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Photo oxidative degradation of azure-B by sono-photo-Fenton and photo-Fenton reagents
*Corresponding author vaishnave.prahlad@gmail.com (Prahlad Vaishnave),
-
Received: ,
Accepted: ,
This article was originally published by Elsevier and was migrated to Scientific Scholar after the change of Publisher.
Available online 20 April 2012
Peer review under responsibility of King Saud University.
Abstract
A model for the decomposition of azure-B by photo-Fenton reagent in the presence of ultrasound in homogeneous aqueous solution has been described. The photochemical decomposition rate of azure-B is markedly increased in the presence of ultrasound. It is a rather inexpensive reagent for wastewater treatment. The effect of different variables like the concentration of ferric ion, concentration of dye, hydrogen peroxide, pH, light intensity etc. on the reaction rate has been observed. The progress of the sono-photochemical degradation was monitored spectrophotometrically. The optimum sono-photochemical degradation conditions were experimentally determined. The results showed that the dye was completely oxidized and degraded into CO2 and H2O. A suitable tentative mechanism for sono-photochemical bleaching of azure-B by sono-photo-Fenton’s reaction has been proposed.
Keywords
Ultrasonic irradiation
Sono-photo-Fenton reagent
Advanced oxidation process
Sono-photochemical bleaching
Azure-B
1 Introduction
Among the methods aimed at the degradation of pollutants in aqueous solution, much attention has recently been focused on the so-called advanced oxidation processes for water and wastewater decontamination. In these processes, various techniques (e.g., photolysis, photocatalysis, Fenton reaction, sonochemistry, UV-H2O2, UV-O3 and photo-Fenton) are applied to produce reactive species (often, but not always, the hydroxyl radical) with the purpose of inducing the transformation of water dissolved organic pollutants. This treated water may then be used for washing, cooling, irrigation and cleaning purposes, otherwise it is of no use before treatment.
Treatment method using the Fenton reaction (Fenton, 1894), utilizes hydroxyl radicals produced by interaction of H2O2 with ferrous salts-
Decolorization of solution containing a common textile and leather dye using advanced oxidation processes like Fenton, UV/H2O2/O2, UV/H2O2/Fe2+, UV/H2O2/Fe3+ and UV/H2O2/Fe3+/oxalate processes has been studied (Daneshvar and Khataee, 2006; Dutta et al., 2001; Ma et al., 2005; Liou et al., 2004; Prousek et al., 1997; Wu et al., 1998). The photo-Fenton reaction as an effective photochemical process to treat the polluted water was described (Ruppert et al., 1993). The use of photo-Fenton’s reaction for the photochemical bleaching of metanil yellow, fast green FCF and rhodamine-B has been reported (Kumar et al., 2008a,b,c) while the photochemical degradation of p-dichlorobenzene and o-chlorobenzoic acid by photo-Fenton’s reagent has also been reported (Mogra et al., 2002, 2003).
In the present study, the sono-photochemical degradation of azure-B by sono-photo-Fenton’s reagent using visible light has been carried out and the results show that the sono-photo-Fenton’s reagent is a better oxidizing reagent as compared to photo-Fenton’s reagent.
2 Experimental
2.1 Materials and methods
All solutions were prepared in doubly distilled water. Azure-B (Qualigen), FeCl3 (CDH) and H2O2 (30%, Merck), were used. The concentrations of the solutions were 1.0 × 10−3 and 5.0 × 10−3 mol/L for azure-B and FeCl3, respectively. These were used as stock solutions. Sono-photochemical degradation of azure-B was investigated taking 30 mL of total reaction mixture consisting of dye solution, FeCl3 solution and H2O2. The concentration of dye is 1.33 × 10−4 mol/L for sono-photo-Fenton (SPF) and 1.0 × 10−4 mol/L for photo-Fenton (PF), of FeCl3 is 5.0 × 10−4 mol/L for sono-photo-Fenton and 6.67 × 10−4 mol/L for photo-Fenton while H2O2 is 0.5 and 1.5 mL for sono-photo-Fenton and photo-Fenton, respectively, in the reaction mixture. The reaction mixture was exposed to the light (75.5 mW cm−2) by a 200 W tungsten lamp (Sylvania Laxman). The light intensity was measured with a Suryamapi (CEL Model SM 201). In sono-photo-Fenton reaction, the reaction mixture was also exposed to the ultrasound (Systronics Ultrasonic Cleaner-392, Italy), with frequency of 40 kHz. A water filter was used to cut off thermal radiations. pH of the solution was adjusted by the addition of standardized sulfphuric acid and sodium hydroxide solutions and measured with a digital pH meter (Systronics Model 335). The necessary condition for the correct measurement of absorbance is that the solution must be free from any suspension. A G 3 sintered glass crucible was used for filtration to obtain the desired accuracy in measurement of absorbance. λmax of the dye was determined using an ultraviolet–visible spectrophotometer (Systronics Model 106).
