Abstract
Photocatalysis disinfection has great potential for irrigation water disinfection to improve fresh produce safety. Titanium dioxide (TiO2) nanoparticle (NP)-embedded cellulose acetate (CA) film has shown effectiveness against Escherichia coli (E. coli) O157:H7 in water. The current study evaluated the effect of natural water compounds on the photo-disinfection efficacy of TiO2 NP-embedded CA film. Humic acid, calcium carbonate (CaCO3), and kaolin clay solutions were prepared at four concentrations, respectively. When concentration increased from 0 to 20 ml/L, inactivation of E. coli O157:H7 in humic acid, CaCO3, and kaolin clay solutions decreased from 6 log to 5, 4, and 2 log CFU/ml, respectively after 3 h treatment. Turbidity, UVT-254, water hardness, total suspended solids (TSS), and total organic carbon (TOC) of the solutions were measured. UVT-254 and turbidity had the highest correlation with the inhibition effect of water compounds on photo-disinfection efficacy. A prediction equation was developed with UVT-254 and water hardness as independent variables to predict photo-disinfection efficacy in natural water. E. coli O157:H7 decreased by 1 and 2.5 log CFU/ml in unfiltered and filtered natural creek water samples after treatment. The results from this study showed promise in the use of TiO2 NP-embedded CA film to inactivate pathogens in natural water.
HIGHLIGHTS
Natural water compounds affect TiO2 photo-disinfection efficacy in different degrees.
UV transmittance and water hardness are important water quality parameters that can affect TiO2 photo-disinfection efficacy.
Prediction equation was developed to predict TiO2 photo-disinfection efficacy in natural water.
Filtration is an effective pre-treatment method for improving TiO2 photo-disinfection in natural water.
INTRODUCTION
Agriculture consumes 70% of the freshwater used worldwide, and the number increases to 95% in developing countries (FAO 2008). As a crucial part of agricultural water, irrigation water is one of the main pathways by which pathogenic microorganisms can reach fresh produce (FDA 2013). Irrigating produce to be eaten raw with contaminated water may increase the risk of foodborne illness (Chalmers et al. 2000; Gu et al. 2019; Rodrigues et al. 2020). Evidence of produce contamination through contaminated irrigation water has been found in epidemiological investigations (Steele & Odumeru 2004). Irrigation water has been implicated in several E. coli O157:H7 outbreaks (Ackers et al. 1998; CDC 1999; Iwu & Okoh 2019). Several studies have demonstrated that pathogens can transfer from contaminated irrigation water to soil and fresh produce and survive for a long period (Islam et al. 2004, 2005; Jokinen et al. 2019; Kabir et al. 2020). Moreover, the occurrence of the internationalization of pathogens in plants through contaminated irrigation water has been reported (Erickson et al. 2010; Erickson et al. 2019). Improving irrigation water safety can effectively reduce the risk of fresh produce contamination.
Chlorination is the most commonly used disinfection method, however, disinfection byproducts (DBPs) that are potentially carcinogenic may be produced when chlorine reacts with natural organic matter (Marugán et al. 2008). Treatment methods such as UV and ozone are effective and have been demonstrated for drinking water treatment (Solomon et al. 2002; Loeb et al. 2012). However, these methods are costly and may not be suitable for irrigation water disinfection. The development and implementation of alternative disinfection methods are therefore needed.
Photocatalysis disinfection inactivates microorganisms by reactive oxygen species (ROS) generated when a semiconductor photocatalyst is activated by light in the presence of water and oxygen. Photocatalysis disinfection is an economic and environmentally friendly process and might be an alternative water disinfection method for irrigation water (Dasgupta et al. 2017). Titanium dioxide (TiO2) has been considered the most suitable photocatalyst for water disinfection due to its strong oxidizing abilities, chemical stability, low cost, and low toxicity (Chong et al. 2010). TiO2 has a bandgap energy of about 3.2 eV, which means light with a wavelength of approximately 385 nm (i.e. UV-A light) can activate TiO2 photocatalysis (Foster et al. 2011). TiO2 has three crystalline structures: anatase, rutile, and brookite. The photocatalytic effectiveness and the agglomeration behavior of TiO2 depends on its structures (Sygouni & Chrysikopoulos 2015; Yemmireddy & Hung 2015b). Mixtures of anatase and rutile have shown higher effectiveness as photocatalysts than other structures (Ishibashi et al. 2000). More than 1,000 research papers have been published regarding TiO2 photocatalytic disinfection of microorganisms (Byrne et al. 2015). It has been proved that TiO2 can kill a wide range of microorganisms, including Gram-negative and Gram-positive bacteria, bacteriophage, fungi, protozoa, and viruses (Foster et al. 2011). More recently, the interaction of human adenoviruses and TiO2 nanoparticles has been investigated (Syngouna et al. 2017).
