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Journal of Catalysts
Volume 2013 (2013), Article ID 582058, 6 pages
Photocatalytic Degradation of Acid Yellow 36 Using Zinc Oxide Photocatalyst in Aqueous Media
Department of Chemistry, University of Mysore, Manasagangotri, Mysore 570006, India
Received 14 September 2012; Revised 26 December 2012; Accepted 16 January 2013
Academic Editor: David W. Mazyck
Copyright © 2013 Sajjad Khezrianjoo and Hosakere Doddarevanna Revanasiddappa. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
A detailed investigation of photocatalytic degradation of Acid Yellow 36 (AY36) has been carried out in aqueous heterogeneous medium containing ZnO as photocatalyst in a batch reactor. The effects of some parameters such as pH, catalyst loading, and ethanol concentration were examined. Solutions with initial concentration of 50 mg L−1 of dye, within the range of typical concentration in textile wastewaters, were treated at natural pH of 6.93 and catalyst concentration of 1 g L−1 after 180 min irradiation. Investigations on the active species indicated that hydroxyl radicals play the major role in the process. Experiments showed that the most efficient pH on the removal of the dye with photocatalytic degradation process was 8; however, acidic pH was favored for the dark surface adsorption. Electrical energy consumption per order of magnitude for photocatalytic degradation of AY36 has been also determined.
Textile processing industries nowadays are widespread sectors in developing countries. Among the various processes in the textile industry, dyeing process uses large volume of water for dyeing, fixing, and washing processes. The textile industry uses about 10000 different dyes and the worldwide annual production of dyestuffs is over 7 105 tons . Among several classes of textile dyestuffs, the reactive dyes contribute about 50%  of the total market share and the most common group used as chromophore is the azo (70%), followed by anthraquinone . It has been documented that dye loss in wastewaters could vary up to 50% during manufacturing or processing operations . The release of those colored wastewaters in the ecosystem constitutes a dramatic source of pollution which causes these effluents to be toxic and mostly nonbiodegradable. Namely, the coloration is visible even in a very low dye concentration (below 1 mg L−1) [4, 5]. Consequently, technological systems for the removal of organic pollutants such as adsorption on active carbon, reverse osmosis, ion exchange on synthetic adsorbent resins, ozonation, and biological methods were examined . All of them have advantages and drawbacks but these processes have very high operating costs. However, these conventional treatment methods cannot effectively remove the dyes from effluents, so finding an effective technique is necessary .
Recently, an increasing attention has been devoted to developing dye treatment methods from waste stream at its source (ISO 14001, October 1996). An alternative to conventional methods, “advanced oxidation processes” (AOPs) have been developed based on the generation of very reactive species such as hydroxyl radicals. The generated hydroxyl radicals can oxidize a broad range of organic pollutants quickly and non-selectively [7, 8]. Among the (AOPs), heterogeneous photocatalysis appears as an emerging solution to the environmental pollution of aquatic system. This process consists of the nonselective destruction of organic compounds in presence of UV light and photocatalysis systems such as TiO2, ZnO, and CdS . TiO2 has been the dominant semiconductor photocatalyst; the domination of this catalyst can be attributed to its superior photocatalytic oxidation ability and nonphoto-corrosive and nontoxic characteristics . However, the widespread use of TiO2 and platinum catalyst is uneconomic for large-scale water treatment operations. ZnO appears to be a suitable alternative to TiO2 since its photodegradation mechanism has been proven to be similar to that of TiO2 . ZnO has been reported, sometimes, to be more efficient than TiO2; its efficiency has been reported to be particularly noticeable in the advanced oxidation of pulp mill bleaching wastewater , the photooxidation of 2-phenylphenol , and photocatalytic degradation of Acid Violet 7 . The biggest advantage of ZnO in comparison with TiO2 is that it adsorbs over a larger fraction of UV spectrum and the corresponding threshold of ZnO is 425 nm .
AY36 is a water soluble substantive dye and has a vast amount of applications in several industries . Several photocatalytic degradation methods have been attempted to the treatment of this azo dye. Titanium dioxide (Degussa P25)  and photocatalytic membrane reactors (PMRs)  have been used to remove the AY36; meanwhile, degradation of this azo dye with methylene blue immobilized resin Dowex 11 photocatalyst was carried out by Pratibha and Meena . The aim of the present work is to investigate the influence of various parameters on photocatalytic degradation of a monoazo dye, “Acid Yellow 36,” in the presence of ZnO particles, and irradiated by the UV light in a suspended and circulated reactor.
