Indian Journal of Chemical Technology Vol. 18, May 2011, pp. 169-176 Solar photocatalytic detoxification of cyanide with bacterial disinfection by oxide ceramics C Karunakaran*, P Gomathisankar & G Manikandan Department of Chemistry, Annamalai University, Annamalainagar 608 002, India Received 8 June 2010; accepted 1 March 2011 Under natural sunlight (975±25 Wm-2), CeO2 catalyzes the oxidation of cyanide to cyanate in alkaline medium and the photokinetic behaviour of the reaction is similar to those on TiO2 and ZnO surfaces; the oxidation follows the LangmuirHinshelwood kinetics on cyanide ion, and depends on the area of the catalyst bed and dissolved oxygen. However, the adsorption of cyanide on the oxides in dark is too small to be measured analytically and detected spectroscopically. Although the photocatalytic efficiencies under identical solar irradiance are of the order: CeO2 < ZnO < TiO2, which is in accordance with the charge-transfer resistance and capacitance of the oxides, CeO2 and ZnO show bactericidal activity as well. At a loading of 0.8 gL-1 they inactivate 40 and 44% of 2.5 × 1012 CFU mL-1 E. coli in 30 min even without direct light. Keywords: Photocatalysis, Semiconductor, Charge-transfer resistance, Capacitance, Bactericidal activity Cyanide ion is a highly toxic pollutant and originates from electroplating and metal finishing shops. Although dissolved cyanide can be removed by physical, chemical and biological methods, the physical methods involve only transfer cyanide to another phase. The very slow biodegradation is limited to low concentration of cyanide and encounters the difficulty of disposal of activated sludge. Alkaline chlorination is the best available chemical method but the limitations are the formation of highly toxic cyanogen chloride gas and the leftover complex metal cyanide in sludge. A promising method of detoxification of cyanide is a photocatalytic one and reports on TiO2 or ZnOcatalyzed oxidation of cyanide with artificial UV light are many1-5. Illumination of nanocrystalline semiconductor with light of energy not less than the band gap generates electron-hole pairs, electrons in the conduction band and holes in the valence band6,7. Some of these pairs diffuse to the crystal surface and react with the adsorbed electron donors and acceptors resulting in photocatalysis. The hole oxidizes the substrates and the adsorbed oxygen molecule accepts the electron and transforms into highly active superoxide radical (O2•–). In presence of moisture, O2•– generates reactive species like HO•, HO2•, and H2O2, which act as oxidants. Water is adsorbed on the semiconductor surface, molecularly and dissociatively. —————— *Corresponding author (E-mail: [email protected]) Hole-trapping by either the surface hydroxyl groups or the adsorbed water molecules produces short-lived HO• radicals, which are the primary oxidizing agents. Natural sunlight is free of cost and tapping the same for detoxification is the objective of semiconductorcatalyzed environmental remediation. Studies on semiconductor-catalysis with natural sunlight are rare, probably due to the fluctuation of solar irradiance. The problem of fluctuation of sunlight intensity during the experiment has been overcome by exposing the semiconductors to identical solar irradiance by carrying out the experiments simultaneously, side by side. The simple experimental set-up and the easy separation of the particulate semiconductors make the technique highly adoptable for the electroplating and metal finishing shops. Further, microbial contamination and growth in water are potential health hazards necessitating disinfection. In recent years, the use of inorganic antimicrobial agents, compared to the organics, has attracted interest due to their improved safety and stability8,9; ceramics with inherent antimicrobial activity are convenient to employ as they are insoluble. The present results reveal that CeO2, besides ZnO, exhibits antimicrobial activity; unlike ZnO, CeO2 is stable in acidic and basic media10. Hence, it is a two-in-one advantage, photocatalyzed detoxification of cyanide with bacterial disinfection; the bactericidal activity in this study has been assessed using Escherichia coli (E. coli) bacteria as the index. 