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Asian Transactions on Basic and Applied Sciences (ATBAS ISSN: 2221-4291) Volume 03 Issue 02<strong>Study</strong> <strong>the</strong> <strong>Photodegradation</strong> <strong>of</strong> <strong>Anil<strong>in</strong>e</strong> <strong>Blue</strong> <strong>dye</strong><strong>in</strong> <strong>aqueous</strong> <strong>Phase</strong> by us<strong>in</strong>g DifferentPhotocatalystsHanaa Kadtem Egzar, Muthana Saleh Mashkour and Amer Muosa JudaChemistry Department, College <strong>of</strong> Science,Kufa University, Najaf, Iraq.Abstract-- This study <strong>in</strong>volves <strong>the</strong> photocatalytic degradation <strong>of</strong><strong>Anil<strong>in</strong>e</strong> blue(AB) <strong>dye</strong>, employ<strong>in</strong>g heterogeneous photocatalyticprocess. Photocatalytic activity <strong>of</strong> different semiconductors suchas z<strong>in</strong>c oxide (ZnO) ,z<strong>in</strong>c sulfide (ZnS) and T<strong>in</strong> dioxide (SnO 2 )has been <strong>in</strong>vestigated. An attempt has been made to study <strong>the</strong>effect <strong>of</strong> process parameters through amount <strong>of</strong> catalyst,concentration <strong>of</strong> <strong>dye</strong>, pH <strong>of</strong> <strong>dye</strong> solution and temperature onphotocatalytic degradation <strong>of</strong> AB solution. The experiments werecarried out by vary<strong>in</strong>g pH (2-12), amount <strong>of</strong> catalyst (0.05–1.5 g),<strong>in</strong>itial concentration <strong>of</strong> <strong>dye</strong> (25–100ppm ) and temperaturerange(293-323)K. The optimum catalyst dose was found to be( 0.1,0.5 g and 1) g\L by us<strong>in</strong>g ZnO ,ZnS and SnO 2 , respectively. In<strong>the</strong> case <strong>of</strong> ZnO and SnO 2 , maximum rate <strong>of</strong> photoreaction <strong>of</strong>AB solution was observed <strong>in</strong> acidic medium at pH 4, whereas <strong>the</strong>degradation <strong>of</strong> AB reached maximum at pH 5 when us<strong>in</strong>g ZnScatalyst . The performance <strong>of</strong> photocatalytic system employ<strong>in</strong>gZnO/UV light was observed to be better than ZnS /UV andSnO 2 /UV system. The complete degradation <strong>of</strong> AB was observedafter 12 m<strong>in</strong> with ZnO, whereas with ZnS, only 75% <strong>dye</strong>degraded and 24.5% with SnO 2 <strong>in</strong> 12 m<strong>in</strong>. Photocatalyticdegradation was found to <strong>in</strong>crease with <strong>in</strong>creas<strong>in</strong>g temperature.Arrhenius plot shows that <strong>the</strong> activation energy is equal to 20.94kJ mol −1 with ZnO, 17.97 kJ mol −1 with ZnS and 14.1 mol −1 withSnO 2 catalyst.Index Term-- Decolorization; Triphenylmethane;<strong>Anil<strong>in</strong>e</strong> blue ; Photocatalysis1. INTRODUCTIONThe treatments <strong>of</strong> <strong>in</strong>dustrial wastewater for <strong>aqueous</strong> wasteeffluents <strong>in</strong>clude different techniques such as biologicaltreatment, reverse osmosis and activated carbon adsorption. (1)These techniques <strong>of</strong>ten utilize potentially hazardous orpollut<strong>in</strong>g materials and even most <strong>of</strong> <strong>the</strong>m are nonbiodegradable.(2) Therefore, <strong>the</strong> development <strong>of</strong> an effectivetreatment technique that can convert pollutants <strong>in</strong>to non-toxicor less harmful materials is highly required.Advanced oxidation processes are <strong>of</strong> ample <strong>in</strong>terestcurrently for <strong>the</strong> effective oxidation <strong>of</strong> a wide variety <strong>of</strong>organics and <strong>dye</strong>s (3) . Advanced Oxidation Processes (AOP)are an attractive alternative for <strong>the</strong> treatment <strong>of</strong> contam<strong>in</strong>atedground, surface, and waste waters conta<strong>in</strong><strong>in</strong>g hardlybiodegradableanthropogenic substances as well as for <strong>the</strong>purification and dis<strong>in</strong>fection <strong>of</strong> dr<strong>in</strong>k<strong>in</strong>g waters (4) .Photocatalysis is a phenomenon that occurs when a reactioncha<strong>in</strong> is tak<strong>in</strong>g place <strong>in</strong> <strong>the</strong> presence <strong>of</strong> light and solid catalyst<strong>in</strong> <strong>the</strong> solution (5) .Photocatalyst is also called photochemical catalyst and <strong>the</strong>function is similar to <strong>the</strong> chlorophyll <strong>in</strong> <strong>the</strong> photosyn<strong>the</strong>sis. Ina photocatalytic system, photo-<strong>in</strong>duced moleculartransformation or reaction takes place at <strong>the</strong> surface <strong>of</strong> catalystFig.