| Adsorption model |
T (°C) |
KL |
q0 |
Adj-R2 |
RMSE |
| Langmuir |
25 |
0.526 |
2.690 |
0.725 |
0.286 |
| |
30 |
0.717 |
2.184 |
0.751 |
0.198 |
| |
35 |
0.924 |
1.796 |
0.830 |
0.114 |
| |
50 |
1.497 |
1.548 |
0.931 |
0.046 |
|
| Adsorption model |
T (°C) |
KF |
nF |
Adj-R2 |
RMSE |
| Freundlich |
25 |
1.346 |
5.387 |
0.871 |
0.196 |
| |
30 |
1.234 |
6.328 |
0.849 |
0.154 |
| |
35 |
1.121 |
7.615 |
0.975 |
0.044 |
| |
50 |
1.128 |
11.063 |
0.888 |
0.058 |
|
| Adsorption model |
T (°C) |
KS |
aS |
βS |
Adj-R2 |
RMSE |
| Sips |
25 |
1.752 |
0.406 |
0.376 |
0.827 |
0.227 |
| |
30 |
1.829 |
0.634 |
0.441 |
0.820 |
0.169 |
| |
35 |
1.804 |
0.721 |
0.355 |
0.992 |
0.024 |
| |
50 |
2.550 |
1.522 |
0.589 |
0.975 |
0.028 |
|
| Adsorption model |
T (°C) |
KRP |
αRP |
βRP |
Adj-R2 |
RMSE |
| Redlich- |
25 |
9.713 |
6.637 |
0.836 |
0.813 |
0.236 |
| Peterson |
30 |
5.001 |
3.480 |
0.882 |
0.803 |
0.176 |
| |
35 |
5.689 |
4.525 |
0.898 |
0.992 |
0.025 |
| |
50 |
3.749 |
2.783 |
0.958 |
0.981 |
0.024 |
|
| Adsorption model |
T (°C) |
bK |
q0 |
nK |
Adj-R2 |
RMSE |
| Khan |
25 |
7.343 |
1.013 |
0.829 |
0.811 |
0.237 |
| |
30 |
3.411 |
1.201 |
0.876 |
0.801 |
0.177 |
| |
35 |
4.284 |
1.064 |
0.895 |
0.992 |
0.025 |
| |
50 |
2.717 |
1.277 |
0.956 |
0.982 |
0.023 |
|
| Adsorption model |
T (°C) |
AT |
bT |
Adj-R2 |
RMSE |
| Temkin |
25 |
23.567 |
6386.6 |
0.878 |
0.191 |
| |
30 |
56.442 |
8814.2 |
0.872 |
0.142 |
| |
35 |
186.64 |
12536.0 |
0.992 |
0.024 |
| |
50 |
5066.8 |
20808.0 |
0.920 |
0.049 |
Biological Adsorption of Co(II) by Schizosaccharomyces pombe: kinetic and
thermodynamic studies for process design |
| Table 3: Parameters and statistics of the fitted isotherm models. |
