Volume 2012, Issue 1 371714
Research Article
Open Access

Photocatalytic Degradation of Pesticides in Natural Water: Effect of Hydrogen Peroxide

Natividad Miguel

Corresponding Author

Natividad Miguel

Department of Chemical Engineering and Environmental Technologies, University of Zaragoza, Pedro Cerbuna 12, 50009 Zaragoza , Spain unizar.es

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María P. Ormad

María P. Ormad

Department of Chemical Engineering and Environmental Technologies, University of Zaragoza, Pedro Cerbuna 12, 50009 Zaragoza , Spain unizar.es

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Rosa Mosteo

Rosa Mosteo

Department of Chemical Engineering and Environmental Technologies, University of Zaragoza, Pedro Cerbuna 12, 50009 Zaragoza , Spain unizar.es

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José L. Ovelleiro

José L. Ovelleiro

Department of Chemical Engineering and Environmental Technologies, University of Zaragoza, Pedro Cerbuna 12, 50009 Zaragoza , Spain unizar.es

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First published: 15 February 2012
Citations: 48
Academic Editor: Jae Sung Lee

Abstract

The aim of this paper is to evaluate the effectiveness of photocatalytic treatment with titanium dioxide in the degradation of 44 organic pesticides analyzed systematically in the Ebro river basin (Spain). The effect of the addition of hydrogen peroxide in this treatment is studied, and a monitoring of effectiveness of photocatalytic processes is carried out by measurements of physical-chemical parameters of water. The application of photocatalytic treatment with 1 g L−1 of TiO2 during 30 minutes achieves an average degradation of the studied pesticides of 48%. Chlorine demand, toxicity, and dissolved organic carbon (DOC) concentration of water are reduced. If hydrogen peroxide is added with a concentration of 10 mM, the average degradation of pesticides increases up to 57%, although chlorine demand and toxicity of water increase while DOC concentration remains unchanged with this treatment. The application of either photocatalytic treatments does not produce variations in the physical-chemical parameters of water, such as pH, conductivity, colour, dissolved oxygen, and hardness. The pesticides which are best degraded by photocatalytic treatments are parathion methyl, chlorpyrifos, α-endosulphan, 3,4-dichloroaniline, 4-isopropylaniline, and dicofol while the worst degraded are HCHs, endosulphan-sulphate, heptachlors epoxide, and 4,4′-dichlorobenzophenone.

1. Introduction

During recent years, numerous organic substances considered to be hazardous have been detected in waters of Ebro river basin (Spain). These substances have been detected in surface and ground waters and they can be considered hazardous substances according to the current legislation because they are toxic, persistent, and bioaccumulative substances.

Pesticides, artificially synthesized substances used to fight pests and improve agricultural production, are especially problematic. These are monitored by the Pesticides Control Network (Ebro river basin), which systematically analyzes 44 organic pesticides in surface waters. These pesticides were selected because of their appearance in lists of hazardous substances and/or their high level of use in Spanish agriculture. The 44 pesticides analyzed in the Ebro river basin are alachlor, aldrin, ametryn, atrazine, chlorfenvinfos, chlorpyrifos, pp′-DDD, op′-DDE, op′-DDT, pp′-DDT, desethylatrazine, 3,4-dichloroaniline, 4,4′-dichlorobenzophenone, dicofol, dieldrin, dimethoate, diuron, α-endosulphan, endosulphan-sulphate, endrin, α-HCH, β-HCH, γ-HCH, δ-HCH, heptachlor, heptachlor epoxide A, heptachlor epoxide B, hexachlorobenzene, isodrin, 4-isopropylaniline, isoproturon, metholachlor, methoxychlor, molinate, parathion methyl, parathion ethyl, prometon, prometryn, propazine, simazine, terbuthylazine, terbutryn, tetradifon, and trifluralin.

Due to the presence of hazardous substances, both natural water used to supply the population and water which is to be reused have to be treated in water treatment plants to ensure that they comply with the minimum criteria established in the current legislation [13].

Water treatments consist of several operations which often do not achieve the removal of hazardous substances or entail other problems deriving from the treatment.

