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1000
Half-life time
10 d
50 d
Adsorption: R = 2
20 d
inf.
100
10
1
0.1
0
100
200
Time (days)
Figure 5.11 Breakthrough curves at retardation factor R = 2 for different rates of
decomposition. The experimental data of Figure 5.2 apply.
where μ is the irst-order decomposition parameter (d -1 ). Suppose we have the amount
M = M 0 at t = 0. Integration of Eq. ( 5.19 ) results in an exponential decline of M 0
with time:
0 e µ
t
Mt
()=
M
(5.20)
This means that 50% of the mass is left at t = (ln 2)/ μ , which is called the half-life
T 50 (d).
Question 5.10: Derive the expression for half-life T 50 = (ln 2)/ μ with Eq. ( 5.20 ).
A mobile chemical with irst-order decay can be simulated with the convection-
dispersion equation (Eq. ( 5.8 )), putting S s = μ θ C l . Therefore, for steady low condi-
tions ( θ = constant) the transport equation may be written as:
=
C
t
2
C
z
C
z
l
D
l
v
l
µ
C
(5.21)
e
2
l
Proceeding with the leaching experiment of Figure 5.2 , Figure 5.11 shows the break-
through curves in case of convection, dispersion, adsorption ( R = 2) and different
half-lives T 50 . In case of T 50 = ininity, no decay occurs and the breakthrough curve
is similar to the one in Figure 5.10 with R = 2. At the soil surface we started with
solute concentrations equal to 1000 μg L -1 . Note how effective the solute concentra-
tion decrease is owing to the combined effect of adsorption and decomposition: from
1000 μg L -1 to less than 1 μg L -1 ! Figure 5.12 shows that in case of higher adsorption,
the decomposition is much more effective. By increasing the retardation factor from
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