1. Context
Physico-chemical Properties of MTN (1)
2. Evidence Acquisition
3. Results
3.1. Conventional Methods of Eliminating Metronidazole (MTN) Antibiotics
3.2. Various Oxidation Methods
3.2.1. Fenton Method
3.2.2. Electro-Fenton Process
3.2.3. The Effect of Ultrasound (US) and UV on Antibiotics Removal
3.2.4. Different Processes using Nanoparticles
3.2.5. Adsorption Methods and Use of Activate Carbon
3.3. Comparison of Some Metronidazole Elimination Methods
| Antibiotic | Concentration | Matrix | Treatment | Operating conditions | Results and comments | References |
|---|---|---|---|---|---|---|
| Metronidazole | 10 - 30 mg/L | Distilled water, natural waters and wastewater | Simultaneous | pH = 2- 9 | The ozonation degradations were higher than 90% and 10- 20% of TOC removal. - Ozonation generates highly toxic oxidation by-products. | (26) |
| Application of ozonation and adsorption | 0.25- 0.50 g/L activated carbon | - The presence of activated carbon during the ozonation produces an increase in the removal rate, a reduction in the toxicity of oxidation by-products and a reduction of around 30% in the TOC. | ||||
| Metronidazole | 100 - 600 mg/L | Distilled water, Natural waters and wastewater | Adsorption/Bioadsorption on activated carbon | T = 25 C; pH = 2- 11 | The pH of the medium and the electrolyte concentration did not influence the adsorption removal. | (27) |
| 0 - 0.1 M NaCl | - Antibiotics were not degraded by the microorganisms used in the biological treatment. | |||||
| 1 g/L activated carbon | - The presence of these microorganisms during the adsorption increases their adsorption/ bioadsorption on the activated carbon. | |||||
| Metronidazole | 150 mg/L | Distilled water | Adsorption on activated carbons | T = 25 C; 0.2 - 1 g/L activated carbon | 90% removal was achieved with 1 g/L of activated carbon. | (28) |
| pH = 7 | - 2nd order kinetic fits suitably the experimental data | |||||
| Metronidazole | 1 mg/L | Deionised water | Direct and indirect Photolysis | Photolysis: LP UV at 254 nm | Photo-degradation exhibited pseudo 1st order kinetics. | (12) |
| Fenton | MP UV at 200 - 400 nm; pH = 6; 0 - 50 mg/L; H2O2 | - MP irradiation was more effective than LP. | ||||
| Photo-Fenton | Photo-and Fenton: LP UV at 254 nm; pH = 3.5; 29.4 mM H2O2; 2.94 - 11.76; mM Fe2+ | - Direct photolysis (6% - 12% removal) was less effective than UV/H2O2 oxidation (58% - 67% removal). | ||||
| - Fenton oxidation followed 2nd order kinetics and the rate was increased with High Fe2+ concentrations. | ||||||
| - An increase in the removal efficiency and in the reaction rate occurred when photo-Fenton (74% - 94% removal) is compared to Fenton oxidation (53% - 76% removal). | ||||||
| Metronidazole | 1 - 25 mg/L | Deionised water | adsorption on various carbon materials | pH = 2 - 12; temperature, = 15-35 C°; NaCl = 0.1 - 1 N | - The adsorption of MNZ was enhanced when the MNZ solutions were prepared using wastewater. Therefore, the electrolytes present in the wastewater cooperated rather than competed with the MNZ molecules for the adsorption sites. | (1) |
| - Desorption equilibrium data of MNZ on all carbon materials demonstrated that the adsorption was reversible corroborating the weakness of the adsorbent-adsorbate interactions. | ||||||
| Metronidazole | 40 - 120 mg/L | Deionised water | Photocatalytic degradation | dosage (0.5 - 3 g/L) pH = 3 - 11 | - Maximum removal of MNZ was observed at near neutral pH. | (29) |
| A 125 W medium-pressure UVC lamp emitting maximum wavelength at 247.3 nm and a low-pressure UV lamp with irradiation intensity 8 W were applied as light sources | - Removal efficiency was decreased by increasing dosage and initial MNZ concentration. | |||||
| - The reaction rate constant (kobs) was decreased from 0.0513 to 0.0072 min-1 and the value of electrical energy per order (EEo) was increased from 93.57 to 666.67 (kWh/m3) with increasing initial MNZ concentration from 40 to 120 mg/L, respectively. | ||||||
| - The biodegradability estimated from the BOD5/COD ratio was increased from 0 to 0.098. |
