Some of the main and influential journals of interest to readers where the authors usually publish their works about ‘photocatalytic degradation of pesticides in water’ (source: JCR, 2015).
The water bodies’ pollution with phytosanitary products can pose a serious threat to aquatic ecosystems and drinking water resources. The usual appearance of pesticides in surface water, waste water and groundwater has driven the search for proper methods to remove persistent pesticides. Although typical biological treatments of water offer some advantages such as low cost and operability, many investigations referring to the removal of pesticides have suggested that in many cases they have low effectiveness due to the limited biodegradability of many agrochemicals. In recent years, research for new techniques for water detoxification to avoid these disadvantages has led to processes that involve light, which are called advanced oxidation processes (AOPs). Among the different semiconductor (SC) materials tested as potential photocatalysts, titanium dioxide (TiO2) is the most popular because of its photochemical stability, commercial availability, non-toxic nature and low cost, high photoactivity, ease of preparation in the laboratory, possibility of doping with metals and non-metals and coating on solid support. Thus, in the present review, we provide an overview of the recent research being developed to photodegrade pesticide residues in water using TiO2 as photocatalyst.
- photocatalytic degradation
Pesticide may be defined as ‘any substance or mixture of substances intended for preventing, destroying, or controlling any pest including vectors of human or animal diseases, unwanted species of plants or animals causing harm during, or otherwise interfering with, the production, processing, storage, or marketing of food, agricultural commodities, wood and wood products, or animal feedstuffs, or which may be administered to animals for the control of insects, arachnids or other pests in or on their bodies. The term includes chemicals used as growth regulators, defoliants, desiccants, fruit thinning agents, or agents for preventing the premature fall of fruits, and substances applied to crops either before or after harvest to prevent deterioration during storage or transport’ . There are many hundreds of them including herbicides, insecticides, fungicides, rodenticides, nematicides, plant growth regulators and others. Pesticide products contain both ‘active’ and ‘inert’ ingredients: active ingredients are the chemicals in pesticide products that kill, control or repel pests. All other ingredients are called ‘inert ingredients,’ which are important for product performance and usability.
Pesticides have been widely applied to protect agricultural crops since the 1940s, and their use increased steadily during the subsequent decades. The
Protection of crop losses/yield reduction and increase in food quality are key benefits associated with the use of pesticides in agriculture. However, most organic pesticides characterised as persistent in the environment can bioaccumulate through the food web and can be transported in long distances , as evidenced by the accumulation in regions where persistent pesticides have never been used . Persistent organic pollutants (POPs) are
In addition, many pesticides are endocrine-disrupting chemicals (EDCs),
Worldwide consumption of pesticides for agricultural use is constantly increasing as increased human population and crop production, and it has undergone significant changes since the 1960s. Nowadays, the worldwide consumption of pesticides is about 2 million tonnes per year, which 45% is used by Europe alone, 25% is consumed in the USA and 30% in the rest of the world. The proportion of herbicides in pesticide consumption increased rapidly, from 20% in 1960 to 47.5% in 2015. However, the proportion of consumption of insecticides (29.5%) and fungicides/bactericides (17.5%) declined despite their sales increased with other accounts for 5.5% only . The rapid increase of herbicide consumption enhanced agricultural intensification and productivity.
The application of chemical pesticides, in particular the organic-synthesised pesticides, has been a significant mark of human civilisation, which greatly protects and facilitates agricultural productivity. Worlwide, insect pests cause an estimated 14% loss, plant pathogens cause a 13% loss, and weeds causes a 13% loss . Pesticides are so indispensable in agricultural production. About one-third of the agricultural products are produced by using pesticides . Without pesticide application, the loss of fruits, vegetables and cereals from pest injury would reach 78, 54 and 32%, respectively . Ideally, a pesticide must be lethal to the targeted pests, but not to nontarget species, including humans. Unfortunately, this is not the case, so the controversy of use and abuse of pesticides is obvious. Consequently, the risks of using pesticides are serious as well . Most pesticides are not spontaneously generated, and they are toxic to humans and the environment in greater or lesser degree . Pesticides and their degraded products can pass into the atmosphere, soils and water, resulting in the accumulation of toxic substances and thus threatening human health and the environment. In addition, accumulated application leads to loss of biodiversity. Because many pesticides are barely degradable, they persist in soil and pollute surface water and groundwater. Depending on their chemical properties, they can bioaccumulate in food chains and consequently affect human health.
For many pesticides, there is evidence of long-term ubiquity in the aquatic environment at the European Union (EU) level, and therefore they need special consideration as regards their impact on the presentation of chemical status under the European Water Framework Directive (EWFD) . The EWFD establishing a framework for community action in the field of water policy lays down a strategy against the pollution of water. Directive 2008/105/EC , amended by Directive 2013/39/EU  on environmental quality standards in the field of water policy, lays down environmental quality standards in accordance with the EWFD, for the 33 priority substances. The EWFD also sets out general provisions for the protection and conservation of groundwater. The establishment of detailed quality criteria for the assessment of groundwater chemical status in Europe was laid down in the European Groundwater Directive . For this reason, the EU established the following groundwater quality standards: 0.1 μg L−1 for individual pesticide and 0.5 μg L−1 for the sum of all individual pesticides to safeguard people from harmful effects.