TiO2 NP-embedded cellulose acetate (CA) film has shown effectiveness in the inactivation of bacteria in water (Xie & Hung 2019). This film might be combined with different types of solar photocatalytic reactors for water treatment. However, when applyied in natural water, various organic and inorganic compounds may detrimentally affect photocatalysis disinfection of water. The effect of these water compounds on photocatalysis disinfection needs to be understood before this technology can be practically applied. Humic substances constitute the major fraction of natural organic matter (NOM) in natural water and 90% of total dissolved organic carbon (DOC) in surface water may come from humic acid (Alkan et al. 2007). It has been reported that humic acid can inhibit the photocatalysis process by acting as an ·OH scavenger (Garbin et al. 2007; Cheng et al. 2018). Calcium carbonate (CaCO3) occurs in rocks, soil, and natural water world-wide. The presence of CaCO3 affects water hardness and alkalinity, and it is the predominant component of scales deposited from natural water (Wang et al. 2009). The effect of CaCO3 on photocatalysis inactivation is rarely reported. Kaolin clay is one of the common inorganic particles in natural water, and it contributes to turbidity in water and might be the worst particle for shielding (Liu & Zhang 2006). The effect of kaolin clay on photocatalysis disinfection in water has not been reported. Also, there is a lack of information on the comparison of the inhibition effect of different water compounds on photocatalysis disinfection.
The overall purpose of this study was to determine the effect of natural water compounds on the photo-disinfection efficacy of TiO2 NP-embedded CA films. Specific objectives include:
- (i)
to determine the photo-disinfection efficacy of TiO2 NP-embedded CA film in water containing humic acid, CaCO3, and kaolin clay;
- (ii)
to evaluate the correlation between water quality parameters and the photo-disinfection efficacy of TiO2 NP-embedded CA film in water;
- (iii)
to develop a prediction equation for predicting the disinfection efficacy of TiO2 NP-embedded CA film in natural water.
MATERIALS AND METHODS
Preparation of TiO2 NPs-embedded film
Aeroxide® P25 TiO2 nanoparticles (anatase–rutile), acetone, cellulose acetate (average Mn ∼30,000 by GPC), and triethyl citrate (TEC) (>99%) were purchased from Sigma-Aldrich (St Louis, MO, USA). TiO2 NPs-embedded CA film was prepared using a solution casting method as described in Xie & Hung (2018). An optimum TiO2 NPs concentration at 0.82 mg/cm2 on the film to achieve the highest bactericidal effect had been determined in a previous study (Xie & Hung 2020 submitted). To fabricate the film, 4 g of CA and 0.4 g of TiO2 were dissolved and suspended in 20 ml of acetone at room temperature (24 °C), separately. TEC (1.2 g) was added to TiO2 NPs suspension as plasticizer. An ultra-sonication bath (Model FS60, Fisher Scientific, Waltham, MA, USA) was used to assist the suspension of TiO2 NPs. After sonication, TiO2-solvent suspension was added into the CA solution gradually using a pipette with stirring, and the solution was continuously stirred for 2 h. Five millilitres of the mixed solution was added into each glass Petri dish (88 mm in diameter, Corning®, Sigma-Aldrich (St Louis, MO, USA)) and allowed to dry with Petri dish lid covering in a fume hood at 24 °C overnight, and then stored in a vacuum desiccator for 24 h. The thickness of the prepared film was 53.5–54.7 μm.
Preparation of bacterial strains and inoculum
A five-strain cocktail of nalidixic-acid-adapted E. coli O157:H7 strains (E009 (beef), EO932 (cattle), O157-1 (beef), O157-4 (human), O157-5 (human)) was used in this study. The strains were stored at −70 °C in tryptic soy broth (Becton Dickson and Company, Sparks, MD, USA; TSB) containing 20% glycerol. To resuscitate the bacteria, each strain was streaked on Sorbitol MacConkey agar (Hardy Diagnostics, Santa Maria, CA, USA) supplemented with 50 μg/ml nalidixic acid (Sigma-Aldrich, St Louis, MO, USA; SMACNA) and incubated at 37 °C for 24 h.
One isolated colony of each strain was then transferred into 10 ml of tryptic soy broth supplemented with 50 μg/ml nalidixic acid (TSBNA) using a sterile inoculation loop and incubated at 37 °C overnight. Then one loopful (10 μL) of bacterial culture was transferred again into 10 ml of TSBNA and incubated overnight. After incubation, bacterial suspension was centrifuged at 4,000 × g for 12 min, and the supernatant was decanted and the cell pellet was resuspended in 9 ml of sterilized phosphate-buffered saline (Acros Organics, NJ, USA; PBS, pH 7.2). The inoculum was prepared by mixing 9 ml of each strain to obtain a five-strain cocktail with a concentration of about 9 log CFU/ml. The inoculum was further adjusted to a concentration of about 8 log CFU/ml by making ten-fold dilution.
Preparation of water samples
CaCO3 was purchased from Fisher Scientific (Waltham, MA, USA). Kaolin clay and humic acid were purchased from Sigma-Aldrich (St Louis, MO, USA). Stock solutions of CaCO3, kaolin clay and humic acid were prepared at 200 mg/L each and stored at 4 °C until use. Water samples containing various levels of CaCO3, kaolin clay, or humic acid were prepared using the stock solutions before the experiment. The pH of these water samples was measured as about 6.5 ± 0.4. The natural water sample was obtained from a creek in Griffin, Georgia (33.2545488, −84.3114407).
