Table 2.
Number | Field | Experimental results of steam distillation yields for V w/V oi | Crude oil properties | |||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|
1 | 2 | 3 | 4 | 5 | 10 | 15 | 20 | API | Kinematic viscosity at 37.8°C | Characterization factor | ||
1 | South Belridge | 0.031 | 0.046 | 0.06 | 0.069 | 0.075 | 0.1 | 0.119 | 0.13 | 12.4 | 0.4085 | 9.7 |
2 | Winkleman Dome | 0.089 | 0.111 | 0.125 | 0.136 | 0.142 | 0.17 | 0.182 | 0.195 | 14.9 | 0.0488 | 9.6 |
3 | White Castle | 0.07 | 0.095 | 0.11 | 0.122 | 0.137 | 0.185 | 0.21 | 0.23 | 16 | 0.0308 | 9.7 |
4 | Edison | 0.092 | 0.12 | 0.14 | 0.151 | 0.164 | 0.19 | 0.198 | 0.209 | 16.1 | 0.0397 | 9.7 |
5 | Red Bank | 0.128 | 0.162 | 0.18 | 0.195 | 0.205 | 0.231 | 0.241 | 0.25 | 17.1 | 0.03 | 9.9 |
6 | Slocum | 0.032 | 0.08 | 0.097 | 0.11 | 0.122 | 0.172 | 0.195 | 0.2 | 18.8 | 0.0395 | 10.0 |
7 | Hidden Dome | 0.119 | 0.148 | 0.169 | 0.19 | 0.205 | 0.25 | 0.28 | 0.295 | 20.7 | 0.0086 | 10.1 |
8 | Toborg | 0.196 | 0.239 | 0.267 | 0.285 | 0.3 | 0.339 | 0.349 | 0.36 | 22.2 | 0.0036 | 10.1 |
9 | Brea | 0.21 | 0.24 | 0.265 | 0.283 | 0.296 | 0.33 | 0.34 | 0.354 | 23.5 | 0.0039 | 10.0 |
10 | Shannon | 0.14 | 0.192 | 0.22 | 0.24 | 0.26 | 0.307 | 0.328 | 0.331 | 24.7 | 0.0032 | 10.2 |
11 | Robinson | 0.128 | 0.176 | 0.208 | 0.228 | 0.245 | 0.295 | 0.312 | 0.32 | 26 | 0.0029 | 10.3 |
12 | El Dorado | 0.345 | 0.4 | 0.43 | 0.441 | 0.45 | 0.47 | 0.475 | 0.48 | 32.5 | 0.0005 | 10.1 |
13 | Shiells Canyon | 0.378 | 0.438 | 0.47 | 0.49 | 0.508 | 0.541 | 0.558 | 0.57 | 33 | 0.0006 | 10.2 |
14 | Teapot Dome | 0.24 | 0.32 | 0.36 | 0.396 | 0.425 | 0.503 | 0.534 | 0.57 | 34.5 | 0.0006 | 10.4 |
15 | Rock Creek | 0.295 | 0.36 | 0.4 | 0.412 | 0.42 | 0.447 | 0.465 | 0.48 | 38.2 | 0.0005 | 10.4 |
16 | Plum Bush | 0.28 | 0.338 | 0.36 | 0.38 | 0.4 | 0.46 | 0.489 | 0.53 | 39.9 | 0.0006 | 10.5 |
aWu and Elder, 1983 [10].