During the 1990s of the last century, atrazine (herbicide) and endosulfan (insecticide) were found most often in surface waters in the USA and Australia due to their widespread use. In addition, although in lower proportions, other pesticides such as pronofos, dimethoate, chlordane, diuron, prometryn and/or fluometuron were detected . Studies that are more recent also reported the presence of several pesticides in environmental waters (surface water, groundwater and seawater) close to agricultural lands over the world [22–34]. In addition, different studies have corroborated the presence of some pesticides in drinking water [35–38].
Pesticides are being continuously released into the aquatic environment through anthropogenic activities. Their detection in storm and wastewater effluent has been reported to be a major obstacle as regards wide-ranging acceptance of water recycling . In addition, their variety, toxicity and persistence present a threat to humans through pollution of drinking water resources (e.g. surface water and groundwater). The frequent occurrence of pesticides in surface water and groundwater has prompted the search for suitable methods to destroy them. Although conventional biological treatments of water offer some advantages such as their low cost and easy operation, most studies concerning the treatment of pesticides have concluded that they are not very effective due to their low biodegradability [40, 41]. Other technologies such as adsorption or coagulation merely concentrate pesticides by transferring them in other phases but still remain and not being completely eliminated. To solve this problem, apart from reducing emissions, two main water strategies are followed: (i) chemical treatment of drinking water, surface water and groundwater and (ii) chemical treatment of wastewaters containing biocides and bio-recalcitrant pollutants as pesticides. Chemical treatments of polluted surface water, waste water and groundwater are part of a long-term strategy to improve the quality of water by removing toxic compounds of anthropogenic origin before returning the water to its natural cycle. The Directive 2013/39/EU  promotes the preventive action and the polluter pays principle, the identification of pollution causes, dealing with emissions of pollutants at the source, and finally the development of innovative wastewater treatment technologies, avoiding expensive solutions. Therefore, effective, low-cost and robust methods to decontaminate waters are needed, as long as they do not further stress the environment or endanger human health, particularly prior to direct or indirect reuse of reclaimed water. In this context, the development of Solar Chemistry Applications is of special relevance, especially photochemical processes where solar photons are absorbed by reactants and/or a catalyst causing a chemical reaction. Consequently, in recent years there has been growing interest in the use of advanced oxidation processes (AOPs) to remove pesticide residues as alternative to methods that are more conventional because they allow the abatement of them by mineralisation.
2. Advanced oxidation processes to remove pesticides from water
AOPs have been commonly defined as
When the chemical process (mineralisation) destroys the contaminants and their reaction intermediate products (metabolites), critical secondary wastes are not generated and, thus, post-treatment or final disposal is not required . However, if complete mineralisation is not achieved or the reaction period is too long, a final post-treatment may be necessary. A higher biodegradability and lower toxicity of the reaction by-products, in comparison with the parent compounds, are desirable benefits of applying AOPs to treat wastewaters. However, in some cases, these by-products are less biodegradable and/or more toxic than the parent compounds. For this reason, AOPs can be applied as post- or pretreatment of biological processes. The integration of different AOPs in a sequence of treatment processes is a common approach to achieve a biodegradable effluent, which can be further treated by a conventional biological process, reducing the residence time and reagent consumption in comparison with AOPs alone. Figure 2 shows possible integration of AOPs in wastewater and drinking water treatment plants.
One drawback of these processes is the presence of scavengers in wastewaters because these species consume •OH, competing with pesticides. They can be organic matters (e.g. humic and/or fulvic acids, amino acids, proteins and carbohydrates) or inorganic ions (CO3=, HCO3−, S=, Br−, NO3− and others). Because most natural waters contain these scavengers, optimisation of AOPs must be performed bearing them in mind. The knowledge of their effect on the process efficiency is difficult because they have different reactivities, as well as due to the constant variations in the aqueous phase when the parent pollutants are continuously transformed into many different intermediates. Among these techniques, photocatalytic methods in the presence of artificial or solar light, like heterogeneous photocatalysis (HP), have been proven very effective for the degradation of a wide range of pesticides .
2.1. Basis of heterogeneous photocatalysis
Photocatalysis may be defined as the
As a rule, TiO2 is considered the best photocatalyst due to different qualities such as high photochemical stability, high efficiency, non-toxic nature and low cost, whose behaviour is very well documented in the recent literature [53, 54]. Excellent reviews have been published during the last years on the photoactivity of TiO2 to purify pesticide-polluted waters [39, 48, 55–60].