170 INDIAN J. CHEM TECHNOL., MAY 2011 Experimental Procedure Characterization The oxides used were supplied by Merck and their powder XRDs were recorded using a Siemens D-5000 XRD employing Cu-Kα X-rays of wavelength 1.5406 Å under a scan range of 5-60° with a scan speed of 0.2° s-1 or a Bruker D8 system using Cu-Kα radiation of 1.5406 Å in a 2θ range of 5-60° at a scan speed of 0.050° s-1 or with a PANalytical X’Pert PRO diffractometer using Cu-Kα rays at 1.5406 Å in a 2θ range of 15-75º with a scan rate of 0.020º s-1. The specific surface areas of the oxides were determined by the nitrogen-adsorption desorption method using the Brunauer-Emmett-Teller (BET) equation. A Perkin-Elmer Lambda 35 spectrophotometer was employed to record the UV-visible diffuse reflectance spectra of the oxides. The impedance spectra of the oxides were obtained using a HP 4284A Precision LCR meter over the frequency range of 1 MHz to 20 Hz at room temperature in air; the disk area was 0.5024 cm2 and the thicknesses of CeO2, ZnO and TiO2 pellets were 3.8, 1.87 and 2.98 mm, respectively. An Avatar 330FT-IR spectrometer was used to record the Fourier-transform infra-red (FTIR) spectra of the semiconductors. Photocatalytic studies The semiconductor-catalyzed solar photooxidation was carried out with AM 1 sunlight under clear sky in summer (March-July). The sunlight intensity was measured using a Daystar solarmeter (USA). Fresh solutions of KCN (25 mL) of required ppm of pH 12.5 (using NaOH) were air-saturated and taken in wide cylindrical glass vessels of uniform diameter. The entire bottom of the vessel was covered with the catalyst powder forming the catalyst bed which was not disturbed till the completion of the experiment. The dissolved oxygen was determined using an Elico dissolved oxygen analyzer PE 135 and the cyanide ion was estimated argentometrically using p-dimethylaminobenzylidene rhodanine as the indicator11, before and after illumination. Spectrophotometric determination of cyanide ion at 590 nm by complexing it with ninhydrin in alkaline medium12 also provided identical results. Cyanide ion analysis using cyanide ion selective electrode with Ag/AgCl electrode as the reference was also in agreement with the other two methods. Cyanate was analyzed spectrophotometrically5. The decrease of cyanide concentration for a finite time of illumination provided the oxidation rate and under identical solar irradiance the rates were reproducible to ±5%. Calcinations were made in a muffle furnace fitted with PID temperature controller and the heating rate was set at 10°C min-1 uniformly for all the oxides. Further, all the samples were calcined at the desired temperatures for 2 h. Acid treated TiO2 were prepared by stirring continuously 2 g of TiO2 in 50 mL of 5 N sulfuric or hydrochloric or nitric or phosphoric or acetic acid for 24 h, separating the oxide and calcining at 150 or 450°C. Bactericidal study A nutrient broth culture medium of pH 7.4 was prepared by dissolving 13.0 g nutrient broth (5.0 g peptone, 5.0 g NaCl, 2.0 g yeast extract, 1.0 g beef extract) in 1 L distilled water followed by sterilization in an autoclave at 121°C. MacConkey agar plates were prepared separately by dissolving 55 g MacConkey agar (20 g peptic digest of animal tissue, 10 g lactose, 5 g sodium taurocholate, 0.04 g neutral red, 20 g agar) in 1 L boiling distilled water followed by sterilization in an autoclave at 121°C and poured into Petri dish. E. coli bacteria were inoculated in 10 mL of a nutrient broth and incubated for 24 h at 37°C. The cultured bacteria were centrifuged at 3500 rpm for 5 min before washing with an autoclaved 0.9% NaCl solution twice and suspended in 50 mL of an autoclaved 0.9% NaCl solution. For the counting of E. coli colonies in CFU mL-1, the bacterial solution was successively diluted to109 times using 0.9% NaCl solution in order to achieve about 100 to 200 colonies on the Petri dish; using a loop, 10 µL of the diluted E. coli was streaked on the MacConkey agar plate and incubated at 37°C for 24 h. The CFU was counted by a viable count method. The bactericidal studies were made as follows. 