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download pdf version of PhD book - Universiteit Utrecht

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4. Upscaling Adsorbing Solutes: Pore-Network Modeling<br />

. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .<br />

Figure 4.9: Upscaled distribution coefficient, K c , as a function <strong>of</strong><br />

D<br />

local-scale distribution coefficient, k d . The circles are the results <strong>of</strong><br />

network simulations. A linear equation fits the data: K c = Sk D d. S is<br />

equal to 5.28 × 10 3 m −1 .<br />

4.5 Discussion<br />

Figures (4.6) and (4.7) show that the core-scale attachment and detachment<br />

rate constants are functions <strong>of</strong> the local-scale adsorption coefficient and the<br />

average pore-water velocity. Combining these graphs results in a surface plot <strong>of</strong><br />

k c det (k d, v), as shown in Figure (4.10) for the network (R throat = 0.17×10 −3 m).<br />

We have fitted an equation to this surface<br />

k c det = D 0.95<br />

0 v 0.05<br />

(0.02 + 0.5 k d )R 0.95 (4.16)<br />

Using a volume averaging method, Rao<strong>of</strong> and Hassanizadeh [2010a] derived<br />

the following relationship for macro-scale kinetic adsorption coefficient for a<br />

general porous medium<br />

k c det = 2D 0<br />

k d R<br />

(4.17)<br />

If, in Equation (4.16), we neglect the dependency on velocity and approximate<br />

(0.02 + 0.5 k d ) ≈ 0.5 k d , we can confirm that the two equations are in full<br />

agreement.<br />

Clearly, knowing the upscaled detachment rate coefficient and the upscaled<br />

distribution coefficient, we can obtain a relationship for upscaled attachment<br />

coefficient<br />

82

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