2.2. Properties and characteristics of titanium dioxide photocatalysts
Titanium dioxide is by far, the most investigated photocatalyst to remove organic pollutants from water. The photocatalytic activity of TiO2 slurries depends on physical properties of the catalyst (crystal and pore structure, surface area, porosity, band gap, particle size and surface hydroxyl density) [61, 62]. On the other hand, operating conditions such as light intensity and wavelength, initial concentration and type of pollutants, catalyst loading, oxygen content, interfering substances, presence of oxidants/electron acceptor, pH value and configuration of photoreactor have a key role [39, 58, 63–66]. Finally, the mode of TiO2 application (suspended, immobilised or doped) is fundamental to rate the photocatalytic activity.
2.2.1. Composition of TiO2 and its types
Titanium dioxide is known to occur in nature as anatase (At), brookite (Bk) and rutile (Rl) (Figure 4). Rl is usually considered to be the high-temperature and high-pressure phase relative to At, whereas Bk is often considered to be of secondary origin. Rl is the most common, most stable and chemically inert and can be excited by both visible and ultraviolet (UV) light (wavelengths smaller than 390 nm) . At is only excited by UV light and can be transformed into Rl at high temperatures. Both Rl and At have a tetragonal ditetragonal dipyramidal crystal system but have different space group lattices. UV light does not excite Bk, but its orthorhombic crystal system can be transformed into Rl with the application of heat.
Generally, At exhibits higher photocatalytic activities than Rl. However, the reasons for the differences in photocatalytic activity between At and Rl are still being debated. Although At has lower absorbance ability to solar light than Rl because its band gap is larger (3.2 eV) than that of Rl (3.0 eV), the photocatalytic activity of At is higher than that of Rl. This can be explained because At has a higher surface adsorption capacity to hydroxyl groups and a lower charge carrier recombination rate than Rl . Also, the lower photocatalytic activity of Rl is due to its larger grain size , lower specific surface areas and less capacity for surface adsorption. In addition, the lifetime of photo-generated e− and h+ in Rl is about an order of magnitude smaller than that of At. Consequently, the chance of participation of photoexcited e- and h+ of At in surface chemical reactions is greatly enhanced. According to Zhang et al. , Rl and Bk belong to the direct band-gap SC category, while At appears to be an indirect band-gap SC. As a consequence, At exhibits a longer lifetime of photoexcited e− and h+ than Rl and Bk because the direct transition of photo-generated electrons from the conduction band to valence band of At is not possible. Moreover, At has the lightest average effective mass of photo-generated e− and h+ than Rl and Bk suggesting the fastest migration of photo-generated e− and h+ from the interior to the surface of At. This results in the lowest recombination rate of photo-generated charge carriers within At. Therefore, it is not surprising that Rt and Bk show a smaller photocatalytic activity than At.
TiO2 can use natural sunlight because it has an appropriate energetic separation between its valence and conduction bands which can be surpassed by the energy content of a solar photon (380 nm > λ >300 nm). The sunlight puts 0.2–0.3 mol photons of m−2 h−1 in the 300–400 nm range with a typical UV flux of 20–30 W m−2. In addition, photons can be generated by artificial irradiation although it is the most important source of costs during the treatment of wastewater . Different available TiO2 catalysts (with different surface areas, crystal sizes and compositions) such as Degussa P25, Hombikat UV100, PC500, PC10, PC50, Rhodia and others have been tested for the photolytic degradation of pesticides in aqueous environments . From them, Degussa P25 has been the most used because it has good properties (i.e. typically a 70:30 At:Rl composition, non-porous, Brunauer, Emmett and Teller (BET) around 55 m2 g−1 and average particle size 30 nm) and a substantially higher photocatalytic activity than other commercial TiO2 . The higher photocatalytic activity of P25 has been attributed to its crystalline composition of Rl and At. It is known that the smaller band gap of rutile absorbs the photons and generates e−/h+ pairs. Then, the electron transfer takes place from the rutile to electron traps in the At phase. Thus, the recombination is inhibited and allows the hole to move to the surface of the particle to react .
2.2.2. Operating conditions
The e−/h+ formation in the photochemical reaction is strongly dependent on the light intensity at a given wavelength . Therefore, the dependency of pollutant degradation rate on the light intensity has been studied in numerous investigations of various organic pollutants. According to Herrmann , the reaction rate is proportional to the radiant flux (φ) < 25 mW cm−2, while above this value, the rate varies as φ½, which indicates a too high value of the flux increasing the e−/h+ recombination rate. When the intensity is high, the reaction rate does not depend on light intensity because at low intensity, reactions involving e−/h+ formation are predominant, while e−/h+ recombination is not significant .
