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Article

Inactivation of E. Coli in Water Using Photocatalytic, Nanostructured Films Synthesized by Aerosol Routes

1
Aerosol and Air Quality Research Laboratory, Department of Energy, Environmental and Chemical Engineering, School of Engineering and Applied Science, Washington University in St. Louis, Campus Box 1180, St. Louis, MO 63130, USA
2
Department of Environmental Health, University of Cincinnati, Cincinnati, OH 45267, USA
*
Author to whom correspondence should be addressed.
Catalysts 2013, 3(1), 247-260; https://doi.org/10.3390/catal3010247
Submission received: 10 December 2012 / Revised: 13 January 2013 / Accepted: 30 January 2013 / Published: 4 March 2013
(This article belongs to the Special Issue Photocatalysts)

Abstract

:
TiO2 nanostructured films were synthesized by an aerosol chemical vapor deposition (ACVD) method with different controlled morphologies: columnar, granular, and branched structures for the photocatalytic inactivation of Escherichia coli (E. coli) in water. Effects of film morphology and external applied voltage on inactivation rate were investigated. As-prepared films were characterized using scanning electron microscopy (SEM), transmission electron microscopy (TEM), X-ray diffractometry (XRD), and UV-VIS. Photocatalytic and photoelectrochemical inactivation of E. coli using as-prepared TiO2 films were performed under irradiation of UVA light (note: UVA has a low efficiency to inactivate E. coli). Inactivation rate constants for each case were obtained from their respective inactivation curve through a 2 h incubation period. Photocatalytic inactivation rate constants of E. coli are 0.02/min (using columnar films), and 0.08/min (using branched films). The inactivation rate constant for the columnar film was enhanced by 330% by applied voltage on the film while that for the branched film was increased only by 30%. Photocatalytic microbial inactivation rate of the columnar and the branched films were also compared taking into account their different surface areas. Since the majority of the UV radiation that reaches the Earth’s surface is UVA, this study provides an opportunity to use sunlight to efficiently decontaminate drinking water.

1. Introduction

Currently, nearly 20% of the world’s population lacks clean drinking water [1,2]. With a rapidly increasing world population, this problem is further exacerbated. Many groundwater and surface water sources are contaminated, thus necessitating safe and reliable disinfection techniques [3]. Conventionally, water is disinfected by chlorination, which uses free chlorine as a strong oxidant [4]. The biggest drawback to this method is the possible production of carcinogenic disinfection by-products (DBPs) such as trihalomethanes and haloacetic acids [5]. Ozone is an alternative strong oxidant for disinfection of water. However, ozonation may also produce toxic DBPs during the disinfection process [6]. Therefore, safe and sustainable alternative water disinfection methods are required.
Photocatalytic disinfection is considered a promising alternative due to several advantages. First, photocatalytic disinfection does not produce any toxic or carcinogenic DBPs. Photocatalytic materials used for disinfection can be recycled while the conventional chemical methods consume chemical disinfectants. In addition, titanium dioxide (TiO2) is a non-hazardous photocatalytic material. Oxidants generated by such photocatalytic materials are strong enough to inactivate pathogenic microorganisms in water [7].
TiO2 nanoparticles have been studied extensively as a photocatalytic material for inactivation of pathogenic microorganisms such as bacteria, viruses, algae, and fungi because they have several desirable features: a large surface area, thermal and chemical stability, and they are rather inexpensive [8,9,10,11,12,13]. Matsunaga et al. [8] first reported photocatalytic inactivation of microorganisms. They inactivated Lactobacillus acidophilus, Saccharomyces cerevisiae and E. coli using a TiO2 particle suspension. Wei et al. [9] used P25 (TiO2, Degussa) to inactivate E. coli in water. They reported effects of particle dosage, light intensity etc. on the inactivation rate. Hu et al. [10,11] have synthesized Ag/TiO2 and Ag/AgBr/TiO2 composites to inactivate bacteria under irradiation with visible light. However, TiO2 nanoparticles must overcome a number of challenges before replacing conventional water disinfection methods. First, TiO2 nanoparticles must be removed from disinfected water post-treatment. Unfortunately, removing nano-sized particles from liquid is very difficult and energy intensive. Secondly, particle suspensions in water can block light, an essential shading effect during microbial photoactivation [12]. In addition, inactivation efficiency is low because electron-hole (e-h) pairs generated by photoactivation recombine rapidly [7,14].
To overcome these problems, several research groups have studied inactivation of pathogenic microorganisms using immobilized TiO2 films [15,16,17,18]. Photocatalytic inactivation using an immobilized TiO2 film alleviates post-treatment removal of nanoparticles and reduces light blockage. Kuhn et al. [16] reported inactivation of E. coli, Pseudomonas aeruginosa (P. aeriginosa), Staphylococcus aureus (S. aureus), Enterococcus faecium (E. faecium) and Candida albicans (C. albicans) using P25-coated glass under UV light. They investigated susceptibility of the bacteria, which was shown as follows: E. coli > P. aeriginosa > S. aureus > E. faecium > C. albicans. Sunanda et al. [17] also investigated inactivation of E. coli using a dip-coated TiO2 film. To enhance inactivation rates, Reddy et al. [18] prepared TiO2 coated on zeolite for use in inactivation of E. coli.
Recently, a few research groups have studied photoelectrochemical inactivation by applying an electric potential on the TiO2 film to effectively separate electron-hole (e-h) pairs to reduce their recombination rate [10,19]. Yu et al. [19] prepared a Ti-based photocatalytic film by electrodeposition and investigated the photoelectrochemical inactivation of E. coli by applied voltage on the film. Heyden el al. [20] also studied both photocatalytic and photoelectrochemical inactivation of E. coli using a quantum dot-deposited TiO2 nanotube film.
When using TiO2 films for photocatalytic and photoelecrochemical reactions, the morphology of the TiO2 film is a determinant factor, which influences photogenerated electron mobility [21]. However, the effect of the morphology of the film on efficiency of photocatalytic inactivation of microorganism has not been systemically studied. In this paper, inactivation of a microorganism using TiO2 films with different morphologies is reported. E. coli was selected as the model species in this study because it is a representative indicator of contamination of water [14]. Several morphological TiO2 films were synthesized via the aerosol chemical vapor deposition (ACVD) method [22,23]. This study describes the effect of three TiO2 film morphologies (columnar, granular, and branched structures) on the efficiency of inactivation of E. coli in water. In addition, the effect of applied voltage on the photocatalytic inactivation is also investigated.

