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

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where vmax [s -1 ] is a maximum growth rate,<br />

Ci [kg m -3 ] is the concentration <strong>of</strong> the i th<br />

substrate, MCi [kg m -3 ] is the corresponding<br />

half velocity concentration [kg m -3 ], Cj<br />

[kg m -3 ] is the concentration <strong>of</strong> the j th substance<br />

inhibiting microbial growth, ICj is the<br />

corresponding inhibition concentration<br />

[kg m -3 ] <strong>and</strong> �(X) is a microbial decay term,<br />

which is <strong>of</strong>ten modeled as being <strong>of</strong> first<br />

order. Consumption <strong>of</strong> substrates or production<br />

<strong>of</strong> k metabolites Ck [kg m -3 ] is both<br />

coupled to microbial growth via (Schäfer et<br />

al., 1998)<br />

�Ck �1<br />

��X<br />

�<br />

�<br />

�t<br />

Y �<br />

� �t<br />

�<br />

�<br />

6<br />

(21)<br />

k growth<br />

where Yk [-] is the yield coefficient for<br />

substrate or metabolite Ck, <strong>and</strong> [·]growth<br />

refers to the growth term only in eq. (20).<br />

From the generalized Monod-type equation<br />

different more simple kinetic formulations<br />

can be derived. For a temporally constant<br />

microbial population, i.e. growth <strong>and</strong> decay<br />

terms are constant <strong>and</strong> <strong>of</strong> equal magnitude,<br />

no inhibition <strong>and</strong> dependence on only a<br />

single substrate, eq. (20) <strong>and</strong> (21) can be<br />

combined to yield the Michaelis-Menten<br />

(MM) kinetics model (Simkins <strong>and</strong><br />

Alex<strong>and</strong>er, 1984)<br />

dC<br />

dt<br />

C<br />

� �kmax<br />

(22)<br />

C � M C<br />

where k max is the maximum degradation rate<br />

[kg m -3 s -1 ] <strong>and</strong> M C is the MM half-saturation<br />

concentration [kg m -3 ]. This approximation<br />

may be applicable e.g. when aquifer<br />

sediments have been exposed to contaminants<br />

for several years (Bekins et al., 1998)<br />

<strong>and</strong> is used in application 2 (section 3.2).<br />

Often, contaminant degradation is also<br />

described by simple first order kinetics, e.g.<br />

to simulate abiotic degradation reactions<br />

like hydrolysis <strong>and</strong> dehydrohalogenation <strong>of</strong><br />

halogenated compounds (Wiedemeier et al.,<br />

1999). First order kinetics can be derived<br />

from eq. (22) for C > MC eq. (22)<br />

approaches zero order kinetics. The first<br />

order model is used in application 1 <strong>and</strong> 3<br />

(sections 3.1 <strong>and</strong> 3.3). Extensive reviews on<br />

kinetic models <strong>of</strong> biodegradation can be<br />

found e.g. in Baveye <strong>and</strong> Valocchi (1989),<br />

Rittmann <strong>and</strong> VanBriesen (1996) or Islam<br />

et al. (2001).<br />

2.4. Numerics <strong>and</strong> s<strong>of</strong>tware<br />

methods<br />

Numerical solution <strong>of</strong> the governing<br />

equations<br />

The governing equations for <strong>flow</strong> <strong>and</strong> reactive<br />

transport presented in sections 2.1 - 2.3<br />

belong to the group <strong>of</strong> partial differential<br />

equations (PDE), containing derivatives <strong>of</strong><br />

first order in time <strong>and</strong> <strong>of</strong> first as well as<br />

second order in space. The classification <strong>of</strong><br />

PDE can be based on mathematical aspects<br />

(highest order derivatives in the dependent<br />

variables) or on a physical point <strong>of</strong> view<br />

(problem type <strong>of</strong> physical process) (Kolditz,<br />

2002). Parabolic PDE are used for timedependent<br />

problems with dissipation process,<br />

such as diffusion (eq. (11)) or transient<br />

groundwater <strong>flow</strong> (eq. (3)), which<br />

convert to elliptic PDE for steady state<br />

conditions (eq. (4)). A third class <strong>of</strong> PDE<br />

are hyperbolic equations like the linear advection<br />

equation (eq. (10)), which are used<br />

to describe time-dependent problems without<br />

dissipation process. The transport equations<br />

(15) <strong>and</strong> (16) are <strong>of</strong> mixed type with a<br />

parabolic dispersion-diffusion term <strong>and</strong> a<br />

hyperbolic advection term. Their behaviour<br />

for a particular problem depends on the<br />

relative magnitudes <strong>of</strong> these flux components.<br />

In general the transport equations are<br />

<strong>of</strong> parabolic character which changes to<br />

hyperbolic for large ratios <strong>of</strong> v/�L as in this<br />

case the advective flux term is dominant<br />

(Kolditz, 2002).<br />

In general, PDE describing physical<br />

problems are well-posed when appropriate<br />

initial <strong>and</strong> boundary conditions are specified<br />

for the domain where a solution is<br />

required. While analytical solutions can be

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