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Applied numerical modeling of saturated / unsaturated flow and ...

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v<br />

�<br />

�C�Cx) �<br />

� C0<br />

�<br />

ln��<br />

C�x���<br />

M � � 1<br />

�<br />

�<br />

( k C � C(<br />

x)<br />

k<br />

x C<br />

(25).<br />

a 0<br />

max 0<br />

max<br />

With the same type <strong>of</strong> center line<br />

investigation data used for the estimation <strong>of</strong><br />

the first order degradation rate constant (i.e.<br />

local concentrations, heads, hydraulic conductivities),<br />

eq. (25) can be utilized to<br />

estimate the MM parameters kmax <strong>and</strong> MC<br />

by linear regression.<br />

The Monte Carlo scenario definition <strong>and</strong><br />

site investigation procedure for this study<br />

are similar to those explained in section 3.1.<br />

Numerical simulations <strong>of</strong> plume development<br />

in homogeneous <strong>and</strong> heterogeneous<br />

aquifers were performed with the GeoSys /<br />

Rock<strong>flow</strong> code. Here, however, the contaminant<br />

plumes investigated were generated<br />

using MM instead <strong>of</strong> first order degradation<br />

kinetics. The parameters k max <strong>and</strong> M C<br />

estimated with eq. (25) for the different<br />

plume realizations were normalized to the<br />

true values used in the <strong>numerical</strong><br />

simulations <strong>and</strong> are shown in a 3D-scatterplot<br />

versus aquifer heterogeneity (Fig. 12).<br />

Fig. 12: Normalized Michaelis-Menten parameters<br />

(given as overestimation factors)<br />

versus aquifer heterogeneity.<br />

In general an overestimation <strong>of</strong> both k max<br />

<strong>and</strong> M C is observed, which increases with<br />

heterogeneity. An overestimation <strong>of</strong> k max increases<br />

the velocity <strong>of</strong> contaminant degradation<br />

as long as concentrations are much<br />

higher than MC. The simultaneous overestimation<br />

<strong>of</strong> MC counterbalances this effect<br />

because the concentration threshold is<br />

raised at which the kinetic begins to show a<br />

dependence on concentration <strong>and</strong> transits<br />

from zero to first order <strong>and</strong> hence decreases<br />

the rate <strong>of</strong> degradation.<br />

To obtain an indicator for the significance<br />

<strong>of</strong> the estimated degradation potential, the<br />

MM parameters determined were used in an<br />

analytical transport model to estimate the<br />

contaminant plume lengths. These then<br />

were compared to the respective true plume<br />

lengths from the <strong>numerical</strong> simulations<br />

(Fig. 13 (a)). As a consequence <strong>of</strong> overestimating<br />

the degradation parameters, calculated<br />

plume lengths for high heterogeneities<br />

are estimated to about 75 % <strong>of</strong> the true<br />

length on average <strong>and</strong> thus are not conservative.<br />

For low heterogeneities, however,<br />

the suggested regression approach on average<br />

yields good estimates <strong>of</strong> the plume<br />

length <strong>and</strong> the degradation potential.<br />

In addition to the effect <strong>of</strong> aquifer heterogeneity<br />

on estimated MM parameters <strong>and</strong> the<br />

resultant plume length estimates, also the<br />

effect <strong>of</strong> a wrong process identification<br />

(compare Fig. 5) is studied in Beyer et al.<br />

(2006 [EP 3]). Although it is well known<br />

that contaminant degradation in natural<br />

aquifers is governed by complex processes<br />

<strong>and</strong> kinetic laws, simple first order models<br />

are routinely used at many field sites. This<br />

study therefore highlights some <strong>of</strong> the<br />

problems that result from an insufficient<br />

wrong process identification. For this end<br />

investigation <strong>of</strong> the plumes following MM<br />

degradation kinetics is repeated, assuming<br />

the appropriateness <strong>of</strong> a first order rate law<br />

to approximate the contaminant degradation<br />

behaviour. Hence the methods <strong>of</strong> Tab. 1<br />

were used to derive first order rate constants<br />

for the multiple plume realizations.<br />

As for the estimated MM parameters the<br />

estimated first order rate constants were<br />

evaluated by analytical transport models to<br />

yield estimates <strong>of</strong> the contaminant plume<br />

length. Results for method 1 (Tab. 1) are<br />

presented in Fig. 13 (b).<br />

17

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