Several authors have indicated that when the level of the target pesticide increases, a large number of molecules of the compound are adsorbed on the photocatalyst surface and, consequently, the reactive species (•OH and O2•−) required for pesticide degradation also increase. However, the formation of •OH and O2•− on the catalyst surface remains constant for a given catalyst amount, light intensity and irradiation time. Hence, at higher concentrations the available •OH is inadequate for pollutant degradation. Therefore, as the concentration increases, the pollutant degradation rate decreases . In addition, an increase in pesticide concentration leads to the generation of intermediates (metabolites), which may be adsorbed on the surface of the catalyst.
Because TiO2 is often used as suspension, the photocatalytic degradation rate initially increases with catalyst loading and then decreases at high concentrations due to light scattering and screening effects. Although the number of active sites in solution will increase with catalyst loading, light penetration is compromised because of excessive particle concentration. The interaction between particles (agglomeration) increases at high concentration, and, consequently, the surface area available for light adsorption is reduced and photocatalytic activity decreases. The optimum catalyst loading has to be found in order to avoid excess catalyst and ensure the maximum absorption of photons. Although the results in the literature are very different, it may be deduced that the incident radiation and path length inside the photoreactor are of special interest in determining the optimum catalyst mass.
Waste water, surface water, groundwater and drinking water pHs vary significantly and play an important role in the photodegradation of pesticides since it determines the size of aggregates it forms and the surface charge of the photocatalyst. The surface charge of the photocatalyst and the ionisation or speciation (p
At low pH, the positive holes are considered as the major oxidation step, whereas at neutral or high pHs, •OH is the predominant species . It is expected that the generation of •OH will be higher due to the presence of more available OH− on the TiO2 surface. Thus, the degradation efficiency of the process will be enhanced at high pH. A very important feature of the photocatalytic process is that in many cases, a great number of different metabolites are produced, which may behave in a different way depending on the pH of the solution. As regards temperature, photocatalytic systems do not require heating and operate at room temperature because of photonic activation .
The e−/h+ recombination is one of the main drawbacks in the application of semiconductor photocatalysis as it causes waste of energy. In the absence of suitable electron acceptor, recombination step is predominant, and thus, it limits the quantum yield . In HP reactions, O2 is generally used as electron acceptor. Addition of exogenous oxidant/electron acceptors into a semiconductor suspension has been shown to improve the photocatalytic degradation of many pesticides because they can eliminate the e−/h+ recombination by accepting the conduction band electron, increase the •OH concentration and oxidation rate of intermediate compound and produce more radicals and oxidising species to accelerate the degradation efficiency of intermediate compounds. Because •OH plays an important role in photodegradation, several researchers have investigated the effect of addition of different electron acceptors (i.e. H2O2, KBrO3 or Na2S2O8) on the photocatalytic degradation of many pesticides [75, 78].
The ability of peroxydisulfate is not only attributed to the promotion of charge separation but also to the production of sulphate radicals (SO4•−), which are very strong oxidising agents (
Besides, the addition of H2O2 enhances the degradation due to the increase in the •OH concentration as follows:
The quantum yield of S2O82− (1.8 mol Einstein−1) is much larger than that of H2O2 (1 mol Einstein−1), which can be related to the rate of recombination of •OH (5.3×109 M−1 s−1) and SO4•− (8.1×108 M−1 s−1) .
As reviewed by Ahmed et al. , many studies have demonstrated that water components like Ca2+, Mg2+, Fe2+, Zn2+, Cu2+, HCO3−, PO43−, NO3−, SO42− and Cl− and dissolved organic matter (DOM) can affect the photodegradation rate of organic pollutants since they can be adsorbed onto the surface of TiO2 [80, 81]. These dissolved components can compete with the pesticide for the active sites depending on the solution pH, reducing the formation of •OH. Anions result in corresponding anion radicals scavenged by •OH. However, they have lower oxidation potential. In addition, DOM, ubiquitously present in storm and wastewater effluent, also plays an important role regarding pesticide degradation. The observed slowdowns are related to the inhibition (surface deactivation), competition and light attenuation effects. Moreover, the presence of humic acids in the reaction solution has been reported to significantly reduce light transmittance and consequently the photooxidation rate.
As usual, two types of photoreactors are used for photocatalytic wastewater treatment processes: (i) slurry photoreactors and (ii) fixed-bed photoreactors . The slurry photoreactors utilise suspended photocatalyst particles, while the other type utilises immobilised photocatalyst particles on a surface. Currently, the catalysts are applied in the form of a slurry in most cases. However, the separation of catalyst after the reaction in the slurry systems is an expensive and tedious stage, which adds to the overall running costs of the plant. Therefore, immobilised catalyst systems are preferred in order to avoid an increase in cost and time. However, the immobilised catalyst systems have low interfacial surface areas and consequently a very low activity, being also difficult to scale . It is noted that configuration of photoreactor has an important role in the efficiency of the photocatalytic wastewater treatment processes.
