Bubble point pressure | pb | psia | | LaTeX Math Inline |
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| body | --uriencoded--\displaystyle p_b(T) = \left[ \frac%7BR_%7Bsb%7D%7D%7Bc_1 \, \gamma_g \, \exp \left[ \frac%7Bc_3 \, \gamma_%7BAPI%7D%7D%7BT+459.67%7D \right ]%7D \right]%5e%7B1/c_2%7D |
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| LaTeX Math Inline |
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| body | --uriencoded--\gamma_%7BAPI%7D \leq 30 \ %7B\rm API%7D : \quad c_1 = 0.0362, \, c_2 = 1.0937, \ c_3 = 25.7240 |
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| LaTeX Math Inline |
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| body | --uriencoded--\gamma_%7BAPI%7D > 30 \ %7B\rm API%7D : \quad c_1 = 0.0178, \, c_2 = 1.1870, \ c_3 = 23.9310 |
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where
See Also
Petroleum Industry / Upstream / Petroleum Engineering / Subsurface E&P Disciplines / Reservoir Engineering (RE) / PVT correlations / Oil correlations
[ Vasquez-Beggs (1980) oil correlations ]
References
Vasquez, M., and H.D. Beggs. "Correlations for Fluid Physical Property Prediction." J Pet Technol 32 (1980): 968–970, doi.org/10.2118/6719-PA
