# Fenton Process Coupled to Ultrasound and UV Light Irradiation for the Oxidation of a Model Pollutant

Authors: Karen E. Barrera-Salgado; Gabriela Ramírez-Robledo; Alberto Álvarez-Gallegos; Carlos A. Pineda-Arellano; Fernando Z. Sierra-Espinosa; J. Alfredo Hernández-Pérez; Susana Silva-Martínez
Journal: Journal of Chemistry
 (2016)

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## Abstract

The Fenton process coupled to photosonolysis (UV light and Us), using Fe2O3 catalyst supported on Al2O3, was used to oxidize a model pollutant like acid green 50 textile dye (AG50). Dye degradation was followed by AG50 concentration decay analyses. It was observed that parameters like iron content on a fixed amount of catalyst supporting material, catalyst annealing temperature, initial dye concentration, and the solution pH influence the overall treatment efficiency. High removal efficiencies of the model pollutant are achieved. The stability and reusability tests of the Fe2O3 catalyst show that the catalyst can be used up to three cycles achieving high discoloration. Thus, this catalyst is highly efficient for the degradation of AG50 in the Fenton process.


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## Body

## 1. Introduction

There is an increasing concern regarding the detrimental effects of textile dyes on the environment because they can be potentially toxic, carcinogenic, and mutagenic [1]. Degradation and mineralization of textile effluents have become of increasing importance in recent years due to the more stringent environmental legislation. Currently, advanced oxidation processes represent a feasible technology since these methods are efficient for the treatment of industrial dyes and organic pollutants in the textile industry wastewater [2]. The Fenton process is amongst these processes and it is a viable option because of its high oxidizing power and its cost/benefit ratio [3]. The Fenton process is a homogeneous advanced oxidation process (AOP) involving the reaction of Fe(II) with hydrogen peroxide, generating hydroxyl radicals. This catalytic reaction is propagated in chain reactions in which the hydroxyl radicals will subsequently attack the organic compounds present in solution [4]. Nevertheless, the homogeneous Fenton process is limited to acidic pH solutions (2.5 < pH < 4.0) [5] generating iron sludge in the neutralization step which requires proper disposal [6]. The heterogeneous Fenton process involves the use of solid Fenton catalyst that would minimize such problems. Several catalyst supporting materials have been synthetized like pillared clay-based catalysts [7], iron-oxide mineral catalysts [8, 9], Fe(II)Fe(III)-layered double hydroxides [10], iron-activated carbon catalyst [11, 12], and Fe(II)/(III)-Al2O3 [13–15], among others. Organic pollutants such as textile dyes [7, 9, 10, 13, 16–18], phenol and related compounds [11, 12, 19, 20], and lignin [21] have been oxidized by the heterogeneous Fenton process.The Fenton process has also been combined with other AOP such as ultrasound [22, 23], UV light [20, 23, 24], UV light and ultrasound [25], TiO2 photocatalysis [26], and ozone [27]. Basturk and Karatas [22] observed that the highest decolorization of an anthraquinone dye was achieved by the sono-Fenton process because of the production of some oxidizing agents as a result of sonication. Ultrasound coupling with the heterogeneous Fenton-like reagent over copper oxide was investigated for the abatement ofp-chlorophenol in aqueous solutions; synergistic effects in the