2.2.3. Bare, doped and immobilised application of TiO2
Generally, the use of TiO2 slurries has been demonstrated to have higher photocatalytic activity as compared to the same immobilised catalyst. This is due to changes on the surface of the catalyst by blocking pores and the appearance of by-products causing the loss of active sites on its surface. Usually, TiO2 is prepared in the form of nanopowders, crystals, thin films, nanotubes and nanorods. As a rule, the immobilisation of TiO2 onto supporting material has been carried out via one of two major routes: (i) physical (thermal treatment) and (ii) chemical (sol-gel, electrodeposition, etc.). The evolution of different supports and the benefits and drawbacks of various immobilisation techniques to obtain a high-surface-area TiO2 can be seen in the reviews by Shan et al.  and Dahl et al. . Nonetheless, the interest for the development of TiO2 supported on different materials is growing because the use of the bare TiO2 phases presents some drawbacks as (i) necessity of irradiation with UV light due to the small amount of photons absorbed in the Vis region, (ii) high recombination rate for the photoproduced e−/h+ pairs, (iii) difficulty to improve the performance by doping with some materials that often act as recombination centres, (iv) deactivation in the absence of H2O vapour when aromatic molecules must be abated and (v) difficulty to support powdered TiO2 on some materials . Consequently, the research line in HP has been driven to modify some electronic and morphological properties of TiO2 to enhance its photoefficacy. In this context, nanosized particles and films on glasses or other supports and powdered samples with high specific surface areas have been obtained to increase the possibility for the involved species to avoid the separation step . Doping, loading and sensitisation of TiO2 are methods aimed to shift the light absorption towards visible light and/or to increase the lifetime of the photoproduced e−/h+ pairs.
A number of approaches have been suggested in recent years to enhance photocatalytic activity of TiO2 in the visible light region for its use in water detoxification . Metal ion doping and co-doping with non-metals can improve trapping of the photoexcited conduction band electrons at the surface, thereby minimising charge carrier recombination. Several dopants used (e.g. Sn, Ag, Pd, Re, Bi, V, Mo, Th or Pt among others), have been shown to enhance photocatalytic activity for the systems examined. However, the photoactivity of the metal-doped TiO2 photocatalyst significantly depends on the dopant ion nature and concentration, preparation method and operating conditions . The deposition of metal ions on TiO2 can modify the photoconductive properties by increasing the charge separation efficiency between electrons and holes, which will enhance the formation of both free hydroxyl radicals and active oxygen species . Recent research indicates that the desired narrowing on the band gap of TiO2 can be achieved using non-metal elements such as N, F, S and C. Thus, modified TiO2 showed a significant improvement on the absorption in the Vis light region due to band-gap narrowing and enhancing the degradation of pesticides under Vis light irradiation, mainly under sunlight [90, 91]. Also, it is possible to produce coupled colloidal structures using TiO2 such as TiO2-SnO2, TiO2-CdS, TiO2-Bi2S3, TiO2-WO3 or TiO2-Fe2O3, in which illumination of one semiconductor produces a response in the other at the interface between them by increasing the charge separation and extending the energy range of photoexcitation. On the other hand, the coating of one semiconductor or metal nanomaterial on the surface of another semiconductor or metal nanoparticle core is called capping. Semiconductor nanoparticles of TiO2 can be coated with another semiconductor (i.e. SnO2) with a different band gap to enhance its emissive properties .
2.3. Heterogeneous photocatalytic degradation of pesticide residues in water over titanium dioxide
A desirable feature in the photodegradation of pesticides in water is the transformation of the parent compounds in order to avoid their toxicity. However, the main objective is the mineralisation of the pesticides. As previously commented, •OH is the main species involved for organic substrate oxidation, but the free radical HO2• and its conjugate O2•− also play an important role although those radicals are much less reactive than •OH. All these free radicals react with pesticides by hydrogen abstraction or electrophilic addition to double bonds. Further, the radicals react with O2 to give organic peroxyl radicals (ROO−) initiating different oxidative reactions that may lead to the complete mineralisation of the pesticides. Since •OH is non-selective, numerous and different transformation products (intermediates) can be formed at low concentrations being in certain cases more persistent and toxic than the parent compounds.
The presence of pesticide residues in water is usually monitored using chromatographic techniques such as gas chromatography (GC) and liquid chromatography (LC) coupled to mass spectrometry (MSn) and time-of-flight (TOF) detection systems. However, since identification of all the transformation products generated during the photooxidation is not possible, the measure of total organic carbon (TOC) and more specifically dissolved organic carbon (DOC) is crucial in the process because determination of CO2 must be stoichiometric with the organic carbon in the parent pesticide. This determination can be carried out in a simple and rapid way to know the mass balance and the remaining amount of metabolites. As example, Figure 5 shows the photodegradation pathways proposed for chlorantraniliprole  and tebuconazole  dissolved in water when illuminated in the presence of TiO2.
