perhitungan nme
DESCRIPTION
perhitungan menara distilasi type tray cepuTRANSCRIPT
flow 25 T/d a-pinen 74.81% 18.70 b-pinen 7.69% 1.92 d-carene 12.18% 3.05 d-limonen 1.02% 0.26 other 4.30% 1.08
total den.cam
NERACA PANAS C-2001
in preheating panas masuk 6,474,569.92 Cp 1.96 panas keluar 3,526,649.89 dT 100.00 loses 2,947,920.03 m 25,000.00 Q 4,900,000.00 Efisiensi C-2001
0.46 0.54
out bottom columncp 2.19 dT 105.00 total keluar C-2001m 6,860.00 kg/d L/d Q 1,574,575.80 a-pinen 18585.48 21,636.18
b-pinen 1872.96 2,155.30 d-carene 3040.03 3,530.81
out condensor d-limonen 255.192 303.73 cp 1.91 other 1246.34 3,608.40 dT 56.00 25000 31,234.42 m 18,288.81 Q 1,952,074.09
in hot oilcp 2.72 dT 60.00 m 9,648.10 Q 1,574,569.92
flow 18.14 T/d a-pinen 97.74% 17.730036 b-pinen 0.33% 0.059862 d-carene 0.21% 0.038094 other 1.72% 0.312008
totalden.cam
Kg/d L/d18702.5 21772.41
1922.5 2212.3133045 3536.585
255 303.49921075 1380.8
25000 29205.610.856
flow 6.86 T/d a-pinen 12.47% 0.855442 b-pinen 26.43% 1.813098 d-carene 43.76% 3.001936 d-limonen 3.72% 0.255192 other 13.62% 0.934332
totalden.cam
8,289,263.16 2,958,183.87
NERACA PANAS TOTAL
panas masuk 8,289,263.16 panas keluar 4,532,759.67
loses 3,756,503.49
Efisiensi totalpanas yang hilang 45%
C-2001
efisiensi kolom 55%
GCF kJ/kg 42,705.40 massa 69.03
18.93
Kg/d L/d17730.04 20640.321 densitas
59.862 68.886076 a-pinen 0.86 38.094 44.243902 b-pinen 0.87
312.008 1556.1 d-carene 0.86 18140 22309.551 d-limonen 0.84
0.813103
Kg/d L/d855.442 995.85797
1813.098 2086.41893001.936 3486.5691
255.192 303.72768934.332 2052.295
6860 8897.53570.771 NERACA PANAS C-2002
in preheating panas masukCp 2.19 panas keluardT 100.00 losesm 6,860.00 Q 1,499,596.00 Efisiensi C-2002
44.56%55.44%
in hot oilcp 2.72 bottom columndT 19.00 Cp 2.164m 89,785.00 dT 19Q 240,117.44 m 5840
Q 240117.44
out condensorcp 1.91 dT 43.00 m 1,020.00 Q 83,553.30
C-2002
out bottom condensorcp 2.16 dT 73.00 m 5,840.00 Q 922,556.48
total keluar C-2002 flow 1.02 T/d Kg/d L/d a-pinen 47.44% 0.483888 483.888 563.3155 a-pinen b-pinen 41.74% 0.425748 425.748 489.9287 b-pinen d-carene 0.09% 0.000918 0.918 1.066202 d-carene other 10.73% 0.109446 109.446 192.28 d-limonen
total 1020 1246.59 otherden. Cam 0.81823
neraca massa total flow 5.84 T/d Kg/d L/d in a-pinen 0.95% 0.05548 55.48 64.58673 out b-pinen 2.75% 0.1606 160.6 184.8101 d-carene 69.82% 4.077488 4077.488 4735.758 d-limonen 9.49% 0.554216 554.216 659.6239 other 16.99% 0.992216 992.216 1876.7
total 5840 7521.479den.cam 0.776443
1,814,693.24 1,006,109.78 808,583.46
total keluar C-2002kg/d L/d
539.368 627.90221586.348 674.73878
4078.406 4736.8246554.216 659.6239
1101.662 2068.986860 8768.0695
neraca massa total2500025000