Photo-disinfection of E. coli O157:H7 in water
Photo-disinfection of E. coli O157:H7 in water was performed as described in Xie & Hung (2019). In brief, the photocatalytic inactivation of E. coli O157:H7 in water was carried out in 150 ml glass beakers. TiO2 NP-embedded CA films (4.5 cm in diameter) were adhered to the bottom of the beakers using ethylene-vinyl acetate (EVA, AdTech™, adhesive technologies, Hampton, NH, USA). The beakers were sterilized with UV-C light for 30 min in a bio-safety cabinet (Class II Type A/B3, Nuaire, Plymouth, MN, USA) before the experiment. The beakers were then placed on a platform shaker (Model Classic 10, New Brunswick Scientific Co., Inc., Edison, NJ, USA) inside a photocatalytic disinfection chamber (Figure 1). Four 40 W UV-A lamps (American DJ®, Model UV Panel HP™, LL-UV P40, Los Angeles, CA, USA) were fitted on the inside top of the photocatalytic disinfection chamber. The shaker was set at a speed of 100 rpm during the photo-disinfection experiment. Water samples were inoculated right before the photo-disinfection experiment. In this study, 30 ml of water sample was inoculated with 300 μl inoculum. The experiments were carried out at a light intensity of 1 mW/cm2.
Experiment setting of photo-disinfection of water using TiO2 NP-embedded CA film.
Experiment setting of photo-disinfection of water using TiO2 NP-embedded CA film.
Sampling and bacterial enumeration
Water samples were taken hourly for three hours and 1 ml of sample was taken each time. Serial dilutions were made in PBS and appropriate dilutions were plated on SMACNA agar and incubated at 37 °C for 24 h. Colonies were counted and recorded as log CFU/ml.
Water quality parameter measurement
Water quality parameters including turbidity, UV transmittance at 254 nm (UVT-254), total organic carbon (TOC), total suspended solids (TSS), and total hardness of all the lab-prepared water samples and natural water samples were measured. Turbidity, TOC, and TSS were measured following Hach methods 8237, 10129, and 8006, respectively, using a DR/90 colorimeter (HACH, Loveland, CO, USA). UVT-254, which measures the percentage of light that passes through a water sample at 254 nm, was measured using a UV-vis spectrophotometer (Orion™ AquaMate 8000, Thermo Fisher Scientific, Waltham, MA, USA). Total hardness was determined following USEPA method 8226.
Statistical analysis
Experiments were replicated at least twice. Duplicate measurements were made on each sample. Pearson correlation analysis and partial correlation analysis on the water quality parameters and bacterial reduction were conducted using JMP 14 (SAS Institute, Cary, NC, USA). The regression equation was developed by least squares regression also using JMP 14. All the tests were performed at a significance level of 0.05.
RESULTS AND DISCUSSION
Effect of water compound on photo-disinfection efficacy of TiO2 embedded CA film
Figure 2 shows the results of the photo-disinfection of E. coli O157:H7 using TiO2 NP-embedded CA film in DI water and lab-prepared water samples with different natural water compounds under UV-A light illumination. In DI water, E. coli O157:H7 population was reduced by about 5.8 log after 3 h of photo-disinfection treatment. Increasing humic acid concentration from 2 to 20 mg/L reduced bacterial reduction from 3.9 to 0.8 log CFU/ml. Increasing CaCO3 concentration from 2 to 20 mg/L reduced bacterial reduction from 4.3 to 1.9 log CFU/ml. In comparison with humic acid and CaCO3, kaolin clay had the least inhibition effect on photo-disinfection. When adding 2 mg/L of kaolin clay in water, 5 log reductions were achieved after 3 h of photo-disinfection treatment. When the concentration of kaolin clay was increased to 20 mg/L, more than 4 log reductions could still be achieved after 3 h of treatment.
Effect of different water compounds on photo-disinfection of E. coli O157:H7 using TiO2 NP-embedded CA film. Vertical bars represent the standard error of three replicates.
Effect of different water compounds on photo-disinfection of E. coli O157:H7 using TiO2 NP-embedded CA film. Vertical bars represent the standard error of three replicates.
Inactivation of bacteria using TiO2 immobilized systems has been demonstrated in published studies. Xiong & Hu (2013) evaluated the inactivation of E. coli using a UVA/LED system with a crystallizing dish coated with TiO2. They reported that at a light intensity of 6 mW/cm2, it took 145 min for 3 log inactivations of E. coli in 30 ml of inoculated distilled water. Rodrigues et al. (2007) evaluated the inactivation of E. coli in synthetic water and natural water using a glass reactor with immobilized TiO2 (catalyst). They found 100% bacterial reduction in synthetic water, and 80% bacterial recution in natural water after 1 h treatment under solar light illumination. Due to the variation in factors such as experimental setting, TiO2 immobilized system, light intensity, and water volume among different studies, the treatment efficiency may not be compared directly.
