Table 5.
The pollutants degradation based on the activation of O2 by electro-Fenton process.
| Cathodes | Anodes | Contaminants | Reaction conditions | O2 supply | ROS | Removal efficiency | TOC removal | Reference |
|---|---|---|---|---|---|---|---|---|
| FeCuC | BDD | BPA | [BPA]0 = 2.0 mg L−1, Na2SO4 = 50.0 μM, I = 30.0 mA, pH = 3.0 | O2 aeration | H2O2, •OH | - | 97.0% | [87] |
| GF-C | Pt | RhB | [RhB]0 = 60.0 mg L−1, Na2SO4 = 50.0 μM, j = 6.0 mA cm−2, pH = 3.0 | O2 aeration | H2O2, •OH | 99.0% | 80.0% | [88] |
| Ti sheet | BiN3/MXene membrane | SMX | [SMX]0 = 10.0 mg L−1, Na2SO4 = 20.0 mmol L−1, I = 10.0 mA, pH = 3.0–9.5 | O2 aeration | H2O2, •OH | >95.0% | 60.0% | [91] |
| GA | Pt sheet | CIP | [CIP]0 = 50.0 mg L−1, Na2SO4 = 50.0 μM, j = 30.0 mA cm−2, pH = 3.0, | O2 aeration | H2O2, •OH | Almost 100.0% | 91.0% | [92] |
| CrN4/MXene | Ti sheet | SMX | [SMX]0 = 10.0 mg L−1, pH = 6.8 | O2 aeration | 1O2 | 95.0% | 61.2% | [94] |
| FE-ECM | Titanium plate | ATZ | [ATZ]0 = 20.0 μM, Na2SO4 = 100.0 mM, j = 2.0 mA cm−2, pH = 7.0 | O2 aeration | H2O2, •OH, 1O2 | 93.1% | 73.04% | [95] |
| Carbon aerogels | Pt foil | BPA | [BPA]0 = 10.0 mg L−1, Na2SO4 = 50.0 μM, pH = 3.0 and 9.0 | O2 aeration | H2O2, 1O2, •O2−, •OH | 98.0% | 72.3% | [96] |
| MOF-SnO2@CF | Fe@CF membranes | PRO | [PRO]0 = 5.0 mg L−1, Na2SO4 = 10.0 μM, pH = 3.0 | O2 aeration | H2O2, 1O2, •O2−, •OH | 97.5% | 83.0% | [97] |
Abbreviations: FeCuC, iron-copper-embedded carbon aerogel; BDD, boron-doped diamond; GF-C, graphite felt-C; GA, graphene aerogel; FE-ECM, Fe(II)-modulated FeCo LDHs on a conductive OCNT-precoated membrane; MOF-SnO2@CF, metal organic frameworks-SnO2@ carbon fibers; Fe@CF, Fe@carbon fibers; BPA, bisphenol A; RhB, rhodamine B; SMX, sulfamethoxazole; CIP, ciprofloxacin; ATZ, atrazine; PRO, propranolol.