In the case of chlorantraniliprole, a new class of anthranilic diamide insecticide, several transformation products are generated during irradiation as a result of different reactions such as hydroxylation, deamination, hydrolysis of the amide bridge and rearrangement followed by cyclisation, methyl amine transfer and fragmentation. For tebuconazole, a common triazole fungicide with numerous agricultural and urban uses, the transformation pathway was found to proceed through tert-butyl chain cleavage, hydroxylation, oxidation and dechlorination and showed that its degradation mechanism was mainly driven by •OH and h+.
The use of HP has showed a powerful growth in recent years. Today, pesticides constitute an important group concerning pollutant treatment. The large number of papers published in the last years proves this interest. A review to the literature extracted from the Web of Science™ (formerly ISI Web of Knowledge, www.isiknowledge.com) managed by Thomson Reuters (Philadelphia, USA) using the following keywords,
Table 1 shows some of the most popular journal publishing on the topic “photocatalysis and pesticides” according to the following criteria: impact factor > 2 and Eigenfactor score > 0.01 (Journal Citation Reports (JCR) Science Edition 2015).
|Journal title (ISO)||Editorial/country||ISSN a||IF b||5Y-IF c||ES d|
|Chemical Reviews||American Chemical Society (USA)||0009-2665||37.369||51.560||0.24503|
|Journal of Photochemistry and Photobiology C: Photochemistry Reviews||Elsevier Science BV (Japan)||1389-5567||12.162||15.268||0.00442|
|Applied Catalysis B: Environmental||Elsevier Science BV (The Netherlands)||0926-3373||8.328||8.142||0.05714|
|Journal of Catalysis||Academic Press INC Elsevier Science (USA)||0021-9517||7.354||7.482||0.03438|
|Water Research||Pergamon-Elsevier Science Ltd. (England)||0043-1354||5.991||6.769||0.08394|
|Environmental Science and Technology||American Chemical Society (USA)||0013-936X||5.393||6.396||0.20232|
|Chemical Engineering Journal||Elsevier Science SA (Switzerland)||1385-8947||5.360||5.439||0.09715|
|Catalysis Science and Technology||Royal Society of Chemistry (England)||2044-4753||5.287||5.547||0.02367|
|Journal of Hazardous Materials||Elsevier Science BV (The Netherlands)||0304-3894||4.836||5.641||0.09715|
|Solar Energy Materials and Solar Cells||Elsevier Science BV (The Netherlands)||0927-0248||4.732||5.016||0.04275|
|Catalysis Today||Elsevier Science BV (The Netherlands)||0920-5861||4.312||4.105||0.03376|
|Applied Catalysis A: General||Elsevier Science BV (The Netherlands)||0926-860X||4.012||4.403||0.03476|
|Science of the Total Environment||Elsevier Science BV (The Netherlands)||0048-9697||3.976||4.317||0.08394|
|Journal of Molecular Catalysis A: Chemical||Elsevier Science BV (The Netherlands)||1381-1169||3.958||4.045||0.01727|
|Chemosphere||Pergamon-Elsevier Science Ltd. (England)||0045-6535||3.698||4.068||0.06483|
|Solar Energy||Pergamon-Elsevier Science Ltd. (USA)||0038-092X||3.685||4.414||0.02277|
|Journal of Environmental Management||Academic Press-Elsevier Science Ltd. (England)||0301-4797||3.131||4.049||0.03326|
|Catalysts||MDPI AG (Switzerland)||2073-4344||2.964||3.194||0.16915|
|Journal of Agricultural and Food Chemistry||American Chemical Society (USA)||0021-8561||2.857||3.308||0.08776|
|Environmental Science and Pollution Research||Springer Heidelberg (Germany)||0944-1344||2.760||2.876||0.02617|
|Journal of Chemical Technology and Biotechnology||Wiley-Blackwell (England)||0268-2575||2.738||2.744||0.01051|
|Journal of Photochemistry and Photobiology A: Chemistry||Elsevier Science SA (Switzerland)||1010-6030||2.477||2.573||0.01025|
|Photochemical and Photobiological Science||Royal Society of Chemistry (England)||1474-905X||2.235||2.673||0.01040|
|Journal of Environmental Science||Science Press (Mainland China)||1001-0742||2.208||2.699||0.01282|
Following the criteria above, some of the most representative publications are presented in this summary (Table 2). Results show that sunlight photoalteration (photolysis) processes are well now to play an important role in the degradation of pesticides and other contaminants in the aquatic environment. These technologies allow the removal of pesticides by mineralisation. When the exciting energy used comes from the Sun, the process is called
|Pesticides||Photocatalysts||Light source||Main findings||References|
|Pyrimethanil||TiO2 P25 and home made||Solar||Similar photoefficiences in mineralisation|||
|Acephate, omethoate, methyl parathion||Fe3O4@SiO2@mTiO2 nanomicrospheres||UV||Disappearance after 45–80 min|||
|Imidacloprid||TiO2 and TiO2-based hybrid||Solar||TiO2 + fly ash is 2–3 times less active than sol-gel TiO2|||
