|Abriola, Linda - U. MICHIGAN, ANN ARBOR,MI|
|Lang, John - U. MICHIGAN, ANN ARBOR,MI|
|Gaither, Charles - JC STEELE & SONS, N.C.|
Submitted to: Vadose Zone Journal
Publication Type: Peer Reviewed Journal
Publication Acceptance Date: April 20, 2004
Publication Date: June 20, 2004
Citation: Abriola, L.M., Bradford, S.A., Lang, J., Gaither, C.L. 2004. Volatilization of binary NAPL mixtures in unsaturated porous media. Vadose Zone Journal. 3:645-655. Interpretive Summary: Hazardous organic liquid mixtures have been spilled or improperly disposed of at many industrial waste sites. Cleanup of these sites commonly involves pumping air through the contaminated soil zone, either to stimulate microbial destruction or evaporation of the organic compounds. Laboratory studies and computer simulations were conducted to better describe the evaporation process of residual organic mixtures in soil. Evaporation rates were found to decrease with increasing pumping rates. Computer simulations indicate that the observed evaporation rates were not accurately described by conventional approaches that show a strong dependence on the organic mixture composition. Various explanations were investigated as potential causes for this discrepancy.
Technical Abstract: This study examines the volatilization behavior of binary nonaqueous phase liquid (NAPL) mixtures consisting of styrene, and toluene or tetrachloroethylene (PCE). Residual NAPL saturations were emplaced in unsaturated (residual water saturation) soil columns packed with Wagner 50-80 sand. Initial column effluent concentrations were measured for the NAPL mixtures at several pore gas phase velocities. Rate-limited volatilization occurred at higher gas phase pore velocities, and mass transfer coefficients could be reasonably predicted with a correlation developed from single component NAPL volatilization data. Long-term volatilization studies for the binary NAPL mixtures were also conducted. The effluent concentrations for both NAPL components were observed to be initially proportional to their mole fractions. After the more volatile component became depleted, a rapid drop in the effluent concentration of this component was accompanied by an increase in the mole fraction and effluent concentration of the remaining constituent to near saturated values until the free phase NAPL was volatilized. The final stage of removal was associated with a dramatic decrease in effluent concentration, attributed to reduction in the gas-NAPL interfacial area, followed by low concentration tailing. The tailing and subsequent flow interruption behavior are likely a consequence of rate-limited desorption. Equilibrium and rate-limited simulations of the long-term volatilization experiments did not provide a satisfactory description of the data. A simulation that included a fixed concentration gradient and fitted activity coefficients provided a better characterization of the volatilization data. Various potential explanations for this "fixed gradient" volatilization behavior were considered, but additional research is needed to test these hypotheses.