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Quantifying the Influence of Intra-Aggregate Concentration Gradients on Solute Transport

C.M. Cotea, K.L. Bristowa and P.J. Rossa

a CSIRO Land and Water, Davies Lab., University Rd., Townsville, Australia



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Fig. 1 Schematic diagram showing the sequence of wet and dry periods imposed on a single spherical aggregate

 


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Fig. 2 Single Spherical Aggregate (SSA) model output showing the fraction leached as a function of t* for continuous leaching

 


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Fig. 3 Single Spherical Aggregate (SSA) model output showing the fraction leached as a function of t*L for various values of wet period duration ({tau}*). Note that {tau}* -> {infty} gives continuous leaching

 


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Fig. 4 Single Spherical Aggregate (SSA) model output showing the fraction leached as a function of t*L for various wet period frequencies. Note that {tau}*/T* -> {infty} gives continuous leaching

 


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Fig. 5 Comparison between the Single Spherical Aggregate (SSA) model output and experimental data obtained with a column of packed spherical aggregates

 


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Fig. 6 Experimentally determined breakthrough curve for the Hydrosol as compared with ideal miscible displacement. These experimental data show very early breakthrough and pronounced tailing, both indicators of preferential flow

 


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Fig. 7 Comparison between the Single Spherical Aggregate (SSA) model output and experimental data for flow interrupted leaching experiments carried out on the Hydrosol core (Run 1)

 


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Fig. 8 Comparison between the Single Spherical Aggregate (SSA) model output and experimental data for flow interrupted leaching experiments carried out on the Hydrosol core (Run 2)

 


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Fig. 9 Comparison between experimental data for the flow interrupted leaching experiment (Run 1) and continuous leaching experiment (Run 3)

 





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