20 mg of the oxide was added to 25 mL of E. coli solution taken in a 150 mL bottle and shaken well continuously without any illumination. At the required time interval, a finite volume of E. coli solution was removed from the oxide, diluted stepwise and enumerated as already stated. Results and Discussion Catalyst characterization The XRD of CeO2 matches with the standard JCPDS pattern (898436, face centered cubic) confirming its crystal structure. The XRD pattern of the TiO2 used is identical with the standard pattern of anatase (JCPDS 01-078-2486 C, tetragonal, body- 171 KARUNAKARAN et al.: SOLAR PHOTOCATALYTIC DETOXIFICATION OF CYANIDE centered) and the rutile lines (01-089-0553 C) are absent. This clearly reveals that the TiO2 employed in this study is of anatase phase. The XRD of ZnO is that of the JCPDS pattern of zincite (00-005-0664 D, hexagonal, primitive). The specific surface areas (S), determined by the BET nitrogen-adsorption desorption method, are presented in Table 1. The average particle sizes (D) of the oxides, deduced using the relationship D = 6/ρS, where ρ is the material density, are also listed in Table 1. The UVvisible diffuse reflectance spectra of the oxides show that they require UV-A light for excitation (spectra not shown). Electrochemical impedance spectroscopy (EIS) is a relatively new and powerful tool to probe the electrical properties of semiconductors13. It could be used to investigate the dynamics of the mobile and bound charges in the interfacial or bulk region of the semiconductors. In polycrystalline materials, the overall sample resistance may be a combination of the intragranular or bulk crystal resistance and intergranular or grain boundary resistance. Generally, the impedance data are analyzed in terms of an equivalent circuit model; an electrode interface undergoing an electrochemical reaction is typically analogous to an electric circuit consisting of a specific combination of capacitors and resistors. By fitting the EIS data to a model or an equivalent circuit the electrical properties of the semiconductors could be inferred. The impedance spectra (not given) show decrease of impedance with increase of frequency indicating the capacitance of the semiconductors employed. The Nyquist plot, a popular format of evaluating the impedance data, is presented in Fig. 1. The ohmic or uncompensated resistance (RΩ) corresponds to the grain boundary or intergranular resistance and the polarization or electron-transfer (charge-transfer) resistance (RP or RCT) refers to the intragranular or bulk crystal resistance; the latter is related to the Warburg resistance, the resistance to mass transfer, which is controlled by the specific conductance, σ. The constant phase element, CPE, can be associated with a non-uniform distribution of current due to material heterogeneity and is equivalent to a double layer capacitance, C. The Nyquist plot of TiO2, compared to those of ZnO and CeO2, displays a very small charge-transfer resistance with a very large frequency region where mass transfer is a significant factor, thus suggesting TiO2 to be kinetically facile; the semiconductor may be more photocatalytically active than others. The Nyquist plots of CeO2 and ZnO display large regions of mass-transfer and kinetic Table 1—Band gap (Eg), BET surface area (S), particle size (D), ohmic (RΩ) and charge-transfer (RCT) resistances, specific conductance (σ) and capacitance (C) Oxide Eg (eV) S (m2 g-1) D (nm) RΩ (kΩ) RCT (MΩ) CeO2 ZnO TiO2 2.89 3.15 3.18 11.0 12.2 14.7 76 87 104 754 6.13 56.8 14.9 7.26 0.0579 C σ (µS m-1) (pF) 5.08 5.13 1020 5.34 7.31 13.7 Fig. 1—The Nyquist plots control at low and high frequencies, respectively. Further, the Nyquist plots reveal the presence of appreciable (but not large or insignificant) series capacitance in the equivalent circuit and the Warburg impedance is also important. Table 1 presents the determined specific conductance, capacitance and the ohmic and charge-transfer resistances of the oxides; the specific conductance has been deduced from the measured charge-transfer resistance and the capacitance has been obtained using the equations ωmax = 1/CRCT and ωmax = 2πf, where f is the frequency corresponding to the top of the semicircle of the Nyquist plot. The specific conductance and capacitance are of the order CeO2 < ZnO < TiO2. Figure 2 presents the truncated FTIR spectra of the semiconductors as such, i.e., before use, exposed to the atmosphere only. TiO2 and ZnO show strong absorption around 3430 cm-1 indicating abundant adsorption of water molecules on the oxide surface. However, the corresponding spectrum of CeO2 does not exhibit such absorbance implying insignificant adsorption of water molecules on its surface. Cyanide photodetoxification CeO2, like TiO2 and ZnO, catalyzes the oxidation