The disinfection kinetics in the current study follows a non-linear trend with a ‘shoulder’. The ‘shoulder’ can be explained by the cumulative-damage nature of photo-disinfection treatment on the cytoplasmic membrane rather than an instantly lethal effect (Gyürék & Finch 1998). The disinfection kinetics for CaCO3 and humic acid tend to have a longer ‘shoulder’ period. This indicates that the bacterial inactivation process was subject to interference by these two water compounds. Many empirical kinetic models have been reported in the literature for the interpretation of photo-disinfection data. The following models have been summarized as the most well-known disinfection kinetic models (Marugán et al. 2008; Chong et al. 2010; Yemmireddy & Hung 2015a).
Comparison of kinetic models to predict photo-disinfection of TiO2 NP-embedded CA film in different water compound solutions
Testing solution and concentration . | Root mean squared error (RMSE) . | Model selected . | ||||
---|---|---|---|---|---|---|
Chick–Watson . | Delayed Chick–Watson . | Modified Chick–Watson . | Homs . | Modified Homs . | ||
2 mg/L humic acid | 0.7901 | 0.6603 | 0.7920 | 1.3289 | 0.7920 | Delayed Chick–Watson |
20 mg/L humic acid | 0.0612 | 0.1732 | 0.0625 | 10.0704 | 0.1871 | Chick–Watson |
2 mg/L CaCO3 | 0.8688 | 0.6229 | 0.8688 | 1.5220 | 0.7920 | Delayed Chick–Watson |
20 mg/L CaCO3 | 0.4980 | 0.3873 | 0.4981 | 0.7381 | / | Delayed Chick–Watson |
2 mg/L kaolin clay | 0.5904 | 0.3502 | 0.5909 | 4.8774 | 1.5642 | Delayed Chick–Watson |
20 mg/L kaolin clay | 0.5009 | 0.2933 | 0.5014 | 1.3154 | 0.5014 | Delayed Chick–Watson |
DI water | 1.0485 | 0.7071 | 1.0516 | 1.9343 | 1.0516 | Delayed Chick–Watson |
Testing solution and concentration . | Root mean squared error (RMSE) . | Model selected . | ||||
---|---|---|---|---|---|---|
Chick–Watson . | Delayed Chick–Watson . | Modified Chick–Watson . | Homs . | Modified Homs . | ||
2 mg/L humic acid | 0.7901 | 0.6603 | 0.7920 | 1.3289 | 0.7920 | Delayed Chick–Watson |
20 mg/L humic acid | 0.0612 | 0.1732 | 0.0625 | 10.0704 | 0.1871 | Chick–Watson |
2 mg/L CaCO3 | 0.8688 | 0.6229 | 0.8688 | 1.5220 | 0.7920 | Delayed Chick–Watson |
20 mg/L CaCO3 | 0.4980 | 0.3873 | 0.4981 | 0.7381 | / | Delayed Chick–Watson |
2 mg/L kaolin clay | 0.5904 | 0.3502 | 0.5909 | 4.8774 | 1.5642 | Delayed Chick–Watson |
20 mg/L kaolin clay | 0.5009 | 0.2933 | 0.5014 | 1.3154 | 0.5014 | Delayed Chick–Watson |
DI water | 1.0485 | 0.7071 | 1.0516 | 1.9343 | 1.0516 | Delayed Chick–Watson |
Effect of kaolin clay on water property and disinfection efficacy
The effects of kaolin clay on water quality parameters and bacterial reduction are shown in Table 2. Kaolin clay did not have a strong inhibition effect on photo-disinfection in the current study compared with humic acid and CaCO3. Results of water property analysis showed that increasing kaolin clay concentration in water did not significantly change TOC and hardness. UVT-254 slightly decreased when kaolin clay concentration increased. However, kaolin clay concentration significantly affected the total suspended solids (TSS) and turbidity. It has been reported that kaolin clay might be the worst particle for shielding light (Liu & Zhang 2006) and hence may affect photo-disinfection efficacy. However, the current study showed that when the turbidity and TSS of kaolin clay solution were increased to 24 FAU and 24 mg/L, respectively, more than 4.2 log bacterial reductions were achieved. This indicates that turbidity and TSS might not be significant parameters affecting photo-disinfection efficacy.
