Applied numerical modeling of saturated / unsaturated flow and ...
Applied numerical modeling of saturated / unsaturated flow and ...
Applied numerical modeling of saturated / unsaturated flow and ...
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samples taken at all eight wells do not allow for an estimation <strong>of</strong> lY<strong>and</strong> σY 2 , which would be required<br />
to derive αL <strong>and</strong> αT. A detailed study on the effects <strong>of</strong> dispersivity parameterization on the<br />
performance <strong>of</strong> methods 2 <strong>and</strong> 3 is presented in Bauer et al. (2006).<br />
The information obtained by the site investigation allows the application <strong>of</strong> the five methods for<br />
estimation <strong>of</strong> the degradation kinetic parameters <strong>and</strong> the subsequent calculation <strong>of</strong> contaminant<br />
plume lengths as presented in Sections 4.1 <strong>and</strong> 4.2. The investigation setup is designed to resemble<br />
ideal conditions for this purpose. All measurements are assumed to be exact, i.e. without measurement<br />
error, <strong>and</strong> are obtained by reading the model output at the respective well positions. The<br />
only uncertainty <strong>and</strong> variability is introduced by the heterogeneity <strong>of</strong> the hydraulic conductivity.<br />
6. Results <strong>and</strong> discussion<br />
C. Beyer et al. / Journal <strong>of</strong> Contaminant Hydrology 87 (2006) 73–95<br />
As outlined in Section 3, three different cases A, B <strong>and</strong> C are investigated here (see Table 1). The<br />
next three Sections 6.1, 6.2 <strong>and</strong> 6.3 present detailed results <strong>and</strong> discussions for each case studied. A<br />
detailed comparison <strong>and</strong> discussion <strong>of</strong> the performance <strong>of</strong> the different approaches is given in<br />
Section 6.4.<br />
6.1. Case A: estimation <strong>of</strong> first order degradation rate constants <strong>and</strong> plume lengths for plumes<br />
following a first order degradation kinetics<br />
6.1.1. Estimation <strong>of</strong> rate constants<br />
In case A methods 1–4 are tested <strong>and</strong> compared based on their ability to estimate the first order<br />
degradation rate constant λ <strong>and</strong> the contaminant plume length in heterogeneous aquifers.<br />
Therefore, plumes following first order degradation kinetics are investigated here. The four<br />
estimated rate constants λi are divided by the true rate constant to yield corresponding normalized<br />
Λi, which can be interpreted as an over- or underestimation factor. Fig. 3 presents ensemble means<br />
with corresponding st<strong>and</strong>ard deviations as error bars, medians, coefficients <strong>of</strong> variation <strong>and</strong> the<br />
single realization results for methods 1–4 against the aquifer heterogeneity σY 2 .<br />
Results for method 1 (Fig. 3 (a)) show that Λ1=1 in the homogeneous case (σY 2 =0), thus in this case<br />
the true rate is obtained. However, already for the lowest degree <strong>of</strong> heterogeneity (σY 2 =0.38), about<br />
77% <strong>of</strong> the rate constants estimated fall above the reference line which indicates the true rate constant,<br />
overestimating λ up to factors <strong>of</strong> 4.79 in the worst case. In the remaining realizations λ is<br />
underestimated. The spread <strong>of</strong> the ensemble <strong>of</strong> 100 realizations covers about one order <strong>of</strong> magnitude.<br />
When σY 2 is further increased, spread <strong>and</strong> st<strong>and</strong>ard deviation also increase. For σY 2 =4.5 the Λ1 cover<br />
almost two orders <strong>of</strong> magnitude with single realizations showing overestimation factors N10. Mean Λ1<br />
is 3.3 with st<strong>and</strong>ard deviation <strong>and</strong> coefficient <strong>of</strong> variation <strong>of</strong> 3.65 <strong>and</strong> 1.11, respectively. Increasing the<br />
heterogeneity <strong>of</strong> the aquifer thus results in a higher uncertainty <strong>of</strong> λ <strong>and</strong> increases the probability <strong>of</strong> a<br />
significant overestimation. For method 2 normalized rate constants Λ2 are shown in Fig. 3 (b). As seen<br />
for method 1 a systematic overestimation <strong>of</strong> λ can be observed, increasing with σ Y 2 . However, the Λ2<br />
are significantly larger than the corresponding Λ 1. In the homogeneous case method 2 yields Λ 2=1.7,<br />
increasing to 9.38 for σY 2 =4.50. In extreme cases, overestimation <strong>of</strong> λ is larger than a factor <strong>of</strong> 50. Also<br />
spread <strong>and</strong> st<strong>and</strong>ard deviations are larger than for Λ1. Estimated rate constants Λ3 obtained by method<br />
3(Fig. 3 (c)) are only slightly lower than those <strong>of</strong> method 2, ranging from 1.17 in the homogeneous<br />
case to 7.39 for σY 2 =4.5. Method 4 (Fig. 3(d)) yields the true rate for homogeneous conditions, i.e.<br />
Λ4=1. As for the other methods, spread <strong>and</strong> uncertainty increase with σY 2 . Compared to methods 1–3<br />
the spread is smaller <strong>and</strong> balanced around the true rate constant. For σY 2 ≤2.7 the ensemble averages<br />
<strong>and</strong> medians match the true rate constant well. For σ Y 2 =4.50 the average Λ4 reaches 1.73.<br />
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