Heater udara E – 119 Gas heater 1 E – 120 Gas heater 2 E – 125

IV - 2 Pra Rencana Pabrik Urea Formaldehyde Concentrate Jumlah 12298,6991 Jumlah 290187,3988 Entalpi recycle metanol dari F - 112 Entalpi metanol cair ke V - 115 CH 3 OH 8032,1390 CH 3 OH 8032,1390 HCHO 332,8482 HCHO 332,8482 HCOOH 0,0405 HCOOH 0,0405 H 2 O 637,9125 H 2 O 637,9125 Jumlah 9002,9402 Jumlah 9002,9402 Q supply 286065,2686 Q loss 14303,2634 Total 313493,6024 Total 313493,6024

3. Heater udara E – 119

Masuk kkal Keluar kkal Entalpi udara dari G - 118 : Entalpi udara ke E - 120 O 2 797,2987 O 2 6589,0450 N 2 3093,4973 N 2 25494,6877 H 2 O 144,8392 H 2 O 1198,6319 Jumlah 4035,6352 Q supply 30786,0310 Q loss 1539,3016 Total 34821,6662 Total 34821,6662

4. Gas heater 1 E – 120

Masuk kkal Keluar kkal Entalpi metanol +udara dari MP : Entalpi metanol + udara ke E 121 : CH 3 OH 205921,2819 CH 3 OH 297408,5773 HCHO 7217,2298 HCHO 29731,5145 HCOOH 1,9933 HCOOH 13820,8106 H 2 O 78245,5257 H 2 O 1,5161 N 2 25494,6877 N 2 197463,4908 IV - 3 Pra Rencana Pabrik Urea Formaldehyde Concentrate O 2 6589,0450 O 2 51697,2550 Jumlah 323469,7634 Jumlah 590123,1644 Entalpi flue gas dari R – 130 : Entalpi flue gas ke E – 131: HCHO 1149234,5027 HCHO 961108,4673 CH3OH 174115,8858 CH3OH 148214,4490 H2O 163524,7164 H2O 142758,3303 N2 382089,7022 N2 334799,3390 H2 211483,3165 H2 188794,6812 CO 403992,3479 CO 321882,1129 CO2 48088,0316 CO2 41718,5623 HCOOH 59,5338 HCOOH 51,0953 HCOOCH3 201,3075 HCOOCH3 164,8090 Jumlah 2532789,3445 Jumlah 2139491,8463 Q loss 126639,4672 Total 2856259,1079 Total 2856259,1079

5. Gas heater 2 E – 125

Masuk kkal Keluar kkal Entalpi metanol + udara dari E – 120: Entalpi metanol + udara ke R - 130 : CH 3 OH 297408,5773 CH 3 OH 627457,4011 HCHO 29731,5145 HCHO 56303,0528 HCOOH 13820,8106 HCOOH 31405,2358 H 2 O 1,5161 H 2 O 3,1244 N 2 197463,4908 N 2 368508,4467 O 2 51697,2550 O 2 96475,2587 Jumlah 590123,1644 Jumlah 1180152,5195 Q supply 621083,5320 Q loss 31054,1769 Total 1211206,6964 Total 1211206,6964 IV - 4 Pra Rencana Pabrik Urea Formaldehyde Concentrate 6. Reaktor Fixed bed R – 210 Masuk kkal Keluar kkal Entalpi metanol +udara dari E - 121 : Entalpi produk gas ke E - 131 : CH 3 OH 627457,4011 HCHO 1149234,5027 HCHO 56303,0528 CH3OH 174115,8858 HCOOH 31405,2358 H2O 163524,7164 H 2 O 3,1244 N2 382089,7022 N 2 368508,4467 H2 211483,3165 O 2 96475,2587 CO 403992,3479 Jumlah 1180152,5195 CO2 48088,0316 Entalpi reaksi Eksotermis : HCOOH 59,5338 1431602,8911 HCOOCH3 201,3075 Jumlah 2532789,3445 Q terserap 78966,0661 Total 2611755,4106 Total 2611755,4106

7. Absorber D – 220