16. Expander Valve 03 EV-303
Tabel 4.32 Neraca Energi Expander Valve 03 EV-303
17. Cooler 01 CO-301
Tabel 4.33 Neraca energi CO-301
Panas Masuk Panas Keluar
Keterangan kJjam
Keterangan kJkg
Qumpan 1.466.485,76396
Qliquid out 75.537.97807
Q cooling water 1.390.947,78589
Total 1.466.485,76396
Total 1.466.485,76396
18. COOLER 02 CO-302
Tabel 4.34 Neraca energi CO-302
Panas Masuk Panas Keluar
Keterangan kJjam
Keterangan kJkg
Qumpan 405.471,3299
Qliquid out 357.614,7562
Q cooling water 47.856,5737
Total 405.471,3299
Total 405.471,3299
19. Kolom Distilasi 02 DC-302
Tabel 4.35 Neraca energi DC-302
Panas Masuk Panas Keluar
Keterangan kJjam
Keterangan kJkg
Q umpan 357.614,7562
Q bottom 84.667,2491
Q reboiler 3.256.904,8765
Q distilat 282.434,6474
Q condenser 3.247.417,7362
Total 3.614.519,6327
Total
3.614.519,6327 Panas Masuk
Panas Keluar
Keterangan kJjam
Keterangan kJkg
Q15a 1.466.485,7640
Q15 1.466.485,7640
Total 1.466.485,7640
Total 1.466.485,7640
20. Expander Valve 04 EV-304
Tabel 4.36 Neraca Energi Expander Valve 04 EV-304
Panas Masuk Panas Keluar
Keterangan kJjam
Keterangan kJkg
Q32 84.667,2491
Q38 84.667,2491
Total 84.667,2491
Total 84.667,2491
21. Cooler 03 CO-303
Tabel 4.37 Neraca energi CO-303
Panas Masuk Panas Keluar
Keterangan kJjam
Keterangan kJkg
Qumpan 84.667,2491
Qliquid out 4.907,3448
Q cooling water 79.759,9043
Total 84.667,2491
Total 84.667,2491
22. Expander Valve 05 EV-305
Tabel 4.38 Neraca Energi Expander Valve 05 EV-305
Panas Masuk Panas Keluar
Keterangan kJjam
Keterangan kJkg
Q35 282.434,6474
Q37 282.434,6474
Total 282.434,6474
Total 282.434,6474
23. COOLER 04 CO-304
Tabel 4.39 Neraca energi CO-304
Panas Masuk Panas Keluar
Keterangan kJjam
Keterangan kJkg
Qumpan 282.434,6474
Qliquid out 25.416,4983
Q cooling water 257.018,1491
Total 282.434,6474
Total 282.434,6474
V. SPESIFIKASI PERALATAN
A. Peralatan Proses
Peralatan proses pabrik butynediol dengan kapasitas 40.000 tontahun terdiri dari :
1. Tangki Penyimpanan Formaldehyde TP-101
Spesifikasi Tangki Penyimpanan Formaldehyde TP - 101 Fungsi
: Tempat menyimpan bahan baku formaldehyde liquid Tipe
: Silinder tegak vertikal dengan dasar datar flat bottom dan atap head berbentuk conical
Kondisi operasi : Tekanan = 2 atm
Temperatur, T in = 30
o
C Dimensi
: Laju alir massa = 6.448,6456 kgjam Volume tangki = 1.314,9468 m
3
Diameter tangki = 8,7478 m Panjang tangki = 8,7478 m
Tebal shell =
4 1
2
in Tebal head =
16 3
in Material = Carbon steel SA 285 Grade C
Kapasitas : 525,9787 m
3
Tekanan Desain : 8,12 atm
Jumlah : 3 buah
Harga satuan, : 48.954,423