of cyanide ion under natural sunlight at pH 12.5 (vide 172 INDIAN J. CHEM TECHNOL., MAY 2011 Fig. 2—The FTIR spectra infra for the experimental conditions). The pKa of HCN is 9.3 and to avoid its liberation into the atmosphere the detoxification was carried out in a highly alkaline medium. Under identical conditions cyanide ion is not oxidized in the absence of any of the oxides. Spectrophotometric analysis of cyanate in the cyanide solution illuminated with CeO2 or ZnO or TiO2 reveals formation of cyanate at the expense of cyanide and conforms to the carbon balance ([CN–]0 = [CN–] + [OCN–]). This is in agreement with the earlier studies using TiO2; the nitrate generation due to further oxidation of the cyanate formed is insignificant till the cyanide is completely oxidized to cyanate4,5. It has been stated that the adsorption sites of cyanide and cyanate are the same and cyanide gets adsorbed in preference to cyanate resulting in the commencement of the cyanate oxidation only after the near complete oxidation of cyanide. Even under clear sky in summer the sunlight intensity fluctuates during the course of experiment (975±25 Wm-2). Also, it varies from day-to-day. To obtain analyzable solar results the solar irradiance in a set of experiments was kept identical by carrying out the experiments simultaneously, side by side. The solar results obtained with CeO2 or ZnO or TiO2 are consistent (vide infra for the experimental conditions). For each catalyst, a couple of experiments under identical reaction conditions carried out simultaneously with sunlight yield results within ±5%. Carrying out a control experiment along with others under the required experimental conditions simultaneously makes possible the comparison of the solar results. Fig. 3—Cyanide photooxidation on CeO 2, ZnO and TiO2, The Langmuir-Hinshelwood kinetics. Catalyst bed = 16.7 cm2, catalyst loading = 0.50 g, pH = 12.5, [O2]dissolved = 26.8 ppm, cyanide solution = 25 mL. Each catalysis corresponds to identical solar irradiance Photokinetic characteristics The photokinetic characteristics of the CeO2, ZnO and TiO2-catalyzed oxidation were deduced individually. The solar irradiance in each study was kept identical by carrying out a set of experiments simultaneously. Under identical solar irradiance, the cyanide oxidation rates increase with its concentration as shown by Fig. 3. The variation of cyanide-removal rates with its concentration is characteristic of the Langmuir-Hinshelwood kinetics14. However, the adsorption of cyanide ion on CeO2, ZnO and TiO2 in dark at pH 12.5, even at the highest concentration of cyanide ion employed, is too small to be measured analytically. Also, the infrared spectra of the dried catalysts, prior to illumination but after allowed to attain equilibrium with cyanide solution, fail to show characteristic absorbance of cyanide (~2250 cm-1) indicating insignificant adsorption of cyanide ion on the semiconductors (spectra not shown). The removal of cyanide in 2½ h from 25 ppm solution, under the conditions given in Fig. 3, with CeO2, ZnO and TiO2 are 24%, 52% and 68%, respectively. The photooxidation rates show linear dependence on the apparent surface area of the catalyst bed (Fig. 4). This is also in accordance with the Langmuir-Hinshelwood model. In 2½ h, under the conditions stated in Fig. 4, the percentages of cyanide oxidation with 50.0 cm2bed of CeO2, ZnO and TiO2 are 48, 60 and 92, respectively. CeO2, ZnO and TiO2 show sustainable KARUNAKARAN et al.: SOLAR PHOTOCATALYTIC DETOXIFICATION OF CYANIDE Fig. 4—Cyanide photooxidation as a function of catalyst bed area, Catalyst loading = 0.50 g, pH = 12.5, [CN–]0 = 100 ppm, [O2]dissolved = 26.8 ppm, cyanide solution = 25 mL. Each catalysis corresponds to identical solar irradiance photocatalytic activities. Recycling the catalysts without any pre-treatment provides identical results (conditions as in Fig. 3 with 100 ppm cyanide solution). Cyanide detoxification requires dissolved oxygen. The photooxidation of cyanide does not occur in nitrogen-purged solution (conditions as in Fig. 3 but with 100 ppm cyanide and 1.8 ppm of dissolved O2). Initial addition of acryl amide (10%) to the cyanide solution exposed to sunlight along with CeO2 or ZnO or TiO2 leads to polymer formation indicating the involvement of free radical in the photooxidation process. Nitrate (0.01M), sulfate (0.01M) and phosphate (0.01M) do not interfere in the semiconductor-catalyzed cyanide oxidation process. In the case of reducing ions, sulfite (0.01M) inhibits the photooxidation whereas nitrite (0.01M) does not. Also, the photooxidation is suppressed by citrate (0.01M) but not by oxalate (0.01M). Azide ion (0.01M) also slows down the photooxidation; the reaction conditions for all the stated experiments are as given in Fig. 3 with 100 ppm cyanide. Generally, sonication modifies the surface and particle size of the catalyst and the photocatalytic activity is susceptible to the surface and size modification of semiconductor particles15. But, pre-sonication for 10 min at 37±3 kHz and 100 W does not influence the solar detoxification of cyanide by all the three semiconductors studied; the experimental conditions remain the same. However, the degradation of salicylic acid on Hombikat TiO2 under UV light enhances on sonication16. Generally, the photocatalytic activity of the semiconductor 173 depends on its sintering temperature17. But, calcination of the oxides studied does not enhance the photodetoxification of cyanide. While the catalytic efficiencies of ZnO and CeO2 calcined at 300, 400, 500, 600, 700, 800 and 900°C and that of TiO2 at 300, 400, 500, 600 and 700°C are not different from those of the uncalcined samples TiO2 calcined at 800 and 900°C show lower catalytic efficiencies, the former by about 70% and the latter by about 50% of the uncalcined sample (16.7 cm2-catalyst bed, 0.10 g-catalyst loading, 12.5 pH, 26.8 ppm-dissolved O2, 25 mL 250 ppm-cyanide solution, 2½ h-sunshine); it is known that at these temperatures photocatalytically active anatase transforms into less active rutile. Sulfuric or nitric or hydrochloric or phosphoric or acetic acid-treatment of TiO2 does not modify the photocatalytic activity (conditions remain the same). Mixed semiconductors enable a vectorial transfer of electrons and holes from one semiconductor to another and hence show enhanced activity18,19. But, the 1:1 (w/w) mixture of TiO2 and CeO2 or TiO2 and ZnO or ZnO and CeO2 does not exhibit improved photocatalysis under the conditions stated already. The experiments show that the adsorption of cyanide ion in dark on CeO2, ZnO and TiO2 is too small to be determined analytically or detected spectroscopically. In alkaline medium adsorption of HO– on semiconductor results in negatively charged surface which is the reason for the insignificant adsorption of cyanide ion on the semiconductors. But, the title study exhibits Langmuir-Hinshelwood kinetics (Fig. 3) which is based on the adsorption of cyanide ion on the oxides. Hence, it is possible that cyanide ion gets adsorbed significantly on the illuminated photoactive surfaces of the semiconductors. However, the fact that acryl amide gets polymerized during the semiconductor-catalyzed oxidation of cyanide in aqueous alkaline solution indicates the involvement of radicals such as HO• in the cyanide oxidation; the detailed mechanism of cyanide photooxidation on semiconductor surface has been discussed elsewhere3,5. A possible explanation for the inhibition of cyanide oxidation (i) by sulfite ion but not by nitrite ion and (ii) by citrate ion but not by oxalate ion is the site of adsorption. Sulfite and citrate ions may compete with cyanide ion for adsorption at the same site on the illuminated oxides while the adsorption sites of oxalate and nitrite ions could be different. Probing the adsorption of citrate and oxalate on the catalysts supports the proposition. The FTIR spectral studies reveal adsorption of oxalate 174 INDIAN J. CHEM TECHNOL., MAY 2011 and citrate ions on the surfaces of CeO2, ZnO and TiO2. The IR spectra of CeO2, ZnO and TiO2 (not shown), recovered from citrate solution and dried (0.50 g catalyst from 25 mL 0.01 M solution), show strong absorption at 1579, 1589 and 1587 cm-1, respectively; the corresponding frequencies for the catalysts recovered from oxalate solution are 1639, 1641 and 1649 cm-1. While the adsorption of oxalate on CeO2 is insignificant that on TiO2 as well as ZnO is 40%; citrate adsorbs on all the three oxides to 54%. Lack of inhibition by nitrate, sulfate and phosphate suggest that these ions do not compete with cyanide for adsorption on the catalyst surface. Absence of enhanced photocatalysis in semiconductor mixtures may be due to strong adsorption of water molecules on the semiconductor surfaces. The