Multi-phase fluid model based on three pseudo-components  :

water pseudo-component, which may include minerals (assuming formation water and injection water composition is the same)

dead oil pseudo-component 

dry gas pseudo-component


existing in three possible phases :

water phase, consisting of water componentdead oil pseudo-component and dry gas pseudo-component

oil phase, consisting of dead oil pseudo-component and dissolved dry gas pseudo-component (called Solution Gas) and water

gas phase, consisting of dry gas pseudo-component and vaporized dead oil pseudo-component (called Volatile Oil)



The volumetric phase-balance equations is:

s_w + s_o+s_g =1

where

share of total fluid volume occupied by water phase

share of total fluid volume occupied by oil phase

share of total fluid volume occupied by gas phase


The accountable cross-phase exchanges are illustrated in the table below:


xxx

xxx

xxx


Injection water and production water are assumed to have the same dynamic fluid properties and not being discerned.


It's a typical case for 
saturated reservoir.

See Also


Petroleum Industry / Upstream / Subsurface E&P Disciplines / Fluid (PVT) Analysis / Fluid (PVT) modelling