combination of ultrasound-H2O2-catalyst were observed [20]. It was reported that combining the Fenton process with TiO2 photocatalysis [26] and with ozone [27] gave higher removal efficiencies of the organic pollutant than that obtained by the Fenton process alone.The aim of this work is to study the degradation of acid green 50 industrial textile dye by Fenton process, using Fe2O3 catalyst supported on Al2O3, in tandem with ultrasound and UV light irradiation to evaluate the possible beneficial effects on the use of coupled systems. The influences of iron catalyst content, initial dye concentration, and pH of the solution are studied to assess the overall treatment efficiency of the degradation processes in a batch recirculation system. The catalyst stability is also studied.AG50 is a triarylmethane anionic dye (derivative of triphenyl methane). Its molecular structure and chemical formula are depicted in Scheme1.Scheme 1
Molecular structure of the acid green 50 dye.One hundred and forty-two electrons need to be removed from the AG50 dye to achieve conversion into carbon dioxide and mineral acids (mineralization) in the Fenton reaction. This is by considering the notion that the nitrogen atom gets converted into nitrates. Thus, the stoichiometry of AG50 reacting with H2O2 is given by(1)
C
27
H
25
N
2
N
a
O
7
S
2
+
71
H
2
O
2
⟶
27
C
O
2
+
2
H
2
S
O
4
+
N
a
N
O
3
+
H
N
O
3
+
81
H
2
OThe mechanism of hydrogen peroxide activation by iron ions in the homogeneous Fenton process mainly involves the generation of OH• radicals [4, 28]:(2)
F
e
2
+
+
H
2
O
2
⟶
F
e
3
+
+
O
H
-
+
O
H
•Reaction (2) is followed by the subsequent chain reactions(3)
F
e
2
+
+
O
H
•
⟶
F
e
3
+
+
O
H
-
(4)
O
H
•
+
H
2
O
2
⟶
H
2
O
+
O
O
H
•
(5)
F
e
3
+
+
H
2
O
2
⟶
F
e
2
+
+
H
+
+
O
O
H
•
(6)
F
e
3
+
+
R
•
⟶
F
e
2
+
+
R
+
(7)
F
e
3
+
+
O
O
H
•
⟶
F
e
2
+
+
H
+
+
O
2Nevertheless, the formation of a highly reactive iron-oxo complex (the ferryl ion, F
e
I
V
O
2
+) as the oxidative intermediate in the homogeneous Fenton reaction has also been proposed [29]:(8)
F
e
2
+
+
H
2
O
2
⟶
F
e
I
V
O
2
+Thus, a controversy still exists on whether the chemical mechanism involves radical or ferryl ion generation as the active intermediate species. Then, the chemical pathway in the heterogeneous Fenton reaction is less understood. It has been suggested to be through either the adsorption of the H2O2 molecule or the adsorption of the organic compounds onto ≡
F
e
I
I
I sites [30]. Hence, Fe3+ is reduced with the generation of less oxidative OOH• radicals, followed by Fe3+ regeneration with the formation of OH• radicals [7, 8, 12, 30]:(9)
≡
F
e
3
+
+
H
2
O
2
⟶
≡
F
e
2
+
+
O
O
H
•
+
H
+
(10)
≡
F
e
2
+
+
H
2
O
2
⟶
≡
F
e
3
+
+
O
H
-
+
O
H
•where ≡ represents the surface of the catalyst. Also, many other radical reactions can occur similar to those in the homogeneous Fenton reaction [4]. The OH• radical production in the Fenton reaction increases upon UV light illumination [31], reaction (11), and with ultrasound, denoted by )
)
) [22], reactions (12)–(17):(11)
F
e
I
I
I
O
H
2
+
→
h
ν
F
e
2
+
+
O
H
•
(12)
H
2
O
+
)))
⟶
O
H
•
+
H
•with the subsequent chemical reactions(13)
O
H
•
+
H
•
⟶
H
2
O
(14)
H
•
+
O
2
⟶
H
O
2
(15)
2
O
H
•
⟶
H
2
O
2
(16)
O
O
H
•
⟶
H
2
O
2
+
O
2Also, hydroxyl radicals are generated as shown by the following reaction:(17)
H
2
O
2
+
)))
⟶
2
O
H
•Thus, the combination of heterogeneous Fenton process with the ultrasound and UV light irradiation will increase the hydroxyl radical production which will make the treatment process more efficient.