primary sheath of water molecules around the semiconductor particles could prevent physical contact between adjacent semiconductor particles thus hindering inter-particle charge transfer. The Langmuir-Hinshelwood kinetic model is applicable to semiconductor-photocatalysis and the corresponding kinetic equation is20: rate = kK1K2IS[CN–][O2]/(1 + K1[CN–])(1 + K2[O2]) where K1 and K2 are the adsorption coefficients of cyanide ion and molecular oxygen on the illuminated surface of the catalyst, k is the surface pseudo-firstorder rate constant, S is the surface area of the catalyst and I is the light intensity in Einstein m-2 h-1. The cyanide solutions are oxygen-saturated and the dissolved oxygen concentration remains almost constant during the photooxidation. Since K2 is a constant for a given catalysis K2[O2]/(1 + K2[O2]) turns to be a constant for a given catalyzed oxidation. For a set of experiments conducted simultaneously I is a constant. The Langmuir-Hinshelwood kinetic model holds good as seen from the data fit to the curve governed by the kinetic equation and drawn using a computer program. The kinetic parameters deduced from the fit are presented in Table 2. Physicochemical properties and photodetoxification Experiments carried out simultaneously, side by side, under identical conditions and solar irradiance reveal the relative cyanide oxidation rates on TiO2, Table 2—The kinetic parameters Kinetic parameter 103K1 (ppm-1) kK2I/(1 + K2[O2]) (m-2 h-1) CeO2 ZnO TiO2 4.5 487 11.6 462 11.9 692 ZnO and CeO2 surfaces as 1.0, 0.7 and 0.4, respectively. The photocatalytic efficiency depends on the crystal size; smaller the size, higher is the reactivity. In smaller crystals the photoinduced holes and electrons have to diffuse shorter distance to reach the interface. Consequently, the holes and electrons can be effectively captured by the substrates in the solution. However, in the title study the particle size is of the order CeO2 < ZnO < TiO2 and so is the photocatalytic activity. This indicates that some other factor overrules this effect. The solar detoxification has been carried out by temporarily immobilizing the semiconductor powder in the form of a catalyst bed and the observed photocatalytic efficiencies are not in strict compliance with the BET surface area. While the relative photocatalytic activities of TiO2, ZnO and CeO2 under identical solar irradiance are 1.0, 0.7 and 0.4, respectively, the corresponding relative BET surface areas are 1.0, 0.83 and 0.75. Hence, some other factor influences strongly the photocatalytic activities of the oxides. The solar detoxification has been carried out in highly alkaline medium (pH 12.5) and hence the point of zero charge (PZC) of the semiconductor is of no significance; the PZC of CeO221, and ZnO and TiO222 are 8.1, 8.8 and 5.8, respectively. Adsorption of water molecules may also be a reason for the observed low catalytic activity of CeO2; the FTIR spectra of the oxides show insignificant adsorption of water molecules on CeO2. Although the band gap energies of TiO2 and ZnO do not differ significantly the former is more photocatalytically active than the latter. The adsorption of water and hydroxyl groups may also be an explanation; anatase TiO2 actively adsorbs water and hydroxide ion23 and the photocatalytic activity depends on the surface-adsorbed water and hydroxyl group. However, with xenon lamp ZnO is reported to be more efficient than TiO224. The observed solar photocatalytic activities of the oxides are in accordance with the determined chargetransfer resistance, capacitance and the specific conductance of the semiconductors; while the electron-transfer resistance is of the order CeO2 > ZnO > TiO2, the capacitance and the specific conductance are as follows: CeO2 < ZnO < TiO2 (Table 1). A recent EIS study on the Ag/TiO2photocatalyzed degradation of rhodamine B also reveals a similar relationship between the photocatalytic activity and the charge-transfer resistance as well as the capacitance25. Of the 0.5% to 7% Ag-doped TiO2 studied, the most active 3% Ag- KARUNAKARAN et al.: SOLAR PHOTOCATALYTIC DETOXIFICATION OF CYANIDE doped TiO2 shows the lowest charge-transfer resistance and highest capacitance. A similar study on the photodegradation of acid red 44 also supports such relationships26. While the observed photocatalytic activity is of the order TiO2 nanospheres < TiO2 