2. Experimental Section

2.1. Preparation and Characterization of TiO2 Films by ACVD

TiO2 films with different morphologies were prepared using the ACVD method. Titanium tetraisopropoxide (TTIP, Sigma-Aldrich, St. Louis, MO, USA) was used as a precursor for the synthesis of the films. Tin-doped indium oxide (ITO) coated aluminosilicate glass (Delta Technologies, Stillwater, MN, USA) was selected as a substrate for the deposition of the TiO2 films. Synthesis of TiO2 films via the ACVD method has been described by An et al. [22,23]. Process parameters for each morphology—columnar, granular, and branched structures—are summarized in Table 1.
Table 1. Summary of experimental parameters for synthesis of TiO2 films via aerosol chemical vapor deposition (ACVD).
Table 1. Summary of experimental parameters for synthesis of TiO2 films via aerosol chemical vapor deposition (ACVD).
TestMorphologyTemperature of substrate (°C)Precursor feed rate (μmol/min)Particleratio (%)Residence time (ms)Depositiontime (min)
1Columnar5001.53132050
2Granular4504.34305370
3Branched4504.34183023
A field emission scanning electron microscope (FESEM, Nova 2300, FEI) and a transmission electron microscope (TEM, Spirit Lab6, FEI) were used for morphology and thickness characterization of as-prepared films. The crystal structure of as-prepared TiO2 films was characterized using an X-ray diffractomer (XRD, Geigerflex D-MAX-A, Rigaku, Tokyo, Japan) with Cu-Kα radiation at 35 kV and 35 mA. XRD patterns of columnar, granular, and branched structured films were scanned from 20° to 60° of 2θ. A UV-Vis spectroscope (Cary 100, Varian, Palo Alto, CA, USA) was used for absorption spectra of as-prepared films across the ultraviolet and visible light spectra. The bandgap energy of each film was obtained from their respective UV-Vis absorption spectra by plotting the correlation between photon energy () and (αKM)0.5. αKM is the light absorption coefficient of the TiO2 films calculated using the Kubelka-Munk formalism which is expressed as [24]:
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where R is the reflectance of an infinitely thick sample. Since TiO2 is an indirect semiconductor, bandgap energy can be obtained from the linear correlation between the photon energy and the square root of the absorption coefficient [24].

