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

dead oil pseudo-component

dry gas pseudo-component


existing in two possible phases :

oil phase, consisting of dead oil pseudo-component and dissolved natural gas pseudo-component (called solution gas)

gas phase, consisting of natural gas pseudo-component and vaporized dead oil pseudo-component (called volatile oil)


The volumetric phase-balance equations is:

s_o+s_g =1

where

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:



xx

xx


It's a typical case for reservoirs  with poor or no aquifer.


See Also


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