Research Journal of Chemical Sciences ______________________________________________ ISSN 2231-606X Vol. 2(10), 75-79, October (2012) Res.J.Chem. Sci. International Science Congress Association 75 Photo-Oxidation Process – Application for Removal of Color from Textile Industry EffluentDeshannavar U.B., Murgod A.A., Golangade M.S., Koli P.B., Banerjee Samyak and Naik N.M. Chemical Engg. Dept., K.L.E. Society’s Dr. M.S. Sheshgiri College of Engineering and Technology, Belgaum, Karnataka, INDIAAvailable online at: www.isca.in Received 25th June 2012, revised 3rd July 2012, accepted 4th July 2012Abstract A series of batch experiments were conducted to investigate the feasibility of hydrogen peroxide (H), a strong oxidizing agent along with lathe turnings as a heterogeneous catalyst in presence of solar irradiation for the decolorization of textile industry effluent. Operating parameters such as pH, H concentration, and catalyst dosage affecting decolorization were investigated and optimal values were determined. A maximum decolorization of 86% was achieved. The results indicate advanced oxidation process (AOP) is one of the promising methods for textile industry effluent decolorization. Keywords: Decolorization, effluent, lathe turnings, textile industry, solar irradiation. Introduction Textile industries use large amounts of water in their production processes and most of it is rejected as effluent. Textile industry effluent comprises of variety of dyes and chemical additives and posses a challenge for textile industry to treat this liquid waste of varying chemical composition, in an eco-friendly manner1,2. Conventional methods for color removal from textile industry effluents are: adsorption by activated carbon, electrochemical treatment, coagulation / flocculation, ozonation, reverse osmosis, membrane filtration, biological treatments and chemical oxidation process3-8. Membrane filtration, adsorption and coagulation / flocculation produce solid waste that requires additional treatment before disposal. Advanced oxidation process (AOP) refers to chemical treatment process designed to remove organic materials in water and effluent by oxidation through reactions with hydroxyl radicals10The objective of AOP is catalytic conversion of a strong oxidizing agent to hydroxyl free radicals which are more effective oxidizing agents in presence of UV or ultrasound. AOP with H as oxidizing agent has gained considerable interest due to its highly oxidative nature11. In the present study, decolorization experiments were conducted in a batch process using a strong oxidizing agent H with iron turnings waste from lathe operations in local machining industry (lathe turnings) as heterogeneous catalyst in presence of solar irradiation. The experimental data were analyzed and reported. Material and MethodsTextile Industry effluent and its characterization: The effluent sample used for the present study was collected from the nearby textile industry and was preserved in the refrigerator at 4C in accordance with the standard methods for the examination of water and effluent. The effluent was characterized in terms of pH, color, turbidity, chemical oxygen demand (COD), biological oxygen demand (BOD), and total dissolved solids (TDS) using standard methods12. The characteristics of the effluent are tabulated in table-1. Table-1 Characteristics of Textile Industry effluent S. No. Characteristics Value 1 COD (mg/l) 1540 2 BOD (mg/l) 770 3 pH 10.75 4 TDS (mg/l) 1990 5 Turbidity (NTU) 23 Experimental: A series of batch experiments were conducted to investigate the feasibility of oxidizing agent H along with lathe turnings as heterogeneous catalyst in presence of solar irradiation. Lathe turnings collected from nearby industry, cleaned to remove dirt, oil and then dried in an oven All batch experiments were conducted on 500 ml of textile industry effluents for a time period of 30 minutes. Samples were collected at 5 minutes interval and oxidation was ceased by adjusting pH of the effluent to 7 using sodium hydroxide (NaOH). The collected samples were centrifuged for half an hour and were analyzed for color using UV-Vis Spectrophotometer according to Method 2120C in standard methods12. The effects of pH, oxidizing agent concentration, catalyst dosage on decolorization of textile industry effluent were further investigated by varying one variable at a time (OVAT) and the optimum values at which the maximum decolrization occurs were obtained. Results and DiscussionHydrogen peroxide effects on color removal: A batch experiment was carried out to investigate hydrogen peroxide effects on decolorization. Figure-1 shows the decolorization Research Journal of Chemical Sciences ___________________________________________________________ ISSN 2231-606XVol. 2(10), 75-79, October (2012) Res. J. Chem. Sci. International Science Congress Association 76 profile at pH value, 3 and H concentration, 20 ml/l. It can be seen that color removal was negligible ( 5%). Several studies have also stated negligible color removal when H alone was used for decolorization13-16. Effect of pH: A series of batch experiments were conducted to investigate the effect of pH on decolorization by maintaining concentration and catalyst (lathe turnings) dosage as 20 ml/l and 2.5 g/l, respectively. pH values were varied in the range of 2 to 6. Figure-2 shows percentage decolorization vs. time at different pH values. It was observed that maximum decolorization of 86% was achieved at pH value, 3 and decolorization