2.2. Estimation of Surface Area of TiO2 Films

The total surface area of each film type was estimated by mimetic methods. For the columnar film, a column was considered as a cone shape (Figure S1a) and the arrangement of columns on the film was assumed as the hexagonal packing of circles (Figure S1b). The granular structure was mimicked with two cases: granular film-1 and granular film-2 (Figure S1a). Granular film-1 was considered to be the arrangement of a single layer of small, primary particles on the lateral surface of a hexagonally packed column. Granular film-2 was assumed to be numerous hexagonally close-packed primary particle spheres within the boundary of the column (Figure S1c). In the case of the branched structure, the film was mimicked as cone-shaped columns with cone-shaped branches on their lateral surface as shown in Figure S1a. The cone-shaped branches on the lateral surface of the column were arranged as the hexagonal packing of circles (Figure S1b). Table S1 lists the dimensions for the deposited area of the film, the single column, the single primary particle and the single branch as determined from their photos and electron microscope images.

2.3. Culture and Sampling Cells

E. coli BL21 was cultured for 18 h in growth medium at 37 °C. Growth medium was prepared by dissolving 25 g of Luria-Bertani (LB) broth powder (LB broth, Difco) in 1 L of deionized (DI) water and autoclaving for 15 min at 121 °C. During culturing, the optical density at 600 nm (OD600) of the culture solution was measured every hour to establish the onset of the stationary growth phase of E. coli growth (which corresponded to 1.4 × 109 cells/mL after 18 h of growth time).
The culture solution was sampled at t = 18 h and cells were pelleted by centrifugation for 10 min at 3000 rpm. Pelleted cells were suspended in 50 mL of buffer solution (5.0 mM sodium sulfate) creating a working cell suspension with a concentration of approximately 108 cells/mL. Viable E. coli concentration was determined from CFU (colony forming unit) plate counts: after serial dilutions, culture samples were plated on LB agar (Difco) followed by incubation for 12 h at 37 °C. Each sample was plated in triplicate.

2.4. Light and Material Control Tests

In order to determine the direct effect of light on E. coli viability, a light control was conducted. An arc Xe lamp (Oriel, Stratford, CT, USA) was used as the light source and was operated at 450 W. A water filter was attached to the lamp to remove infrared light. The E. coli solution was irradiated by the arc Xe lamp and 100 μL solution was sampled at 0, 30, 60, 90 and 120 min. In order to cut off ultra violet (UV) light (UVB and UVC), a blue band pass filter was attached and the effect of light on E. coli cells with and without the blue band pass filter was compared. In addition, the light intensity of the lamp was measured using a spectroradiometer (RPS900, International Light, Peabody, MA, USA) with and without the blue band pass filter to verify that it could effectively remove the strong UV wavelengths. UVB and UVC have been reported to inactivate some microorganisms [25]. Thus, in order to clearly investigate inactivation of E. coli by photocatalytic and photoelectrochemical reaction, the direct effect of UVB and UVC on E. coli should be minimized.
The effect of non-irradiated nanostructured TiO2 films on E. coli viability was also examined. As-prepared TiO2 film was immersed in the 50 mL E. coli solution and samples taken at 0, 30, 60, 90 and 120 min. A second material control experiment was conducted with 0.8 V of external voltage applied to the TiO2 film to determine the effect of the TiO2 film with electric bias. During the material control experiments, the reactor was covered with aluminum foil to block ambient light.

