Review Article
Zeolite Application in Wastewater Treatment
Table 5
Zeolites used in ammonium removal, along with experimental conditions and adsorption and kinetic models.
| | Zeolite | (°C) | Contact time (h) | Concentration (mg·L-1) | S/L ratio (g·L-1) | pH | NH4+ sorption capacity (mg·L-1) | Isotherm model | Kinetic model | References |
| | Clinoptilolite | 25 | 12 | 1-20 | 0-0.6 | — | 4.3 | Langmuir | Pseudo-first-order | [89] | | NaNO3-modified clinoptilolite | 25 | 12 | 1-20 | 0-0.6 | — | 8.1 | Freundlich | Pseudo-first-order | | Zeolite P+analcime | 25 | 1 | 5-500 | 5 | 6 | 17.5 | Koble-Corrigan | Pseudo-second-order | [90] | | Zeolite X | 25 | 8 | 100-400 | 2 | 7 | 89.1 | Freundlich | Pseudo-second-order | [86] | | Zeolite A | 59.3 | | Chabazite | 25 | 5 | 130-2080 | 75 | 7 | 39.3 | Langmuir | Pseudo-second-order | [91] | | Zeolite NaY | 25 | 2 | 40-615 | 6.3 | — | 26.5 | Langmuir | Pseudo-second-order | [4] | | Modified Na-clinoptilolite | 25 | 24 | 0-83 | — | 7.2 | 14.5 | Langmuir | — | [167] | | Clinoptilolite+mordenite | 25 | 8 | 5-120 | 10 | 6 | 6.3 | Freundlich | Pseudo-second-order | [88] | | Zeolite NaA | 25 | 0-2 | — | — | 7.9 | 10.5 | Freundlich | Pseudo-second-order | [87] | | Magnetic zeolite NaA | 10.4 |
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