In the case of drinking water production, an important successful development is the possible formation of organic-halogenated compounds, potentially carcinogenic and chlorinated deriving from methane, as reaction products between chlorine (common disinfectant product) and the organic matter in water. The most abundant of these are trihalomethanes (THMs) whose concentration is limited by Spanish Royal Decree 140/2003 at to 100 μg L−1.

The drawbacks in the use of compounds with chlorine, among others, have derived in the research of other alternative treatments for removing pollutants in water treatments. Among these, advanced oxidation processes (AOPs) are based on the generation of reactive oxygen species, which are highly reactive, nonselective, and do not generate toxic byproducts [4, 5]. These species are capable of degrading a substantial number of pollutants by radicalary mechanisms. The generation of these species can be carried out by processes with ozone, hydrogen peroxide, metallic catalysts, UV radiation, and so forth.

One of the most frequently investigated AOPs in recent years is the photocatalytic process. Photocatalysis entail the combination of radiation and catalyst. Both are necessary in order to achieve or accelerate a chemical reaction, and therefore photocatalysis can be defined as the “acceleration of a photoreaction by the presence of a catalyst.”

Catalysts used in these processes are semiconductor metallic oxides materials. The surface of semiconductor metallic oxides provides a place where oxidation-reduction reactions can be started by radiation. Semiconductors have bands associated with energy levels spaced between them. Photoexcitation with energy equal to or greater than that of the gap between the valence and conduction bands moves an electron from the valence band to the conduction band, generating a hole deficient in electrons. The oxidation of an adsorbed molecule can be produced in holes and simultaneously the reduction of another molecule can be produced in the opposite part of the catalyst.

Numerous semiconductor substances have been tried as catalyst in photocatalytic processes. Generally, it is known that titanium dioxide is one of the most effective. Moreover, it has a high stability and photoactivity, low cost, nontoxicity, and solubility. The activation of titanium dioxide is produced with radiation at λ < 387 nm.

As a result of the application of photocatalytic processes based on titanium dioxide, the number of references in the literature in recent decades related to the degradation of toxic and hazardous substances in water can be counted in their thousands. As regards the group of pesticides under study, photocatalytic processes have been applied in several ways and there are many references to the degradation of such pesticides such as triazines [6, 7], organic-phosphorated pesticides [810], alachlor [11, 12], diuron [7, 13], and parathion methyl [14].

The addition of hydrogen peroxide to photocatalytic treatment with titanium dioxide can be used to increase the effectiveness of the latter process because, as hydrogen peroxide is a more powerful oxidant than oxygen, it generates a larger collection of electrons and this avoids the recombination of electron-hole pairs formed in the photocatalytic process. Hydrogen peroxide is an electron acceptor and it can react with electrons in the conduction band and generate radicals.

Similarly, there are several references concerning the removal of pesticides by photocatalytic treatments with hydrogen peroxide, such as the degradation of atrazine, isoproturon, alachlor and diuron [7], organic-phosphorated pesticides [9, 10], and other triazines [15].

However, the results show a big disparity with respect to the effect of hydrogen peroxide. It is sometimes beneficial while at other times it is damaging to the effectiveness of the process. This phenomenon, the effect of hydrogen peroxide in photocatalytic treatments, produces additional drawbacks when complex mixtures of pollutants are used. The damaging effect in the degradation rate is produced by a modification of the catalyst surface by hydrogen peroxide adsorption [16] and the inhibition of generated holes in the valence band and reaction with hydroxyl radicals [17]. When the effect of hydrogen peroxide is beneficial, a substantial consumption of hydrogen peroxide is sometimes necessary in order to obtain only a small increment of the degradation rate.

The aim of this research work is to evaluate the degradation of the 44 pesticides systematically analyzed in the Ebro river by photocatalytic treatment with titanium dioxide and to study the effect of hydrogen peroxide in this treatment. Moreover, a monitoring of the effectiveness of the photocatalytic processes is carried out by measuring the physical-chemical parameters of water.

2. Materials and Methods

2.1. Samples

Samples of natural water from the Ebro river upstream from Zaragoza (Spain) were prepared by fortification with 44 pesticides in concentrations of 500 ng L−1. These 44 organic pesticides, listed in the introduction section, are systematically analysed in surface waters by the Network of Control of Pesticides in the Ebro river basin.

2.2. Sample Characterization

The characterization of the samples was carried out using the parameters shown in Table 1. The equipment used and standard methods applied are detailed below.

