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(1) \epsilon_f(T) = 0.25 \cdot \left[ 1+ 9 \cdot P_f + 3 \cdot \sqrt{ 9 P_f^2 + 2 P_f +1} \right]
(2) P_f(T) = s_w \cdot P_w + s_o \cdot P_o + s_g \cdot P_g
(3) P_w(T) = \frac{(\epsilon_w-1)(2\epsilon_w+1)}{9 \, \epsilon_w}
(4) \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
(5) P_o(T) = \frac{\epsilon_o-1}{\epsilon_o+2}

(6) P_g(T) = = \frac{\epsilon_g-1}{\epsilon_g+2}

where

s_w, \, s_o, \, s_g

volumetric fractions of water, oil and gas phases:  s_w + s_o + s_g = 1

P_w, \, P_o, \, P_g

electrical polarization of water, oil and gas phases

\epsilon_w, \, \epsilon_o, \, \epsilon_g

relative dielectric permittivity of water, oil and gas phases

T

fluid temperature


See also


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

Dielectric permittivity of water @model ]








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