4.4. Flash Tank I FT-110
Tabel 4.4 Neraca panas Flash Tank I FT-110
Komponen Q in
kjjam Q out
kjjam
Trikaprilin 4.865,4389
4.865,4389 Trikaprin
4.552,9897 4.552,9897
Trilaurin 61.178,3288
61.178,3288 Trimiristin
20.399,8403 20.399,8403
Tripalmitin 10.734,0379
10.734,0379 Tristearin
2.642,3423 2.642,3423
Triolein 20.580,9579
20.580,9579 Trilinolein
3.005,1559 3.005,1559
Triarachidin 253,6427
253,6427 Gliserol
550.027,9949 550.027,9949
H
2
O 2.535.911,6476
2.535.911,6476
Total 3.214.152,3769
3.214.152,3769
4.5. Flash Tank II FT-120
Tabel 4.5 Neraca Panas Flash Tank II FT-120
Komponen Q in
kjjam Q out
kjjam
Asam Kaprilat 213.145,8807
213.145,8807 Asam Kaproat
203.092,2875 203.092,2875
Asam Laurat 2.764.760,89
2.764.760,89 Asam Miristat
931.041,0116 931.041,0116
Asam Palmitat 493.692,5717
493.692,5717 Asam Stearat
123.636,9132 123.636,9132
Asam Oleat 874.278,1572
874.278,1572 Asam Linoleat
114.452,4132 114.452,4132
Asam Arachidic 11.798,41877
11.798,41877 H
2
O 397.538,4691
397.538,4691
Total 6.127.437,013
6.127.437,013
4.6. Kondensor I E-103 Tabel 4.6 Neraca Panas Kondensor I E-103
Komponen Qin
kjjam Qout
kjjam
H
2
O 86.561,56366
8.848,548032 Pendingin
- 77.713,01563
Total 86.561,56366
86.561,56366
4.7. Kondensor II E-105
Tabel 4.7. Neraca Panas Kondensor II E-105
Komponen Qin
kjjam Qout
kjjam
H
2
O 13.569,69654
1.387,129651 Pendingin
- 12.182,56688
Total 13.569,69654
13.569,69654
4.8. Cooler I E-104
Universitas Sumatera Utara
Tabel 4.8 Neraca Panas Cooler I E-104
SENYAWA Q masuk
Kjjam Q out
Kjjam
Trikaprilin 2.009,638
105,770 Trikaprin
1.880,583 98,978
Trilaurin 25.269,310
1.329,964 Trimiristin
8.426,021 443,475
Tripalmitin 4.433,624
233,349 Tristearin
1.091,402 57,442
Triolein 8.500,830
447,412 Trilinolein
1.241,260 65,329
Triarachidin 104,765
5,514 Gliserol
30.287,743 1.594,092
H
2
O 202.552,227
15.471,455 Air pendingin
- 265.944,6237
Total 285.797,404
285.797,404
4.9. Dryer D-210
Tabel 4.9 Neraca Panas Dryer D-210
Komponen Q in
kjjam Q out
kjjam
Asam Kaprilat 88.038,51592
115.840,15253 Asam Kaproat
83.885,94482 110.376,24319
Asam Laurat 1.141.966,455
1.502.587,44041 Asam Miristat
384.560,4178 506.000,54979
Asam Palmitat 203.916,497
268.311,18026 Asam Stearat
51.067,42067 67.193,97457
Asam Oleat 361.114,891
475.151,17237 Asam Linoleat
47.273,82285 62.202,39849
Asam Arachidic 4.873,259927
6.412,18411 H
2
O 762.344,6514
- Steam
310.624,0989 325.590,67931
Total 3.439.665,975
3.439.665,97503
4.10. Heater III E-201
Tabel 4.10. Neraca Panas Heater III E-201
SENYAWA Q masuk
Kjjam Q out
Kjjam
Asam Kaprilat 115.840,153
164.029,656 Asam Kaproat
110.376,243 156.292,760
Asam Laurat 1502.587,440
2.127.663,816 Asam Miristat
506.000,550 716.496,778
Asam Palmitat 268.311,180
379.928,631 Asam Stearat
67.193,975 95.146,668
Asam Oleat 475.151,172
672.814,060 Asam Linoleat
62.202,398 88.078,596
Asam Arachidic 6.412,184
9.079,653 Steam
1.295.455,323 -
Total 4.409.530,619
4.409.530,619
4.11 Kondensor III E-211
Universitas Sumatera Utara
Tabel 4.11. Neraca Panas Kondensor III E-211
SENYAWA Q masuk
Kjjam Q out
Kjjam
Asam Kaprilat 738.327,0707
753.391,4 Asam Kaproat
312.272,9352 213.474,7
Asam Laurat 3.246,556124
2.219,397 Air Pendingin
- 84.761,03
Total 1.053.847
1.053.847
4.12 Reboiler I E-213