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Saturated oil gas solubility 


Rsscf/stbp ≤ pb

\displaystyle R_s(p, T) = c_1 \, \gamma_g \, p^{c_2} \, \exp \left[ \frac{c_3 \, \gamma_{API}}{T + 459.67} \right]

\gamma_{API} \leq 30 \ {\rm API} : \quad c_1 = 0.0362, \, c_2 = 1.0937, \ c_3 = 25.7240

\gamma_{API} > 30 \ {\rm API} : \quad c_1 = 0.0178, \, c_2 = 1.1870, \ c_3 = 23.9310

where

p

psiaFluid pressure

T

°FFluid temperature

\gamma_{API}

°APIOil API gravity

\gamma_o

fracOil specific gravity

\gamma_g

fracGas specific gravity

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


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