s_w  \cdot \frac{(\epsilon -1)(2\epsilon+1)}{9\epsilon} + \left( 1-s_w \right) \cdot \frac{\epsilon-1}{\epsilon+2} = s_w P_w + s_o P_g + s_g P_g
P_w =  \frac{(\epsilon_w-1)(2\epsilon_w+1)}{9 \, \epsilon_w}
P_o(T) = \frac{\epsilon_o-1}{\epsilon_o+2}
P_g(T) = \frac{\epsilon_g-1}{\epsilon_g+2}
\epsilon_w(T) = 87.74 - 0.40008 \cdot T + 9.398 \cdot  10^{-4} \cdot T^2
- 1.41  \cdot  10^{-6} \cdot T^3
\epsilon_o(T) = 16 ÷ 20
\epsilon_g(T) = 1 ÷ 2

where

volumetric fractions of water, oil and gas phases: 

electrical polarization of water, oil and gas phases

relative dielectric permittivity of water, oil and gas phases

fluid temperature


See also


Petroleum Industry /  Upstream / Subsurface E&P Disciplines / Fluid Analysis / Fluid Capacitance

Dielectric permittivity of water @model ]


References


[pdf] A. H. Harvey and E. W. Lemmon, Method for Estimating the Dielectric Constant of Natural Gas Mixtures, International Journal of Thermophysics, Vol. 26, No. 1, January 2005 ,DOI: 10.1007/s10765-005-2351-5

[pdf] Eric F. May et al, Density, dielectric constant and PVT measurementsof a gas condensate fluid, Journal of Petroleum Science and Engineering 41 (2004) 297–308