Table 1. Parameters, equipment, and standardized methods used for the characterization of samples.
Parameter Equipment Standard method Reference
pH and temperature pH-meter CRISON GLP21 SM 4500-HB [18]
Conductivity Conductivity-meter CRISON Basic30 UNE-EN 27888 : 1994 [19]
Dissolved organic carbon (DOC) concentration Analyzer Shimadzu TOC-VCSH SM 5310B [18]
Chlorine Demand SM 5710B [18]
Turbidity Turbidity-meter Hanna LP2000 ISO 7027: 1999 [20]
Color Multiparametric Photometer Hanna C99 SM 2120B [18]
Dissolved oxygen concentration Multiparametric Photometer Hanna C99 SM 4500-O C [18]
Hydrogen peroxide concentration [21]
Hardness Multiparametric Photometer Hanna C99 SM 2340B [18]
Suspended solids concentration Multiparametric Photometer Hach Lange DR2800 SM 2540D [18]
Phosporous concentration Multiparametric Photometer Hanna C99 SM 4500-P C [18]
Ammonia concentration Multiparametric Photometer Hanna C99 SM 4500-NH3 C [18]
Cyanide concentration Multiparametric Photometer Hanna C99 SM 4500-CN E [18]
Fluoride, chloride, nitrate, phosphate, and sulphate concentration Ionic Chromatographer DIONEX ICS-1000 SM 4110B [18]
Toxicity Toxicity-meter LUMIStox 300 ISO 11348: 1999 [22]
Pesticides Gas chromatographer TRACE2000 and mass spectrometer POLARIS EPA 525.2 [23]

The analysis of the chromatographic conditions of the pesticides is shown in Table 2 and the results of the validation of this analysis in Table 3.

Table 2. Conditions of pesticide analysis.
Gas chromatographer TRACE GC 2000 (Thermo Finnigan)
Column DB5-MS (J&W, 30 m, 0.25 mm, 0.25 μm)
Program of temperatures 90°C (1 min), 20°C min−1, 180°C (1 min), 2°C min−1, 240°C (1 min), 20°C min−1, 310°C (10 min)
Injector temperature 250°C
Injection volume 1 μL, splitless 0.8 min
Carrier gas He (N55), 1 mL min−1
Mass spectrometer POLARIS (Thermo Finnigan)
Ionization energy 70 eV
Acquisition mode Full scan
Mass interval 50–450 amu
Screen speed 1 scan s−1
Acquisition time 32.5 min
Table 3. Results of the methodology validation of the pesticide analysis.
Pesticide Quantification limit (μg L−1) Calibration interval (μg L−1) Validity interval (μg L−1) Recovery interval (%)
Instrumental step Full method Instrumental step Full method
Isoproturon 20 0.030 20–500 0.030–300 75–130 63–110
Diuron 20 0.030 20–500 0.030–300 82–128 70–123
3,4-Dichloroaniline 20 0.030 20–500 0.030–300 88–130 47–106
4-Isopropylaniline 20 0.030 20–500 0.030–300 80–130 60–125
Desethylatrazine 20 0.030 20–500 0.030–300 76–130 80–129
Trifluralin 20 0.015 20–500 0.030–300 70–130 70–127
Dimethoate 20 0.030 50–500 0.030–300 66–124 54–137
Simazine 50 0.030 20–500 0.030–600 75–135 64–127
Prometon 20 0.030 20–500 0.030–300 76–124 0–125
Atrazine 200 0.100 200–5000 0.100–300 78–130 75–127
Propazine 20 0.015 20–500 0.015–300 86–130 73–127
Terbuthylazine 20 0.015 20–500 0.015–300 79–130 83–128
Parathion methyl 50 0.030 50–500 0.030–300 78–139 72–130
Parathion ethyl 20 0.030 20–500 0.030–300 74–122 64–128
Alachlor 20 0.015 20–500 0.015–300 75–125 70–124
Ametryn 20 0.030 20–500 0.030–300 78–130 0–116
Prometryn 20 0.030 20–500 0.030–300 80–120 17–116
Terbutryn 20 0.030 20–500 0.030–300 80–120 13–114
Chlorpyrifos 20 0.015 20–500 0.015–300 75–120 73–116
Chlorfenvinfos 20 0.015 20–500 0.015–300 76–130 70–126
HCHs 20 0.015 20–500 0.015–300 84–124 70–120
Hexachlorobenzene 20 0.030 20–500 0.030–300 70–130 74–136
Heptachlor 20 0.015 20–500 0.015–300 75–130 58–113
Heptachlor epoxide A 20 0.015 20–500 0.015–300 85–125 62–112
Heptachlor epoxide B 20 0.015 20–500 0.015–300 84–130 58–113
Aldrin 20 0.015 20–500 0.015–300 85–125 64–126
4,4′-Dichlorobenzophenone 20 0.015 20–500 0.015–300 75–120 68–126
Isodrin 20 0.015 20–500 0.015–300 85–125 66–120
α-Endosulphan 20 0.015 20–500 0.015–300 70–125 70–93
pp′-DDE 20 0.015 20–500 0.015–300 89–122 64–107
Dieldrin 20 0.015 20–500 0.015–300 70–125 62–120
Endrin 20 0.015 20–500 0.015–300 80–125 74–122
pp′-DDD + op′-DDT 40 0.030 40–1000 0.030–600 79–125 66–139
Endosulphan-sulphate 20 0.015 20–500 0.015–300 83–125 73–126
pp′-DDT 20 0.030 20–500 0.030–300 76–130 50–120
Dicofol 50 0.030 50–500 0.030–300 80–148 63–136
Methoxychlor 20 0.015 20–500 0.015–300 77–126 75–130
Metholachlor 20 0.015 20–500 0.015–300 76–115 73–128
Molinate 20 0.015 20–500 0.015–300 91–130 75–113
Tetradifon 20 0.015 20–500 0.015–300 85–130 70–116