2.1. Reagents and Photocatalytic Reactor
All reagents were used as received without further purification. The Acid Yellow 36 dye C18H14N3NaO3S (CI No. 13065, CAS No. 587-98-4, MW = 375.38) was provided from S.D Fine Chem., India, with purity of 98%. The molecular structure of this dye is shown in Figure 1. ZnO catalyst was obtained from Lobal Chemie, India, the crystal structure of this material was zinc blende; with particle size of 1–5 and purity of 99%. Hydrochloridric acid, sodium hydroxide, and ethanol were of laboratory reagent grade (Merck products). Distilled water was used to prepare the solutions and the experiments were done in ambient temperature.
For the degradation process a circulating photoreactor made of glass with a cube body shape (27 cm length, 20 cm width, and 4 cm height) was used. The 18 watt low-pressure mercury UV lamp (Philips TUV PL-L) was positioned on top of the reactor with 15 cm distance from the surface of solution. The liquid film in the reactor was 19 mm thick. The photocatalytic reactor system was operated in a batch mode and after each experiment the reactor solution was disposed. A pump was circulating the solution from on corner to the opposite corner; in this way, both the well mixing and fluidizing of catalyst particles were provided. The whole reactor body was covered with reflectors of polished aluminum thin layer. Since the photocatalysis is sustained by a ready supply of dissolved oxygen, air was supplied to the four corners of the reactor at constant flow rate using a microair compressor.
2.2. Photocatalytic Experimental Procedure
To perform the experiments, one liter of solution containing 50 mg L−1 of AY36 ( M), which is within the range of typical concentration in textile wastewaters  and a known amount of ZnO concentration, was prepared. The pH was adjusted to the desired value by using a pH meter (Elico LI 127). The experiments were carried out in room temperature. To start the degradation, the solution was transferred to the reactor, and the lamp was switched on. During each experiment, circulation of suspension was maintained to keep suspension homogenous. Samples (5 mL) were taken at regular time intervals and then centrifuged to separate the ZnO particles from the samples. Analyses were performed with UV-Vis spectrophotometer (Systronics 168) provided with 1 cm matched quartz cells. The degradation efficiency or conversion (X) of AY36 with respect to its initial concentration at any time can be obtained by where and are its initial and concentration at a given time.
3. Results and Discussion
3.1. Effect of UV Irradiation and ZnO Particles
Figure 2 demonstrates the enhancement of AY36 photodegradation in the presence of ZnO particles. In the presence of ZnO, about 97% of dye degrades in an irradiation time of 180 min; under its natural pH (6.93). This was contrasted with 3.1% decolorization for the same experiment performed without ZnO (photolysis). These experiments demonstrated that both UV light and a photocatalyst were needed for the effective destruction of AY36.
The more activity of the UV/ZnO process is due to the well-known electron promotion from the valance band to the conduction band of the semiconducting oxide to give electron-hole pairs [17, 18]. The valance band hole () potential is positive enough to generate hydroxyl radicals at the surface; also, they can react with the adsorbed dye molecules. The conduction band electron () is negative enough to reduce the oxygen molecules present in the solution. The hydroxyl radical is an extremely strong, nonselective oxidant ( = +3.06 V) which leads to the partial or complete degradation of several organic chemicals. The simplified notional mechanism of photocatalytic degradation of pollutions white zinc oxide photocatalyst is described as follows [17, 18]: Subscript “ads” refers to species adsorbed on the surface of catalyst.
3.2. UV-Vis Spectra Changes
AY36 is a monoazo dye in which the chromophore part of molecular structure contains azo linkage. Azo bond is most active in this dye and it can be decomposed by positive holes and hydroxyl radicals . Figure 3 shows the changes in the optical densities at 450 nm and at 330 nm of AY36 in different irradiation times under natural pH of 6.93 and ZnO concentration of 1 g L−1. The decrease of absorption peak at λ = 450 nm relating to the –N=N– double bond of the azo dye reveals AY36 decolorization in the presence of ZnO suspension after about 180 min. However, the degradation of aromatic part of the dye molecule at λ = 330 nm takes more time.
3.3. Effect of Catalyst Concentration
For economic removal of dye effluent from wastewater, it is necessary to find the optimum amount of catalyst for efficient degradation. The influence of ZnO concentration on the degradation is shown in Figure 4. The photodegradation efficiency increases with the increase in the amount of photocatalyst until about 1 g L−1 and then decreases moderately. Increase in the number of ZnO particles increases the active site of the catalyst. This cause an enhancement in the hydroxyl radical generation; meanwhile, the greater number of the dye molecules could be adsorbed on catalyst surface. On the other hand, adding extra catalyst particles lead to an opacity enhancement which in turn would provide reductions in the light intensity throughout the solution .