2.5. Photocatalytic and Photoelectrochemical Inactivation of E. coli

Figure 1. A schematic diagram of the experimental setup used for photocatalytic and photoelectrochemical inactivation of E. coli.
Figure 1. A schematic diagram of the experimental setup used for photocatalytic and photoelectrochemical inactivation of E. coli.
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Photocatalytic and photoelectrochemical inactivation of E. coli was conducted as shown in Figure 1. For photocatalytic inactivation, only the TiO2 film was immersed in the E. coli solution (no platinum wire was used). Both the TiO2 film and the platinum (Pt) wire were immersed in solution while 0.8 V electric potential was applied between the two electrodes using a sourcemeter (SourceMeter 2400, Keithley, Cleveland, OH, USA) for photoelectrochemical inactivation. The arc Xe lamp was used as the light source at 450 W with the water and the blue band pass filters in place. The intensity of UVA (315–400 nm) range of the lamp was 2.9 μW/cm2. The E. coli solution in the inactivation reactor was sampled at 0, 5, 10, 15, 20, 30, 60 and 120 min. During E. coli inactivation, the culture was kept mixed by a magnetic stirrer. Experimental parameters of this study are summarized in Table 2.
Table 2. Summary of experimental parameters of inactivation for E. coli.
Table 2. Summary of experimental parameters of inactivation for E. coli.
No.TestObjectiveExperimental conditions
1Light control testExamine effect of light on viability of E. coli cells without TiO2 filmsReactor volume: 50 mL
2Material control testExamine effect of TiO2 films on viability of E. coli cells without irradiation of lightInitial active cell concentration (C0): 108 cells/mL
3Photocatalytic inactivationStudy inactivation of E. coli with TiO2 films under irradiation of light without external voltageLight source: 450 W arc Xe lamp
4Photoelectrochemical inactivationStudy inactivation of E. coli with TiO2 films under irradiation of light with external voltageTiO2 films: columnar, granular, and branched structure

