Table 6. As removal from water of different origins via electrocoagulation.
| No | Sample | Coagulation agent | Conditions | Removal efficiency% | Reference | |
|---|---|---|---|---|---|---|
| AsIII | AsV | |||||
| 1 | Water | Fe | Electrocoagulation: pH = 6–8 | 99 | 99 | 235 |
| 2 | Water | Fe | Chemical coagulation; pH = 6 for AsIII; pH = 6–7 for AsV | 98 | 99 | 235 |
| 3 | Water | Fe3+ + Al3+ | Electrocoagulation; pH = 4–10, As removal = 1–1000 μg mL−1 | — | — | 236 |
| 4 | Natural ground water | Cu–Cu | Electrocoagulation: pH = 6–7 | 99.89 | — | 237 |
| 5 | Natural ground water | Zn–Zn | Electrocoagulation; pH = 6–7 | 99.56 | — | 237 |
| 6 | Wastewater | Stainless steel | Electrocoagulation; AsIII is oxidized to AsV; pH = 5.2 | 86–99.6 | 91 | |
| 7 | Groundwater | Al and Fe scrap anodes | Electrocoagulation; AsIII is oxidized to AsV; pH = 5–8 | — | 93.5 | 238 |
| 8 | Drinking water | Graphene oxide-manganese ferrite (GMF) | Adsorptive mixed matrix membrane; pH = 4 | — | 102a | 239 |
| 9 | Drinking water | adsorptive mixed matrix membrane | MMMs incorporated with different loading of hydrophilic GMF nanomaterial (0.5–2.0 wt%) | — | 75.5 a | 239 |
mg g−1