nanorods < Ag-TiO2 nanorods, the measured charge-transfer resistance is as follows: TiO2 nanospheres > TiO2 nanorods > Ag-TiO2 nanorods; the determined capacitance is in the order of observed photocatalytic activities. Table 2 shows that the adsorption of cyanide ion on the illuminated surfaces of TiO2 and ZnO are not significantly different but that on CeO2 is much less. This may be one of the reasons for the slow photodetoxification of cyanide on CeO2. The solar irradiances, monitored during the course of cyanide detoxification, on CeO2, ZnO and TiO2 do not differ remarkably and hence, the variation in the kK2I/(1 + K2[O2]) values of TiO2 and ZnO may be taken as that of kK2/(1 + K2[O2]); the dissolved O2-concentration remains unaltered for all the three photocatalysis. Since the kK2I/(1 + K2[O2])-value of TiO2 is larger than that of ZnO the combined processes of (i) O2adsorption on the illuminated surface, and (ii) the cyanide oxidation on the surface are more feasible with TiO2 than with ZnO. The kK2I/(1 + K2[O2])values of CeO2 and ZnO do not differ significantly. Hence, the combined processes of adsorption of O2 and the cyanide oxidation on the illuminated surface on ZnO and CeO2 are equally feasible. Bactericidal activity Figure 5 shows the E. coli disinfection by CeO2 and ZnO in aqueous suspension without any illumination. The antibacterial efficiencies of the oxides in a population of 2.5 × 1012 CFU mL-1 in 30 min are 40 and 44%, respectively. In absence of the oxides the E. coli population remains unaffected during the experimental period revealing the Fig. 5—E. coli inactivation by CeO2 and ZnO without illumination in 30 min, oxide loading = 0.8 g L-1, pH = 7.4 175 bactericidal activity of ZnO and CeO2. However, experiments with TiO2 under identical conditions do not show any significant killing of the bacteria. E. coli bacteria in 0.9% saline were used for the evaluation of the bactericidal activity. The cell population was determined by a viable count method on MacConkey agar plates after proper dilution of the culture. The antibacterial efficiency is the ratio of the decrease of E. coil population at a given time to its initial population; antibacterial efficiency = 100 (C0 – Ct)/C0, where Ct and C0 are the E. coli population at time t and zero, respectively. Although there are a few reports on the inactivation of E. coli by ZnO nanoparticles and bulk particles in absence of any illumination the mechanism of action still remains obscure8,9,27-29. In spite of the detected release of Zn2+ from ZnO suspension8,27,29 examination of E. coli inactivation by added Zn2+ ions separately shows that the Zn2+ ion release from the oxide is not the reason for the E. coli disinfection8,29. Some workers have also detected the generation of H2O2 by ZnO in absence of light27,29 and have suggested the same as a main factor for the bacterial activity27-29. But the observed extent of inactivation of E. coli population in the present study (vide supra) makes the proposition unviable. As the antibacterial activities of some synthesized ZnO nanorods do not correlate with their photoluminescence features corresponding to surface defects (green emission) it has been concluded that the surface defects do not play any significant role in the antibacterial activity of ZnO27. The SEM and TEM images displayed in a few reports reveal the binding of ZnO nanoparticles to the surface of E. coli bacteria8,27,28. There are several possible attachment mechanisms of the oxide to the bacterial surface: electrostatic forces, van der Waals forces and receptor-ligand interactions8. The zeta potential of ZnO suspended with E. coli at pH ~ 7 is approximately +24 mV28. The overall E. coli surface is negatively charged at neutral pH due to the polysaccharides of lipopolysaccharide, which predominate over the amide28, and its potential is 7.2 mV at pH 6.58. Hence, the interaction of ZnO with E. coli is favored by the electrostatic forces. The receptor-ligand interactions may dominate in the ZnO bound E. coli bacteria; carboxyl, amide, phosphate, hydroxyl groups and carbohydrate-related moieties in the bacterial cell wall may provide sites for the molecular-scale interactions with the oxide8. Operation of similar attachment mechanism is likely 176 INDIAN J. CHEM TECHNOL., MAY 2011 with CeO2. It has been reported that ZnO causes membrane damage, which leads to leakage of cell