3.4. Effect of pH
An important operational parameter in wastewater treatments is pH. Figure 5 demonstrates the photocatalytic degradation of AY36 at different pH values. The maximum degradation (98%) was observed at pH 8 after 120 min of irradiation. In alkaline solutions photodegradation efficiency was more than that in acidic solutions. It can be due to more efficient formation of hydroxyl radicals in alkaline solution  and photodecomposition of ZnO in acidic solutions . The dissolution mechanism of ZnO due to a classical chemical process has been demonstrated in the literature .
On the other hand, adsorption of AY36 molecules on the catalyst surface can affect the degradation efficiency. To study the influence of substrate adsorption on the catalyst particles surface, a series of experiments was carried out while the UV light was absent; results are presented in Figure 6. Since the zero point charge (pHzpc) of ZnO particles is , catalyst surface is positively charged in acidic media (pH < 9) whereas it is negatively charged under alkaline condition (pH > 9). Meanwhile, AY36 has a sulfuric group in its structure, which is negatively charged; therefore, dye cannot be adsorbed on photocatalyst surface effectively in the alkaline solution (pH ≥ 9). Maximum amount of dye adsorption on the catalyst surface was observed in the pH of 4.
3.5. The Role of Different Active Species
It is well known that in the photocatalytic degradation process two main species have the major contributions; electrons and holes (, ) and hydroxyl radicals. In order to evaluate these two paths, experiments were performed by adding different amounts of ethanol to the solution. Alcohols such as ethanol are commonly used to quench hydroxyl radicals . The rate constant of reaction between hydroxyl radicals and ethanol is 1.9 × 109 M−1 s−1, which is significantly high . As it is observed from Figure 7, adding small amounts of ethanol, up to 0.3% (v/v), decreases the degradation efficiency of AY36. On the other hand, adding extra amount of ethanol leads to a mild increase in the process efficiency due to the formation of ethoxy radicals (C2H5O•) from direct photocatalytic oxidation of ethanol; meanwhile, the ethanol molecules can produce hydroxyl radicals in direct photolysis with respect to the level of C–O energy bond .
From data given in Figure 7, the contribution of hydroxyl radicals and electron holes in the photocatalytic degradation process at different times is determined and compared in Figure 8. As it can be seen in this figure, hydroxyl radicals play a major role in photocatalytic degradation of AY36 in all the times. Another species involved which does not react with alcohols is most probably the positive holes () formed on the irradiated photocatalyst, which react with the adsorbed dye molecules.
3.6. Electrical Energy Efficiency
The effect of light intensity on the photoconversion efficiency is an interesting approach to simulate a real utilization condition. Recently, the determination of the electrical energy by order of magnitude was recommended by the IUPAC as a figure of merit of the photocatalytic system. is defined as the number of kW/h required to remove the concentration of pollutant by one order of magnitude (90%) in 1 m3 of contaminated water. Equation (8) can be used to calculate the UV dose; also, the value of was obtained using (9) from the energy dose (kWh m−3) versus inverse of the slope of a plot of [16, 22]: where and are the initial and final AY36 concentrations. Since, at natural pH of 6.93 and catalyst concentration of 1 g L−1, the required time for 90% decolorization of the one liter of solution containing 50 mg L−1of AY36 was 122 min, the value has been determined as 36.6 kWh m−3. However, at pH of 8, the required time for 90% decolorization of the one liter of solution containing 50 mg L−1of AY36 in presence of 1 g L−1 of catalyst was 93 min; thus, the value has been determined as 27.9 kWh m−3.
Effective photocatalytic degradation of the monoazo dye Acid Yellow 36 (AY36) is available in ZnO catalyst suspended aqueous solutions and during short times of UV irradiation when compared with only photo-degradation process. We learned that optimal amount of photocatalyst was 1 g L−1, with dye concentration of 50 mg L−1. The most efficient pH for the photocatalytic decomposition of AY36 was 8, and zinc oxide cannot be used in acidic solution (pH 4) as a photocatalyst; however, the maximum amount of dark surface adsorption was observed at pH of 4. As our results showed that ethanol inhibited the photodegradation of dye, we concluded from the inhibitory effect of ethanol that hydroxyl radicals play a major role in photocatalytic degradation of AY36 in all the times. The complete removal of color, after selection of optimal concentration of catalyst (1 g L−1), could be achieved in a relatively short time of about 120 min at pH of 8.
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