Review Article
Recent Development in Ammonia Stripping Process for Industrial Wastewater Treatment
Table 2
Comparison of the different ammonia stripping processes.
| Ammonia stripping processes | Wastewater volume | Process efficiency (%) | Removal of other contaminant | Suspended solids tolerance | Fouling problem | Stripping time (h) | Airflow rate | Mass transfer coefficient | References |
| Packed tower | 1000 | 75 | Not available | Low | High | 3.5 | 25 (air to water ratio) | 0.42/h | [69] | Semibatch jet loop reactor | 9 L | 97 | Not available | High | Low | 5.8 | 5.6 (air to water ratio) | 0.63/h | [42] | Water-sparged aerocyclone | 10 L | 98 | Total P and COD | High | Low | 3.5 | 11.4 (air to water ratio) | 1.2/h | [41] | Rotating packed bed reactor | 0.025–0.01 L/min | 64 | Not available | High | Low | 0.0037 | 1800 L/min (continuous flow) | 12.3/h | [40] | Membrane contactor | 0.94 L | 99.83 | Not available | Low | High | 10 | Not available | 0.011 m/h | [57] | Membrane distillation | 1 L | 98.5 | Not available | Low | High | 4h | Not available | 0.079 | [70] | Ion exchange loopstripping | 2 L | 84.6 | Not available | low | High | 2.5 | Not available | Not available | [27] | Microwave radiation | 0.75 L | 94.2 | Not Available | High | Not available | 0.0167 | 10 (air to water ratio) | 3.354 | [71] |
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