Makalah Crude Oil,Proses Pengolahan Migas & Produk Minyak Bumi
Tugas 1 - Produk Migas
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%vol 10 30Nafta, oF 180 194
Kerosin, oF 317 334
UOP 375Slope CABP A
1.4375 229.0092397859 -3.21164453131.5625 374.9172279492 -3.6043945313
A. VABP
VABP (Nelson) VABP(UOP 375) Selisih233.75 231.6 2.15381.75 377.4 4.35
Selisih12.0003293906 11.9860287819 0.014300608711.7970061062 11.7882020117 0.0088040945
B. KUOP
KUOP (UOP 375) KUOP (Nelson)
C. BERAT MOLEKUL
BM (UOP 375) BM (Fig. 5-9 Nelson) Selisih103.2787203171 105 1.7212796829149.1119726998 151 1.8880273002
KESIMPULAN
LAMPIRAN
50 70 90 95 SG230 259 295 334 0.7359384 410 442 455 0.7981
UOP 375E MeABP F H I
1.0026808477 224.0420587836 -14.7066132813 1.0094192188 0.0013159471.0029719727 369.9242970996 -16.3567382813 1.0103023438 0.0012274941
Figure 5-4 Nelson fk MeABPNafta -7.5 226.25Kerosin -9 372.75
Figure 5-4 Nelson API fk MABPNafta 60.7815599946 -13 220.75Kerosin 45.7960781857 -14.5 367.25
KESIMPULAN
LAMPIRAN
UOP 375UOP 375
J L1.74338 -5.420959
1.736692 -6.384695
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LAMPIRAN
UOP 375
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LAMPIRAN
UOP 375
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LAMPIRAN