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

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W01420 BAUER ET AL.: ASSESSING FIRST-ORDER RATES W01420<br />

as can be seen by exp<strong>and</strong>ing the squared brackets in<br />

equation (3) <strong>and</strong> using C(x) C0:<br />

l3 ¼ va aL<br />

va<br />

lnð Cx ðÞ=C0<br />

Dx<br />

lnð Cx ðÞ=C0<br />

Dx<br />

2<br />

¼ l1<br />

!<br />

lnðCx ðÞ=C0Þ<br />

Dx<br />

[26] If a L = 0, method 3 reduces to the advection only<br />

case, i.e., method 1. Method 3 still does not account for<br />

transverse dispersion, which is the process causing smaller<br />

concentrations on the plume center line. Method 4 is based<br />

on a two-dimensional solution to the transport equation<br />

including advection, longitudinal <strong>and</strong> transverse dispersion<br />

<strong>and</strong> first-order degradation. Results from method 4<br />

(Figure 4d) show an underestimation <strong>of</strong> the true rate<br />

constant for homogeneous or slightly heterogeneous conditions<br />

(sY 2<br />

1.71), while for high degrees <strong>of</strong> heterogeneity<br />

(sY 2<br />

2.7), the ensemble averages <strong>of</strong> the estimated rate<br />

constants approach the respective values obtained with<br />

method 3. The underestimation for low heterogeneities is<br />

a consequence <strong>of</strong> the correction for transverse dispersion,<br />

represented by the error function b in equation (4). The<br />

effect <strong>of</strong> lower concentrations along the plume center line<br />

due to transverse dispersion is strong for small source<br />

widths, large transversal dispersivities <strong>and</strong> large well spacings.<br />

b is always less than 1 <strong>and</strong> asymptotically approaches<br />

unity for arguments <strong>of</strong> the error function larger than 2, i.e.,<br />

l4 converges toward l3 for small aT or large WS. For<br />

arguments

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