contents and cell death27. Further, only a few E. coli cells show internalization of ZnO nanoparticles while a large number of them do not exhibit such thing revealing that internalization is not a general occurrence27. The TEM displays also shrinkage of cytoplasmic material inside the cell wall of some of the E. coli cells27. The interaction of oxide nanoparticles with the bacterial cell walls and possible permeation of the nanoparticulate oxide into the bacterial cells are still not clearly understood8. It has been proposed that the induction of intracellular oxidative stress seems to be a key event of the toxicity mechanisms of many nanomaterials9. Once inside the cell, nanomaterials may induce intracellular oxidative stress by disturbing the balance between oxidant and anti-oxidant processes. On one hand, the oxidative stress induced by exposure to nanomaterials may stimulate an increase of the cytosolic calcium concentration or may cause the translocation of transcription factors to the nucleus, which regulate pro-inflammatory genes. Alternatively, exceeding oxidative stress may also modify proteins, lipids and nucleic acids, which further stimulates the antioxidant defense system or even leads to cell death. Conclusions With natural sunlight, CeO2 catalyzes the oxidation of cyanide ion to cyanate ion and its photocatalytic behaviour is similar to those of ZnO and TiO2 anatase; follows the Langmuir-Hinshelwood kinetics on cyanide, and depends on the area of the catalyst bed and dissolved O2. However, the adsorption of cyanide ion on CeO2, ZnO and TiO2 in dark is insignificant. Although the solar photocatalytic efficiencies are of the order: CeO2 < ZnO < TiO2, which is in accordance with charge-transfer resistance and capacitance, CeO2 and ZnO exhibit bactericidal activity in absence of direct light itself. Acknowledgement The authors thank the Council of Scientific and Industrial Research (CSIR), New Delhi, for the financial support through research grant no. 01(2031)/06/EMR-II and one of the authors (PG) is grateful to CSIR for Junior Research Fellowship. References 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 Marugan J, van Grieken R, Cassano A E & Alfano O M, Catal Today, 144 (2009) 87. Marugan J, van Grieken R, Cassano A E & Alfano O M, Appl Catal B, 85 (2008) 48. Karunakaran C, in Photo/Electrochemistry & Photobiology in the Environment, Energy and Fuel edited by Kaneco S (Research Signpost, Trivandrum) 2006, pp 259-294. Bozzi A, Guasaquillo I & Kiwi J, Appl Catal B, 51 (2004) 203. Chiang K, Amal R & Tran T, J Mol Catal A, 193 (2003) 285. Hu X, Li G & Yu J C, Langmuir, 26 (2010) 3031. Gaya U I & Abdullah A H, J Photochem Photobiol C, 9 (2008) 1. Jiang W, Mashayekhi H & Xing B, Environ Pollut, 157 (2009) 1619. Hu X, Cook S, Wang P & Hwang H M, Sci Total Environ, 407 (2009) 3070. Lee J D, Concise Inorganic Chemistry, 5th ed (Blackwell Science, London) 2005. Kim H J, Lu L, Kim J H, Lee C H, Hyeon T, Choi W & Lee H I, Bull Korean Chem Soc, 22 (2001) 1371. Nagaraja P, Hemanthakumar M S, Yathirajan H S & Prakash J S, Anal Sci, 18 (2002) 1027. Bard A J & Faulkner L R, Electrochemical Methods: Fundamentals and Applications, 2nd ed (Wiley, New York), 2000. Karunakaran C, Senthilvelan S & Karuthapandian S, J Photochem Photobiol A, 172 (2006) 207. Hirano K, Nitta H & Sawada K, Ultrason Sonochem, 12 (2005) 271. Reddy E P, Davydov L & Smirniotis P, Appl Catal B, 42 (2003) 1. Enriquez R, Agrios A G & Pichat P, Catal Today, 120 (2007) 196. Karunakaran C, Dhanalakshmi R & Gomathisankar P, Int J Chem Kinet, 41 (2009) 716. Karunakaran C, Dhanalakshmi R, Gomathisankar P & Manikandan G, J Hazard Mater, 176 (2010) 799. Karunakaran C & Dhanalakshmi R, Solar Energy Mater Solar Cells, 92 (2008) 1315. de Faria L A & Trasatti S, J Colloid Interface Sci, 167 (1994) 352. Xu Y & Schoonen M A A, Am Mineral, 85 (2000) 543. Ding Z, Lu G O & Greenfield P F, J Phys Chem B, 104 (2000) 4815. Frank S K & Bard A J, J Phys Chem, 81 (1977) 1484. Xin B, Ren Z, Hu H, Zhang X, Dong C, Shi K, Jing L & Fu H, Appl Surf Sci, 252 (2005) 2050. Yun H J, Lee H, Kim N D & Yi J, Electrochem Commun, 11 (2009) 363. Tam K H, Djurisic A B, Chan C M N, Xi Y Y, Tse C W, Leung Y H, Chan W K, Leung F C C & Au D W T, Thin Solid Films, 516 (2008) 6167. Zhang L, Ding Y, Povey M & York D, Prog Nat Sci, 18 (2008) 939. Sawai J, J Microbiol Meth, 54 (2003) 177.
© Copyright 2026 Paperzz