3. Results and Discussion

Figure 2 shows SEM and TEM images of as-prepared columnar, granular, and branched TiO2 films. In all cases, thickness of films was well controlled around 2 μm. In Figure 2a–c, it is shown that TiO2 was well developed in one direction without any grains or branches. In addition, the tip of the single column was very sharp so that TiO2 monomers or small primary particles deposited on the film were completely sintered and formed a single column. The granular structure was composed of numerous small grains (Figure 2d,e) while the branched structure had some sharp branches on its surface, which were composed of well-sintered grains (Figure 2g,h). TEM images of these structures more clearly depict this distinction (Figure 2f,i). In the case of granular TiO2, small grains are observed whereas 1-D branches are shown in the branched TiO2.
XRD patterns of as-prepared TiO2 films are shown in Figure 3. For all morphologies, the anatase phase of TiO2 was synthesized. The XRD pattern of the columnar TiO2 film shows a peak only for the [112] direction of the anatase phase. This indicates that columns of the film were grown only in the preferred direction of [112]. On the other hand, the XRD pattern of the granular film matches well with the particle diffraction file (PDF) reference peak of the anatase phase and depicts numerous peak directions. This implies that the small grains composing the granular structure were randomly deposited and not well oriented. The XRD pattern of the branched TiO2 film also closely matches the peaks from the PDF of anatase. However, the relative intensity of the peak of [101] direction was lower than that of the granular structure, possibly because the [101] direction from small primary particles initially deposited on the film was lost by sintering among them when forming branches.
Figure 2. Scanning electron microscopy (SEM) and transmission electron microscopy (TEM) images of (a), (b), (c) columnar, (d), (e), (f) granular and (g), (h), (i) branched TiO2 films.
Figure 2. Scanning electron microscopy (SEM) and transmission electron microscopy (TEM) images of (a), (b), (c) columnar, (d), (e), (f) granular and (g), (h), (i) branched TiO2 films.
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Figure 3. X-ray diffraction (XRD) patterns of columnar, granular, and branched TiO2 films synthesized by ACVD. Black solid circles indicate peaks from Tin-doped Indium oxide (ITO) substrate.
Figure 3. X-ray diffraction (XRD) patterns of columnar, granular, and branched TiO2 films synthesized by ACVD. Black solid circles indicate peaks from Tin-doped Indium oxide (ITO) substrate.
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UV-Vis absorption spectra of the TiO2 films are shown in Figure S2. In all films, the bandgap energy of TiO2 was determined to be about 3.2 eV, which matches the reference bandgap energy of anatase TiO2. This result means that all as-prepared films can be activated by light at wavelengths below 390 nm.
In Figure S3, measurement of light intensity of the arc Xe lamp shows that the blue band pass filter cuts off UVB and UVC. Although both UVB and UVC are completely removed with the filter, the filtered light still includes UVA, which can activate TiO2 films to inactivate microbes.
Figure S4 shows the effect of irradiation light on the viability of E. coli with and without the blue band pass filter. While 10% of E. coli was inactivated after 2 h of irradiation with the filter in place, 99.999% of E. coli were killed within 30 min by irradiation of light without the filter. This result implies that UVB and UVC are lethal to E. coli cells whereas the effect of UVA is rather minimal over a period of two hours. Therefore, the blue band pass filter was attached to the lamp to minimize the effect of UVB and UVC light on the inactivation of E. coli cells when examining inactivation efficiency by photocatalytic and photoelectrochemical reactions. In addition, it was confirmed that TiO2 itself does not have any effect on the inactivation of E. coli with and without external voltage in dark conditions. (Figure S5).
Results of photocatalytic and photoeletrochemical inactivation of E. coli using columnar, granular and branched TiO2 films are shown in Figure 4. In all cases, the concentration of E. coli seems to exponentially decrease with respect to inactivation time. This indicates that inactivation of E. coli follows Chick’s Law which says that the inactivation rate of bacteria can be expressed as a first ordered reaction with respect to the concentration of viable cells in a reactor [24]. According to Chick’s Law, the inactivation rate can be given as follows:
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where Ct is the active cell concentration at time t. From Equation (2) the inactivation rate constant can be obtained as Equation (3).
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where the inactivation rate is normalized by the surface area of the films. The normalized rate can be obtained as follows:
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where A is the surface area of the films and k’ is the normalized rate constant.
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Figure 4. Photocatalytic and photoelectrochemical inactivation of E. coli using columnar, granular, and branched TiO2 films. Error bars represent the standard deviation of triplicate measurements.
Figure 4. Photocatalytic and photoelectrochemical inactivation of E. coli using columnar, granular, and branched TiO2 films. Error bars represent the standard deviation of triplicate measurements.
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Since the initial concentration C0 was fixed as 108 cells/mL, the inactivation rate constant can represent the inactivation efficiency by photocatalytic and photoelectrochemical reaction for each film morphology. The k value for each case was obtained from the linear slope of a log scale plot of photocatalytic and photoelectrochemical inactivation of E. coli. The inactivation rate constant, k for each case is shown in Figure 5.
Figure 5. Inactivation rate constant of photocatalytic and photoelectrochemical inactivation of E. coli using columnar, granular, and branched TiO2 films.
Figure 5. Inactivation rate constant of photocatalytic and photoelectrochemical inactivation of E. coli using columnar, granular, and branched TiO2 films.
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In the case of inactivation using the columnar TiO2 film, the rate constant of photoelectrochemical inactivation was 330% higher than that of photocatalytic inactivation. This could be caused by a reduced electron-hole recombination rate due to enhancement of electron transfer to the cathode (platinum wire) through the column, which does not have any grain boundary effect (Figure 6).
Figure 6. Electron transfer through a columnar, a granular and a branched TiO2 film.
Figure 6. Electron transfer through a columnar, a granular and a branched TiO2 film.
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Thus, more electron-hole pairs could generate more reactive oxygen species, which could result in a higher inactivation rate of E. coli. On the other hand, the photoelectrochemical reaction rate constant by the branched TiO2 film was only 30% higher than photocatalytic reaction rate constant. Although an applied voltage (0.8 V) between the anode (TiO2 film) and the cathode (platinum wire) was able to promote separation of electron-hole pairs generated in the TiO2, grain boundaries between branches and the main column could interrupt the fast transfer of electrons, consequently limiting the overall enhancement of the inactivation rate constant (Figure 6). In the case of the granular film, the photocatalytic and the photoelectrochemical rate constants were almost the same, which means that the electric bias could not enhance e-h separation in the film.
The surface area of the films could also significantly affect the inactivation rate. The larger surface area of TiO2 can promote the release of electrons and holes from the TiO2 film into the buffer solution generating reactive oxygen species. Eventually this could enhance inactivation rate. The photocatalytic reaction rate constants in Figure 5 exhibits this surface area effect for three different morphologies. No separation of electron-hole pairs by an applied electric potential occurred in the case of photocatalytic inactivation, therefore the rate constants could be affected by the surface area of the films. As shown in Figure 5, the photocatalytic inactivation rate constants of the branched and the granular TiO2 film were 280% and 160% higher, respectively, than that of the columnar film. These larger inactivation rate constants reflect the fact that the branched film and the granular film (case of Granular film-1 in Table 3) have a 820% and 360% larger surface area, respectively, than the columnar film (Table 3).
Table 3. Estimated surface area of TiO2 films.
Table 3. Estimated surface area of TiO2 films.
Columnar filmGranular film-1Granular film-2Branched film
Total surface area of TiO2 (m2)6.88 × 10−43.18 × 10−31.69 × 10−26.34 × 10−3
Normalized rate constant of PC a by surface area (k’, min−1·m−2)31.116.93.2 11.8
Normalized rate constant of PEC b by surfance area (k’, min−1·m−2)129.415.72.9 14.4
a Photochemical inactivation; b Photoelectrochemical inactivation.
Sunanda et al. [17] established a mechanism for inactivation of E. coli cells by reactive oxygen species that is generated by a photocatalyst. The reactive species such as hydroxyl radicals can oxidize and eventually destruct bacterial membrane and DNA strand, leading to cell lyses (release of metabolites, protein, and RNA from the cell [26]. Such an inactivation process breaks cellular structures. SEM images of the films support this mechanism (Figure S6), which show the top view of the columnar TiO2 film before and after inactivation. In Figure S6b, the integrity of E. coli cells was destroyed and cellular biomaterials or cell debris “dissolved” on the surface of TiO2 film.
Figure 7 shows the change in the inactivation rate constant obtained from a columnar film with respect to repeated use in 2-h photoelectrochemical inactivation trials. The inactivation rate initially decreased by about 22% between the first and second 2-h trial, with little drop-off observed in subsequent trials. The initial drop in inactivation rate could occur due to inactivated cell debris attached to the film surface as shown in Figure S6. These residual cells could block activation sites of the TiO2 film. After time, the cell debris is eventually decomposed in the aqueous solution, allowing the inactivation rate to thereafter be sustained. The results demonstrate that the TiO2 film is a sustainable material for the photocatalytic inactivation of E. coli in water.
Figure 7. Photoelectrochemical inactivation rate constant with respect to repeated inactivations.
Figure 7. Photoelectrochemical inactivation rate constant with respect to repeated inactivations.
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4. Conclusions

