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Table 3 Kinetics parameters on the adsorption of Diamine Green B (DG-B), Acid
Black 24 (AB-24) and Congo red (CR) onto CRHC.
Dyes
Pseudo-first-order
Pseudo-second-order
Elovich
q
e.exp
k
1
q
e.cal
R
2
K
2
q
e.cal
R
2
α
β
R
2
DG-B
303.15 K
0.054
162.30
0.6471
0.0014
172.00
0.9636
21.01 0.074 0.9076
185.22
313.15 K
0.049
149.13
0.8463
0.0013
158.25
0.9939
10.51 0.076 0.8522
157.32
323.15 K
0.019
141.12
0.9192
0.00037
157.87
0.9852
36.83 0.038 0.9396
151.03
AB-24
303.15 K
0.079
146.69
0.4897
0.0027
152.71
0.9114
72.80
0.12
0.9311
162.76
313.15 K
0.052
139.44
0.8038
0.0015
147.67
0.9880
16.02 0.085 0.8792
153.20
323.15 K
0.054
131.98
0.6556
0.0017
139.87
0.9566
15.75 0.090 0.9155
145.54
CR
303.15 K
0.12
230.97
0.4913
0.0036
236.07
0.9283
50.79
0.15
0.9136
248.10
313.15 K
0.11
234.86
0.4898
0.0034
240.24
0.9263
16.62
0.14
0.9071
249.34
323.15 K
0.10
238.06
0.5170
0.0033
243.52
0.9385
19.39
0.13
0.8898
252.11
Adsorption is a complex process that usually involves three stages. The first
stage mainly reflects
the external diffusion, the second and the third stages mainly
reflect the internal diffusion. Therefore, the adsorption behavior cannot be completely
analyzed with only one or two kind of kinetic models. The
intra-particle diffusion
model is mainly applicable to describe the kinetics of the diffusion process. It is
necessary to analyze the kinetic data by using an intra-particle diffusion model. The
expression of the intra-particle diffusion model is shown as below.
c
t
k
q
id
t
2
/
1
Where c is the intercept (mg g
-1
) and k
id
is the intraparticle diffusion
rate constant
(mg g
–1
min
–1/2
). The values can be obtained by plotting q
t
vs t.
The intra-particle diffusion kinetics of Diamine Green B (DG-B), Acid Black 24
(AB-24) and Congo Red (CR) onto CRHC at different temperatures are shown in Fig.
6. The first fitting line does not pass through the origin of the coordinates, indicating
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that the adsorption process includes not only intra-particle diffusion, but in fact its key
rate limiting step should have other reasons, and the entire purification process should
be subject to a variety of adsorption stages. The fitted curve is divided into three
straight lines. The first is the instantaneous adsorption
process in which the dye
adsorbent is adsorbed on the surface of the adsorbent. This stage is the step where the
adsorption process occurs fastest and the adsorption rate is the highest; followed by
the
gradual adsorption process, the adsorption rate decreases at this stage; the
adsorption reaches a state of equilibrium
in the last process, in which the dye
concentration in the solution is reduced and the adsorption rate is lowest.
Fig. 7. The intra-particle diffusion kinetics of DG-B, AB-24 and CR onto CRHC.
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