(1). The <strong>in</strong>itial step <strong>of</strong> photocatalysis is <strong>the</strong> adsorption <strong>of</strong>photons by a molecule to produce highly reactiveelectronically excited states. The photon needs to have energy<strong>of</strong> (hυ) equal to or more than <strong>the</strong> band gap energy <strong>of</strong> <strong>the</strong>semiconductor. The energy absorbed will cause an electron tobe excited from <strong>the</strong> valence band to <strong>the</strong> conduction band,leav<strong>in</strong>g a positive hole <strong>in</strong> <strong>the</strong> valence band. This movement <strong>of</strong>electrons forms (e-/h+) or negatively chargedelectron/positively charged hole pairs . The positively chargedholes <strong>in</strong> valence band are powerful oxidants, whereas <strong>the</strong>negatively charged electrons <strong>in</strong> conduction band are goodreductants (5) .Fig. 1. Mechanism <strong>of</strong> radical formation reactions dur<strong>in</strong>g photocatalyticprocess as a results <strong>of</strong> photocatalyst excitation with light (6)Follow<strong>in</strong>g are <strong>the</strong> reactions <strong>in</strong>volv<strong>in</strong>g <strong>in</strong> photocatalysis:-Concern<strong>in</strong>g photocatalysis with photocatalyst, electrons <strong>in</strong>conduction band (ecb-) and holes <strong>in</strong> <strong>the</strong> valence band (hvb+) areproduced when <strong>the</strong> catalyst is irradiated with light energyhigher than its band gap energy Ebg(hν>Ebg).TiO2+ hν (UV< 400nm) → TiO2(ecb-+ hvb+) (1)hvb++ H2 O → h + + HO (2)hvb++ HO-→ HOOrganic molecule +hvb+→ oxidation products (4)ecb-+ O2 → O2-(3)(5)May 2013 ATBAS-80314020©Asian Transactions 23


Asian Transactions on Basic and Applied Sciences (ATBAS ISSN: 2221-4291) Volume 03 Issue 02O2-+ h+→ HO2Organic molecule +ecb-reduction products (7)HO , HO2 + organic compounds → degradation products (8)Semiconductor compounds have drawn much attention dur<strong>in</strong>g<strong>the</strong> last few years because <strong>of</strong> <strong>the</strong>ir novel optical and transportproperties which have great potential for many optoelectronicapplications. (7)Among <strong>the</strong> listed semiconductors, TiO 2 has proven to be <strong>the</strong>most suitable for widespread environmental applications. ZnOalso seems to be a suitable photocatalyst but it dissolves <strong>in</strong>acidic solutions it is a semiconductor material for variousphotonic and electrical applications. ZnO shows a unique set<strong>of</strong> physical and chemical properties, such as a wide band gap(3.2 eV), large exaction b<strong>in</strong>d<strong>in</strong>g energy (60 meV) at roomtemperature, radiation hardness (8) .T<strong>in</strong> dioxide (SnO 2 ) is a n-type semiconductor with a largeband gap (Eg = 3.9 eV ) which shows promise for a number <strong>of</strong>applications <strong>in</strong>clud<strong>in</strong>g transparent conductors.Z<strong>in</strong>c sulfide (ZnS) is a wide band gap and direct transitionsemiconductor (9) . Z<strong>in</strong>c sulfide is an important semiconductormaterial with a wide direct band gap Eg = 3.68 eV (10) .Dyes are typically organic compounds that absorblight <strong>in</strong> specific areas <strong>of</strong> <strong>the</strong> visible spectrum. <strong>Anil<strong>in</strong>e</strong> <strong>Blue</strong><strong>dye</strong> it is water soluble <strong>dye</strong> (11) , it is used for dy<strong>in</strong>g wool andcotton directly and widely used <strong>in</strong> <strong>dye</strong> <strong>in</strong>dustries <strong>the</strong>refore itspresence <strong>in</strong> <strong>the</strong> <strong>in</strong>dustrial discharge water also contributes toenvironmental pollution (12) . Due to its stability , it has longresidence time <strong>in</strong> water. (13) Molecular structure <strong>of</strong> <strong>Anil<strong>in</strong>e</strong><strong>Blue</strong> has been illustrated <strong>in</strong> Fig. 2. <strong>Anil<strong>in</strong>e</strong> <strong>Blue</strong>, also calledacid blue 22, ch<strong>in</strong>a blue, soluble blue 3M, and Mar<strong>in</strong>e blue. Itis very soluble <strong>in</strong> water,(6)<strong>in</strong>sulated <strong>in</strong> a wooden box to prevent <strong>the</strong> escape <strong>of</strong> harmfulradiation and m<strong>in</strong>imized temperature fluctuations caused bydraughts.Z<strong>in</strong>c oxide with 99% purity were supplied by Fluka-Garantie, Z<strong>in</strong>c sulfide with 99.3% purity supplied byM.B.LTD Dagenham and T<strong>in</strong> dioxide SnO 2 with 99% puritywas supplied by Fluka-Garantie . <strong>Anil<strong>in</strong>e</strong> blue <strong>dye</strong> (analyticalgrade) was purchased from (RDS-Hannover) and used withoutfur<strong>the</strong>r purification. Solutions were prepared us<strong>in</strong>g doubledistilled water. In all experiments, <strong>the</strong> required amount <strong>of</strong> <strong>the</strong>catalyst was suspended <strong>in</strong> 200 cm 3 <strong>of</strong> <strong>aqueous</strong> solutions <strong>of</strong>AB, us<strong>in</strong>g a magnetic stirrer. At predeterm<strong>in</strong>ed times; 5 cm 3 <strong>of</strong>reaction mixture was collected and centrifuged (3000 rpm, 15m<strong>in</strong>utes) <strong>in</strong> centrifuge. The supernatant was carefully removedby a syr<strong>in</strong>ge with a long pliable needle and centrifuged aga<strong>in</strong>at same speed and for <strong>the</strong> same period <strong>of</strong> time. This secondcentrifugation was found necessary to remove f<strong>in</strong>e particles <strong>of</strong>catalysts. After <strong>the</strong> second centrifugation <strong>the</strong> absorbance at(309, 586) nm <strong>of</strong> <strong>the</strong> supernatants was determ<strong>in</strong>ed us<strong>in</strong>gultraviolet-visible spectrophotometer, type UV-1650pc.P.D.E. <strong>of</strong> AB was followed spectrophotometrically by acomparison <strong>of</strong> <strong>the</strong> absorbance, at specified <strong>in</strong>terval times, witha calibration curve accomplished by measur<strong>in</strong>g <strong>the</strong>absorbance, at(λ max 586) nm, with different concentrations <strong>of</strong><strong>the</strong> <strong>dye</strong> solution.%Decolorization = 100 × (C 0 − C)/C 0where C 0 = <strong>in</strong>itial concentration <strong>of</strong> <strong>dye</strong> solution, C =concentration <strong>of</strong> <strong>dye</strong> solution after photoirradiation. In order todeterm<strong>in</strong>e <strong>the</strong> effect <strong>of</strong> catalyst load<strong>in</strong>g, <strong>the</strong> experiments wereperformed by vary<strong>in</strong>g catalyst concentration from 0.05 to 1.5 gfor <strong>dye</strong> solutions <strong>of</strong> 100ppm at natural pH (5.57). Similarexperiments were carried out by vary<strong>in</strong>g <strong>the</strong> pH <strong>of</strong> <strong>the</strong> solution(pH 2–12) and concentration <strong>of</strong> <strong>dye</strong>(25,50,100 )ppm. <strong>the</strong>reaction temperatures amounted to 293,303,313 and 323K.Fig. 2. structure <strong>of</strong> <strong>Anil<strong>in</strong>e</strong> <strong>Blue</strong> <strong>dye</strong> (14) .<strong>Anil<strong>in</strong>e</strong> <strong>Blue</strong> <strong>dye</strong> is a acidic <strong>dye</strong> belongs to triphenylmethane class <strong>of</strong> <strong>dye</strong> (15) Triphenylmethane <strong>dye</strong>s are those <strong>dye</strong>s<strong>in</strong> which a central carbon atom is bonded to two benzene r<strong>in</strong>gsand one p-qu<strong>in</strong>oid group (chromophore) (16) . The auxochromesare - NH 2 , NR 2 and –OH (17) . Triphenylmethane <strong>dye</strong>s are usedextensively <strong>in</strong> <strong>the</strong> textile <strong>in</strong>dustries for <strong>dye</strong><strong>in</strong>g <strong>of</strong> nylon,polyacrylon nitrile, modified nylon, wool, silk and cotton.3. RESULTS AND DISCUSSION3.1. UV–vis spectra <strong>of</strong> <strong>dye</strong>Results <strong>of</strong> <strong>the</strong> present study clearly show that <strong>the</strong>photocatalytic treatment <strong>of</strong> <strong>aqueous</strong> solution <strong>of</strong> anil<strong>in</strong>e blueunder UV light, leads to decolorization and degradation <strong>of</strong><strong>dye</strong>. Figs.3 to 5 shows <strong>the</strong> typical time dependent UV-Visspectrum <strong>of</strong> AB solution dur<strong>in</strong>g photoirradiation with ZnO,ZnS andSnO 2 respectively. The rate <strong>of</strong> degradation wasrecorded with respect to <strong>the</strong> change <strong>in</strong> <strong>the</strong> <strong>in</strong>tensity <strong>of</strong>absorption peak <strong>in</strong> ultraviolet region and visible region. Theprom<strong>in</strong>ent peaks were observed at λ max (309,586) nm whichdecreased gradually and f<strong>in</strong>ally disappeared <strong>in</strong>dicat<strong>in</strong>g (18) that<strong>the</strong> <strong>dye</strong> had been degraded.2. EXPERIMENTALA homemade photoreactor equipped with a Philips 250W,medium pressure mercury lamp as a source for UV radiation,was used to determ<strong>in</strong>e P.D.E. The reactor was consisted <strong>of</strong>graduated 1000 cm 3 Pyrex glass beaker and a magnetic stirr<strong>in</strong>gsetup. The lamp was positioned perpendicularly above <strong>the</strong>beaker. The distance between <strong>the</strong> lamp and <strong>the</strong> graduatedPyrex glass was 15 cm. The whole photocatalytic reactor wasMay 2013 ATBAS-80314020©Asian Transactions 24


P.D.EAsian Transactions on Basic and Applied Sciences (ATBAS ISSN: 2221-4291) Volume 03 Issue 021009080706050403020100Fig. 3. Time dependent UV-Vis absorption spectra for degradation <strong>of</strong> anil<strong>in</strong>eblue <strong>dye</strong>(100ppm) ,(0.1g) ZnO catalyst, time(m<strong>in</strong>).Fig. 4. Time dependent UV-Vis absorption spectra for degradation <strong>of</strong> anil<strong>in</strong>eblue <strong>dye</strong>(100ppm),(0.5g) ZnS catalyst, time(m<strong>in</strong>).Fig. 5. Time dependent UV-Vis absorption spectra for degradation <strong>of</strong> anil<strong>in</strong>eblue <strong>dye</strong> (100ppm),(1.0g) SnO 2catalyst,time(hours) .3.2 Degradation <strong>of</strong> AB solution Under DifferentExperimental ConditionsDegradation <strong>of</strong> AB solution was <strong>in</strong>vestigated under sevendifferent experimental conditions through UV alone, UV +ZnS, UV + ZnO,UV+ SnO 2 , Dark + ZnS , Dark + ZnO andDark + SnO 2 . Fig.1 depicts <strong>the</strong> photocatalytic degradation <strong>of</strong>AB solution under <strong>the</strong>se experimental conditions. Initiallyblank experiments were performed under UV irradiationwithout addition <strong>of</strong> any catalyst (UV alone) and only 10%degradation was observed after 60m<strong>in</strong>.Fig. 6. Photocatalytic degradation <strong>of</strong> AB <strong>dye</strong> (<strong>dye</strong> <strong>in</strong>itial concentration—100ppm, (0.1g)ZnO,(0.5g)ZnS ,(1g) SnO 2 after 12m<strong>in</strong>.Thereafter <strong>the</strong> adsorption <strong>of</strong> <strong>the</strong> <strong>dye</strong> was observed withboth catalysts, i.e., Dark + ZnS, Dark+ SnO 2 and Dark + ZnO.Only 14.3%, 32% and 7.7respectively adsorption <strong>of</strong> <strong>the</strong> <strong>dye</strong>was seen <strong>in</strong> <strong>the</strong> same time with both catalysts under darkconditions. Then photocatalytic experiments were carried outus<strong>in</strong>g all catalysts at fixed <strong>dye</strong> concentration (100ppm) andcatalyst amount <strong>of</strong> 0.1g <strong>of</strong> ZnO ,0.5g <strong>of</strong> ZnS and1g <strong>of</strong> SnO 2 .When experiments were performed under UV irradiation withZnO as photocatalyst (UV + ZnO), <strong>the</strong> complete degradation<strong>of</strong> <strong>dye</strong> was achieved after 12 m<strong>in</strong>, whereas with ZnS as aphotocatalyst (UV + ZnS), only 75% decolorization <strong>of</strong> ABsolution was observed and only 24.3% byus<strong>in</strong>gSnO 2 <strong>in</strong> <strong>the</strong>same duration. It <strong>in</strong>dicates that ZnO exhibits higherphotocatalytic activity than o<strong>the</strong>r semiconductors for <strong>the</strong>decolorization <strong>of</strong> AB <strong>dye</strong>.3.3Degradation <strong>of</strong> Dye by ZnO, SnO 2 and