Effect of water compounds on water quality parameters and bacterial reduction
Water compounds . | Concentration (mg/L) . | Turbidity (FAU) . | UVT-254 (%) . | Total organic carbon (mg/L) . | Total hardness (mg/L) . | Total suspended solids (mg/L) . | Bacterial reduction at 3 h (log CFU/ml) . |
---|---|---|---|---|---|---|---|
Humic acid | 2 | 3 ± 1 | 89.74 ± 2.67 | 1.2 ± 0.1 | 2 ± 0 | 3 ± 0 | 3.9 ± 0.6 |
5 | 9 ± 4 | 74.45 ± 3.04 | 2.2 ± 0.5 | 2 ± 0 | 9 ± 1 | 2.1 ± 0.5 | |
10 | 16 ± 5 | 59.36 ± 3.41 | 3.1 ± 0.5 | 2 ± 0 | 12 ± 3 | 1.6 ± 0.6 | |
20 | 37 ± 6 | 40.35 ± 3.79 | 5.8 ± 0.6 | 2 ± 0 | 27 ± 7 | 0.8 ± 0.6 | |
CaCO3 | 2 | 2 ± 0 | 93.96 ± 2.01 | 0.0 ± 0.0 | 2 ± 2 | 1 ± 1 | 4.3 ± 0.6 |
5 | 6 ± 2 | 93.49 ± 2.23 | 0.0 ± 0.0 | 5 ± 2 | 0 ± 0 | 3.4 ± 0.6 | |
10 | 8 ± 2 | 91.80 ± 1.23 | 0.0 ± 0.0 | 12 ± 2 | 1 ± 1 | 2.8 ± 0.7 | |
20 | 13 ± 2 | 89.90 ± 3.52 | 0.0 ± 0.0 | 22 ± 4 | 2 ± 1 | 1.9 ± 0.9 | |
Kaolin clay | 2 | 2 ± 0 | 91.50 ± 1.45 | 0.0 ± 0.0 | 0 ± 0 | 2 ± 2 | 5.0 ± 0.1 |
5 | 6 ± 2 | 90.25 ± 2.70 | 0.0 ± 0.0 | 0 ± 0 | 4 ± 2 | 5.0 ± 0.1 | |
10 | 13 ± 3 | 81.04 ± 2.38 | 0.0 ± 0.0 | 0 ± 0 | 10 ± 3 | 4.6 ± 0.4 | |
20 | 24 ± 4 | 72.50 ± 2.08 | 0.0 ± 0.0 | 0 ± 0 | 23 ± 2 | 4.2 ± 0.5 | |
DI water | – | 0 ± 0 | 0.00 ± 0.00 | 0.0 ± 0 | 0 ± 0 | 0 ± 0 | 5.8 ± 0.3 |
Water compounds . | Concentration (mg/L) . | Turbidity (FAU) . | UVT-254 (%) . | Total organic carbon (mg/L) . | Total hardness (mg/L) . | Total suspended solids (mg/L) . | Bacterial reduction at 3 h (log CFU/ml) . |
---|---|---|---|---|---|---|---|
Humic acid | 2 | 3 ± 1 | 89.74 ± 2.67 | 1.2 ± 0.1 | 2 ± 0 | 3 ± 0 | 3.9 ± 0.6 |
5 | 9 ± 4 | 74.45 ± 3.04 | 2.2 ± 0.5 | 2 ± 0 | 9 ± 1 | 2.1 ± 0.5 | |
10 | 16 ± 5 | 59.36 ± 3.41 | 3.1 ± 0.5 | 2 ± 0 | 12 ± 3 | 1.6 ± 0.6 | |
20 | 37 ± 6 | 40.35 ± 3.79 | 5.8 ± 0.6 | 2 ± 0 | 27 ± 7 | 0.8 ± 0.6 | |
CaCO3 | 2 | 2 ± 0 | 93.96 ± 2.01 | 0.0 ± 0.0 | 2 ± 2 | 1 ± 1 | 4.3 ± 0.6 |
5 | 6 ± 2 | 93.49 ± 2.23 | 0.0 ± 0.0 | 5 ± 2 | 0 ± 0 | 3.4 ± 0.6 | |
10 | 8 ± 2 | 91.80 ± 1.23 | 0.0 ± 0.0 | 12 ± 2 | 1 ± 1 | 2.8 ± 0.7 | |
20 | 13 ± 2 | 89.90 ± 3.52 | 0.0 ± 0.0 | 22 ± 4 | 2 ± 1 | 1.9 ± 0.9 | |
Kaolin clay | 2 | 2 ± 0 | 91.50 ± 1.45 | 0.0 ± 0.0 | 0 ± 0 | 2 ± 2 | 5.0 ± 0.1 |
5 | 6 ± 2 | 90.25 ± 2.70 | 0.0 ± 0.0 | 0 ± 0 | 4 ± 2 | 5.0 ± 0.1 | |
10 | 13 ± 3 | 81.04 ± 2.38 | 0.0 ± 0.0 | 0 ± 0 | 10 ± 3 | 4.6 ± 0.4 | |
20 | 24 ± 4 | 72.50 ± 2.08 | 0.0 ± 0.0 | 0 ± 0 | 23 ± 2 | 4.2 ± 0.5 | |
DI water | – | 0 ± 0 | 0.00 ± 0.00 | 0.0 ± 0 | 0 ± 0 | 0 ± 0 | 5.8 ± 0.3 |
Effect of CaCO3 on water properties and disinfection efficacy
Results in Table 2 show that increasing CaCO3 concentration did not affect TOC and TSS concentration in water. Increasing CaCO3 slightly increased UVT-254 and turbidity. Water hardness significantly increased when increasing CaCO3 concentration. When the hardness of the CaCO3 solution increased to 22 mg/L, bacterial reduction decreased to about 1.9 log CFU/ml. Similar findings regarding the effect of CaCO3 on photo-disinfection or photo-degradation have been reported in other published reports. Cohen-Yaniv et al. (2008) studied the inactivation of Flavobacterium and E. coli in water by a continuous stirred tank reactor (CSTR) fed with suspended or glass immobilized TiO2. They found water hardness increase reduced photocatalytic inactivation efficiency, and they suggested the treatment of water chemically before disinfection. Sreethawong et al. (2014) studied the degradation of Congo Red (CR) azo dye using nano-Ag/sol-gel TiO2-In2O3 mixed oxide mesoporous-assembled nanocrystals. Their results showed that the water hardness reduced the photocatalytic CR dye degradation activity. In natural water, CaCO3 is the major compound that causes an increase in water hardness (Sreethawong et al. 2014). Increased water hardness can cause a variety of problems such as reduced efficiency of chlorine treatment and decreased life of plumbing and appliances (Pangloli & Hung 2013). Results from the current study suggest that water hardness might be a significant parameter affecting photo-disinfection efficacy.
