Through a systematic experimental study it is found that the effect of liqu
id phase on non-Darcy gas flow through proppant packs cannot be characteriz
ed by Forchheimer correlation alone. An empirical equation that uses liquid
-to-gas ratio to predict the effective permeability or conductivity of a pr
oppant pack under two-phase, non-Darcy flow conditions is proposed in the p
aper. The effective permeability of a proppant pack at different conditions
can then be calculated taking both non-Darcy and two-phase flow effect int
o account. A simplified physical model is developed to calculate a mobile l
iquid saturation at mio-phase flow conditions.