ZnS asPhotocatalystsThe experiments were carried out to study <strong>the</strong> degradation<strong>of</strong> AB solution employ<strong>in</strong>g ZnO, ZnS , SnO 2 as catalysts underUV light. Various parameters which affect <strong>the</strong> degradationefficiency such as catalyst load<strong>in</strong>g (0.05–1.5 g), pH (2-8),<strong>in</strong>itial concentration <strong>of</strong> <strong>dye</strong> (25–100 ppm), and temperature(293-323)K <strong>of</strong> degradation were assessed under UV light.3.3.1Effect <strong>of</strong> Catalyst weightFigures 7 show <strong>the</strong> effect <strong>of</strong> ZnO, ZnS and SnO 2 catalystamount on <strong>the</strong> degradation <strong>of</strong> AB solution at natural pH. It canbe seen that <strong>in</strong>itial slopes <strong>of</strong> <strong>the</strong> curves <strong>in</strong>crease greatly by<strong>in</strong>creas<strong>in</strong>g catalyst weight from 0.05 to 0.1 g for ZnO , 0.5gfor ZnS, and1g for SnO 2 <strong>the</strong>reafter <strong>the</strong> rate <strong>of</strong> degradationrema<strong>in</strong>s constant or decreases. Fur<strong>the</strong>r <strong>in</strong>crease <strong>in</strong> <strong>the</strong> dose <strong>of</strong>catalyst had no effect on degradation <strong>of</strong> <strong>dye</strong>. Thephotocatalytic destruction <strong>of</strong> o<strong>the</strong>r organic pollutants has alsoexhibited <strong>the</strong> same dependency on catalyst dose . This can beexpla<strong>in</strong>ed on <strong>the</strong> basis that optimum catalyst load<strong>in</strong>g is foundto be dependent on <strong>in</strong>itial solute concentration because with<strong>the</strong> <strong>in</strong>crease <strong>in</strong> catalyst dosage, total active surface area<strong>in</strong>creases, hence availability <strong>of</strong> more active sites on catalystsurface (18) . At <strong>the</strong> same time, due to an <strong>in</strong>crease <strong>in</strong> turbidity <strong>of</strong><strong>the</strong> suspension with high dose <strong>of</strong> photocatalyst, <strong>the</strong>re will bedecrease <strong>in</strong> penetration <strong>of</strong> UV light and hence photoactivatedvolume <strong>of</strong> suspension decreases (19) . Thus it can be concludedMay 2013 ATBAS-80314020©Asian Transactions 25


P.D.EP.D.EAsian Transactions on Basic and Applied Sciences (ATBAS ISSN: 2221-4291) Volume 03 Issue 02that higher dose <strong>of</strong> catalyst may not be useful both <strong>in</strong> view <strong>of</strong>aggregation as well as reduced irradiation field due to lightscatter<strong>in</strong>g (20) .1009080706050403020100ZnOZnS0.05 0.1 0.25 0.5 0.75 1 1.25 1.5weight(Fig. 7. Effect <strong>of</strong> ZnO ,ZnS and SnO 2 dose on degradation efficient <strong>of</strong> AB <strong>dye</strong>(at natural pH(5.57), and <strong>in</strong>itial concentration <strong>of</strong> <strong>dye</strong> 100ppm),after (12m<strong>in</strong>)3.3.2Effect <strong>of</strong> pHWastewater conta<strong>in</strong><strong>in</strong>g <strong>dye</strong>s is discharged at different pH;<strong>the</strong>refore it is important to study <strong>the</strong> role <strong>of</strong> pH on degradation<strong>of</strong> <strong>dye</strong>. In order to study <strong>the</strong> effect <strong>of</strong> pH on <strong>the</strong> degradationefficiency, experiments were carried out at various pH values,rang<strong>in</strong>g from 2 to 12 for constant <strong>dye</strong> concentration (100ppm)and catalyst weight (0.1,0.5 and 1 g, respectively, for ZnO,ZnS and SnO 2 ). Figures 4 show <strong>the</strong> photodegradationefficiency <strong>of</strong> AB solution as a function <strong>of</strong> pH. It has beenobserved that by us<strong>in</strong>g ZnO and SnO 2 , <strong>the</strong> degradationefficiency <strong>in</strong>creases with <strong>in</strong>crease <strong>in</strong> pH exhibit<strong>in</strong>g maximumrate <strong>of</strong> degradation at pH 4. In <strong>the</strong> case <strong>of</strong> ZnS, <strong>the</strong> maximumdegradation was observed at pH 5. Similar behavior has alsobeen reported for <strong>the</strong> photocatalytic efficiency <strong>of</strong> ZnS fordecolorization <strong>of</strong> acid <strong>dye</strong>s. The <strong>in</strong>terpretation <strong>of</strong> pH effectson <strong>the</strong> efficiency <strong>of</strong> <strong>the</strong> photocatalytic degradation process is avery difficult task, because <strong>of</strong> its multiple roles. First, it isrelated to <strong>the</strong> acid base property <strong>of</strong> <strong>the</strong> metal oxide surface andcan be expla<strong>in</strong>ed on <strong>the</strong> basis <strong>of</strong> zero po<strong>in</strong>t charge (21) . Theadsorption <strong>of</strong> water molecules at sacrificial metal sites isfollowed by <strong>the</strong> dissociation <strong>of</strong> OH − charge groups, lead<strong>in</strong>g tocoverage with chemically equivalent metal hydroxyl groups(M-OH) (22) . Due to amphoteric behavior <strong>of</strong> most metalhydroxides, <strong>the</strong> follow<strong>in</strong>g two equilibrium reactions areconsidered (Eqs. 9 and 10).M-OH + H + + M-OH 2(9)M-OH M-O - +H + (10)1008060402002 3 4 5 6 7 8pHFig. 8. Effect <strong>of</strong> pH on degradation rate <strong>of</strong> AB <strong>dye</strong> (ZnO dose—0.1 g, ZnSdose—0.5 g and 1.0gSnO 2 ,<strong>dye</strong> <strong>in</strong>itial concentration100ppm ).The zero po<strong>in</strong>t charge (zpc) for ZnO is 9 and 6.7for ZnS,surface is positively charged below this po<strong>in</strong>t and above thispH, surface is negatively charged by adsorbedOH − ions (23) .photocatalytic activity <strong>of</strong> anionic <strong>dye</strong>s (ma<strong>in</strong>lysulfonated <strong>dye</strong>s) such as AB <strong>dye</strong> reaches a maximum value <strong>in</strong>lower zero po<strong>in</strong>t charge. At pH > zpc, <strong>the</strong> surface is positivelycharged and <strong>the</strong> <strong>dye</strong> is anion (24) . The experimental resultsrevealed that higher degradation <strong>of</strong> AB solution was found tobe <strong>in</strong> acidic conditions. This may be attributed to <strong>the</strong>electrostatic <strong>in</strong>teractions between <strong>the</strong> positive catalyst surfaceand <strong>dye</strong> anions lead<strong>in</strong>g to strong adsorption <strong>of</strong> <strong>the</strong> latter on <strong>the</strong>metal oxide support (25) .3.3.3Effect <strong>of</strong> Concentration <strong>of</strong> DyeAfter optimiz<strong>in</strong>g <strong>the</strong> pH conditions and catalyst dose (pH4 and catalyst dose 0.1 g for ZnO, pH 5 and catalyst dose 0.5 gfor ZnS, pH 4 and catalyst dose 1 g for SnO 2 ), <strong>the</strong>photocatalytic degradation <strong>of</strong> <strong>dye</strong> was carried out by vary<strong>in</strong>g<strong>the</strong> <strong>in</strong>itial concentrations <strong>of</strong> <strong>the</strong> <strong>dye</strong> (25,50, 100) ppm <strong>in</strong> orderto assess <strong>the</strong> appropriate amount <strong>of</strong> catalyst dose. As <strong>the</strong>concentration <strong>of</strong> <strong>the</strong> <strong>dye</strong> was <strong>in</strong>creased, <strong>the</strong> rate <strong>of</strong>photoreaction decreased <strong>in</strong>dicat<strong>in</strong>g for ei<strong>the</strong>r to <strong>in</strong>crease <strong>the</strong>catalyst dose or time span for <strong>the</strong> complete removal. Figure 5depict <strong>the</strong> time-dependent graphs <strong>of</strong> degradation <strong>of</strong> ABsolution at different concentrations <strong>of</strong> <strong>dye</strong> . The possibleexplanation for this behavior is that as <strong>the</strong> <strong>in</strong>itial concentration<strong>of</strong> <strong>the</strong> <strong>dye</strong> <strong>in</strong>creases, <strong>the</strong> path length <strong>of</strong> <strong>the</strong> photons enter<strong>in</strong>g<strong>the</strong> solution decreases and <strong>in</strong> low concentration <strong>the</strong> reverseeffect is observed, <strong>the</strong>reby <strong>in</strong>creas<strong>in</strong>g <strong>the</strong> number <strong>of</strong> photonabsorption by <strong>the</strong> catalyst <strong>in</strong> lower concentration (26,27) .ZnOMay 2013 ATBAS-80314020©Asian Transactions 26