Effect of humic acid on water properties and disinfection efficacy
Results in Table 2 show that increasing humic acid concentration significantly increased TOC, turbidity, and TSS in water, whereas the UVT-254 reading decreased significantly. When humic acid concentration increased to 20 mg/L, turbidity increased to 37 FAU, TSS increased to 27 mg/L, TOC increased to 5.8 mg/L, while UVT-254 decreased to 40.35%. At this humic acid concentration, bacterial reduction decreased significantly to 0.8 log CFU/ml. Although humic acid significantly affected the readings of turbidity, UVT-254, TOC, and TSS, turbidity and TSS were found not significantly to affect microbial inactivation as reported above.
The inhibition effect of humic acid on photo-disinfection has also been reported in published reports. Cheng et al. (2018) studied the effect of humic acid on virus removal using a photocatalytic membrane reactor (PMR). They found that when increasing humic acid concentration from 0 to 5 and 7.5 ml/L, the photocatalytic disinfection efficiency of phage f2 decreased from 5.4 to 3.5 and 2.2 log, respectively. Marugán et al. (2008) studied the effect of humic acid on the photocatalytic disinfection kinetics of E. coli suspensions using TiO2/SiO2 photocatalysts. They found that low humic substance concentration could inhibit the disinfection process and when humic acid concentration increased from 0 to 2.0 mg/L, disinfection efficacy reduced from 5 log to about 2 log after 1 h treatment. According to these studies, the main reason that humic acid inhibited photo-disinfection efficacy was due to the consumption of hydroxyl radicals produced by TiO2 photocatalysis.
Humic acid is a major fraction of natural organic matter (NOM) in natural water (Wang & Hsieh 2001). The C = C double bonds and C = O double bonds in humic acid chemical structure can absorb UV light at 254 nm and prevent light at this wavelength transmitting through water (Cheng et al. 2018), and hence caused low UVT-254 readings for humic acid solutions in the current study (Table 2). UVT-254 measures the transmittance of UV light at 254 nm through the water. It has been reported that the efficiency of UV disinfection will be affected by the turbidity of the target water and the resultant transmittance of UV light through the water (Cantwell & Hofmann 2011), while the current study showed that for photocatalytic disinfection, the effect of turbidity and UVT-254 on disinfection efficiency varied among the different compounds studied. For example, kaolin clay caused a significant increase in turbidity, but it did not have as much effect on bacterial reduction as other compounds such as humic acid.
Prediction equation development
As discussed above, various water compounds such as humic acid and CaCO3 have strong inhibition effects on the TiO2 NP-embedded CA film photo-disinfection effect. However, in a practical situation, it is unrealistic to monitor the level of all compounds in water. Identifying common water quality parameters that can be used as water quality indicators for photo-disinfection is a more efficient solution.
To select the proper water quality parameters that can be used for predicting TiO2 NP-embedded CA film disinfection efficacy, the Pearson correlation of all the water quality parameters reported in Table 2 was first performed and the results are presented in Table 3. It shows that several variables are strongly correlated with another variable. For example, turbidity and TSS have a correlation coefficient of 0.899, TOC and UVT-254 have a correlation coefficient of −0.884, turbidity and UVT-254 have a correlation coefficient of −0.881, and UVT-254 and TSS have a correlation coefficient of −0.872. These suggest collinearity exists among these variables and using all the variables for model development would cause an inaccurate predictor contribution to the model. Therefore, only one variable between highly correlated pairs should be considered for regression development.