Previously to the analysis of pesticides by GC/MS a solid-liquid extraction was carried out. This extraction consisted of the retention of organic compounds in a solid phase and subsequent elution with an organic solvent.

The extraction was carried out using an AUTOTRACE WorkStation automatic extractor (Zymark). Before extraction, 100 ng L−1 of surrogate compounds used to control the extraction process (simazine-D5, atrazine-D5, and prometryn-D6) were added to the water sample. During solid-liquid extraction, 900 mL of the sample was passed through cartridges containing a solid ENV+ filter (polystyrene divinyl benzene copolymer) (ISOLUTE cartridges, 200 mg 6 mL−1). The pesticides contained in the sample were retained in the solid phase and dried under N2 for 10 minutes. They were then eluted by passing 10 mL of ethyl acetate (SDS for pesticide analysis) through the cartridge, thus facilitating the passage of these compounds from the water phase to an organic phase. The extracts thus obtained were concentrated under a N2 flow until an approximate volume of 1 mL was obtained, after which 3 mL of isooctane was added (SDS for pesticide analysis) in order to carry out a change of solvent. The extract was then concentrated until obtaining an approximate volume of 0.5 mL. Anthracene deuterate (D10, SUPELCO) was added to each extract as an internal standard for subsequent quantification of the pesticides present in the samples. These extracts were analysed by GC/MS.

2.3. Experimental Procedure in Photocatalytic Treatments

The titanium dioxide used in this work was Degussa P25. The tests were carried out with a dose of 1 g L−1, the same as that used in previous studies and determined as optimal in the stages of disinfection [2426]. The TiO2 was added to 1 L of sample to be treated and shaken at 300 rpm to promote contact between the sample and the catalyst and provide oxygen to the reaction medium. The reaction time was 30 minutes.

For tests with hydrogen peroxide, the compound was added to the sample H2O2 30% v/v (Carlo Erba) with a concentration of 10 mM. This same dose has been used and determined as optimal in many research works evaluating the effectiveness of photocatalytic treatment with hydrogen peroxide on the degradation of different compounds, or even on the generation of ROS: degradation of dyes [2730], pesticides [31, 32], antibiotics [33], and ROS production [34]. In these tests, hydrogen peroxide was removed after the treatment.

The UV/VIS radiation source was provided using an ATLAS SUNTEST CPS+/XLS+ solar chamber. This chamber is an instrument equipped with a xenon lamp used for lighting and the ageing of materials. It can be used as simulator of natural sunlight. The chamber also includes an agitation system, a quartz filter, UV radiation, visible light, temperature control. It is equipped with a programmable system for measuring and for regulating the irradiation intensity. The irradiation range of the equipment is from 250 to 785 W m−2 with a wavelength of 300 to 800 nm. The samples were subjected to a radiation intensity from 500 W m−2 which corresponds to 50% of the intensity of natural solar radiation at midday [35].