3 Results and discussion
The photochemical degradation in the presence of ultrasound of azure-B was observed at λmax = 650 nm. The structure of azure-B has been given in Fig. 1.Structure of azure-B.
The results of a typical run are represented in Fig. 2. It was observed that the absorbance of azure-B solution decreases with increasing time of irradiation; thus, indicating that the dye is consumed. A plot of log (absorbance) against time was linear, following the pseudo-first order kinetics. The rate constant k was calculated from the expression k = 2.303 × slope. The optimum rate constants for these reactions were determined as k1 = 2.99 × 10−3 s−1 for photo-Fenton reaction and k2 = 4.39 × 10−3 s−1 for sono-photo-Fenton reaction. The spectral changes for these reactions have been shown in Figs. 3 and 4.A typical run; photo-Fenton - [azure-B] = 1.0 × 10−4 mol/L, pH = 2.2, [Fe3+] = 6.67 × 10−4 mol/L, H2O2 = 1.5 mL, Llight intensity = 75.5 mW cm−2; sono-photo-Fenton - [azure-B] = 1.33 × 10−4 mol/L, pH = 2.1, [Fe3+] = 5.0 × 10−4 mol/L, H2O2 = 0.5 mL, Llight intensity = 75.5 mW cm−2, Ffrequency = 40 kHz.
Spectral change for photo-Fenton reaction.
Spectral change for sono-photo-Fenton reaction.
3.1 Effect of pH
The effect of pH on the rate of degradation of azure-B was investigated in the pH range 1.5–2.7. The results are reported in Table 1. Photo-Fenton: [Azure-B] = 1.0 × 10−4 mol/L; [Fe3+] = 6.67 × 10−4 mol/L; H2O2 = 1.5 mL; light intensity = 75.5 mW cm−2. Sono-photo-Fenton: [Azure-B] = 1.33 × 10−4 mol/L; [Fe3+] = 5.0 × 10−4 mol/L; H2O2 = 0.5 mL; light intensity = 75.5 mW cm−2; frequency = 40 kHz.
pH
Photo-Fenton k × 103 s−1
Sono-photo-Fenton k × 103 s−1
1.5
0.72
3.19
2.0
0.93
3.51
2.1
1.33
4.39
2.2
2.98
4.21
2.3
1.87
3.87
2.4
1.72
3.51
2.5
1.12
3.19
2.6
0.98
2.83
2.7
0.93
2.34
The degradation of azure-B depends strongly on pH of the reaction medium. The reaction rate increases with increasing pH up to 2.2 and 2.1 in photo-Fenton and sono-photo-Fenton reaction, respectively and then decreases. The hydroxyl radicals are generated in two steps;
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In the reaction between Fe2+ ions with hydrogen peroxide.
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In photochemical reaction of Fe3+ ions and water.
The increase in pH of the medium favors the step (i) where OH− ions are formed along with hydroxyl radicals, whereas protons are generated in step (ii). Thus, it may be concluded that the step (i) dominates over step (ii) at pH below 2.1 and 2.2 in SPF and PF reaction, respectively. However, the retardation of the reaction above pH 2.1 and 2.2 in SPF and PF reaction, respectively, suggests the dominance of step (ii) over step (i).