Pearson correlations of water quality parameters and bacterial reduction
. | Turbidity . | UV-254 . | Total organic carbon . | Total hardness . | Total suspended solids . | Bacterial reduction . |
---|---|---|---|---|---|---|
Turbidity | 1.000 | − 0.881 | 0.674 | 0.027 | 0.899 | − 0.617 |
UV-254 | 1.000 | − 0.884 | 0.179 | − 0.872 | 0.685 | |
Total organic carbon | 1.000 | − 0.161 | 0.672 | − 0.702 | ||
Total hardness | 1.000 | − 0.284 | − 0.432 | |||
Suspended solids | 1.000 | − 0.433 | ||||
Bacterial reduction | 1.000 |
. | Turbidity . | UV-254 . | Total organic carbon . | Total hardness . | Total suspended solids . | Bacterial reduction . |
---|---|---|---|---|---|---|
Turbidity | 1.000 | − 0.881 | 0.674 | 0.027 | 0.899 | − 0.617 |
UV-254 | 1.000 | − 0.884 | 0.179 | − 0.872 | 0.685 | |
Total organic carbon | 1.000 | − 0.161 | 0.672 | − 0.702 | ||
Total hardness | 1.000 | − 0.284 | − 0.432 | |||
Suspended solids | 1.000 | − 0.433 | ||||
Bacterial reduction | 1.000 |
To determine which variable should be excluded from model development, a partial correlation between the predictor variables and the response variable was performed and the results are shown in Table 4. Pearson correlations reported in Table 3 demonstrated the linear correlation between two variables without controlling other variables in the model, while partial correlation measures the correlation between two variables with the effect of other controlling variables removed. Results show that turbidity, TOC, and TSS have Pearson correlation coefficients of –0.617, –0.702, and −0.433 with bacterial reduction, respectively. However, these three variables have much lower partial correlation coefficients of 0.161, −0.272, and 0.097 with bacterial reduction, respectively, after controlling other confounding variables in the model. As a result, UVT-254 and total hardness with high partial correlation coefficients with bacterial reduction (Table 4) are further considered for regression analysis. This conclusion further supports the observations reported above that changes in total hardness and UVT-254, respectively can explain the changes in bacterial reduction.
Partial correlations between water quality parameters and bacterial reduction
. | Turbidity . | UVT-254 . | Total organic carbon . | Total hardness . | Total suspended solids . |
---|---|---|---|---|---|
Bacterial reduction | 0.161 | 0.461 | − 0.272 | − 0.726 | 0.097 |
. | Turbidity . | UVT-254 . | Total organic carbon . | Total hardness . | Total suspended solids . |
---|---|---|---|---|---|
Bacterial reduction | 0.161 | 0.461 | − 0.272 | − 0.726 | 0.097 |
Verification of prediction equation using laboratory-prepared water samples and natural water
In order to test whether the prediction equation can accurately predict bacterial reduction in a complex environment that contains different water compounds, four different simulated water samples were prepared with different combinations of the three water compounds based on the formula shown in Table 5. Table 6 shows the observed and predicted bacterial reductions using TiO2 NP-embedded CA film in these simulated water samples. The highest bacterial reduction was detected in sample 4 (2.1 log CFU/ml), followed by sample 2, sample 1, and sample 3 with reductions of 1.8, 1.6, and 1.5 log CFU/ml, respectively. Water property analysis shows that sample 3 had the lowest UVT-254 of 61.62%. The UVT-254 of sample 1, 4, and 2 was 73.3%, 79.47%, and 81.85%, respectively. Sample 2 had the highest hardness of 20 mg/L. The hardness of sample 1 was 14 mg/L and the hardness of both samples 3 and 4 was 6 mg/L. The prediction results show that half of the samples have a prediction percentage error of less than 15%, however, the other half have a prediction percentage error of more than 30%. The prediction equation developed in the preceding section was based on the disinfection experiment carried out in individual water compounds. The prediction equation might be improved by studying the interaction effects between different water compounds during treatment.
Formula of simulated water samples
Water sample . | Kaolin clay (mg/L) . | Humic acid (mg/L) . | CaCO3 (mg/L) . |
---|---|---|---|
#1 | 10 | 10 | 10 |
#2 | 5 | 5 | 20 |
#3 | 5 | 20 | 5 |
#4 | 20 | 5 | 5 |
Water sample . | Kaolin clay (mg/L) . | Humic acid (mg/L) . | CaCO3 (mg/L) . |
---|---|---|---|
#1 | 10 | 10 | 10 |
#2 | 5 | 5 | 20 |
#3 | 5 | 20 | 5 |
#4 | 20 | 5 | 5 |
Water properties and disinfection efficacy of simulated water samples
. | . | . | Bacterial reduction at 3 h (log CFU/ml) . | . | |
---|---|---|---|---|---|
water sample . | Hardness (mg/L) . | UVT-254 (%) . | Observed . | Predicted . | Prediction percentage error (%)a . |
#1 | 14 ± 1 | 73.30 ± 0.32 | 1.6 ± 0.3 | 1.4 ± 0.1 | −13 |
#2 | 20 ± 1 | 81.95 ± 0.20 | 1.8 ± 0.2 | 1.2 ± 0.1 | −33 |
#3 | 6 ± 1 | 61.62 ± 0.53 | 1.5 ± 0.7 | 1.7 ± 0.1 | 13 |
#4 | 6 ± 1 | 79.47 ± 0.32 | 2.1 ± 0.5 | 3.0 ± 0.1 | 43 |
. | . | . | Bacterial reduction at 3 h (log CFU/ml) . | . | |
---|---|---|---|---|---|
water sample . | Hardness (mg/L) . | UVT-254 (%) . | Observed . | Predicted . | Prediction percentage error (%)a . |
#1 | 14 ± 1 | 73.30 ± 0.32 | 1.6 ± 0.3 | 1.4 ± 0.1 | −13 |
#2 | 20 ± 1 | 81.95 ± 0.20 | 1.8 ± 0.2 | 1.2 ± 0.1 | −33 |
#3 | 6 ± 1 | 61.62 ± 0.53 | 1.5 ± 0.7 | 1.7 ± 0.1 | 13 |
#4 | 6 ± 1 | 79.47 ± 0.32 | 2.1 ± 0.5 | 3.0 ± 0.1 | 43 |
Table 7 shows that in natural creek water, bacteria can be reduced by 1 log CFU/ml after 3 h treatment using TiO2 NP-embedded CA film. After filtration using a 0.45 μm filter, 1.4 log reductions were achieved. After filtration using a 0.2 μm filter, bacterial reductions increased to 2.5 log CFU/ml. As shown in Table 7, filtration also improved water quality. The hardness, turbidity, TSS, and TOC all decreased after filtration, and UVT-254 increased with filtration. Filtration can remove insoluble particles that cause the increase of these parameters and can therefore improve water quality (O'Melia 1985). Bacterial reductions were also calculated using Equation (7). The predicted bacterial reduction was −0.9 CFU/ml reduction for the water sample without filtration, and 0.9 and 1.1 CFU/ml reductions for samples filtered with 0.2 and 0.45 μm filters, respectively. The total hardness of the unfiltered water sample was over the ranges of the hardness of water samples used for the development of the prediction equation, which may affect the prediction accuracy. More types of natural water and more water property information are needed to further improve the prediction equation.
