| Literature DB >> 34070121 |
Ling Xin1, Jiwei Hu2,3, Yiqiu Xiang1, Caifang Li1, Liya Fu3, Qiuhua Li1,4, Xionghui Wei5.
Abstract
Advanced oxidation (e.g., fenton-like reagent oxidation and class="Chemical">ozone oxidation) is a highly important technology that uses strong oxidizing free radicals to degrade organic pollutants and mineralize them. The fenton-like reactions have the characteristics of low <class="Chemical">span class="Chemical">cost, simple operation, thorough reaction and no secondary pollution. Fenton-like reagents refer to a strong oxidation system composed of transition metal ions (e.g., Fe3+, Mn2+ and Ag+) and oxidants (hydrogen peroxide, potassium persulfate, sodium persulfate, etc). Graphene and carbon nanotube possess a distinctive mechanical strength, flexibility, electrical and thermal conductivity and a very large specific surface area, which can work as an excellent carrier to disperse the catalyst and prevent its agglomeration. Fullerene can synergize with iron-based materials to promote the reaction of hydroxyl groups with organic pollutants and enhance the catalytic effect. Fenton-like catalysts influence the catalytic behavior by inducing electron transfer under strong interactions with the support. Due to the short lifespan of free radicals, the treatment effect is usually enhanced with the assistance of external conditions (ultraviolet and electric fields) to expand the application of fenton-like catalysts in water treatment. There are mainly light-fenton, electro-fenton and photoelectric-fenton methods. Fenton-like catalysts can be prepared by hydrothermal method, impregnation and coordination-precipitation approaches. The structures and properties of the catalysts are characterized by a variety of techniques, such as high-resolution transmission electron microscopy, high-angle annular dark-field scanning transmission electron microscopy and X-ray absorption near-edge structure spectroscopy. In this paper, we review the mechanisms, preparation methods, characterizations and applications status of fenton-like reagents in industrial wastewater treatment, and summarize the recycling of these catalysts and describe prospects for their future research directions.Entities:
Keywords: degradation; fenton process; free radicals; hydrogen peroxide; organic pollutants
Year: 2021 PMID: 34070121 PMCID: PMC8158343 DOI: 10.3390/ma14102643
Source DB: PubMed Journal: Materials (Basel) ISSN: 1996-1944 Impact factor: 3.623
Application fields of carbon-based nanomaterials.
| Performance | Applications | References |
|---|---|---|
| Chemical catalysis | Catalytic catalyst medium | [ |
| Mechanical properties | The preferred material for high-strength such as reinforcement and toughening | [ |
| Magnetic properties | Magnetic absorption, storage memory element materials, soft ferrite materials, etc. | [ |
| Electrical performance | Microelectronic device materials, microelectronic device materials, field emission cathode materials | [ |
| Optical performance | Large-capacity supercapacitor materials, superconducting materials, nano-integrated circuit materials | [ |
| Mechanism performance | Light absorbing materials, optical communication materials, optical recording, optical display, optoelectronic materials | [ |
| Thermal properties | Micro-mechanical component materials such as molecular coils and pistons, damping devices and rotary sealing materials | [ |
| Physical properties | Micro weapon materials such as micro engines, micro spy vehicles, micro high-efficiency explosives, and materials for aviation and spacecraft | [ |
| Sensitive characteristics | Hydrogen storage materials, metal nanowire template materials | [ |
| Other | Sensitive materials (sensors, detectors, sensitive electronic scales) | [ |
Figure 13D structure diagram of fullerene.
Figure 23D structure diagram of carbon nanotubes.
Figure 33D structure diagram of graphene.
Oxidation-reduction potentials of various oxidants.
| Oxidants | Equations | Oxidation-Reduction Potential (V) |
|---|---|---|
| ·OH | ·OH + H++ e = H2O | 2.80 |
| O3 | O3+ 2H+ + 2e = H2O + O2 | 2.07 |
| H2O2 | H2O2 + 2H+ + 2e = 2H2O | 1.77 |
| MnO4− | MnO4− + 8H+ + 5e = Mn2+ + 4H2O | 1.51 |
| ClO2 | ClO2 + e = Cl− + O2 | 1.50 |
| Cl2 | Cl2 + 2e = 2Cl− | 1.30 |
Figure 4Basic schematic diagram of fenton reactions.
Figure 5Light-fenton reactions mechanism diagram.
Figure 6Electrical-fenton reactions mechanism diagram.
Comparison of methods for the preparation of carbon nanomaterials.
| Method | Advantages | Limitations |
|---|---|---|
| Method of laser evaporation of graphite | High purity of the products | Low output and valuable equipment |
| Plasma spray deposition technique means | Long electrode life; stable combustion; independent airflow and pressure control; higher efficiency | Expensive carrier gas; small spraying rate; high quality requirements for spraying materials |
| Graphite arc method | No harmful product formation | Obtain high purity products and consumption of too large amount of energy |
| Chemical vapor deposition | Simple process, low cost, high yield, suitable for industrial production | Due to the low reaction temperature, the prepared material is defective and requires some post-treatment |
Summary of some applications of fenton-like degradation of pollutants.
| Pollutant | Materials | Results | References |
|---|---|---|---|
| Dimethyl phthalate | F/fenton; fullerene-Fe(III)/H2O2 and Fe(III)/H2O2 fenton systems; | Under visible light conditions, the F/fenton system can almost completely degrade DMP within 50 min, and its large capacity eventually reaches 0.0771 min−1, which is 18.5 and 45.4 times higher than that of fullerene-Fe(III)/H2O2 and Fe(III)/H2O2, respectively | [ |
| MO | CNT/β-FeOOH | The results revealed that the increase of visible light absorption intensity and the decrease of β-FeOOH particle size were favorable to the photocatalytic and photo-fenton reaction degradation. | [ |
| Phenol | Fe3O4-GO | Under optimal conditions (pH 5.0, hydrogen peroxide concentration 10.0 mmol/L, catalyst dose 0.25 g/L), 98.8% of phenol in phenol solution can be removed after 120 min | [ |
| Rhodamine B | Cu2O/CNTs/PTFE | The degradation of RhB in this E-fenton system reached 80.2% and 89.3% in 120 min at neutral pH and pH of 3, respectively | [ |
| AR14; MB | Fe3O4/GO; Fe3O4/rGO | In the experiments, the removal of AR14 exceeded that of MB and the rGO-GE system exceeded that of GO-GE, demonstrating that magnetic nanoparticles are also effective in generating free radical hydroxyl groups in alkaline pH. | [ |
| Tetracycline | Fe/N−C-2/H2O2/US system | The maximum removal of TC in this type of fenton system was 92.77%, and the catalytic capacity of Fe/N-C-2 remained above 88% after six consecutive runs, which indicates the high stability of Fe/N-C-2 composites in aqueous solutions. | [ |
| Crystal Violet | FeGAC/H2O2 | The optimal conditions for the removal of crystal violet by this class of fenton reagents were an initial pH of 3, a hydrogen peroxide concentration of 1.8 mmol/L, a catalyst loading of 2.5 g/L and a power density of 141 W/L, and a maximum removal rate of 88%. | [ |
Commonly used adsorption isotherm models.
| Adsorption Type | Isotherm Models | Description | References |
|---|---|---|---|
| Langmuir |
| where | [ |
| Freundlich |
| where | [ |
| Temkin |
| In this equation, | [ |
| D-R |
| where | [ |