TiO2 films with different morphologies—columnar, granular, and branched structures—were successfully synthesized via the ACVD method to inactivate E. coli in water. For all morphologies, the thickness was well controlled at about 2 μm and anatase phase films were obtained. E. coli is rapidly killed by UVB and UVC in the absence of the TiO2 films, but most E. coli survives under UVA. The TiO2 films did not have any bactericidal effects on E. coli in the dark condition whereas they inactivated E. coli cells strongly by photocatalytic and the photoelectrochemical reaction under UVA light. In the case of the columnar TiO2 films, the photoelectrochemical inactivation rate was 330% higher than the purely photocatalytic inactivation rate. On the other hand, applying a potential bias to a branched TiO2 film only increased the inactivation rate by 30%. In the case of the granular film, both inactivation rates were similar. The significant difference in the effectiveness of microbial inactivation between morphologies could be caused by different electron transfer rates through the TiO2 films, which affects the recombination rate of e-h pairs generated by photoactivation. Moreover, the surface area of the TiO2 films was another influential factor on microbial inactivation. The branched and the granular structure had a nine times and 2.5 times larger surface area than the columnar structure, respectively. The much larger surface area caused much faster inactivation of E. coli in the photocatalytic reaction. Finally, the TiO2 film showed a sustained inactivation rate after repeated use for inactivation of microbes. Our UVA-based photosensitizers will potentially lead to an improvement of solar disinfection efficiency because the UVA spectrum is the dominant UV radiation in sunlight.

Acknowledgments

This study is partially supported by the Photosynthetic Antenna Research Center (PARC), an Energy Frontier Research Center funded by the U.S. Department of Energy, Office of Science, Office of Basic Energy Sciences under Award Number DE-SC 0001035. This work was also performed in part at the Nano Research Facility (NRF), a member of the National Nanotechnology Infrastructure Network (NNIN), which is supported by the National Science Foundation under Grant No. ECS-0335765. Any opinions, findings, conclusions, or recommendations expressed in this material are those of the author(s) and do not necessarily reflect the views of the National Science Foundation. NRF is part of the School of Engineering and Applied Science at Washington University in St. Louis.

Conflict of Interest

The authors declare no conflict of interest.

