perhitungan nme

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flow 25 a-pinen 74.81% b-pinen 7.69% d-carene 12.18% d-limonen 1.02% other 4.30% tota NERACA PANAS C-2001 in preheating panas masuk Cp 1.96 panas keluar dT 100.00 loses m 25,000.00 Q 4,900,000.00 Efisiensi C-2001 out bottom column cp 2.19 dT 105.00 total keluar C-20 m 6,860.00 kg/d Q 1,574,575.80 a-pinen 18585.48 b-pinen 1872.96 d-carene 3040.03 out condensor d-limonen 255.192 cp 1.91 other 1246.34 dT 56.00 25000 m 18,288.81 Q 1,952,074.09

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Page 1: Perhitungan NME

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

Page 2: Perhitungan NME

in hot oilcp 2.72 dT 60.00 m 9,648.10 Q 1,574,569.92

Page 3: Perhitungan NME

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

Page 4: Perhitungan NME

efisiensi kolom 55%

GCF kJ/kg 42,705.40 massa 69.03

18.93

Page 5: Perhitungan NME

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

Page 6: Perhitungan NME

out bottom condensorcp 2.16 dT 73.00 m 5,840.00 Q 922,556.48

Page 7: Perhitungan NME

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

Page 8: Perhitungan NME

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