## 2. Material and Methods

### 2.1. Chemicals and Materials

The acid green 50 dye (AG50) was provided by the local textile industry. Hydrogen peroxide (30% w/w), ferrous sulfate, sulfuric acid, sodium hydroxide, and hydrated ferric chloride solutions were purchased from Sigma-Aldrich. All reagents were of analytical grade and were used without further purification. Total iron determination analyses were carried out using standard reagents and standard methods [32]. Soft drink empty cans were used as source of aluminum foil which was used after sulfuric acid treatment [33].


### 2.2. Catalyst Preparation

Catalyst preparation followed the procedure reported elsewhere [13]. Briefly, it consisted of dissolving 1 g of aluminum can bits in 50 mL of sodium hydroxide solution (4 mol L−1) followed by filtration. The filtered solution was mixed with 50 mL of different Fe3+ concentrations in acidic solutions of ferric chloride used as precursor salt under stirring. This step neutralized the solution and formed a brownish aluminum hydroxide gel impregnated with iron. The product was filtered, washed with distilled water repeatedly to remove Na+, Cl−, and S
O
4
2
- ions, dried in an oven at 105°C for 12 h, and ground to powder using an agate mortar. The powders were subjected to calcination at different temperatures for 6 h under air atmosphere.


### 2.3. Procedure

All degradation tests were performed in a batch recirculation sonophotoreactor (250 mL) to investigate the effects of sonolysis (Us), photolysis (UV light), Fenton process, and Fenton process combined with Us and UV irradiation on dye degradation using the immobilized catalyst. An ultrasound probe (21 mm diameter) was dipped into a cooling jacketed stainless steel cell powered by an ultrasonic processor of 20 kHz (60% amplitude, 0.5 cycles, Dr. Hielscher). The experimental temperature of the sonophotoreactor was kept within 27°C ± 3°C. A 15 W UV lamp (cut-off wavelength 352 nm, 41 cm long with 3 cm diameter, Cole Parmer) hosted in a Pyrex jacket illuminated the cylindrical photoreactor. Each experiment was carried out using 100 mg L−1 of Fe2O3 catalyst supported on Al2O3 (with three different iron contents calcined at 500°C and a fix iron load calcined at different temperatures) in a solution containing the desired dye concentration together with the stoichiometric amount of H2O2 at the pH under test (2, 3, 5, and 7). Samples were withdrawn at timed intervals and immediately the absorbance and total organic carbon (TOC) were measured to follow the instantaneous oxidation. Dye concentration was known from a calibration curve using the absorbance of the samples. It is worth mentioning that, by only measuring the wavelength of maximum absorption, there is potential interference of the transformation intermediates that could exhibit absorbtion at the same wavelength as the dye. By doing so, one gets a lower limit for degradation since the dye may be degraded faster.


## 2.1. Chemicals and Materials

The acid green 50 dye (AG50) was provided by the local textile industry. Hydrogen peroxide (30% w/w), ferrous sulfate, sulfuric acid, sodium hydroxide, and hydrated ferric chloride solutions were purchased from Sigma-Aldrich. All reagents were of analytical grade and were used without further purification. Total iron determination analyses were carried out using standard reagents and standard methods [32]. Soft drink empty cans were used as source of aluminum foil which was used after sulfuric acid treatment [33].


## 2.2. Catalyst Preparation

Catalyst preparation followed the procedure reported elsewhere [13]. Briefly, it consisted of dissolving 1 g of aluminum can bits in 50 mL of sodium hydroxide solution (4 mol L−1) followed by filtration. The filtered solution was mixed with 50 mL of different Fe3+ concentrations in acidic solutions of ferric chloride used as precursor salt under stirring. This step neutralized the solution and formed a brownish aluminum hydroxide gel impregnated with iron. The product was filtered, washed with distilled water repeatedly to remove Na+, Cl−, and S
O
4
2
- ions, dried in an oven at 105°C for 12 h, and ground to powder using an agate mortar. The powders were subjected to calcination at different temperatures for 6 h under air atmosphere.


