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Numerical Analysis of the Effect of the Lower Boundary Condition on Solute Transport in Lysimeters

Markus Flurya, Marylynn V. Yatesb and William A. Juryb

a Department of Crop and Soil Sciences, Washington State University, Pullman, WA 99164 USA
b Department of Soil and Environmental Sciences, University of California, Riverside, CA 92521 USA



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Fig. 1 Hydraulic properties of the soils used in the simulations. Parameters of the hydraulic functions are given in Table 1

 


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Fig. 2 Steady-state volumetric water content in the lysimeter. (a) Water contents for different flow rates illustrated with the loamy soil, (b) water contents for a constant flow rate of q = 0.1 cm d-1 in sandy and loamy soil

 


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Fig. 3 Breakthrough curves of a nonsorbing solute (K = 0) in the field (solid line) and the lysimeter (dashed line) for different flow rates. Note the different scales of the axes

 


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Fig. 4 Comparison of the transport of a solute with different distribution coefficients K in the sandy and loamy soil (linear equilibrium sorption). The water flux was in all cases q = 0.5 cm d-1. Note the different scales of the axes

 


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Fig. 5 Effect of linear equilibrium sorption on the difference in solute transport between lysimeter and field soil. {eta} is the ratio of the mean travel times in lysimeter and field soil, {zeta} is the ratio of the variances of the travel time, and {kappa} is the ratio of the maximum concentrations of the breakthrough curves. The water flux was in all cases q = 0.5 cm d-1

 


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Fig. 6 Effect of (a) nonlinear equilibrium sorption (S = KCn) and (b) nonequilibrium sorption [C/t = ß(KC - S)] on the ratio {kappa} of maximum concentrations in the sandy soil. The parameters n and ß are the nonlinearity constant of the sorption isotherm and the nonequilibrium rate coefficient, respectively. The water flux for these simulations was q = 0.5 cm d-1

 





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