Page 69 - Characterization and Properties of Petroleum Fractions

P1: KVU/—
AT029-Manual
AT029-Manual-v7.cls
AT029-02
AAD% P2: —/— 0.6 0.7 QC: —/— 1.0 2.7 T1: IML 2.3 3.1 August 16, 2007 2.6 1.7 16:6 2.3 2.3 3.4 3.5 1.0 1.1 1.1 1.7 1.6 0.5 1.0 0.5 1.3 0.5 0.5 0.5 0.5 0.9 0.6 0.4 2.5 1.7 2.6 1.7 2.5 1.6 and T b
1.0
2.6
3.5
0.7
0.5
0.8
2.7
1.9
2.1
2.1
2.4
4.2
1.8
1.8
in cm 3 /g,
0.53691 0.10199 6.51274 6.89383 0.472372 0.73238 6.30280 0.919255 8.04224 0.98960 1.11782 0.82910 0.77078 0.84599 V c
f 4.3469 1.0555 4.0642 1.4191 0.7492 4.0846 18.4302 3.2223 1.6015 12.9148 2.4004 2.052 −1.2028 −2.1548 −1.4439 −1.3036 −4.60413 −1.3362 −10.65067 −1.9985 −0.2727 −10.6 −1.58262 0.4283 1.3489 −3.8798 6.9195 −0.71990 −6.79769 −13.61390 −0.76820 −12.34051 −20.31303 −10.88065
0.81067 0.6154 0.67221 0.2998 0.2383 0.3526 0.1884 0.7506 0.5775 0.1657 0.20378 0.2556 0.0706 0.1417 0.97476 2.0935 1.9273 0.56370 0.6675 0.4748 0.512976 0.262914 0.3228 −0.341800 0.890041 0.289844 −0.235300 0.05721 0.44700 0.16560 0.05166
e −0.4844 −1.0303 −0.1801 −0.8063 −0.8097 −0.6616 −0.4974 4.0167 × 10 −1 −0.07710 −0.00843 −0.01128 −2.72522 −1.37730 −0.68418 −0.37884 −0.14657 −0.17158
properties.
--`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
various
for d 6.48 × 10 −4 4.5236 × 10 −3 0 0 0 −2.7 × 10 −4 0 5.749 × 10 −3 0.0342 0 0 0.0451 0 0 1.971 × 10 −3 7.920 × 10 −3 2.6649 × 10 −4 2.6012 × 10 −3 4.5318 × 10 −3 3.826 × 10 −4 0.4608 2.0 × 10 −3 0 0 0.162470 0 −4.25288 × 10 −3 0 9.22926 × 10 −6 −2.1247 × 10 −2 6.029 × 10 −2 3.98736 × 10 −3 6.49168 × 10 −5 7.34400 × 10 −3 4.92112 × 10 −5 0.253300 −1.0268 × 10 −3 −7.9452 × 10 −5 −4.2451 × 10 −4 0.0 −1.8441 × 10 −2 −2.5935 × 10 −
f 1
+ dθ 1 θ 2 )θ e θ 2

+ cθ 2
(bθ 1 c −0.54444 −16.9097 0 −0.61641 −13.049 −0.1379 −1.2664 −4.8014 −74.5612 −0.3454 −0.3084 −48.5809 −0.265 0 −0.26404 0.91548 0.05345 0.5287 14.1853 0.1082 36.09011 −9.53384 4.2376 0 −9.638970 38.106 2.984036 0 −4.5707 × 10 −2 −1.68759 14.9371 −23.553500 −0.081635 −20.594000 −0.079250 −26.393400 2.46832 −6.0737 × 10 −2 −0.200996 −6.836 × 10 −2 0.231043 −7.019 × 10 −2 16.94020 71.65310 4.74695 60.34840 29.98797 53.73160
exp
a
=
θ Coefficients for Eq. (2.40) have been obtained from data on approximately 140 pure hydrocarbons in the molecular weight range of 70–300 and boiling point range of 300–620 K. Units:
(2.40)

Eq.
of b −9.314 × 10 −4 −1.3171 × 10 −3 0 −1.3478 × 10 −4 2.001 × 10 −4 1.385 × 10 −3 −0.0291 −8.505 × 10 −3 −0.012067 −3.8443 × 10 −3 −1.8078 × 10 −3 −0.01415 −2.139 × 10 −3 0 −2.6422 × 10 −3 −2.720 × 10 −3 −1.6594 × 10 −3 −2.657 × 10 −3 −2.0208 × 10 −3 −2.3533 × 10 −3 −0.16318 9.78 × 10 −4 1.55833 × 10 −5 0 −0.195411 −8.9854 × 10 −2 3.77409 × 10 −3 0 −1.57415 × 10 −4 −1.3051 × 10 −2 −6.5236 × 10 −2 −4.19400 × 10 −4 −1.83321 × 10 −3 −1.588
2.5—Coefficients

TABLE a 9.5232 4.487601 × 10 5 8.6649 308 1.347444 × 10 6 20.74 2.4522 × 10 3 3.195846 × 10 5 8.4027 × 10 23 9.858968 3116.632 2.025 × 10 16 56.26043 393.306 6.049 × 10 −2 6.712 × 10 −3 1.409 × 10 +1 7.529 × 10 −1 6.3429 × 10 −5 1.597 × 10 +1 2.01 × 10 −10 1032.1 8.9205 × 10 −6 1.81456 × 10 −3 1.51723 × 10 6 4 × 10 −9 3.76587 75.775 20.25347 2379.86 0.050629 2.43810 × 10 7 2.86706 × 10 −3 1.1284 × 10 6 6.84403 × 10 −2 3.80830 × 10 7

θ 2 SG I CH SG I CH I SG I CH SG I CH I SG I CH SG I CH I SG I CH SG I SG I CH SG I I CH I CH I SG CH SG CH SG CH SG I SG I SG I
in bar, and ν 38(100)

θ 1 T b T b T b M M M ν 38(100) T b T b T b M M M ν 38(100) T b T b T b M M M ν 38(100) T b T b T b ν 38(100) ν 38(100) M M M ν 38(100) ν 38(100) T b T b M M ν 38(100) T b T b M M ν 38(100 ν 38(100 T b T b M M ν 38(100 ν 38(100

P c
in K,
T c T c T c T c T c T c T c P c P c P c P c P c P c P c V c V c V c V c V c V c V c M M M M M T b T b T b T b T b SG SG SG SG SG CH CH CH CH CH CH T c
θ I I I I I I
49

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