P.D.EAsian Transactions on Basic and Applied Sciences (ATBAS ISSN: 2221-4291) Volume 03 Issue 02100ZnO(0.338232)m<strong>in</strong> -1 , (0.165280)m<strong>in</strong> -1 and (0.017087)m<strong>in</strong> -1 for ZnO, ZnS, and SnO 2 respectively.8060ZnS1412ZnOZnSSnO24020025 50 100Con.(ppFig. 9. Effect <strong>of</strong> <strong>in</strong>itial concentration <strong>of</strong> AB <strong>dye</strong> on photodegradationefficiency when us<strong>in</strong>g (ZnO dose0.1g, pH 4, ZnS dose0.5g and1.0g SnO 2, pH5.57 )3.3.4Effect <strong>of</strong> temperature:The photocatalytic degradation was studied at varioustemperatures <strong>in</strong> <strong>the</strong> range (293–323)K and rate constant, k,was determ<strong>in</strong>ed from <strong>the</strong> first-order plots. An <strong>in</strong>crease <strong>in</strong>temperature helps <strong>the</strong> reaction to compete more efficientlywith e–/H+ recomb<strong>in</strong>ation (28) . The energy <strong>of</strong> activation, Ea,was calculated from <strong>the</strong> Arrhenius plot <strong>of</strong> ln k vs. 1/T (figure10). Arrhenius plot shows that <strong>the</strong> activation energy forphotocatalytic degradation <strong>of</strong> AB solution is equal to 20±1 kJmol-1 ,17±1 and14±1 by us<strong>in</strong>g ZnO ,ZnS and SnO 2respectively. The experimental activation energy wasassociated with <strong>the</strong> energy required to promote photoelectronfrom trapp<strong>in</strong>g centers <strong>in</strong>to t<strong>in</strong> dioxide conduction band. <strong>the</strong>present value probably arises from <strong>the</strong> surface area and <strong>the</strong>purity <strong>of</strong> catalysts (29) .02.9-0.53 3.1 3.2 3.3 3.4 3.5-1-1.5-2-2.5-3-3.5-4-4.5Fig. 10. Arrhenius plot for photocatalytic degradation <strong>of</strong> AB on ZnO , ZnSand SnO 2 catalysts.3.3.5K<strong>in</strong>etic <strong>Study</strong>Figure 11 show <strong>the</strong> k<strong>in</strong>etics <strong>of</strong> disappearance <strong>of</strong> AB foran <strong>in</strong>itial concentration <strong>of</strong> 100ppm under optimizedconditions. The results show that <strong>the</strong> photocatalyticdegradation <strong>of</strong> <strong>dye</strong> <strong>in</strong> <strong>aqueous</strong> ZnO , ZnS and SnO 2 can bedescribed by <strong>the</strong> first-order k<strong>in</strong>etic accord<strong>in</strong>g to <strong>the</strong>Langmuir–H<strong>in</strong>shelwood model (30-32) , ln (C/C 0 ) =- kt, where C 0is <strong>the</strong> <strong>in</strong>itial concentration and C is <strong>the</strong> concentration at anytime, t. The semi-logarithmic plots <strong>of</strong> <strong>the</strong> concentration datagave a straight l<strong>in</strong>e. The rate constants were calculated to beZnOlnCC 010864200 5 10 15 20 25 30Fig. 11. K<strong>in</strong>etics analysis for AB <strong>dye</strong> (<strong>dye</strong> <strong>in</strong>itial concentration100ppm), (0.1gZnO), (0.5g ZnS) , and 1.0gSnO 2.4. CONCLUSIONExperimental results <strong>in</strong>dicated that <strong>the</strong> degradation <strong>of</strong> <strong>dye</strong>is facilitated <strong>in</strong> <strong>the</strong> presence <strong>of</strong> catalyst. Comparison <strong>of</strong>photocatalytic activity <strong>of</strong> different semiconductors has clearly<strong>in</strong>dicated that <strong>the</strong> ZnO is better photocatalyst for degradation<strong>of</strong> AB solution. Besides higher efficiency, <strong>the</strong> o<strong>the</strong>r advantage<strong>of</strong> ZnO is its low cost. The <strong>in</strong>itial rate <strong>of</strong> photodegradation<strong>in</strong>creased with <strong>in</strong>crease <strong>in</strong> catalyst dose up to an optimumload<strong>in</strong>g. Fur<strong>the</strong>r <strong>in</strong>crease <strong>in</strong> catalyst dose showed no effect. As<strong>the</strong> <strong>in</strong>itial concentration <strong>of</strong> <strong>dye</strong>s was <strong>in</strong>creased, <strong>the</strong> rate <strong>of</strong>degradation decreased <strong>in</strong> each semiconductor, Experimentalresults <strong>in</strong>dicated that <strong>the</strong> decolorization <strong>of</strong> <strong>dye</strong>s is facilitated <strong>in</strong><strong>the</strong> presence <strong>of</strong> catalyst and were favorable <strong>in</strong> acidic region,and <strong>the</strong> rate <strong>of</strong> decolorization and degradation <strong>of</strong> anil<strong>in</strong>e bluesolution <strong>in</strong>creases with <strong>the</strong> <strong>in</strong>crease <strong>of</strong> <strong>the</strong> temperature. Thephotocatalytic degradation followed pseudo-first orderk<strong>in</strong>etics.REFERENCE[1] A. S.Erses, , T. T. Onay; 2008.Bioresource Technology;(99):5418,5426[2] J. Lee, E. Kulla , 2008.Physics <strong>of</strong> Fluids; (20): 9[3] B .Boye, M .M .Dieng and E .Brillas , 2002. Env. Sci. & Technol.