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MOBILE PHASE
Na + , K + , Ca 2+ , Mg 2+ ,
Mn 2+ , Fe 2+ , Cl - , O 2 ,
NO 3 - , CH 2 O
MATRIX PHASE
MnO 2 , Fe(OH) 3 ,
SOLID PHASE
Na + , K + , Ca 2+ ,
Mg 2+ , Mn 2+ , Fe 2+
BIO PHASE
X1, X2, X3, O 2 , NO 3 - ,
Mn 2+ , Fe 2+ , CH 2 O,
MnO 2 , Fe(OH) 3
Fig. 1.
Conceptual model.
The one-dimensional mass transport equation is represented by Eq. (1)
when the y -coordinate is taken along the depth of the experimental
apparatus.
θ w D L [ C i ]
∂y
+ S i ,
[ C i ]
∂t
[ C i ]
∂y
1
θ w
∂y
+ v
=
(1)
where θ w is the water content, v the pore velocity, and D L is the lon-
gitudinal dispersion coecient that is calculated by the product of the
longitudinal dispersion length and the pore velocity.
Following equations represent the Fe 2+ concentration change in each
phase.
Mobile phase
d[Fe 2+ ] mob
d t
[Fe 2+ ] mob
∂t
[Fe 2+ ] mob
∂y
Fe 2+ :
+ v
=
θ w D L [Fe 2+ ] mob
∂y
+ T b (1
1
θ w
∂y
n )
=
a
θ bio D L
θ bio + θ w
([Fe 2+ ] bio
[Fe 2+ ] mob )+ S 3 Fe ,
·
(2)
Solid phase
∂t ( θ w [Fe 2+ ] im )=
Fe 2+ :
θ w S 3 Fe
(3)
(1
n ) ρ s
θ w
[Fe 2+ ] im =
m Fe .
(4)
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