## 2.3. Procedure

All degradation tests were performed in a batch recirculation sonophotoreactor (250 mL) to investigate the effects of sonolysis (Us), photolysis (UV light), Fenton process, and Fenton process combined with Us and UV irradiation on dye degradation using the immobilized catalyst. An ultrasound probe (21 mm diameter) was dipped into a cooling jacketed stainless steel cell powered by an ultrasonic processor of 20 kHz (60% amplitude, 0.5 cycles, Dr. Hielscher). The experimental temperature of the sonophotoreactor was kept within 27°C ± 3°C. A 15 W UV lamp (cut-off wavelength 352 nm, 41 cm long with 3 cm diameter, Cole Parmer) hosted in a Pyrex jacket illuminated the cylindrical photoreactor. Each experiment was carried out using 100 mg L−1 of Fe2O3 catalyst supported on Al2O3 (with three different iron contents calcined at 500°C and a fix iron load calcined at different temperatures) in a solution containing the desired dye concentration together with the stoichiometric amount of H2O2 at the pH under test (2, 3, 5, and 7). Samples were withdrawn at timed intervals and immediately the absorbance and total organic carbon (TOC) were measured to follow the instantaneous oxidation. Dye concentration was known from a calibration curve using the absorbance of the samples. It is worth mentioning that, by only measuring the wavelength of maximum absorption, there is potential interference of the transformation intermediates that could exhibit absorbtion at the same wavelength as the dye. By doing so, one gets a lower limit for degradation since the dye may be degraded faster.


## 3. Results and Discussion

### 3.1. Catalyst Content on Supporting Material

Figure1 shows the discoloration of AG50 (4 × 10−5 mol L−1) over 100 mg L−1 of catalysts annealed at 500°C with different iron contents at pH 2 by the Fenton process using Fe2O3 catalyst; this figure also includes two control experiments: (●) H2O2 at stoichiometry (2.85 × 10−3 mol L−1) and (□) absence of H2O2. Initially, faster discoloration up to 20 min is observed as the iron content on the supporting material increases. Then, no further discoloration is obtained. Negligible discoloration is attained either with H2O2 at stoichiometry or in the absence of H2O2. Figure 2 shows the TOC removal of AG50 (4 × 10−5 mol L−1) at 40 min reaction time as a function of different iron contents during the Fenton reaction (Figure 2(a)) and its combinations (Figure 2(b)) with UV light and ultrasound (Us), using 100 mg L−1 of catalyst annealed at 500°C at pH 2. The two higher iron concentrations report similar TOC abatement in the Fenton process (F). The Fenton process combined with Us and UV light (F + UV + Us) in the presence of 14.4 mg of iron/g shows the highest mineralization of the pollutant. Clearly, the combination of these processes enhances dye degradation compared to the Fenton process when the lower iron content is used. The enhancement of discoloration and TOC abatement is attributed to the generation of radicals such as •OH and OOH• by the catalytic decomposition of hydrogen peroxide by the iron present in the solid catalysts.Figure 1
Degradation of 4 × 10−5 mol L−1 AG50 by the Fenton process using 2.85 × 10−3 mol L−1 H2O2 with different iron content (mg/g Fe2O3) in 100 mg L−1 of catalyst calcined at 500°C (at pH = 2). (●) 0.0, (■) 14.4, (▲) 18.1, (◆) 37.4, and (□) 0.0 without H2O2.Figure 2
TOC removal of AG50 at 40 min reaction time as a function of different iron contents during the Fenton process (F) (a) and its combinations (b) with UV light and ultrasound (Us), using 100 mg L−1 of catalyst (with 14.4 mg of iron/g catalyst).
(a)
(b)The effect of processes such as adsorption, UV light, and ultrasonic irradiation on the discoloration efficiency is reported in Figure3. This figure also presents the performance of Fenton reaction (F) combined with ultrasound (F + Us), UV irradiation (F + UV), and F + UV + Us using 100 mg L−1 of solid catalyst (37.4 mg/g Fe2O3) at pH 2. The ultrasonic irradiation achieved 48% discoloration efficiency, 19% adsorption, and only 10% UV irradiation at 40 min reaction time; in contrast, a colorless solution was obtained at 40 min by the Fenton reaction in tandem with UV + Us. When Fenton process is combined with ultrasound and UV light irradiation, 94% and 85% discoloration efficiency are achieved, respectively. The insert of Figure 3 depicts the initial (continuous line) and final (at 30 min, dashed line) absorbance spectra during dye degradation by F + UV + Us. This finding suggests a structural change of the AG50 textile dye.Figure 3
Normalized color removal of AG50 (4 × 10−5 mol L−1) at pH 2 with 37.4 mg/g catalyst annealed at 500°C using 100 mg L−1 of catalyst load by different processes: (⋄) adsorption, (△) UV light only, (○) Us only, (▲) Fenton reaction (F), (■) F + UV light (UV), (●) F + ultrasound (Us), and (◆) F + UV + Us. The insert shows the absorbance spectra during dye degradation: initial (continuous line) and final at 40 min (dashed line) in the F + UV + Us.These results indicate that when the Fenton process, using solid iron catalyst, is combined with ultrasound and UV light irradiation, the discoloration efficiencies are higher than that obtained by the Fenton process alone. The effect of the ultrasonic irradiation is attributed to (a) transient cavitation that increases the mass transfer of the substrates to the catalyst surface [34, 35], (b) additional production of reactive species such as OH• radicals according to reactions (12) and (17), and (c) the acoustic cavitation that also contributes to the increase in the activity of the catalyst surface area due to the continuous cleaning and chemical activation of the catalyst surface. Thus, more reactant surface area is readily formed for further surface reactions [36].