All the tests were performed in duplicate, using glass beakers of 1 L and with shaking. Moreover, blank tests were carried out.

3. Results and Discussion

The results of the two photocatalytic treatments (TiO2/radiation and TiO2/H2O2/radiation) on the solutions of natural water fortified with the 44 pesticides under study relating to the sample characterization and the removal of pesticides are presented below.

3.1. Sample Characterization

The characterization of the initial sample and the samples treated with the two photocatalytic processes is shown in Table 4.

Table 4. Characterization of samples of surface wáter fortified with pesticides in photocatalytic treatments.
Initial sample
Physical-chemical parameters
pH 8.0 Colour (PCU) 0
Conductivity (μS cm−1) 508 Dissolved oxygen (mg L−1) 9.9
Turbidity (NTU) 69 Hardness (mg CaCO3 L−1) 108
Suspended solids (mg L−1) 27 concentration (mg L−1) 0.15
Phosphorous (mg L−1) 0.8 CN- concentration (mg L−1) 0.002
DOC (mg C L−1) 22 Toxicity (% inhibition) 33.6
Chlorine demand (mg Cl2 L−1) 6.0
Anion concentrations in solution (mg L−1)
Fluorides 0.1 Nitrates 10.8
Chlorides 63.8 Phosphates <0.2
Sulphates 98
Sample after treatment TiO2/radiation
Physical-chemical parameters
pH 8.0 Colour (PCU) 0
Conductivity (μS cm−1) 589 Dissolved oxygen (mg L−1) 6.2
Turbidity (NTU) 54 Hardness (mg CaCO3 L−1) 109
Suspended solids (mg L−1) 7 concentration (mg L−1) 0.15
Phosphorous (mg L−1) 0.4 CN- concentration (mg L−1) 0.0015
DOC (mg C L−1) 14 Toxicity (% inhibition) 18.9
H2O2 concentration (mg L−1) 5 Chlorine demand (mg Cl2 L−1) 1.0
Anion concentrations in solution (mg L−1)
Fluorides <0.1 Nitrates 11.6
Chlorides 66.4 Phosphates <0.2
Sulphates 101.0
Sample after treatment TiO2/H2O2/radiation
Physical-chemical parameters
pH 8.0 Colour (PCU) 0
Conductivity (μS cm−1) 625 Dissolved oxygen (mg L−1) 9.8
Turbidity (NTU) 56 Hardness (mg CaCO3 L−1) 95
Suspended solids (mg L−1) 5 concentration (mg L−1) 0.15
Phosphorous (mg L−1) 0.2 CN- concentration (mg L−1) 0.001
DOC (mg C L−1) 22 Toxicity (% inhibition) 43.3
H2O2 concentration (mg L−1) 0.5 Chlorine demand (mg Cl2 L−1) 55.6
Anion concentrations in solution (mg L−1)
Fluorides <0.1 Nitrates 11.4
Chlorides 65.0 Phosphates <0.2
Sulphates 99.2
The results show the following.
  • (i)

    The application of photocatalytic treatments does not produce significant variations with respect to the initial values of pH, conductivity, color, dissolved oxygen, hardness, ammonium concentration, and concentration of ions in solution.

  • (ii)

    The turbidity of the sample, in both cases, declines slightly, and solids in suspension make it significantly through the chemical oxidation of organic matter produced in the treatment.

  • (iii)

    Chlorine demand in the TiO2/radiation-treated sample is reduced significantly, up to a value of of 1 mg L−1. However, the application of TiO2/H2O2/radiation treatment produces an enormous increase in this parameter. This is possibly due to the various byproducts formed after the application.

  • (iv)

    Regarding the toxicity of treated sample, TiO2/radiation treatment reduces the initial toxicity of the sample to approximately half its initial value. On the other hand, the application of TiO2/H2O2/radiation produces an increase in the initial toxicity, due to the formation of byproducts more toxic than the original. This has occurred in other research works concerning the application of these photocatalytic treatments [14, 3638].

