Research Article
Removal of Ammonium from Aqueous Solutions Using Zeolite Synthesized from Electrolytic Manganese Residue
Table 1
Kinetic parameters for ammonia removal using various kinetic models.
| Ammonium concentration (mg·L−1) | qe (exp) (mg·g−1) | Pseudo-first-order model | Pseudo-second-order model | Elovich equation model | Intra-particle diffusion model | qe (mg·g−1) | k1 (min−1) | α (mg·g−1·min−1) | qe (mg·g−1) | k2 (g·mg−1·min−1) | R2 | α (mg·g−1·min−1) | β (g·mg−1) | R2 | kid (mg·min−1/2·g−1) | R2 |
| 50 | 12.09 | 4.43 | 0.02594 | 0.1728 | 13.41 | 0.004335 | 0.9925 | 0.1728 | 0.3747 | 0.8327 | 0.5983 | 0.6740 | 100 | 16.70 | 7.32 | 0.03551 | 0.08929 | 17.79 | 0.005451 | 0.9982 | 0.08929 | 0.3595 | 0.8420 | 0.6239 | 0.6826 | 150 | 21.02 | 12.85 | 0.03274 | 0.04958 | 23.43 | 0.002274 | 0.9962 | 0.04958 | 0.2269 | 0.8496 | 1.0277 | 0.8331 | 200 | 24.28 | 16.75 | 0.03211 | 0.05952 | 27.17 | 0.001841 | 0.9949 | 0.05952 | 0.2005 | 0.9438 | 1.1810 | 0.8719 |
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qe (exp) and qe are the experimental and calculated values of qe, respectively.
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