### 3.2. pH of the Aqueous Solution

The pH in the aqueous system is an important parameter since it affects the catalytic performance and the stability of the catalysts (Fe2O3). The influence of the initial pH on the degradation of AG50 dye using 37.4 mg/g Fe2O3 catalyst by the Fenton reaction combined with UV and Us irradiation is depicted in Figure 4. This figure shows that the discoloration rate increases as the pH decreases and reaches an optimum at initial pH = 2.0. At the initial pH of 2.0, a colorless solution is observed at 40 min; at pH 3.0, 90% of the dye is converted at 40 min reaction time; at pH 5.0, 62%; and at pH 7.0, 17%. One of the drawbacks of the Fenton reaction is the useful pH range (2.5–4.0 [5]). The oxidation potential of •OH is lower at pH 5.0 and pH 7.0 than that at pH 2 and pH 3. At pH > 3, the formation of hydroxyl radicals slows down because of hydrolysis of Fe(III) and Fe3+ precipitation as Fe(OH)3 from the solution. Thus, the efficiency of Fenton oxidation decreases at pH higher than 3. Also, ferric hydroxide formation could decompose H2O2 into O2 and H2O, and consequently the oxidation rate is decreased as a result of the low concentration of hydroxyl radicals [37]. Similar performance in the oxidation of dye solutions using iron-alumina catalyst in the heterogeneous Fenton process was reported [14, 15]. A detrimental effect on decoloration at pH > 3 was found; thus, based on these studies, the alumina-based iron catalysts exhibit higher degradation efficiency in acidic pH.Figure 4
Normalized concentration profile as a function of pH from acid green 50 (4 × 10−5 mol L−1) solutions by Fenton process, using 37.4 mg/g Fe2O3 catalyst, combined with UV and Us irradiation (catalyst annealed at 500°C). ◆ pH 2, ▲ pH 3, ■ pH 5, and ● pH 7.