  • (v)

    The COD undergoes no variation through the TiO2/H2O2/radiation treatment while it is reduced by 36% after the application of TiO2/radiation. This suggests the mineralization of organic matter present in the process with hydrogen peroxide [39].

  • (vi)

    Suspended solids are removed by both photocatalytic treatments. This is due to the organic matter present in the water by this advanced oxidation process.

  • (vii)

    Hydrogen peroxide appears after the TiO2/radiation treatment formed as a by-product in photocatalytic reactions. In the case of the TiO2/H2O2/radiation treatment, where it is used initially as a reagent, almost its total consumption is observed.

3.2. Pesticide Removal

Photocatalytic experiments were carried out in duplicate. Table 5 shows the average concentration of each pesticide studied in the initial sample and the final concentration after the photocatalytic treatments. It is worth noting that average concentrations are shown because the variations obtained in these analyses were very low, always below 2%.

Table 5. Concentration of pesticides in samples in photocatalytic treatments.
Pesticide Concentration (ng L−1)
Initial After TiO2/radiation After TiO2/H2O2/radiation
Alachlor 505 253 177
Aldrin 512 230 26
Ametryn 501 225 225
Atrazine 551 358 331
Chlorfenvinfos 492 295 221
Chlorpyrifos 520 104 104
pp′-DDD 510 332 102
op′-DDE 480 288 144
op′-DDT 482 313 96
pp′-DDT 482 386 145
Desethylatrazine 593 385 356
3,4-Dichloroaniline 658 0 0
4,4′-Dichlorobenzophenone 519 493 363
Dicofol 568 57 57
Dieldrin 508 356 356
Dimethoate 608 274 243
Diuron 501 125 125
α-Endosulphan 475 48 0
Endosulphan-sulphate 483 459 435
Endrin 486 243 243
α-HCH 511 109 409
β-HCH 519 441 441
γ-HCH 521 443 417
δ-HCH 504 428 428
Heptachlor 491 246 246
Heptachlor epoxide A 495 347 347
Heptachlor epoxide B 487 341 341
Hexachlorobenzene 503 327 327
Isodrin 516 206 0
4-Isopropylaniline 512 0 0
Isoproturon 521 78 78
Metholachlor 524 262 210
Methoxychlor 519 234 130
Molinate 551 248 165
Parathion ethyl 507 228 228
Parathion methyl 508 51 51
Prometon 492 271 271
Prometryn 489 220 220
Propazine 508 330 305
Simazine 554 305 277
Terbuthylazine 524 262 262
Terbutryn 514 231 206
Tetradifon 493 296 296
Trifluralin 566 255 170

In addition to the photocatalytic treatments, blank tests were carried out. These blank tests were solution of pesticides with titanium dioxide without radiation and with radiation without catalyst. The results obtained are shown in Table 6. Only for some pesticides were degradations different to zero achieved.

Table 6. Degradation of pesticides in blank experiments.
Pesticide Removal by TiO2 Removal by radiation
Trifluralin 0 28
Heptachlor 14 45
Aldrin 20 50
Isodrin 24 55
pp′-DDE 33 46
pp′-DDD + op′-DDT 21 13
pp′-DDT 25 28

As can be observed, some of the studied pesticides can be degraded by TiO2 without radiation and by radiation without TiO2. The degradation of these pesticides by TiO2 only is due to their adsorption in the catalyst. The degradation of these pesticides by radiation only is due to the advanced oxidation process with UV by which hydroxyl radicals are generated.

Table 7 shows the average removal percentages of the pesticides.

Table 7. % Removal of pesticides by photocatalytic treatments.
Group Pesticide Removal after TiO2/radiation (%) Removal after TiO2/H2O2/radiation (%)
Triazines Simazine 45 50
Atrazine 35 40
Propazine 35 40
Terbuthylazine 50 50
Prometon 45 45
Ametryn 55 55
Prometryn 55 55
Terbutryn 55 60
Desethylatrazine 35 40
  
Organic phosphorated Parathion methyl 90 90
Parathion ethyl 55 55
Chlorpyrifos 80 80
Chlorfenvinfos 40 55
Dimethoate 55 60
  
