Assessing the Sustainability of Photodegradation and Photocatalysis for Wastewater Reuse in an Agricultural Resilience Context
Abstract
:1. Introduction
2. Search Strategy and Theoretical Framework
Analytical Approach
- (1)
- They have selected review principles linked to the purpose of the study;
- (2)
- They have examined the search items, removing nine duplicates, three review papers, one chapter and one ineligible paper;
- (3)
- They have built a filtered sample, considering 22 eligible papers, and have carried out a content analysis and interpretation of three review papers with the aim of underlining the future research directions.
3. Results
3.1. Sample Papers
Cluster Analysis | Technological Approach | Findings * | Ref. |
---|---|---|---|
Experimental method, Municipal wastewater | Natural solar photolysis | Toxicity reduced from 12 to 50% | [43] |
Municipal wastewater | Advanced oxidation process | Implementation of mercury lamps to increase the effectiveness of purification of municipal wastewater | [36] |
Experimental method | Solar irradiation | No differences in quality of lettuce irrigated from treated water | [14] |
Experimental method | Solar photocatalysis | No differences in quality of lettuce grown | [42] |
Experimental method | NFC-doped photocatalytic oxidation | Efficacy of NFC-doped photocatalyst to remove antibiotics and pollutants | [31] |
Experimental method | Photodegradation of bisphenol-A | Photocatalytic efficiency of new materials manufactured under different sources of radiation | [35] |
Experimental method | Photocatalysis | Post-irradiation seed elongation of sprouts promotes the reuse of treated water | [44] |
Experimental method | Solution combustion synthesis, Modified hydrothermal method | Photocatalytic membrane catalytic reactors are an interesting example of an integrated system in which molecular separation and chemical transformation take place in a single stage and at sustainable levels | [45] |
Experimental method | Sorption, Desorption, Concentrations | Absorption and desorption of antibiotics vary according to the soil type and depend on pH, organic carbon, soil texture and cation exchange capacity | [32] |
Experimental method | Photocatalytic activity | Good photocatalytic activity in the degradation of methylene blue using UV and visible light | [46] |
Experimental method | Clay purification, Clay characterization, Adsorption experiments | Physicochemical characteristics of the treated effluent allow the use of wastewater for crop irrigation | [47] |
Experimental method | Solar driven advanced oxidation processes | High-level solar technology with faster degradation kinetics observed for the sunlight process, offsetting the cost of the photocatalyst | [48] |
Comparative method | Modified grafting, Process, Fixed concentration of cinnamic acid | Scaled-up reactors for the purification of agricultural wastewater | [40] |
Experimental method | Raceway pond reactor pilot plant with two types of RPRs (raceway pond reactors) | Improvement in the treatment capacity and reduction in the consumption of chemical reagents such as hydrogen peroxide | [37] |
Experimental method | Ag- and Zr-modified TiO2 nanoparticles used in degradation | Phytotoxicity of the degradation of parents and pollutants to determine the environmental impact of treated water on three plant seeds | [30] |
Experimental method | Novel Zr/Ag-TiO2@rGO hybrid photocatalyst prepared | Analysis of degradation kinetics, products and further toxicity during photocatalysis | [49] |
Comparative method | Comparison environmental profile of different UV-C-based systems | Major impacts due to electricity during the operating phase of the photoreactor | [26] |
Experimental method | Chemical experiment | NH2Cl and NHCl2 contribute to advanced oxidation processes (UV/AOPs) | [39] |
Experimental method | Use of TiO2 for photocatalysis | Simultaneous use of a catalyst increases the percentage of purification for the elimination of pesticides | [34] |
Experimental method | Photooxidation of pollutant parameters from the OMW at different operational conditions | Incorporation of ZrO2 into TiO2 for a higher separation efficiency | [41] |
Experimental method | Natural sunlight irradiation during the summer/autumn of 2017 | PS is effective, low cost and degrades pesticides in agro-wastewater in a reasonable amount of time and with solar energy | [33] |
Methodological proposal | Identification of relevant indicators CEC for performance evaluation of new end-of-tube technology in a reuse project for irrigation purposes | Presents a shortlist of CECs included in regular monitoring programs during reuse operations | [38] |
3.2. Bibliometric Analysis
4. Discussion
5. Conclusions
- Suggests the need for knowledge of sustainable best practices for stakeholders involved in agriculture;
- Provides hypotheses for the reuse of wastewater purified with solar energy;
- Elaborates on hypotheses of circular bioeconomy to best achieve the sustainability objectives of the 2030 Agenda.