decreased with increase in pH. It can be attributed that in alkaline environment, H is unstable and easily decomposes to produce water and oxygen rather than forming hydroxyl radicals. At pH values 4.0, ferrous ions decompose H catalytically yielding hydroxyl radicals most directly. However, at pH values higher than 4.0, ferrous ions easily form ferric ions, which have a tendency to produce ferric hydroxo complexes17. Variation of percentage decolorization with respect to pH is shown in figure-3. A polynomial relationship was established between percentage decolorization and pH for the given range of operating conditions, which is expressed as equation 1. Effect of Hconcentration: Effect of initial concentration of on decolorization was carried out at optimum pH value, 3 and catalyst dosage, 2.5 g/l. H concentrations were varied in the range of 10 to 25 ml/l with an incremental of 5 ml/l. Figure-4 shows the effect of H initial concentration on decolorization. It was observed that decolorization increased with increase in H concentration and maximum decolorization (86%) was achieved at 20 ml/l. It was also observed that when H concentration was raised to 25 ml/l, decolorization decreased which is contributed to the increased concentrations of H. The excess concentration of H will react with hydroxyl radicals that are already present in the solution to form water and oxygen and hence reduction in decolorization15, 18. Variation of percentage decolorization with respect to H concentration is shown in figure-5. It was observed that percentage decolorization varied as 2nd degree polynomial with respect to H concentration. Hence a polynomial relationship was established between percentage decolorization and H concentration for the given range of operating conditions, which is given as equation 2. Effect of catalyst dosage: In order to investigate the effect of catalyst dosage (CD) on decolorization, experiments were conducted at optimum pH value and H concentrations of 3 and 20 ml/l, respectively. Catalyst dosage was varied in the range of 1 to 3 g/l with an incremental of 0.5 g/l. Figure-6 shows the variation of percentage decolorization at different time intervals. Maximum decolorization of 86% was achieved at catalyst dosage of 2.5 g/l. Variation of percentage decolorization with respect to catalyst dosage is shown in figure-7. It was observed from the experimental data that percentage decolorization varied as 3rd degree polynomial with respect to catalyst dosage and hence a polynomial relationship was established for the given range of operating conditions as equation 3. ( ) ( ) ( ) 2442379789041236633(%)tion DecolorizapHpHpH (1) ( ) ( ) 9.107832195162.0(%)tion Decoloriza (2) ( ) ( ) ( ) 25129CD01175CD21110CD18719tionDecoloriza (%) (3) Figure-1 Effect of H alone on decolorization 01020304050Time (min)Decolorization ( Research Journal of Chemical Sciences ___________________________________________________________ ISSN 2231-606XVol. 2(10), 75-79, October (2012) Res. J. Chem. Sci. International Science Congress Association 77 Figure-2 Effect of initial pH on decolorization (H concentration = 20 ml/l, Catalyst dosage = 2.5 g/l)Figure-3 Decolorization vs. pHFigure-4 Effect of initial H concentration on decolorization (pH = 3, Catalyst dosage = 2.5 g/l) 10203040506070809010001020304050Time (min)Decolorization ( ) pH = 2 pH = 3 pH = 4 pH = 5 pH = 6 4050607080901001234567pHDecolorization ( 10203040506070809010001020304050Time (min)Decolorization ( H2O2=10 ml/l H2O2=15 ml/l H2O2=20 ml/l H2O2=25 ml/l Research Journal of Chemical Sciences ___________________________________________________________ ISSN 2231-606XVol. 2(10), 75-79, October (2012) Res. J. Chem. Sci. International Science Congress Association 78 Figure-5 Decolorization vs. H concentration Figure-6 Effect of catalyst dosage on decolorization (pH = 3, H concentration = 20 ml/l)Figure-7 Decolorization vs. catalyst dosage 203040506070809010051015202530concentration (ml/l)Decolorization ( 10203040506070809010001020304050Time (min)Decolorization ( Catalyst =1.0 g/l Catalyst = 1.5 g/l Catalyst = 2.0 g/l Catalyst = 3.0 g/l Catalyst = 2.5 g/l 4050607080901000.511.522.533.5Catalyst Dosage (g/l)Decolorization ( Research Journal of Chemical Sciences ___________________________________________________________ ISSN 2231-606XVol. 2(10), 75-79, October (2012) Res. J. Chem. Sci. International Science Congress Association 79 ConclusionFeasibility of hydrogen peroxide along with lathe turnings in presence of solar irradiation for decolorization of textile industry effluent was investigated by a series of batch experiments. The optimal operating parameters were determined and maximum decolorization of 86% was achieved at pH value, 3, H concentration, 20 ml/l and catalyst dosage, 2.5 g/l. This process was found to be very efficient and economical for textile industry effluent decolorization as it uses lathe turnings an industrial waste as catalyst. The ease in process operation and reuse of catalyst make AOP a promising treatment method for textile waste decolorization. AcknowledgementThe authors of the paper gratefully acknowledge the support and facilities provided by K. L. E. Society’s Dr. M.S. Sheshgiri College of Engineering and Technology, Belgaum - 590008, Karnataka, India in carrying out this work. References1.Shabudeen P.S.S., Study of the removal of malachite green from aqueous solution by using solid agricultural waste, Res. J. Chem. 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