(36):3030[4] E.Pelizzetti, and M.Schiavello, Eds. 1991.PhotochemicalConversion andStorage <strong>of</strong> Solar Energy. <strong>the</strong>sis, Kluwer AcademicPublishers: Dordrecht.[5] D. Oussi, A. Mokr<strong>in</strong>i, and S. Esplugas, 1997. J. Photochem.Photobiol. A: Chem.; (1):77[6] Karpova, T. and y. Lappeenranta teknill<strong>in</strong>en, 2007. AqueousPhotocatalytic Oxidation <strong>of</strong> Steroid Estrogens. <strong>the</strong>sis,Lappeenranta University <strong>of</strong> Technology.[7] M. Barbeni, , E. Pramauro, E. Pelizzetti, E. Borgarello, N.Serpone; 1985. Chemosphere; ( 14):195,208.[8] D.C. Look, C.Coskun, B.Clafl<strong>in</strong> and G.C. Farlow . 2003. PhysicaB: Condensed Matter.(340):32-38.[9] L. I. Berger, B. P. Pampl<strong>in</strong>, 1993.Properties <strong>of</strong> semiconductors, <strong>in</strong>R. C. Weast (ed.) Handbook <strong>of</strong> Chemistry and Physics, 73rd edn.,CRC Press, Boca Raton, FL, p. 12-78 to 12- 85.[10] K. Sooklal, B.S. Cullumn, S.M. Angel, C.J. Murphy, 1996.J. Phys.Chem.(100):45-51,[11] E.L.Grabowska and Gryglewicz. 2007.Dyes Pigm.;(74):34‐40[12] G.R. Eykholt and D.T. Davenport. 1998.Environ. Sci. Technol.,(32):1482-1487,May 2013 ATBAS-80314020©Asian Transactions 27


Asian Transactions on Basic and Applied Sciences (ATBAS ISSN: 2221-4291) Volume 03 Issue 02[13] B. Pare, A. Soni and V.W. Bhagwat . 2008.Rasayan J. Chem .(1):413-420[14] N. Daneshvar, D. Salari, and A.R. Khataee, J. 2003.Photochem.Photobiol. A.(157):111[15] J. Fabian, H. Hartmann . 1980.Spr<strong>in</strong>ger Verlag, Berl<strong>in</strong>, (12):137.[16] L. M. Canle, A. J. Sataballa, et al. .2005.Journal <strong>of</strong> photochemistryand photobiology A: Chemistry , (175):192-200,[17] I. Sires, E. Guivarch, N. Oturan, and M.A. Oturan. 2008.Chemosphere,(72): 592.[18] S.K. Kansal , M. S<strong>in</strong>gh, and D. Sudc.2006. Studies onphotodegradation <strong>of</strong> two commercial <strong>dye</strong>s <strong>in</strong> <strong>aqueous</strong> phase us<strong>in</strong>gdifferent photocatalysts. Panjab University, Chandigarh, India.[19] S. Lathasree, R. Nageswara, B. Sivasankar, V. Sadasivam, K.Rengaraj.2004.J. Mole. Catal. A: Chem. (223) : 101[20] Nevim San, Arzu Hatipo glu, Gul<strong>in</strong> Koçturk, ZekiyeÇ<strong>in</strong>ar.2001.Journal <strong>of</strong> Photochemistry and Photobiology A:Chemistry (139) : 225–232[21] C.Lizama, J.Freer, J.Baeza, H.D.Mansilla.2002. Catal.Today.,(76):235.[22] A. Akyol, H.C. Yatmaz, M. Bayramoglu.2004. Appl. Catal. B:Environ.,(54):19.[23] S.Sakthivel, B.Neppolian, M.V.Shankar , B.Arab<strong>in</strong>doo,M.Palanichamy, and V.Murugesan.2003. Sol. Energy Mater. Sol.Cells. ,(77):65.[24] W. Stumm, J.J.Morgan .1981. Specific Adsorption <strong>of</strong> Cation onHydrous ɤ-Al 2O 3, Aquatic Chemistry. New York: Wiley.[25] M.A.El Hajj Hassan, L.M.A.Fayoumi, and M.M.El Jamal.2011.journal <strong>of</strong> <strong>the</strong> university <strong>of</strong> chemical technology and melallurgy;(46)4:395-400.[26] R.J. Davis, J.L.Ga<strong>in</strong>er, G.O.Neal, I.W.Wu.1994. Water Environ.Res. ,(66): 50.[27] H. Al-Ekabi, P. De Mayo. 1986. J. Phys. Chem (90) :4075.[28] Mills A and Hunte S L 1977 J. Photochem. & Photobiol. A:Chem.(108): 1[29] F.Husse<strong>in</strong>, M. Obies, & D. Bahnemann.2011.PhotocatalyticDegradation <strong>of</strong> Bismarck Brown R Us<strong>in</strong>g Commercial ZnO andTiO 2, to be published later.[30] Pare B, Jonnalagadda S B, Tomar H., S<strong>in</strong>gh P and Bhagwat V W.2008.Desal<strong>in</strong>ation (232):1-3[31] Sharma S D, Sa<strong>in</strong>i K K, Kant C, Sharma C P and Ja<strong>in</strong> S C. 2008.Applied Catalysis B: Environmental, (84):1- 2.[32] Chiou C, HWu CY and Juang, R S. 2008. Sep Purif Technol., 62:3.May 2013 ATBAS-80314020©Asian Transactions 28

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