6. Future Directions and Limitations
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
Abbreviations
4-CP | 4 chlorophenol |
AOPs | advanced oxidation processes |
BiVo4 | bismuth vanadate |
Br | bromide |
CaIn2S4 | series of graphite-like g-C3N4 hybridized in CaIn2S4 |
CECs | compounds of emerging concern |
Cl2 TOX | total organic halogen chloride |
CO2 | carbon dioxide |
COD | chemical oxygen demand |
CPCN | C-doped polymeric carbon nitride catalysis |
DOC | dissolved organic carbon |
GWP | global warming potential |
LCA | Life Cycle Assessment |
Lx | Lux, SI unit of measurement for illuminance |
Min | minutes |
MWWTP | Municipal Wastewater Treatment Plant |
MXene | two-dimensional transition metal carbide, nitride |
Na2S2O8 | sodium peroxydisulfate |
NH2Cl TOX | chloramine total toxicity |
NHCl2 | dichloramine |
pH | potential of hydrogen |
PRISMA | Preferred Reporting Items for Systematic Review and Meta-Analysis |
PS | persulfate |
RPRs | raceway pond reactors |
SUVA | specific ultraviolet absorbance |
TC | tetracycline |
TiO2 | titanium dioxide |
TiO2 | titanium dioxide |
TOC | total organic carbon |
TOX | total organic halogen |
UV-C | germicidal ultraviolet radiation |
UV/AOPs | ultraviolet advanced oxidation processes |
UV/H2O2 | ultraviolet hydrogen peroxide |
WSPs | waste stabilization ponds |
ZnO | zinc oxide |
ZrO2 | zirconium oxide |
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No. | Keyword Combinations | Document Results |
---|---|---|
1 | photodegradation AND photocatalysis AND wastewater AND reuse AND agriculture | 2 |
2 | photodegradation AND photocatalysis AND wastewater AND reuse AND LCA | 0 |
3 | photodegradation AND photocatalysis AND wastewater AND reuse AND water scarcity | 2 |
4 | photodegradation AND wastewater AND reuse AND agriculture | 9 |
5 | photodegradation AND wastewater AND reuse AND LCA | 1 |
6 | photodegradation AND wastewater AND reuse AND water scarcity | 9 |
7 | photocatalysis AND wastewater AND reuse AND agriculture | 7 |
8 | photocatalysis AND wastewater AND reuse AND LCA | 0 |
9 | photocatalysis AND wastewater AND reuse AND water scarcity | 6 |
Document Methodology and Difference from This Manuscript * | Contaminants | Topics Analyzed * | Results * | Ref. |
---|---|---|---|---|
Comprehensive review, not an SLR | Pharmaceuticals, personal care products and endocrine-disrupting compounds | Overview of WSP treatment and performance, removing organic micropollutants in WSPs, pharmaceuticals and personal care products in WSPs, pesticides in WSPS, perfluorinated compounds, other organic micropollutants. | Efficiency, environmental and economic sustainability, performance: variable and influenced by many factors | [13] |
Critical review, not an SLR | Dye molecules and actual organic pollutants | Structure, preparation, other syntheses, standard organic pollutants (methylene blue, methyl orange, rhodamine B, actual organic pollutants). | Effective visible-light-driven photocatalyst with excellent properties: narrow bandgap, resistance to corrosion, low toxicity, good removal efficiency (35–100%) | [11] |
Review, not an SLR | Phenolic compounds (epoxy resin manufacturing, textile and leather industry) | Mechanisms and components of photocatalysis, key parameters in photocatalytic degradation, dominant industrial phenolic pollutants, photocatalytic degradation of phenolic compounds. | Higher energy consumption which depends on the light source, catalyst activity, process capacity, water quality and organic pollutants chemical structure and concentrations. It details the cost-effectiveness of a photocatalytic technique with a 100% removal of antibiotic content, 86% removal of TOC and 79% removal of COD in 420 min. | [3] |
GWP (CO2 eq) | pH | DOC (m/L) | SUVA (m/L) | Br- (mg/L) | Nitrate (mg/L) | Turbidity (NTU) | Cl2 TOX (mg/L) | NH2Cl TOX (mg/L) | Difficulties | Results | Ref. |
---|---|---|---|---|---|---|---|---|---|---|---|
x | 6–8 | 4.13 | 3.03 | 0.12 | 1.62 | 3.9 | 472 | 118 | Typical pH values in natural waters with limited influence on solar photolysis | Photolysis rates of removal: –50% of direct photolysis, Iodinated and brominated DBPs degraded faster than chlorinated DBPs under sunlight irradiation | [43] |
x | x | x | x | x | x | x | x | x | Decentralized systems treating small volumes of water overcame the limited penetration of V-UV light into the water | In aqueous solution, photolysis was much faster when combined | [36] |