References

  1. Shannon, M.A.; Bohn, P.W.; Elimelech, M.; Georgiadis, J.G.; Marinas, B.J.; Mayers, A.M. Science and technology for water purification in the coming decades. Nature 2008, 452, 301–310. [Google Scholar]
  2. Montgomery, M.A.; Elimelech, M. Water and sanitation in developing countries: Including health in the equation. Environ. Sci. Technol. 2007, 41, 17–24. [Google Scholar] [CrossRef]
  3. Kemper, K.E. Groundwater-from development to management. Hydrogeol. J. 2003, 12, 3–5. [Google Scholar] [CrossRef]
  4. Szewzyk, U.; Szewzyk, R.; Manz, W.; Schleifer, K.H. Microbiological safety of drinking water. Annu. Rev. Microbiol. 2000, 54, 81–127. [Google Scholar] [CrossRef]
  5. Gopal, K.; Tripathy, S.S.; Bersillon, J.L.; Dubey, S.P. Chlorination byproducts, their toxicodynamics and removal from drinking water. J. Hazard. Mater. 2007, 140, 1–6. [Google Scholar] [CrossRef]
  6. Krasner, S.W.; Weinberg, H.S.; Richardson, S.D.; Pastor, S.J.; Chinn, R.; Sclimenti, M.J.; Onstad, G.D.; Thruston, A.D. Occurrence of a new generation of disinfection byproducts. Environ. Sci. Technol. 2006, 40, 7175–7185. [Google Scholar]
  7. Zhang, D.; Li, G.; Yu, J.C. Inorganic materials for photocatalytic water disinfection. J. Mater. Chem. 2010, 20, 4529–4536. [Google Scholar] [CrossRef]
  8. Matsunaga, T.; Tomoda, R.; Nakajima, T.; Wake, H. Photoelectrochemical sterilization of microbial cells by semiconductor powders. FEMS Microbiol. Lett. 1985, 29, 211–214. [Google Scholar] [CrossRef]
  9. Wei, C.; Lin, W.Y.; Zaina, Z.; Williams, N.E.; Zhu, K.; Kruzic, A.P.; Smith, R.L.; Rajeshwar, K. Bactericidal activity of TiO2 photocatalyst in aqueous media: toward a solar-assisted water disinfection system. Environ. Sci. Technol. 1994, 28, 934–938. [Google Scholar] [CrossRef]
  10. Hu, C.; Lan, Y.; Qu, J.; Hu, X.; Wang, A. Ag/AgBr/TiO2 visible light photocatalyst for destruction of azodyes and bacteria. J. Phys. Chem. B 2006, 110, 4066–4072. [Google Scholar]
  11. Hu, C.; Guo, J.; Qu, J.; Hu, X. Photocatalytic degradation of pathogenic bacteria with AgI/TiO2 under visible light irradiation. Langmuir 2007, 23, 4982–4987. [Google Scholar] [CrossRef]
  12. Wu, B.; Zhuang, W.Q.; Sahu, M.; Biswas, P.; Tang, Y.J. Cu-doped TiO(2) nanoparticles enhance survival of Shewanella oneidensis MR-1 under ultraviolet light (UV) exposure. Sci. Total Environ. 2011, 409, 4635–4639. [Google Scholar] [CrossRef]
  13. Wang, P.; Huang, B.; Qin, X.; Zhang, X.; Dai, Y.; Whangbo, M.H. Ag/AgBr/WO3 3H2O: Visible-light photocatalyst for bacteria destruction. Inorg. Chem. 2009, 48, 10697–10702. [Google Scholar] [CrossRef]
  14. Mccullagh, C.; Robertson, J.M.C.; Bahnemann, D.W.; Robertson, P.K.J. The application of TiO2 photocatalysis for disinfection of water contaminated with pathogenic micro-organisms: A review. Res. Chem. Intermed. 2007, 33, 359–375. [Google Scholar] [CrossRef]
  15. Amezaga-Madrid, P.; Nevarez-Moorillon, G.V.; Orrantia-Borunda, E.; Miki-Yoshida, M. Photoinduced bactericidal activity against Pseudomonas aeruginosa by TiO2 based thin films. FEMS Microbiol. Lett. 2002, 211, 183–188. [Google Scholar]
  16. Kuhn, K.P.; Chaberny, I.F.; Massholder, K.; Stickler, M.; Benz, V.W.; Sonntag, H.G.; Erdinger, L. Disinfection of surfaces by photocatalytic oxidation with titanium dioxide and UVA light. Chemosphere 2003, 53, 71–77. [Google Scholar] [CrossRef]
  17. Sunada, K.; Watanabe, T.; Hashimoto, K. Studies on photokilling of bacteria on TiO2 thin film. J. Photochem. Photobiol. A 2003, 156, 227–233. [Google Scholar] [CrossRef]
  18. Reddy, M.P.; Phil, H.H.; Subrahmanyam, M. Photocatalytic disinfection of Escherichia coli over titanium (IV) oxide supported on Hβ zeolite. Catal. Lett. 2008, 123, 56–64. [Google Scholar]
  19. Yu, H.; Quan, X.; Zhang, Y.; Ma, N.; Chen, S.; Zhao, H. Electrochemically assisted photocatalytic inactivation of Escherichia coli under visible light using a ZnIn2S4 film electrode. Langmuir 2008, 24, 7599–7604. [Google Scholar] [CrossRef]
  20. Hayden, S.C.; Allam, N.K.; El-Sayed, M.A. TiO2 Nanotube/CdS hybrid electrodes: Extraordinary enhancement in the inactivation of Escherichia coli. J. Am. Chem. Soc. 2010, 132, 14406–14408. [Google Scholar] [CrossRef]
  21. Thimsen, E.; Rastgar, N.; Biswas, P. Nanostructured TiO2 films with controlled morphology synthesized in a single step process: Performance of dye-sensitized solar cells and photo watersplitting. J. Phys. Chem. C 2008, 112, 4134–4140. [Google Scholar] [CrossRef]
  22. An, W.J.; Thimsen, E.; Biswas, P. Aerosol-chemical vapor deposition method for synthesis of nanostructured metal oxide thin films with controlled morphology. J. Phys. Chem. Lett. 2010, 1, 249–253. [Google Scholar] [CrossRef]
  23. An, W.J.; Jiang, D.D.; Matthews, J.R.; Borrelli, N.F.; Biswas, P. Thermal conduction effects impacting morphology during synthesis of columnar nanostructured TiO2 thin films. J. Mater. Chem. 2011, 21, 7913–7921. [Google Scholar] [CrossRef]
  24. Reyes-Coronado, D.; Rodriguez-Gattorno, G.; Espinosa-Pesqueira, M.E.; Cab, C.; Coss, R.; Oskam, G. Phase-pure TiO2 nanoparticles: anatase, brookite and rutile. Nanotechnology 2008, 19. [Google Scholar] [CrossRef]
  25. Chang, J.C.; Ossoff, S.F.; Lobe, D.C.; Dorfman, M.H.; Dumais, C.M.; Qualls, R.G.; Johnson, J.D. UV inactivation of pathogenic and indicator microorganisms. Appl. Environ. Microbiol. 1985, 49, 1361–1365. [Google Scholar]
  26. McGuigan, K.G.; Joyce, T.M.; Conroy, R.M. Solar disinfection: use of sunlight to decontaminate drinking water in developing countries. J. Med. Microbiol. 1999, 48, 785–787. [Google Scholar] [CrossRef]