HCHs α-HCH 20 20
β-HCH 15 15
χ-HCH 15 20
δ-HCH 15 15
  
HCB Hexachlorobenzene 35 35
  
Heptachlors Heptachlor 50 50
Heptachlor epoxide A 30 30
Heptachlor epoxide B 30 30
  
Endosulphans α-Endosulphan 90 100
Endosulphan-sulphate 5 10
  
Drins Endrin 50 50
Dieldrin 30 30
Isodrin 60 100
Aldrin 55 95
  
DDTs pp′-DDE 40 70
pp′-DDD + op′-DDT 35 80
pp′-DDT 20 70
  
Anilines 3,4-Dichloroaniline 100 100
4-Isopropylaniline 100 100
  
Ureas Isoproturon 85 85
Diuron 75 75
  
Carbamate Molinate 55 70
  
Nitroderivate Trifluralin 55 70
  
Anilides Alachlor 50 65
Metholachlor 50 60
Methoxychlor 55 75
  
Chlorophenols Tetradiphon 40 40
Dicofol 90 90
  
Chlorinated diphenyl 4,4′-Dichlrobenzophenone 5 30
  
Average 48 57

The photocatalytic treatments achieved an average degradation of 48% by photocatalysis (TiO2/radiation) and 57% by photocatalysis with hydrogen peroxide (TiO2/H2O2/radiation).

The photocatalytic treatments were very effective in the removal of parathion methyl, chlorpyrifos, α-endosulphan, 3,4-dichloroaniline, 4-isopropylaniline, and dicofol. The treatments were less effective in the degradation of HCHs, endosulphan-sulphate, heptachlors epoxide, and 4,4′-dichlorobenzophenone.

As can be seen in Tables 5 and 7, the addition of hydrogen peroxide to the process slightly improves the average percentage of pesticide removal. However, this improvement does not occur for all the pesticides studied. In fact, some of them present the same removal percentages by both photocatalytic treatments. The increase in the average percentage of degradation is due to an improvement in some of the studied pesticides to add hydrogen peroxide. These are some triazines, α-endosulphan, molinate, trifluralin, and anilides, for which removal is improved by 5–20% using hydrogen peroxide; isodrin, aldrin, DDTs, and 4,4′-dichlorobenzophenone, for which removal is improved by 25–50% using hydrogen peroxide.

The degradation percentages of the pesticides in their individual group are as follows.

Triazines The rates of degradation of triazines obtained by the photocatalytic treatments are between 35 and 60%. By photocatalysis, these percentages are from 35 to 55%. Degradation of these pesticides is very similar, 40–60%, when hydrogen peroxide is added to the treatment. Therefore, the addition of this reagent is not compensated for by the increase of the effectiveness in the degradation of triazines by photocatalytic treatment. Among the triazines studied are atrazine and desethylatrazine, the most difficult to degrade by photocatalytic treatments.

Organic Phosphorated The five organic-phosphorated pesticides studied are degraded between 40 and 90% by photocatalytic treatments. The degradation percentages obtained for these pesticides are similar whether or not hydrogen peroxide is added. The degradation of dimethoate and chlorfenvinfos only slightly improves when hydrogen peroxide is added. Methyl parathion and chlorpyrifos are the pesticides that degrade best by photocatalysis (degradation of 80–90%) while chlorfenvinfos is the most difficult organic-phosphorated pesticide to degrade (maximum degradation of 55%).

HCHs and HCB With regard to HCHs, the degradation percentages obtained by the photocatalytic treatments are the lowest. In all cases, adding hydrogen peroxide makes no difference to the degradation percentages obtained so its use is redundant. The HCB is degraded 35% by the photocatalyisis, and the addition of hydrogen peroxide does not produce any improvement.

Heptachlors Degradation rates obtained for the heptachlors are 50% while the heptachlors epoxides are more difficult to degrade (30%). The addition of hydrogen peroxide to the process does not improve the degradation percentages of these pesticides. In case of heptachlors, the blanks experiments show a degradation of 45% by radiation. The photocatalytic treatment does not therefore improve its degradation with respect to radiation only.

Endosulphans Under photocatalysis, α-endosulphan shows almost total degradation while endosulphan-sulphate is practically undegraded by photocatalytic treatments. Both have the same behavior after the addition of hydrogen peroxide, showing an improvement of 5%, although again this small improvement does not compensate for its use.

