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Fig. 6. Reusability of CRHC.
3.5 Adsorption kinetics
The non-linearized kinetics of the adsorption was studied by analyzing the
adsorption capacity of Diamine Green B (DG-B), Acid Black 24 (AB-24) and Congo
Red (CR) at different time intervals. The adsorption
kinetics of Pseudo-first-order,
Pseudo-two-order and Elovich models are given in Table 2[36]. All the data used for
the above analysis are the mean values from three replicate tests.
Table 2 Lists of adsorption kinetics models
Models
Nonlinear form
Plot
Pseudo-first-order
q
t
= q
e
(1−
e
−
k1
t
)
t vs q
t
Pseudo-second-order
q
t
= k
2
q
e
2
t/(1
+ k
2
q
e
t)
t vs q
t
Elovich
q
t
= ln(1
+ αβt)/β
t vs q
t
Pseudo-first-order kinetics mainly reveals the physical adsorption behavior that
plays a dominant role in the adsorption process. Pseudo-second-order kinetics is
generally more suitable for describing adsorption processes where chemisorption
plays a dominant role. The Elovich kinetic model is commonly
used to describe the
adsorption behavior of contaminants on uneven solid adsorbents. The non-linear
fitting results of the purification of Diamine Green B (DG-B), Acid Black 24 (AB-24)
and Congo red (CR) by CRHC at different temperatures are shown in Table 3.
The correlation R
2
values are typically used to evaluate the correlation
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coefficients, so as to determine the adsorption kinetics during the adsorption process.
In this experiment, at the different temperatures (303.15 K, 308.15 K, 313.15 K), the
R
2
value of the pseudo-second-order kinetics is higher than that of pseudo-first-order
kinetics models from nonlinear fitting results. The higher correlation R
2
value reveals
that it would be more appropriate to use pseudo-second-order kinetics to analyze the
purification behavior of Diamine Green B (DG-B), Acid Black 24 (AB-24) and
Congo red (CR) onto CRHC. In addition, the more closely of adsorption capacity
(q
e
(cal)) obtained by the pseudo-secondary kinetics and the experimentally measured
adsorption capacity (q
e
(exp)) support the above conclusion from another aspect.
Therefore, the pseudo-second-order kinetics was applied
in this experiment to
evaluate and analyze the purification of Diamine Green B (DG-B), Acid Black 24
(AB-24) and Congo red (CR) by CRHC. The purification of the three dyes by CRHC
may be a chemical process. However, the activation energies of Diamine Green B
(DG-B), Acid Black 24 (AB-24) and Congo red (CR) are 13.16 kJ mol
-1
, 4.29 kJ mol
-1
and 1.93
kJ mol
-1
, which are all lower than 40 kJ mol
-1
, so the purification process
belongs to physical adsorption [37]. Moreover, the non-linear fitting of Elovich model
has a high correlation R
2
value indicating that the surface of solid adsorbent may have
non-uniformities existed. Furthermore, as can been seen from Table 2, the adsorption
capacities of Diamine Green B (DG-B), Acid Black 24 (AB-24) and Congo red (CR)
dye onto CRHC were increased with the increasing of temperature. Raising the
temperature favors the adsorption process.
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