### 3.3. Influence of Initial Dye Concentration

Figure5 presents the AG50 dye degradation varying the initial concentration of the dye from 4.6 × 10−5 to 39.4 × 10−5mol L−1 (27 to 227 mg L−1) by the Fenton process in tandem with UV light and ultrasonic irradiation. As can be observed in this figure, the discoloration efficiency decreases as the initial dye concentration increases. This can be explained on the basis that higher initial concentrations of H2O2 are required to degrade higher dye concentrations [13]. Thus, the high amount of H2O2 may react with •OH radicals generating H2O and the less oxidative H
O
2
• radicals (see (18)). Another feasible explanation to this phenomenon is that the number of active sites available was decreased by the dye molecules because of their competitive adsorption on the catalyst surface [38]:(18)
H
2
O
2
+
O
H
•
⟶
H
2
O
+
H
O
2
•Figure 5
AG50 dye degradation varying the initial concentration of the dye by the Fenton process using 37.4 mg/g Fe2O3 catalyst in tandem with UV light and ultrasonic irradiation using H2O2 in stoichiometric amounts. (●) 0.39 mmol L−1, (◆) 0.27 mmol L−1, (▲) 9.8 × 10−2 mmol L−1, and (■) 4.6 × 10−2mmol L−1.


### 3.4. Influence of Annealing Temperature

The performance of the catalyst on color removal is slightly influenced by the thermal treatment and particularly by the catalyst calcination temperature adopted, regardless of the treatment process, as shown in Figure6. The combination of the three processes (F-Us-UV) yields better color removal at all catalyst annealing temperatures, followed by F-Us and F.Figure 6
Influence of catalyst thermal treatment on AG50 degradation at 40 min reaction and pH 2 using 100 mg L−1 of catalyst containing 37.4 mg/g Fe2O3: (▲) F, (◆) F-Us, and (●) F-Us-UV.


### 3.5. Catalyst Stability and Reusability

The reusability and stability of the active phase after successive recycling for four times during the Fenton process are shown in Figure7. It is observed that the discoloration efficiencies decrease after each successive cycle (85, 77, 74, and 65%, resp.) which may be attributed to iron leaching. Indeed, 0.55 mg L−1 of iron was lixiviated at the end of the fourth cycle; this represents the 15% of iron leached from the catalyst at 2.7 h of catalyst reuse. Thus, the active phase exhibits good activity and reusability up to three successive cycles. The leaching of iron may be important because excessive concentrations of dissolved iron in the effluent would need an elimination step. Apart from catalyst reuse, typical levels of leached iron during normal operation should be reported.Figure 7
Catalyst reusability during four cycles using 100 mg L−1 of 37.4 mg/g Fe2O3 catalyst calcined at 500°C.