Drins With regard to these pesticides, it can be seen by these treatments that aldrin and isodrin (isomers between them) are more easily degradable that endrin and dieldrin (isomers between them), especially in the case of using hydrogen peroxide. The rates of degradation of dieldrin and endrin, 50% and 30% respectively, do not improve when adding hydrogen peroxide. In the case of aldrin and isodrin, blank experiments show an important degradation by radiation. Thus radiation and not the photocatalytic treatment is responsible for their degradation. However, the degradation of aldrin and isodrin is noticeably more effective when using hydrogen peroxide treatment, achieving their complete degradation.

DDTs The DDTs studied degrade between 20% and 40% under the photocatalytic treatments. However, similar degradations are achieved in the blank experiments. The degradation could thus occur by the effect of titanium dioxide or radiation only, not by photocatalytic treatment. These degradation rates increase significantly by adding hydrogen peroxide, reaching 70–80%. Therefore, for the DDTs the presence of hydrogen peroxide notably favours their degradation.

Anilines The two studied anilines, 3,4-dichloroaniline and 4-isopropylaniline, are completely degraded by the photocatalytic treatments. Therefore, the use of hydrogen peroxide is not necessary for increasing the effectiveness of the treatment.

Ureas Isoproturon and diuron, the studied pesticides that are derivatives of urea, present high degradation rates under the photocatalytic treatments, being 85% and 75%, respectively. The same percentages are obtained when using hydrogen peroxide, so that its use does not improve the process.

Anilides The three anilides studied also show the same behaviour with photocatalytic treatments, and the addition of hydrogen peroxide produces a slight improvement, from 5% to 20%. Under photocatalysis, the degradation percentages are 50–55%. These percentages increase slightly when hydrogen peroxide is added to the treatment system, achieving rates of 60–75% degradation in this case.

Other Pesticides For the rest of the pesticides under study, molinate, trifluralin, tetradiphon, dicofol, and 4,4′-dichlorobenzophenone, very different degradations are achieved. Molinate and trifluralin are degraded 55% by the photocatalysis and this percentage increases to 70% when hydrogen peroxide is added. Therefore, the use of this reagent represents a significant improvement in the degradation of these two pesticides. In the case of trifluralin, the blank experiment with radiation produced 30% degradation but its removal is greater by photocatalysis. Degradation of dicofol is very effective by the photocatalytic treatment, being 90%. The presence of hydrogen peroxide does not favour degradation in this case. The same applies to tetradiphon, which degrades to a lesser extent (40%), but hydrogen peroxide does not increase the effectiveness of the process. The 4,4′-dichlorobenzophenone is barely degraded at all by photocatalysis but its degradation increases up to 30% when adding hydrogen peroxide to the treatment.

4. Conclusions

After the completion of this study, the following conclusions can be drawn.

  • (i)

    The pesticides most effectively removed by the photocatalytic treatments, reaching yields higher than 80%, are parathion methyl, α-endosulphan, chlorpyrifos, 3,4-dichloroaniline, 4-isopropylaniline, and dicofol. The least degraded, below 30%, are HCHs, endosulphan-sulphate, heptachlors epoxides, and 4,4′-dichlorobenzophenone.

  • (ii)

    Photocatalytic treatment, TiO2/radiation, achieves a partial removal of the studied pesticides of 48%. When hydrogen peroxide is added the average percentage increases to 57%. The addition of hydrogen peroxide improves the degradation of some of the pesticides studied, mainly isodrin, aldrin, DDTs, 4,4′-dichlorobenzophenone, some triazines, molinate, α-endosulphan, trifluralin, and anilides.

  • (iii)

    TiO2/radiation treatment produces a reduction of 36% of the initial COD, 43% of the initial toxicity, and chlorine demand is reduced to 1 mg L−1. The same treatment with hydrogen peroxide produces a large increase in toxicity and chlorine demand of the treated sample and there is no variation in the COD due to the generation of intermediate compounds (no mineralization) that can be more toxic than the original.

  • (iv)

    Both the studied photocatalytic processes produce a reduction of turbidity and of the solids in suspension in the treated samples.

Acknowledgments

The authors wish to thank “MICINN-FEDER” for financing this paper through the project “Regeneración de aguas depuradas mediante procesos de oxidación avanzada (CTM2008-01876/TECNO).”

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