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Fluid properties affecting the fluid dynamics (fluid motion in pipes and porous reservoir):
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w^{\LARGE \circ} w(P^{\LARGE \circ}, T^{\LARGE \circ})density of water phase at standard pressure | P^{\LARGE \circ} | and temperature T^{\LARGE \circ} |
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| body | B_o = B_o(P,T) = \frac{\rho_o^{\LARGE \circ}} |
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= (P^{\LARGE \circ}, T^| } = \frac{V_o}{V_o^{\LARGE \circ}} |
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)density of oil phase at standardpressure P^| B_g = B_g(P,T) = \frac{\rho_g^{\LARGE \circ |
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} and temperature | LaTeX Math Inline |
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body | T^| }}{\rho_g} = \frac{V_g}{V_g^{\LARGE \circ}} |
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| body | B_w = B_w(P,T) = \frac{\rho_ |
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g^ = g(P^{\LARGE \circ}, T^| w} = \frac{V_w}{V_w^{\LARGE \circ} |
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)density of gas phase at standard pressure P^{\LARGE \circ} | and temperature T^{\LARGE \circ}\rho \rhodensity of water phase at arbitrary pressure P | and temperature rhoo rhoodensity of oil phase at arbitrary pressure | | LaTeX Math Inline |
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| body | c_{pg} = c_{pg}(P, T) |
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and temperature | | LaTeX Math Inline |
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| body | c_{pw} = c_{pw}(P, T) |
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| Thermal conductivty | |
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rhog rhogdensity of gas phase at arbitrary pressure and temperature P | | \lambda_g = \lambda_g(P, T) |
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| body | \lambda_w = \lambda_w(P, T) |
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| Cross-phase exchange coefficients | |
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Bw Bw\rhow^\rhow} = | | LaTeX Math Inline |
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| body | R_v = R_v (P,T) = \frac{V_o^{\LARGE \circ}}{V_g} |
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| Transition points | | |
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- density
- compressibility
- formation volume factor
- viscosity
- specific heat capacity at constant pressure
- thermal conductivity
- cross-phase exchange coefficients
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| body | \rho_w^{\LARGE \circ} = \rho_w(P^ |
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| w}{V_w^| {\LARGE \circ}, T^{\LARGE \circ}) |
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| FVF density of water phase at | arbitrary | P | T |
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| body | B_o = B_o(P,T) = \frac{\rho_o^{\LARGE \circ} }{= \rho_o} = \frac{V_o}{V_o^(P^{\LARGE \circ}, T^{\LARGE \circ}}) |
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| FVF density of oil phase at arbitrary standardpressure and temperature |
| LaTeX Math Inline |
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| body | B_g = B_g(P,T) = \frac{\rho_g^{\LARGE \circ} }{= \rho_g} = \frac{V_g}{V_g^(P^{\LARGE \circ}, T^{\LARGE \circ}) |
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| density of gas phase at standard pressure and temperature FVF |
| | gas water phase at arbitrary pressure and temperature |
| density of oil phase at arbitrary pressure | \mu_w = \mu_w(P, T) | |
| | viscosity of water phase at arbitrary pressure and temperature |
| FVF of water phase at arbitrary pressure and temperature |
| FVF \mu_o = \mu_o (P, T) | viscosity of oil phase at arbitrary pressure and temperature |
| FVF of gas phase at arbitrary pressure and temperature |
| viscosity of gas water phase at arbitrary pressure and temperature |
| viscosity of oil phase at arbitrary pressure | LaTeX Math Inline |
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| body | R_s = R_s (P,T) = \frac{V_g^{\LARGE \circ}}{V_o} | P |
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and temperature |
| viscosity of gas solution gas in oil phase at arbitrary pressure and temperature |
| solution gas in oil phase at arbitrary pressure and temperature | LaTeX Math Inline |
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| body | TR_v = R_v (P,T) = \frac{V_o^{\LARGE \circ}}{V_g} |
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| oil vapour in gas phase at arbitrary pressure and temperature | LaTeX Math Inline |
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| boiling pressure at arbitrary temperature | LaTeX Math Inline |
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| dew pressure at arbitrary temperature |
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