## 3.1. Catalyst Content on Supporting Material

Figure1 shows the discoloration of AG50 (4 × 10−5 mol L−1) over 100 mg L−1 of catalysts annealed at 500°C with different iron contents at pH 2 by the Fenton process using Fe2O3 catalyst; this figure also includes two control experiments: (●) H2O2 at stoichiometry (2.85 × 10−3 mol L−1) and (□) absence of H2O2. Initially, faster discoloration up to 20 min is observed as the iron content on the supporting material increases. Then, no further discoloration is obtained. Negligible discoloration is attained either with H2O2 at stoichiometry or in the absence of H2O2. Figure 2 shows the TOC removal of AG50 (4 × 10−5 mol L−1) at 40 min reaction time as a function of different iron contents during the Fenton reaction (Figure 2(a)) and its combinations (Figure 2(b)) with UV light and ultrasound (Us), using 100 mg L−1 of catalyst annealed at 500°C at pH 2. The two higher iron concentrations report similar TOC abatement in the Fenton process (F). The Fenton process combined with Us and UV light (F + UV + Us) in the presence of 14.4 mg of iron/g shows the highest mineralization of the pollutant. Clearly, the combination of these processes enhances dye degradation compared to the Fenton process when the lower iron content is used. The enhancement of discoloration and TOC abatement is attributed to the generation of radicals such as •OH and OOH• by the catalytic decomposition of hydrogen peroxide by the iron present in the solid catalysts.Figure 1
Degradation of 4 × 10−5 mol L−1 AG50 by the Fenton process using 2.85 × 10−3 mol L−1 H2O2 with different iron content (mg/g Fe2O3) in 100 mg L−1 of catalyst calcined at 500°C (at pH = 2). (●) 0.0, (■) 14.4, (▲) 18.1, (◆) 37.4, and (□) 0.0 without H2O2.Figure 2
TOC removal of AG50 at 40 min reaction time as a function of different iron contents during the Fenton process (F) (a) and its combinations (b) with UV light and ultrasound (Us), using 100 mg L−1 of catalyst (with 14.4 mg of iron/g catalyst).
(a)
(b)The effect of processes such as adsorption, UV light, and ultrasonic irradiation on the discoloration efficiency is reported in Figure3. This figure also presents the performance of Fenton reaction (F) combined with ultrasound (F + Us), UV irradiation (F + UV), and F + UV + Us using 100 mg L−1 of solid catalyst (37.4 mg/g Fe2O3) at pH 2. The ultrasonic irradiation achieved 48% discoloration efficiency, 19% adsorption, and only 10% UV irradiation at 40 min reaction time; in contrast, a colorless solution was obtained at 40 min by the Fenton reaction in tandem with UV + Us. When Fenton process is combined with ultrasound and UV light irradiation, 94% and 85% discoloration efficiency are achieved, respectively. The insert of Figure 3 depicts the initial (continuous line) and final (at 30 min, dashed line) absorbance spectra during dye degradation by F + UV + Us. This finding suggests a structural change of the AG50 textile dye.Figure 3
Normalized color removal of AG50 (4 × 10−5 mol L−1) at pH 2 with 37.4 mg/g catalyst annealed at 500°C using 100 mg L−1 of catalyst load by different processes: (⋄) adsorption, (△) UV light only, (○) Us only, (▲) Fenton reaction (F), (■) F + UV light (UV), (●) F + ultrasound (Us), and (◆) F + UV + Us. The insert shows the absorbance spectra during dye degradation: initial (continuous line) and final at 40 min (dashed line) in the F + UV + Us.These results indicate that when the Fenton process, using solid iron catalyst, is combined with ultrasound and UV light irradiation, the discoloration efficiencies are higher than that obtained by the Fenton process alone. The effect of the ultrasonic irradiation is attributed to (a) transient cavitation that increases the mass transfer of the substrates to the catalyst surface [34, 35], (b) additional production of reactive species such as OH• radicals according to reactions (12) and (17), and (c) the acoustic cavitation that also contributes to the increase in the activity of the catalyst surface area due to the continuous cleaning and chemical activation of the catalyst surface. Thus, more reactant surface area is readily formed for further surface reactions [36].


## 3.2. pH of the Aqueous Solution

The pH in the aqueous system is an important parameter since it affects the catalytic performance and the stability of the catalysts (Fe2O3). The influence of the initial pH on the degradation of AG50 dye using 37.4 mg/g Fe2O3 catalyst by the Fenton reaction combined with UV and Us irradiation is depicted in Figure 4. This figure shows that the discoloration rate increases as the pH decreases and reaches an optimum at initial pH = 2.0. At the initial pH of 2.0, a colorless solution is observed at 40 min; at pH 3.0, 90% of the dye is converted at 40 min reaction time; at pH 5.0, 62%; and at pH 7.0, 17%. One of the drawbacks of the Fenton reaction is the useful pH range (2.5–4.0 [5]). The oxidation potential of •OH is lower at pH 5.0 and pH 7.0 than that at pH 2 and pH 3. At pH > 3, the formation of hydroxyl radicals slows down because of hydrolysis of Fe(III) and Fe3+ precipitation as Fe(OH)3 from the solution. Thus, the efficiency of Fenton oxidation decreases at pH higher than 3. Also, ferric hydroxide formation could decompose H2O2 into O2 and H2O, and consequently the oxidation rate is decreased as a result of the low concentration of hydroxyl radicals [37]. Similar performance in the oxidation of dye solutions using iron-alumina catalyst in the heterogeneous Fenton process was reported [14, 15]. A detrimental effect on decoloration at pH > 3 was found; thus, based on these studies, the alumina-based iron catalysts exhibit higher degradation efficiency in acidic pH.Figure 4
Normalized concentration profile as a function of pH from acid green 50 (4 × 10−5 mol L−1) solutions by Fenton process, using 37.4 mg/g Fe2O3 catalyst, combined with UV and Us irradiation (catalyst annealed at 500°C). ◆ pH 2, ▲ pH 3, ■ pH 5, and ● pH 7.


