Abstract. Experiments investigating the mass transfer of several dissolved volatile organic compounds (VOCs) across the air-water interface were conducted using a single-airchannel air-sparging system. Three different porous media were used in the study. Air velocities ranged from 0.2 cm s-• to 2.5 cm s-•. The tortuosity factor for each porous medium and the air-water mass transfer coefficients were estimated by fitting experimental data to a one-dimensional diffusion model. The estimated mass transfer coefficients K G ranged from 1.79 x 10 -3 cm min -• to 3.85 x 10 -2 cm min -•. The estimated lumped gas phase mass transfer coefficients KGa were found to be directly related to the air diffusivity of the VOC, air velocity, and particle size, and inversely related to the Henry's law constant of the VOCs. Of the four parameters investigated, the parameter that controlled or had a dominant effect on the lumped gas phase mass transfer coefficient was the air diffusivity of the VOC. Two empirical models were developed by correlating the Damkohler and the modified air phase Sherwood numbers with the air phase Peclet number, Henry's law constant, and the reduced mean particle size of porous media. The correlation developed in this study may be used to obtain better predictions of mass transfer fluxes for field conditions.
IntroductionIn situ air sparging has been used for more than 10 years with varying success for the remediation of aquifers contaminated with dissolved volatile organic compounds (VOCs) and nonaqueous phase liquids (NAPLs). In a typical air-sparging system, clean air is injected below the water table to Even though the VOC concentrations at the air-water interface may more accurately represent the physics of the system, measurement of the VOC concentrations at the air-water interface is not possible. Therefore the standing issue in the estimation of the mass transfer coefficients between gas and liquid phases during air sparging is to define in a practical way, the driving force (i.e., concentration gradient) for the volatilization of VOCs. Since an air-sparged porous medium is not a completely mixed system, the task of defining the concentration gradient is more challenging. The objective of this work was to investigate the air-water mass transfer process for dissolved VOCs using an experimental setup where the interfacial area between the air and liquid phases was held constant. Mass transfer coefficients deter-
Materials and MethodsThe approach taken was to use an experimental setup which would simulate air flow in a single discrete air channel in saturated porous media. Table 2. Partition coefficients of the VOCs for the three porous media were assumed to be linear for the concentrations tested. The VOC partition coefficients were determined individually using the head space technique as described by Ong and Lion [1991]. Linear partition coefficients were found to range between 0.018 mL g-• and 0.082 mL g-• and