Modeling of contaminant transport resulting from dissolution of nonaqueous phase liquid pools in saturated porous media |
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Authors: | Constantinos V. Chrysikopoulos Evangelos A. Voudrias Marios M. Fyrillas |
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Affiliation: | (1) Department of Civil and Environmental Engineering, University of California, 92717 Irvine, CA, USA;(2) School of Civil Engineering, Georgia Institute of Technology, 30332 Atlanta, GA, USA;(3) Department of Mechanical and Aerospace Engineering, University of California, 92717 Irvine, CA, USA |
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Abstract: | A mathematical model for transient contaminant transport resulting from the dissolution of a single component nonaqueous phase liquid (NAPL) pool in two-dimensional, saturated, homogeneous porous media was developed. An analytical solution was derived for a semi-infinite medium under local equilibrium conditions accounting for solvent decay. The solution was obtained by taking Laplace transforms to the equations with respect to time and Fourier transforms with respect to the longitudinal spatial coordinate. The analytical solution is given in terms of a single integral which is easily determined by numerical integration techniques. The model is applicable to both denser and lighter than water NAPL pools. The model successfully simulated responses of a 1,1,2-trichloroethane (TCA) pool at the bottom of a two-dimensional porous medium under controlled laboratory conditions.Notation a,a1 defined in (45a) and (45b), respectively - b defined in (45c) - b vector of true model parameters (n×1) - vector of estimated model parameters (n×1) - c liquid phase solute concentration (solute mass/liquid volume), M/L3 - cs aqueous saturation concentration (solubility), M/L3 - C dimensionless liquid phase solute concentration, equal toc/cs - molecular diffusion coefficient, L2/t - e effective molecular diffusion coefficient, equal to/*, L2/t - Dx longitudinal hydrodynamic dispersion coefficient, L2/t - Dz hydrodynamic dispersion coefficient in the vertical direction, L2/t - e random vector with zero mean (m×1) - erf[x] error function, equal to (2/1/2) - f vector of fitting errors or residuals (m×1) - Fourier operator - -1 Fourier inverse operator - g vector of model simulated data (m×1) - k mass transfer coefficient, L/t - average mass transfer coefficient, L/t - Kd partition or distribution coefficient (liquid volume/solids mass), L3/M - pool length, L - o distance between the pool and the origin of the specified Cartesian coordinate system, L - Laplace operator - -1 Laplace inverse operator - m number of observations - M Laplace/Fourier function defined in (38) - n number of model parameters - N Laplace/Fourier function defined in (39) - p defined in (46) - Pex Péclet number, equal toUx/Dx - Pez Péclet number, equal toUx/Dz - q defined in (47) - R retardation factor - s Laplace transform variable - S objective function - Sh local Sherwood number, equal tok/e - Sho overall Sherwood number, equal tol/e - t time,t - T dimensionless time, equal toUxt/ - u dummy integration variable - u vector of independent variables - Ux average interstitial velocity, L/t - x spatial coordinate in the longitudinal direction, L - X dimensionless longitudinal length, equal to (x–)/ - y vector of observed data (m×1) - z spatial coordinate in the vertical direction, L - Z dimensionless vertical length, equal toz/ - Fourier transform variable - defined in (37) - defined in (50) - porosity (liquid volume/aquifer volume), L3/L3 - defined in (52a) and (52b), respectively - decay coefficient, t–1 - dimensionless decay coefficient, equal to /Ux - bulk density of the solid matrix (solids mass/aquifer volume), M/L3 - dummy integration variable - * tortuosity |
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Keywords: | NAPL pools TCA dissolution contaminant transport |
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