Neraca Panas DISKRIPSI PROSES

2.4. Neraca Panas

1. Neraca Panas di Sekitar Reaktor R-01 Tabel 2.10. Neraca Panas di Sekitar Reaktor R-01 Masuk kJjam Komponen Arus 1 Arus 2 Arus 3 Arus 7 Keluar kJjam Arus 4 C 6 H 6 12.642,8771 34.563,7059 34.563,7059 H 2 O 17,6363 31,2644 247,4656 296,3663 C 2 H 4 O 8.203,3956 4.417,2130 4.417,2130 AlCl 3 359.866,3143 359.866,3143 C 8 H 10 O 21.418,8724 Subtotal 8.221,0319 12.674,1415 360.113,7799 38.980,9189 420.562,4719 Panas reaksi 1.403.449 Pendingin 1.402.876,11 Total 1.823.438,8721 1.823.438,8721 2. Neraca Panas di Sekitar Washer Tabel 2.11. Neraca Panas di Sekitar Washer Masuk kJjam Komponen Arus 4 Arus 5 Keluar kJjam Arus 6 C 6 H 6 4.066,32 6.141,79 H 2 O 34,87 43.712,01 20.876,78 C 2 H 4 O 519,67 785,19 AlCl 3 42.337,21 61.583,44 C 8 H 10 O 2.519,87 3.802,73 Subtotal 49.477,94 43.712,01 93.189,.94 Total 93.189,.94 93.189,.94 3. Neraca Panas di Sekitar Dekanter Tabel 2.12. Neraca Panas di Sekitar Dekanter Komponen Masuk kJjam Keluar kJjam C 2 H 4 O 785,19 785,19 C 6 H 6 6.141,79 6.141,79 H 2 O 20.876,78 20.876,78 C 8 H 10 O 3.802,73 3.802,73 AlCl 3 61.583,44 61.583,44 Subtotal 93.189,.94 6.926,98 86.262,96 Total 93.189,.94 93.189,.94 3. Neraca Panas di Sekitar Evaporator Tabel 2.13. Neraca Panas di Sekitar Evaporator Komponen Masuk kjjam Keluar kJjam H 2 O 20.876,78 325.420,600 C 8 H 10 O 3.802,73 60.912,847 3.205,939 AlCl 3 61.583,44 276.513,742 Subtotal 86.262,96 386.333,447 279.719,681 Penguapan 618.271,832 Pemanas 1.198.062,0 Total 1.284.324,96 1.284.324,96 4. Neraca Panas di Sekitar Cooler-01 Tabel 2.14. Neraca Panas di Sekitar Cooler-01 Komponen Masuk kJjam Keluar kJjam H 2 O 291.310,4829 143.327,6858 C 8 H 10 O 54.972,2782 26.574,9451 Subtotal 346.282,7611 169.902,6309 Pemanas 176.380,13 Total 346.282,7611 346.282,7611 5. Neraca Panas di Sekitar Menara Distilasi Tabel 2.15. Neraca Panas di Sekitar Menara Distilasi Komponen Umpan kJjam Distilat kJjam Bottom kJjam H 2 O 143.327,6858 102.225,55 98,09 C 8 H 10 O 26.574,9451 51,02 46.902,04 Subtotal 169.902,6309 102.276,57 47.000,13 Kondensor 815.127,9 Reboiler 794.501,98 964.404,61 964.404,61 6. Neraca Panas di Sekitar Cooler-02 Tabel 2.16. Neraca Panas di Sekitar Cooler-02 Komponen Masuk kJjam Keluar kJjam H 2 O 111,4844 21,4658 C 8 H 10 O 52.826,4649 95.85,6794 Subtotal 52.937,9494 9.607,1452 Pemanas 43.330,80 Total 52.937,9494 52.937,9494

2.5. Tata Letak Pabrik dan Peralatan