Page 61 - Characterization and Properties of Petroleum Fractions - M.R. Riazi

P2: —/—
QC: —/—
P1: KVU/—
AT029-02
AT029-Manual-v7.cls
AT029-Manual
RON T1: IML . . . 1.6 August 16, 2007 . . . . . . 16:6 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 0.1 92.3 73.4 42.4 20.6 100.0 . . . . . . (Continued )
93.8
1.8
clear
61.7
0.0
24.8
. . .
. . .
Flammability range, vol.% Max Min 1.00 5.00 13.00 2.90 9.50 2.10 8.40 1.80 8.30 1.40 7.70 1.20 7.00 1.00 6.5 0.96 2.90 0.87 2.60 0.78 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.40 1.80 8.30 1.40 7.70 1.20 7.00 1.00 . . . 0.98 . . . 1.00 . . . . . . . . . . . .
AP, ◦ C 536.9 471.9 449.9 287.9 242.9 224.9 203.9 205.9 204.9 200.9 201.9 202.9 201.9 199.9 201.9 201.9 201.9 201.9 201.9 201.9 201.9 201.9 460.1 420.1 . . . . . . . . . . . . . . . . . .
AI, ◦ C . . . . . . . . . 83.2 70.8 68.7 . . . 220 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 107.7 70.8 73.8 74.1 73.9 79.5 . . . . . .

T F ◦ C . . . . . . . . . . . . −40.0 −21.7 −4.1 12.9 30.9 45.9 65.0 73.9 78.9 100.0 113.9 135.1 147.8 165.1 167.9 166.9 176.9 184.9 . . . −57.2 −35.2 −23.2 4.1 −12.2 22.9 40.9
compounds. CH 2.98 3.97 4.47 4.77 4.96 5.11 5.21 5.30 5.36 5.42 5.46 5.50 5.53 5.56 5.59 5.61 5.63 5.64 5.66 5.67 5.69 5.70 4.77 4.96 5.11 5.21 5.30 5.30 5.36 5.42

selected Viscosity, cSt ν 99(210) . . . . . . . . . 0.1686 0.2643 . . . 0.3515 0.3997 0.4694 0.5537 0.6397 0.7469 0.8624 0.9885 1.1328 1.2859 1.4413 1.5815 1.7940 1.9889 2.1703 2.4099 0.1873 . . . . . . . . . 0.3635 0.3738 0.4329 0.5401

some ν 38(100) . . . . . . 0.1775 0.2533 0.3394 0.4152 0.5046 0.6364 0.8078 1.0154 1.2588 1.5452 1.8634 2.2294 2.6415 3.1229 3.6045 4.1620 4.6090 5.3165 . . . . . . 0.2773 0.3066 0.3862 0.4730 0.5908 0.6077 0.7382 0.9636
of
properties P, sat at 100 ◦ F bar 344.737 55.1579 12.9621 3.5608 1.0745 0.3435 0.1112 0.0370 0.0125 0.0042 0.0014 0.0005 0.0002 0.0001 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 . . . . . . 5.0199 1.4110 0.4666 0.1562 0.0528 0.1181 0.0177 0.0058

2.2—Secondary K W 19.53 19.49 14.74 13.49 13.02 12.79 12.67 12.66 12.66 12.67 12.71 12.74 12.76 12.82 12.87 12.97 13.05 13.01 13.04 13.12 13.11 13.15 13.78 13.01 12.82 12.72 12.65 12.52 12.66 12.66

TABLE API gravity 340.3 266.6 148.0 110.4 92.5 81.2 73.5 68.6 64.5 61.2 58.7 56.6 54.4 53.1 51.9 51.6 51.0 49.0 48.1 47.8 46.4 45.8 119.2 94.4 83.6 75.9 69.8 71.0 65.7 62.1

N C 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 4 5 6 7 8 8 9 10

Formula CH 4 C 2 H 6 C 3 H 8 C 4 H 10 C 5 H 12 C 6 H 14 C 7 H 16 C 8 H 18 C 9 H 20 C 10 H 22 C 11 H 24 C 12 H 26 C 13 H 28 C 14 H 30 C 15 H 32 C 16 H 34 C 17 H 36 C 18 H 38 C 19 H 40 C 20 H 42 C 21 H 44 C 22 H 46 C 4 H 10 C 5 H 12 C 6 H 14 C 7 H 16 C 8 H 18 C 8 H 18 C 9 H 20 C 10 H 22

(isooctane)
(2-Methylpropane) (2-Methylbutane) 2,2,4-Trimethylpentane

Compound Paraffins Methane Ethane Propane n-Butane n-Pentane n-Hexane n-Heptane n-Octane n-Nonane n-Decane n-Undecane n-Dodecane n-Tridecane n-Tetradecane n-Pentadecane n-Hexadecane n-Heptadecane n-Octadecane n-Nonadecane n-Eicosane n-Heneicosane n-Docosane isobutane isopentane 2-Methylpentane 2-Methylhexane 2-Methylheptane 2-Methyloctane 2-Methylnonane

41

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