Table 10.
Parameter | Results (This Study) | Results (Other Studies) |
---|---|---|
COD | ↓86.1% (oxidation using K2FeO4) |
↓78.7 ± 1.3% (carbon felt); ↓93.8 ± 1.7% (LTA zolite-modified anode); ↓96.3 ± 2.1% (bentonite-modified anode); bioelectrocatalytic oxidation [77] |
↓80–87% (UF membranes); ↓65% (MF membranes); ↓96% (RO; reverse osmosis) [78] | ||
↓96.33% (primary treatment process); ↓99.81% (NF; nanofiltration); ↓99.84% (RO; reverse osmosis) [79] | ||
TOC | ↓80.5% (oxidation using K2FeO4) |
↓52%; simulated tannery wastewater (MF membranes) [78]; ↓87%; (hydrodynamic cavitation with addition of H2O2) [80]; ↓50.0%; (coagulation-flocculation/adsorption; CF-ADS) [81]; ↓46.5%; (coagulation-flocculation/ozonation; CF-OZ) [81] |
Color | ↓99.3% (oxidation using K2FeO4) |
↓61.13%; (coagulation-flocculation/adsorption; CF-ADS) [81] ↓85.34%; (coagulation-flocculation/ozonation; CF-OZ) [81] ↓87%; (electrochemical oxidation; EO) [82] |