## 3.3. Influence of Initial Dye Concentration

Figure5 presents the AG50 dye degradation varying the initial concentration of the dye from 4.6 × 10−5 to 39.4 × 10−5mol L−1 (27 to 227 mg L−1) by the Fenton process in tandem with UV light and ultrasonic irradiation. As can be observed in this figure, the discoloration efficiency decreases as the initial dye concentration increases. This can be explained on the basis that higher initial concentrations of H2O2 are required to degrade higher dye concentrations [13]. Thus, the high amount of H2O2 may react with •OH radicals generating H2O and the less oxidative H
O
2
• radicals (see (18)). Another feasible explanation to this phenomenon is that the number of active sites available was decreased by the dye molecules because of their competitive adsorption on the catalyst surface [38]:(18)
H
2
O
2
+
O
H
•
⟶
H
2
O
+
H
O
2
•Figure 5
AG50 dye degradation varying the initial concentration of the dye by the Fenton process using 37.4 mg/g Fe2O3 catalyst in tandem with UV light and ultrasonic irradiation using H2O2 in stoichiometric amounts. (●) 0.39 mmol L−1, (◆) 0.27 mmol L−1, (▲) 9.8 × 10−2 mmol L−1, and (■) 4.6 × 10−2mmol L−1.


## 3.4. Influence of Annealing Temperature

The performance of the catalyst on color removal is slightly influenced by the thermal treatment and particularly by the catalyst calcination temperature adopted, regardless of the treatment process, as shown in Figure6. The combination of the three processes (F-Us-UV) yields better color removal at all catalyst annealing temperatures, followed by F-Us and F.Figure 6
Influence of catalyst thermal treatment on AG50 degradation at 40 min reaction and pH 2 using 100 mg L−1 of catalyst containing 37.4 mg/g Fe2O3: (▲) F, (◆) F-Us, and (●) F-Us-UV.


## 3.5. Catalyst Stability and Reusability

The reusability and stability of the active phase after successive recycling for four times during the Fenton process are shown in Figure7. It is observed that the discoloration efficiencies decrease after each successive cycle (85, 77, 74, and 65%, resp.) which may be attributed to iron leaching. Indeed, 0.55 mg L−1 of iron was lixiviated at the end of the fourth cycle; this represents the 15% of iron leached from the catalyst at 2.7 h of catalyst reuse. Thus, the active phase exhibits good activity and reusability up to three successive cycles. The leaching of iron may be important because excessive concentrations of dissolved iron in the effluent would need an elimination step. Apart from catalyst reuse, typical levels of leached iron during normal operation should be reported.Figure 7
Catalyst reusability during four cycles using 100 mg L−1 of 37.4 mg/g Fe2O3 catalyst calcined at 500°C.


## 4. Conclusions

These results demonstrate that the performance of the Fenton reaction catalyzed by Fe2O3 is improved by its combination with UV light and ultrasonic irradiation, using low iron content on the catalyst which yields high discoloration and mineralization of AG50. Thus, such combination is a promising advanced oxidation technology for the treatment of wastewater containing AG50 textile dye. The pH of the solution is the parameter that influences more the performance of the catalyst compared to the rest of the parameters tested.



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*Source: 4262530-2016-04-19.xml*