3.2 Effect of azure-B concentration
Effect of variation of dye concentration on the reaction rate was also studied by taking different concentrations of azure-B solutions. The results are given in Table 2. Photo-Fenton: pH = 2.2; [Fe3+] = 6.67 × 10−4 mol/L; H2O2 = 1.5 mL; light intensity = 75.5 mW cm−2. Sono-photo-Fenton: pH = 2.1; [Fe3+] = 5.0 × 10−4 mol/L; H2O2 = 0.5 mL; light intensity = 75.5 mW cm−2; frequency = 40 kHz.
[Azure-B] × 104 mol/L
Photo-Fenton k × 103 s−1
Sono-photo-Fenton K × 103 s−1
0.33
1.59
1.08
0.67
2.27
1.23
1.0
2.98
2.30
1.33
2.89
4.39
1.67
2.56
3.87
2.0
1.71
2.30
2.33
1.52
1.53
2.67
1.27
0.69
The rate of degradation of the dye was found to increase with increasing concentration of azure-B up to 1.33 × 10−4 and 1.0 × 10−4 mol/L in SPF and PF reaction, respectively. On further increasing its concentration, a sudden decrease in the rate of degradation was observed. On increasing the concentration above 1.33 × 10−4 and 1.0 × 10−4 mol/L in SPF and PF reaction, respectively, the reaction rate was found to decrease. This may be attributed to the fact that as the concentration of azure-B was increased, it may start acting as a filter for the incident light. The larger concentrations of dye azure-B will not permit the desired light intensity to reach the dye molecules in the bulk of the solution.
3.3 Effect of ferric ion concentration
The effect of concentration of Fe3+ ions on the rate of degradation of azure-B was observed by keeping all other factors identical. The results are summarized in Table 3. Photo-Fenton: [Azure-B] = 1.0 × 10−4 mol/L; pH = 2.2; H2O2 = 1.5 mL; light intensity = 75.5 mW cm−2. Sono-photo-Fenton: [Azure-B] = 1.33 × 10−4 mol/L; pH = 2.1; H2O2 = 0.5 mL; light intensity = 75.5 mW cm−2; frequency = 40 kHz.
[Fe3+] × 104 mol/L
Photo-Fenton k × 103 s−1
Sono-photo-Fenton k × 103 s−1
0.83
0.30
1.07
1.67
0.69
1.43
2.50
0.82
2.01
3.33
1.03
2.09
4.17
1.52
2.51
5.00
2.44
4.39
5.83
2.93
2.51
6.67
2.98
2.31
It is clear from the data in the table that in both these cases; sono-photodegradation and photodegradation of the dye, the rate of degradation increases on increasing the concentration of Fe3+ ions up to 6.67 × 10−4 and 5.0 × 10−4 mol/L for PF and SPF, respectively. This may be explained on the basis that with the increase in Fe3+ concentration, there will be an enhanced generation of •OH radicals and as a consequence, the rate of sono-photodegradation and photodegradation increases. However, on increasing the concentration of Fe3+ ions further (in sono-photodegradation), the rate of the reaction was found to decrease. This is because of the fact that Fe3+ ions imparts a yellow color to the solution and at larger concentrations, it may also act as a filter for the incident light. As the concentration of Fe3+3 was increased above its optimum concentration, the rate of the reactions (6) and (7) become very fast. In reaction (6), hydroperoxyl radicals (•OOH) are generated, which consume more amounts of Fe3+ ions in PF but in SPF, an extra reaction (8) also consume Fe3+ ions and hence, Fe3+ ions are less available for reaction (5) and as a result, less •OH radicals are generated. Therefore, the rate of sono-photodegradation and photodegradation also decreases.
3.4 Effect of hydrogen peroxide
The effect of the amount of hydrogen peroxide on the sono-photodegradation and photodegradation of azure-B was also investigated. The results are reported in Table 4. Photo-Fenton: [Azure-B] = 1.0 × 10−4 mol/L; pH = 2.2; [Fe3+] = 6.67 × 10−4 mol/L; light intensity = 75.5 mW cm−2. Sono-photo-Fenton: [Azure-B] = 1.33 × 10−4 mol/L; pH = 2.1; [Fe3+] = 5.0 × 10−4 mol/L; light intensity = 75.5 mW cm−2; frequency = 40 kHz.
