Environmental Engineering Reference
In-Depth Information
The Tóth model was found from a modification of the Langmuir model
and suggests that the biosorption occurs via multilayer formation. This
model is given by Equation 8.8 [125]:
qC
(8.8)
mT
e
q
e
mT
1
k
mT
C
e
T
where q
mT
is the maximum biosorption capacity from the Tóth model
(mg g
-1
), k
T
is the Tóth constant (mg L
-1
)
mT
and m
T
is Tóth exponent. This
model was adequate to describe the biosorption of Methylene Blue and
Eriochrome Black onto
Scolymus hispanicus
L. [130].
The fit of these mathematical models on the biosorption isotherm curves
and the consequent determination of the adjustable isotherm parameters
are fundamental to know a biosorption process, since these can furnish
the following information: i) a equilibrium relation which can be used in
kinetic studies; ii) an idea about the biosorbent-dye interactions; iii) the
affinity between biosorbent and dye; iv) the maximum biosorption capacity
of the biosorbent in a specific condition; v) the amount of biosorbent which
should be used for the removal of a certain quantity of dye from an effluent;
vi) the influence of the experimental conditions on the equilibrium.
8.4.2 Thermodynamic Parameters
In the biosorption field, the thermodynamic is generally studied thought
the estimation of Gibbs free energy change (ΔG
0
, kJ mol
-1
), enthalpy change
(ΔH
0
, kJ mol
-1
) and entropy change (ΔS
0
, kJ mol
-1
K
-1
) [6,16,19,43,44]. From
a thermodynamic viewpoint, the biosorption is considered as a uniphasic
reaction [12,13], and so the Gibbs free energy change can be estimated by
Equation 8.9 [131]:
0
(8.9)
G
RTln(K)
where R is the universal gas constant (8.314 J mol
−1
K
−1
), T the tem-
perature (K) and K thermodynamic equilibrium constant (dimension-
less) [132]. The K values are obtained in different ways in the literature
[23,35,43,90,92,102,113,132-135]. Detailed and consistent forms to obtain K
can be found in the works of Liu [132], Milonjic [133] and Zhou
et al.
[134].
The relationship of ΔG
0
to enthalpy change (ΔH
0
) and entropy change
(ΔS
0
) of biosorption is expressed in the form of Equation 8.10 [131]:
0
0
0
(8.10)
GHTS
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