELECTIVE TOLUENE DISPROPORTIONATION
KAPASITAS 200.000 TONTAHUN
BAB II DESKRIPSI PROSES
Tabel 2.15 Neraca Panas Pada FlashDrum FD–01 Komponen
Input Output
Q umpan 43.357.617,255
Qtop 2.299.746,335
Qbott 26.389.008,479
Q vapor 14.668.862,441
Total 43.357.617,255
Total 43.357.617,255
Tabel 2.16 Neraca Panas PadaMenara Destilasi 1 MD–01
Panas masuk kJjam Panas keluar kJjam
Qumpan 31.330.301,447
Qdestilat 2.758.153,354
Q reboiler 1142039,129
Qbottom 29.576.079,435
Qkondenser 138.107,787
Jumlah
32.472.340,576
Jumlah
32.472.340,576
Tabel 2.17 Neraca Panas PadaMenara Destilasi 2 MD–02
Panas masuk kJjam Panas keluar kJjam
Qumpan 29.482.830,107
Qdestilat 22.197.475,666
Q reboiler 162.901.299,380
Qbottom 7.908.989,095
Qkondenser 162.277.664,726
Jumlah
192.384.129,487
Jumlah
192.384.129,487
commit to user 40
PRARANCANGAN PABRIK PARAXYLENE PROSES SELECTIVE TOLUENE DISPROPORTIONATION
KAPASITAS 200.000 TONTAHUN
BAB II DESKRIPSI PROSES
Tabel 2.18 Neraca Panas PadaCrystallizer CR–01 Komponen
Input Output
Q umpan 986.517,124
Qproduk -220.139,424
Q Kristal 174.133,886
Qbeban pendingin
1.380.790,434
Total 1.160.651,010
total 1.160.651,010
Tabel 2.19 Neraca Panas PadaMelter MT–01 Komponen
Input Output
Q umpan –166.263,914
Qproduk 56.649,574
Q pemanas 267.886,506
Qlebur 44.973,018
Total 101.622,593
total 101.622,593
commit to user 41
PRARANCANGAN PABRIK PARAXYLENE PROSES SELECTIVE TOLUENE DISPROPORTIONATION
KAPASITAS 200.000 TONTAHUN
BAB II DESKRIPSI PROSES
Tabel 2.20 Neraca Panas total Input
Output Komponen
kJjam Komponen
kJjam Arus 1
539.891,358 Vaporizer 102.630.085,248
Arus 4 168.720,192 Qreaksi
425,570 Furnace
108.499.489,966 Arus 7 2.304.484,506
HE-01 4.877.300,375 Arus 9
242.941,489 RB-01
1.142.039,129 Arus 13 236.039,893
RB-02 1.101.936,980 Arus 14
206.716,529 Melter
1.114.776,689 Cooler-01 2.913.557,915
Cooler-02 6.939.703,352
CD-01 138.107,787
CD-02 478.302,326
CR 1.380.790,43
Total 117.444.155,048
Total 117.444.155,048
2.5 Lay Out Pabrik dan Peralatan Proses 2.5.1 Lay OutPabrik
