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Oil isothermal compressibilitycopsi-1p > pb

c_o(p, T) = c_1 \, R_s^{c_2}(p, T) \, \gamma_g^{c_3} \, \gamma_{API}^{c_4} \, T^{c_5} \, p^{c_6}

c_1 = 1.705 \cdot 10^{-7}, \ c_2 = 0.69357, \ c_3 = 0.1885, \ c_4 = 0.3272, \ c_5 = 0.6729, \ c_6 = -0.5906

where

p

psiaFluid pressure

T

°FInitial formation temperature

\gamma_{API}

APIOil API gravity

\gamma_o

fracOil specific gravity

\gamma_g

fracGas specific gravity

R_{sb}

scf/stbGas Solubility at Bubble point pressure

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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