x | 6–8 | x | x | x | x | x | x | x | Iron salts in Fenton homogeneous oxidation systems for negligible mass transfer limitations between catalysts and oxidants | Rate of oxidized pesticides > 99.5% | [14] |
x | x | x | x | x | x | x | x | x | x | Rate of removal 90% | [14] |
x | x | x | x | x | x | x | x | x | TiO2 limited applications, with a 3.2 eV band gap energy | Purification yield between 62 and 99% | [31] |
x | 6.5 | x | x | x | x | x | x | x | Very soluble clusters in aqueous solutions, limited recyclability and reuse as a photocatalyst, introduction of organic pollution to the treated environment | Degradation of the recalcitrant pollutant of between 50.3 and 100% in 90 min of irradiation with UV, solar and solar lamp and LED | [35] |
x | 8.5 | x | x | x | x | x | x | x | Phosphomolybdic and decatungstate composites limited ability to adsorb (–18%) | Irradiation tests for 210 min produced minor and negligible toxicity, showing rapid increase in shoot lengths of tomato, onion and lettuce | [44] |
x | 5–5.5 | x | x | x | x | x | x | x | Greater dispersion of photocatalysts in the aqueous system due to the limited availability of catalysts with little exposure to dyes in the photocatalytic process | Catalysts synthesized with exposure 1–51.71 min | [45] |
x | 4.5–6.5 | x | x | x | x | x | x | x | Antibiotic absorption with plastic materials | Recovery rate between 15 and 81% of the compound | [32] |
x | x | x | x | x | x | x | x | x | x | 85% removal efficiency under visible light | [46] |
x | 8 | x | x | x | x | x | x | x | High cost of adsorbent and its difficult regeneration | Removal efficiency rate of 80% in 60 min | [47] |
x | 6.24–7.44 | x | x | x | x | x | x | x | Photocatalyst removal and poor absorption of semiconductor radiation under visible light | Complete removal in 96 h of treatment; between 27 min and 25 h, the removal rate was 93.5% | [48] |
x | 3.8 | x | x | x | x | x | x | x | x | After 90 min of irradiation, effective photocatalysis for use in photodegradation | [40] |
x | 5–5.5 | x | x | x | x | x | x | x | After 15 min, the final yield (–80%) was limited by photodegradation | Removal of more than 60% (5 min of exposition, 50% removal) | [37] |
x | 3–9 | x | x | x | x | x | x | x | x | x | [30] |
x | x | x | x | x | x | x | x | x | x | Rate removal 80.5% in 3 h | [49] |
x | x | x | x | x | x | x | x | x | Elimination of antibiotics with different durations of UV exposure | According to the type of treatment, times of exposure (from 30 to 120 min) to UV rays for the removal of contaminants change | [26] |
x | 5.8 | x | x | x | x | x | x | 2 | x | Removal rate: between 60 and 80% compared to 2 mM chloramine | [39] |
x | 5–5.5 | x | x | x | x | x | x | x | Use of a higher UV intensity increased the degradation of imidacloprid | Complete removal (>99%) in 20 min with simultaneous catalysts, 30 min if only one photocatalyst is used. | [34] |
x | 4.6 | x | x | x | x | x | x | x | Regeneration of the TiO2–ZrO2 nanocomposite is the crucial step for heterogeneous photocatalysis | 98% of pollutants photodegraded in 60 min of photooxidation at 21 °C and 300 W UV | [41] |
x | 7.3 | 0.45 | x | x | x | x | x | x | Authorized reagent to treat the residue, avoid phytotoxicity problems in plants and prevent surface water contamination and filtration of PPP in underground soil | Rate of degradation of all pesticides was +90% | [33] |
x | x | x | x | x | x | x | x | x | x | Rate of removal was between 20 and 80% | [38] |
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Crovella, T.; Paiano, A. Assessing the Sustainability of Photodegradation and Photocatalysis for Wastewater Reuse in an Agricultural Resilience Context. Water 2023, 15, 2758. https://doi.org/10.3390/w15152758
Crovella T, Paiano A. Assessing the Sustainability of Photodegradation and Photocatalysis for Wastewater Reuse in an Agricultural Resilience Context. Water. 2023; 15(15):2758. https://doi.org/10.3390/w15152758
Chicago/Turabian StyleCrovella, Tiziana, and Annarita Paiano. 2023. "Assessing the Sustainability of Photodegradation and Photocatalysis for Wastewater Reuse in an Agricultural Resilience Context" Water 15, no. 15: 2758. https://doi.org/10.3390/w15152758
APA StyleCrovella, T., & Paiano, A. (2023). Assessing the Sustainability of Photodegradation and Photocatalysis for Wastewater Reuse in an Agricultural Resilience Context. Water, 15(15), 2758. https://doi.org/10.3390/w15152758