This study was conducted to investigate the mass transfer behavior for a mu
lticomponent system in the soil venting process. Soil venting experiments w
ere conducted using gasoline-contaminated soil and models of local equilibr
ium assumption (LEA) and the first-order kinetic approach were used to desc
ribe the gasoline volatilization process. However, the focus was on the app
lication of the kinetic model In both models, thirteen major components of
gasoline were selected for the model input and the rest of the gasoline was
divided into 11 groups based on the retention times in the gas chromatogra
phy of gasoline. The LEA model had the tendency of underestimating the gas
concentration at the initial phase and overestimating at the later phase du
e to the different volatilities of multi-components. In the kinetic model t
he estimation of mass transfer coefficient values were carried out by adopt
ing the relationship developed in the single-components system and choosing
the appropriate modified Sherwood number. This method resulted in the good
agreement with the simulation and the experimental results.