|Spirotetramat, spirodiclofen, spiromesifen||ZnO, TiO2 P25, TiO2 Kronos vlp 7000, Zn2TiO4 and ZnTiO3||UV||ZnO > TiO2 P25 > TiO2 Kronos vlp 7000 > Zn2TiO4 > ZnTiO3|||
|Flubendiamide||ZnO/Na2S2O8 and TiO2 P25/Na2S2O8||UV||ZnO and TiO2 oxides strongly enhance the degradation rate|||
|Thiamethoxam, imidacloprid, acetamiprid||ZnO/Na2S2O8 and TiO2 P25/Na2S2O8||UV/solar||Solar irradiation was more efficient compared to artificial light for the removal of these insecticides (t½ = 0.3–2 min)|||
|Chlorantraniliprole||ZnO, TiO2 P25, TiO2 Kronos vlp 7000, Zn2TiO4||UV||Half-lives of 53 and 71 min for ZnO/Na2S2O8 and TiO2/Na2S2O8 systems, respectively|||
|Metamitron, metribuzin||Different TiO2 nanopowders||UV||t½ lower than 8 min using TiO2 P25|||
|Dichlorvos||TiO2 supported on zeolites||UV||Complete degradation in 360–540 min|||
|Atrazine||N-Doped TiO2 supported by phosphors||UV||Enhanced performance compared to either pure N-TiO2 nanoparticles or bare phosphors microparticles|||
|Spinosad, indoxacarb||ZnO/Na2S2O8 and TiO2 P25/Na2S2O8||UV||95% degradation rate was observed for both spinosyns after 2 min when using Na2S2O8|||
|Methabenzthiazuron||ZnO, TiO2 P25||UV||Half-lives of 2 and 7 min for ZnO and TiO2, respectively|||
|Monocrotophos, endosulfan, chlorpyriphos||TiO2 coated on polymeric beads||Solar||Rapid photodegradation using immobilised bead photoreactor|||
|Isoproturon||TiO2 coated on inert cement beads||UV||85% degradation rate after 6 h|||
|Diazinon||TiO2 doped with N, NS and FeFNS||UV LED||The FeFNS-doped TiO2 was found to be an efficient catalyst (96% degradation after 100 min)|||
|Methyl oxidemeton, methidathion, carbaryl, dimethoathe||TiO2 P25, Hombikat UV 100, Millennium PC (50, 100, 105), Kronos 7101||UV||TiO2 P25 was the most effective for pesticide degradation. Removal of pesticides in less than 300 min|||
|30 sulfonylurea herbicides||ZnO and TiO2 P25 in tandem with Na2S2O8||UV||Average time required for 90% degradation about 3 and 30 min for ZnO/Na2S2O8 and TiO2/Na2S2O8 systems, respectively|||
|Chlorotoluron, diuron, fluometuron, isoproturon, linuron||ZnO, TiO2, WO3, SnO2 and ZnS||Solar||The time required for 90% degradation ranged from 23 to 47 min for isoproturon and linuron, respectively, when using the tandem ZnO/Na2S2O8|||
|Carbofuran||ZnO, TiO2 P25 Degussa||Solar||Half-lives ranging from 6 to 385 min|||
|Malathion||WO3/TiO2||2% WO3/TiO2 exhibited the best photocatalytic activity achieving abatement of 76% TOC after 300 min|||
|Ethoprophos, isoxaben, metalaxyl, metribuzin, pencycuron, pendimethalin, propanil, tolclofos-methyl||ZnO, TiO2, WO3, SnO2, ZnS||Solar||Half-lives for ZnO ranged from 9 to 38 min (t30W 0.3–1.7 min), while in the presence of TiO2, ranged from 41 to 260 min (t30W 1.9–16.3 min)|||
|Simazine, prometryn, terbutryn, atrazine, terbuthylazine, propachlor, S-metolachlor, alachlor||ZnO, TiO2||Solar||Degradation rate >70% after 240 min in the ZnO/Na2S2O8 system|||
|Fenamiphos||ZnO, TiO2, WO3, SnO2||Solar||Half-life <3 min for ZnO, TiO2 in tandem with Na2S2O8|||
|Cyprodinil, fludioxonil||ZnO, TiO2||Solar||DT75, referred to the normalised illumination time (t30W), was lower than 40 and 550 min (t30W = 2 and 40 min) for both fungicides using ZnO and TiO2, respectively|||
|Methyl parathion, dichlorvos||N-doped and P25 TiO2||UV/solar||N-doped TiO2 showed higher photocatalytic activity under solar radiation compared to UV and visible light|||
|MCPA, clopyralid, mecoprop||Fe- and N-doped TiO2||UV||Lowering of the band gap of titanium dioxide by doping is not always favourable for increasing photocatalytic efficiency of degradation|||
|2,4-D, Diuron, ametryne||TiO2 slurry||Solar||Results showed that the overall model fitted the experimental data of herbicides mineralisation in the solar CPC reactor satisfactorily for both cloudy and sunny days|||
|Carbendazim||TiO2 slurry||UV||More than 90% of fungicide was degraded after 75 min|||
|Glyphosate||TiO2 slurry||UV||Addition of Fe3+, Cu2+, H2O2, K2S2O8 or KBrO3 enhances the photodegradation|||
|Alachlor, atrazine, chlorfenvinphos, diuron, isoproturon, pentachlorophenol||TiO2 slurry and Fe2+||Solar||Photo-Fenton treatment was found to be shorter than TiO2 and more appropriate for these compounds|||
|Triclopyr, dantinozid||Different types of TiO2 slurries in tandem with electron acceptors||Solar||The photocatalyst Degussa P25 was found to be more efficient as compared with other photocatalysts|||
|Cymoxanil, methomyl, oxamyl, dimethoate, pyrimethanil, telone||TiO2 slurry and Fe2+||Solar||Total disappearance of the parent compounds and nearly complete mineralisation were attained with all pesticides tested|||