Water properties and disinfection efficacy of natural creek water samples
Filter (μm) . | Hardness (mg/L) . | Turbidity (FAU) . | Total suspended solids (mg/L) . | Total organic carbon (mg/L) . | UVT-254 (%) . | Bacterial reduction at 3 h (log CFU/ml) . | Prediction percentage error (%)a . | |
---|---|---|---|---|---|---|---|---|
actual . | predicted . | |||||||
0.2 | 20 ± 1 | 3.5 ± 2.1 | 0 | 4.9 ± 1.6 | 85.75 ± 2.25 | 2.5 ± 0.4 | 1.4 ± 0.2 | −44 |
0.45 | 24 ± 1 | 7 ± 2.8 | 1.5 ± 0.7 | 5.9 ± 1.6 | 80.71 ± 0.95 | 1.4 ± 0.1 | 0.5 ± 0.1 | −64 |
w/o | 32 ± 1 | 10.5 ± 2.1 | 3 ± 1.4 | 8.7 ± 3.3 | 77.82 ± 1.90 | 1.0 ± 0.3 | −0.9 ± 0.1 | −190 |
Filter (μm) . | Hardness (mg/L) . | Turbidity (FAU) . | Total suspended solids (mg/L) . | Total organic carbon (mg/L) . | UVT-254 (%) . | Bacterial reduction at 3 h (log CFU/ml) . | Prediction percentage error (%)a . | |
---|---|---|---|---|---|---|---|---|
actual . | predicted . | |||||||
0.2 | 20 ± 1 | 3.5 ± 2.1 | 0 | 4.9 ± 1.6 | 85.75 ± 2.25 | 2.5 ± 0.4 | 1.4 ± 0.2 | −44 |
0.45 | 24 ± 1 | 7 ± 2.8 | 1.5 ± 0.7 | 5.9 ± 1.6 | 80.71 ± 0.95 | 1.4 ± 0.1 | 0.5 ± 0.1 | −64 |
w/o | 32 ± 1 | 10.5 ± 2.1 | 3 ± 1.4 | 8.7 ± 3.3 | 77.82 ± 1.90 | 1.0 ± 0.3 | −0.9 ± 0.1 | −190 |
Nevertheless, the current study has demonstrated that using TiO2 NP-embedded CA film has the potential to inactivate pathogens in natural water. Filtration has also been found as a simple and effective method to remove water compounds that may affect bacterial inactivation during the photo-disinfection process.
CONCLUSIONS
The results of this study showed that natural water compounds such as humic acid, CaCO3, and kaolin clay can all affect the photo-disinfection efficacy of TiO2 NP-embedded CA film. Humic acid had the highest inhibition effect on photo-disinfection, followed by CaCO3 and kaolin clay. The effect of different water quality parameters on TiO2 NP-embedded CA film indicates that different water compounds affect photo-disinfection efficacy through different mechanisms. It was found that UVT-254 and turbidity can be used as indicators for predicting the effect of natural water compounds on photo-disinfection efficacy. A predictive equation was developed using UVT-254 and turbidity as independent variables. Photo-disinfection using TiO2 NP-embedded CA film reduced E. coli O157:H7 by 1 log CFU/ml in the inoculated natural creek water sample. After filtration using a 0.2 μm filter, about 2.5 log CFU/ml reductions were achieved with the same treatment. Hence, filtration can be used as an effective pre-treatment for photo-disinfection by TiO2 NP-embedded CA film.
ACKNOWLEDGEMENTS
This research was supported by State and Hatch funds allocated to the University of Georgia Agriculture Experiment Station, Griffin Campus.
DATA AVAILABILITY STATEMENT
All relevant data are included in the paper or its Supplementary Information.