| LaTeX Math Block |
|---|
| RP_vd = \exp \big [ 3.6848.48 + 0.6196732239 \cdot Z + 0.015359000477 \cdot Z^2 \big ] |
|
| LaTeX Math Block |
|---|
| Z = \sum_{n=01}^4^3 \, Z_n |
| | LaTeX Math Block |
|---|
| Z_n = C_{n0} + C_{n1} \cdot {\rm VAR}_n + C_{n2} \cdot {\rm VAR}_n^2 + C_{n3} \cdot {\rm VAR}_n^3 + C_{n4} \cdot {\rm VAR}_n^4 |
|
where
and
Cn3| Cn4 | pFluidpsia208096709551360 | 01751.2965042311-00054382.49E-6-133652765218.5984.3658 | 0 | 4
The correlation is built over the following range:
| T_r | Fluid temperature | °F | -1.5309 | 0.0058453 | 1.4E-6 | 0 | 0 | The correlation is built over the following range:
| Minimum | Maximum |
| Initial stock-tank condensate API gravity for recombined dewpoint gas composition | | LaTeX Math Inline |
|---|
| body | --uriencoded--\gamma_%7Bo%7B\rm API%7D%7D |
|---|
|
| °API | 35.6 |
|---|
378 recombined to the dew point| for recombined dewpoint gas composition | | LaTeX Math Inline |
|---|
| body | --uriencoded--\gamma_%7Bg Rd%7D |
|---|
|
| frac | 0.609 | 0. |
|---|
643568126Fluid 1159015
The correlation has been built for the measured at the first stage of separator (as the oil yield measurements at second stage separator and stock tank are not readily available).
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