H2O2 (mL)
Photo-Fenton k × 103 s−1
Sono-photo-Fenton k × 103 s−1
0.5
1.42
4.39
1.0
1.71
3.29
1.5
2.98
2.59
2.0
1.71
2.36
2.5
1.42
2.22
3.0
1.14
1.56
3.5
0.75
1.41
4.0
0.58
1.11
It was observed that the reaction rate increases on increasing the amount of H2O2, attaining an optimum value of H2O2 at 1.5 mL for PF reaction. It is because of the fact that as the amount of H2O2 was increased above its optimum value (1.5 mL for PF reaction) the rates of the reactions (6) and (9) increase in PF system. Thereafter, the rate of degradation decreases on increasing the amount of hydrogen peroxide more than 0.5 and 1.5 mL for SPF and PF reaction, respectively. From Eq. (9), •OH radicals are consumed rapidly due to availability of more H2O2 molecules. From Eqs. (6) and (9), •OOH radicals are generated in more amounts. This •OOH radical is utilized in Eq. (10) and H+ ions are produced. As a consequence, the rate of sono-photodegradation and photodegradation decreases.
3.5 Effect of light intensity
The effect of light intensity on the sono-photodegradation and photodegradation of azure-B was also investigated. The results obtained are reported in Table 5. Photo-Fenton: [Azure-B] = 1.0 × 10−4 mol/L; pH = 2.2; [Fe3+] = 6.67 × 10−4 mol/L; H2O2 = 1.5 mL. Sono-photo-Fenton: [Azure-B] = 1.33 × 10−4 mol/L; pH = 2.1; [Fe3+] = 5.0 × 10−4 mol/L; H2O2 = 0.5 mL; frequency = 40 kHz.
Light intensity (mW cm−2)
Photo-Fenton k × 103 s−1
Sono-photo-Fenton k × 103 s−1
27.7
1.03
1.97
30.6
1.13
2.26
34.6
1.23
2.63
39.6
1.33
3.15
45.6
1.69
3.29
53.2
2.26
3.51
62.9
2.68
4.29
75.5
2.98
4.39
Plots of the rate constant versus light intensity were linear, which indicate that an increase in the light intensity increases the reaction rate. This may be attributed to the increased number of photons reacting with Fe3+ ions and, as a result, increased numbers of active species, the hydroxyl radicals are formed. Therefore, an overall increase in the rate of reaction was observed.
4 Mechanism
On the basis of experimental observations and the existing literature, a tentative mechanism has been proposed for sono-photodegradation of azure-B with the sono-photo-Fenton (SPF) reagent.
The •OH radicals are consumed in five reactions. They can induce the dissociation of H2O2 into and water or they combine (dimerize) to form H2O2 molecules. They can also induce the dissociation of water and O2. Secondly, these may react with azure-B to give colorless degradation products.
In SPF reaction, •OH radicals are produced in two reactions. The ultrasonic wave can induce the dissociation of H2O into •OH and H•, and H• can induce the dissociation of H2O2 into •OH and water, and this extra generation of •OH radicals enhances the rate of SPF of reaction.
The main advantage of using sono-photo-Fenton’s and/or photo-Fenton’s reagents is the regeneration of the consumed Fe2+ ions on illumination. Each Fe2+ ion can produce many •OH radicals in contrast to the dark Fenton reaction. The process is a cyclic one. It means that the amount of ferrous salt required under SPF and PF conditions is very small as compared to Fenton conditions, where ferrous ions are to be added at regular intervals; otherwise, the reaction will stop after complete conversion of ferrous ions to ferric ions. This is important from an industrial point of view because further separation of ferric ions is not required after wastewater treatment (Zepp et al., 1992; Tao et al., 2005; Collins, 2002; Chen et al., 2002; Ma et al., 2003; Bozzi et al., 2004).
Acknowledgment
The authors are thankful to the Head, Department of Chemistry for providing Laboratory facilities.
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