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MDPI and ACS Style

Park, J.; Kettleson, E.; An, W.-J.; Tang, Y.J.; Biswas, P. Inactivation of E. Coli in Water Using Photocatalytic, Nanostructured Films Synthesized by Aerosol Routes. Catalysts 2013, 3, 247-260. https://doi.org/10.3390/catal3010247

AMA Style

Park J, Kettleson E, An W-J, Tang YJ, Biswas P. Inactivation of E. Coli in Water Using Photocatalytic, Nanostructured Films Synthesized by Aerosol Routes. Catalysts. 2013; 3(1):247-260. https://doi.org/10.3390/catal3010247

Chicago/Turabian Style

Park, Jinho, Eric Kettleson, Woo-Jin An, Yinjie J. Tang, and Pratim Biswas. 2013. "Inactivation of E. Coli in Water Using Photocatalytic, Nanostructured Films Synthesized by Aerosol Routes" Catalysts 3, no. 1: 247-260. https://doi.org/10.3390/catal3010247

APA Style

Park, J., Kettleson, E., An, W. -J., Tang, Y. J., & Biswas, P. (2013). Inactivation of E. Coli in Water Using Photocatalytic, Nanostructured Films Synthesized by Aerosol Routes. Catalysts, 3(1), 247-260. https://doi.org/10.3390/catal3010247

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