|Dimethoate||ZnO, TiO2||UV||Both catalysts were unable to mineralise dimethoate, but the addition of oxidants improved the efficiency of the processes|||
|Dichlorvos, monocrotophos, parathion, phorate||TiO2·SiO2 beads||Solar||After 420 min illumination by sunlight, 0.65 × 10−4 mol dm−3 of four organophosphorus pesticides can be completely photocatalytically degraded into PO43−.|||
2.4. Environmental impact and treatment cost
As previously stated, there is a very extensive literature (at laboratory and pilot plant scale) on the photocatalytic degradation of organic pollutants in water. However, there are not many works devoted to the study of the impact of the process from an environmental and economic point of view. In this context, the well-known life cycle impact assessment (LCIA) tool has been successfully used to assess the environmental impact of chemical processes. This tool finds the potential impacts associated with the entire life cycle of a product or a process. This methodology has been devised to study and compare processes at the industrial level but can be perfectly used at the laboratory level. On the other hand, there are several methods of estimating the costs of implementing each of the different AOPs. In general, the following items are proposed: (i) facility cost, (ii) project contingency, (iii) engineering project and (iv) replacement costs. The sum of these four concepts is the total installed cost, based on which the yearly economic impact can be evaluated. Then, operating costs have to be calculated. These costs are normally yearly and consist of the following items: (i) personnel, (ii) maintenance, (iii) electricity and (iv) materials and services. These costs added to the annual facility costs are the total annual costs .
Currently, population growth, technology development, inadequate agricultural practices and land use have created unprecedented water pollution problems. Agricultural wastewater is characterised by high organic matter content and traces of organic pollutants, mainly pesticides. In addition, effluents from the agro-food and other industries have a potentially environmental risk that requires appropriate and comprehensive treatment. The most often used methods for the treatment of the industrial wastewaters, including membrane filtration, chemical coagulation/flocculation, ion exchange, precipitation, adsorption, biological degradation and ozonation, are not efficient enough and have important limitations to remove bio-recalcitrant compounds as many pesticides. In recent years, advanced oxidation processes (AOPs) have been proposed as a most promising way for degradation of various pollutants. Among them, heterogeneous photocatalysis technology is an interesting route among AOPs, which can be conveniently used for the complete degradation of different hazardous compounds including pesticides. Results show that sunlight photoalteration processes are well now to play an important role in the degradation of pesticides and other contaminants in water. These technologies allow pesticides to be removed by mineralisation. Photocatalytic oxidation by semiconductor oxides is an area of environmental interest for the treatment of polluted water, particularly relevant for Mediterranean agricultural areas, where solar irradiation is highly available (more than 2800 h of sunshine per year on average) making this process quite attractive. Due to its specific characteristics, titanium dioxide (TiO2) has been demonstrated to be an excellent catalyst, and its behaviour is very well documented for the photodegradation of pesticide residues in water. Recently, many authors have also developed combined AOP and biological systems to implement in wastewater treatment plants. In addition to the experimental and modelling work, the aspect most lacking of this combination systems for the treatment of bio-recalcitrant specific industrial wastewater is the performance of complete economic studies, which could present this innovative technology as a cost-competitive one.
The authors acknowledge the financial support received from the European Commission through the LIFE+ program (LIFE 13 ENV/ES/000488) and the EU’s funding instrument for the environment and climate action.
|POPs||Persistent organic pollutants|
|EWFD||European Water Framework Directive|
|AOPs||Advanced oxidation processes|
|SEM||Scanning electron microscopy|
|BET||Brunauer, Emmett and Teller|
|PZC||Point of zero charge|
|TOC||Total organic matter|
|DOM||Dissolved organic matter|
|TOF||Time of flight|
|JCR||Journal Citation Reports|
|LCIA||Life cycle impact assessment|
|ISSN||International Standard Serial Number|
|5Y-IF||5-year impact factor|