Taiwan's oyster industry produces shell waste in abundant quantities every year. This study explored the feasibility of applying this resource as a simple and low-cost disinfectant to improve the microbial quality of harvested rainwater. Critical parameters affecting the disinfection efficacy of calcined oyster shell particles, i.e., heating temperature and duration, dosage, and contact time of the calcined shell material against Bacillus subtilis endospores in rainwater, were investigated. A central composite design of response surface methodology was employed to study the relative effects. As estimated from R2 coefficients, a quadratic model was identified to predict the response variable satisfactorily. Results indicated that the heating temperature, dosage, and contact time of the calcined material in the rainwater significantly influenced (p < 0.05) the sporicidal effect, consistent with the prior literature on calcined shells of similar nature. However, heating time had a relatively low influence on the sporicidal impact, suggesting that the rate of shell activation, i.e., conversion of the carbonate compound in the shell material to oxide, occurs rapidly at high calcination temperatures. In addition, the sterilization kinetics for heated oyster shell particles in aqueous media under stagnant storage conditions were investigated and found to be in good agreement with Hom's model.

  • Sporicidal effects of heated oyster shell on Bacillus subtilis endospores were explored.

  • Heating temperature, dosage, and contact time of the calcined material have a significant influence on the sporicidal effects.

  • Oyster shell heating time has a relatively low influence on the sporicidal effect compared to temperature.

  • The heated oyster shell can be potential antibacterial building material for rainwater storage tanks.

Oysters, a nutrient-rich bivalve mollusk (Chakraborty et al. 2016; Zhu et al. 2018; Maurya 2021), can be found in many parts of the world. They inhabit salty or brackish coastal waters, congregating on old shells, rocks, piers, or hard, submerged surfaces. In Taiwan, oyster cultivation accounts for more than one-sixth of the total aquaculture area, generating more than 2 billion USD in annual revenue (Vaschenko et al. 2013). Along the western coast of Taiwan, oyster fields stretch from Xiangshan in Hsinchu City in the north to Dapeng Bay in Pingtung County in the south (Liu et al. 2015; Ueng et al. 2020). Although oyster farming has substantial economic potential, the environmental impact from its by-products/wastes is unavoidable. Oyster shells (OSs) abandoned along the coast can cause a variety of health and environmental issues, involving noxious odors (Chilakala et al. 2019; Sadeghi et al. 2019) from the decomposition of remaining attached flesh, natural water contamination, soil pH increase, and marine ecosystem modification (Mohamed et al. 2012b; Li et al. 2015; Thenepalli et al. 2017).

According to the Council of Agriculture, an estimated 160,000 metric tons of OSs are generated annually as marine industrial waste in Taiwan, placing a significant burden on the fishing community in waste management and disposal (Hwang & Weng 2017). Many efforts toward sustainable recycling of OS waste into value-added products have been made (Hellen et al. 2019; Jovic et al. 2019; Andrade et al. 2020; Bonnard et al. 2020). With the main components being aragonite and calcite (Chilakala Ramakrishna & Whan 2018) (CaCO3 > 95 wt.%), OSs can be a renewable natural calcium resource for well-known applications, especially as an alkali activator in the production of unfired fly ash bricks (Li et al. 2015; Mo et al. 2018; Thomas et al. 2020) or as filler in composites (Lee et al. 2014; AlBadr et al. 2020), bio-concrete production (Hong et al. 2021), agricultural supplements (Lee et al. 2008; Mako et al. 2017; Hellen et al. 2019), pollutant remediation (Chiou et al. 2014; Xu et al. 2019; Khirul et al. 2020; Xu et al. 2021; Zheng et al. 2022), soil quality improvement (Ok et al. 2011; Torres-Quiroz et al. 2021; Wu et al. 2022), and high-tech polymer synthesis (Li et al. 2017). When calcined at 550 °C and above, the calcite structure of OSs transforms into calcium oxide (CaO) (Kwon et al. 2004; Alidoust et al. 2015; Huh et al. 2016), a promising versatile raw material. OS-derived CaO powder can be utilized in medical preparations to prevent osteoporosis or treat diseases related to calcium metabolism (Bonnard et al. 2020), and in industries as a catalyst, material synthesis (Rujitanapanich et al. 2014; Khan et al. 2018), or a standard reagent (Ferraz et al. 2019). Calcined OS is also a potential antibacterial agent with strong antimicrobial properties, diverse bactericidal mechanisms, and biocompatibility (Sadeghi et al. 2019).

Taiwan receives more than 2.6 times the global average rainfall (Hsu & Hung 2019). However, water scarcity on the island has reached alarming levels in recent years due to topographical factors and the rapid expansion of industries. Semiconductor manufacturing and agriculture are the two main economic drivers of the island, both heavily dependent on water. On this account, Taiwan has pushed for strategic measures to promote the sustainable development of water resources, which requires initiatives such as rainwater harvesting in urban and rural settlements. A fundamental problem often encountered with this approach is that the water extracted through rainwater harvesting systems is exposed to contaminants from various sources (Schets et al. 2010; Hamilton et al. 2017).

Harvested rainwater's overall physical, chemical, and microbiological qualities degrade rapidly during storage without proper treatment, resulting in change in odor, color, and taste, making it unsuitable for direct or indirect use. Therefore, it is important to obtain a cost-effective way to inactivate microorganisms in stored rainwater. Bacillus produces spores during their stationary phase of development, which are capable of long dormancy and are also highly resistant to heat, radiation, and toxic chemicals (Sunde et al. 2009). Bacillus spore inactivation can be utilized as a standard for the decontamination of biological agents from drinking water infrastructure due to their disinfection resistance (Szabo et al. 2017). A simple yet effective solution being explored is processed seashells, a promising alternative material for low-cost water treatment and disinfection. The antibacterial activity of calcined seashells is related to CaO by two mechanisms in which the primary mechanism is the alkalinity of the medium and the secondary mechanism is the generation of Ca2+ and reactive oxygen species (ROS) on the surface of CaO, leading to cell wall rupture. Unlike other shells, OSs are explored less for this application. Therefore, for the practical application of heated oyster shell particles (HOSP) as a disinfectant, it is necessary to understand the effect of different processing and activation parameters contributing to its sterilization potency.

This study investigated the sporicidal activity of HOSP against Bacillus subtilis spores. The relative effects of four operating parameters – (i) OS particle heating temperature, (ii) OS particle heating duration, (iii) HOSP concentration, and (iv) treatment time – on disinfection efficacy were assessed by employing response surface methodology (RSM) based on a five-level, four-factorial central composite design (CCD). Besides, a kinetic analysis of the bactericidal action of HOSP was also determined.

Heated oyster shell particle preparation

Figure 1 depicts the process of calcining oyster shell wastes (Crassostrea sp.), locally sourced from Chiayi County, Taiwan, to produce HOSPs. Shells were scrubbed and soaked overnight in tap water to remove salt, biomass, and other surface residues before rinsing in deionized water. Washed shells were dried at 60 °C for 24 h and then ground thoroughly with a commercial grinder and passed through a 150-μm stainless steel sieve (Advantech L3-S100 Standard Sieve, USA series: #100) to collect natural oyster shell particles (OSPs). Fine OSP was calcined in a muffle furnace at the desired temperature (600–1,000 °C) and duration (10–50 min) to obtain HOSP. Their qualitative composition was inspected using a Bruker D8 Advance X-ray diffractometer (XRD) with CuKα radiation at 40 kV and 40 mA, a 2θ range of 15–65° with a step size of 0.05° and a scan speed of 0.25°/min.
Figure 1

HOSP production process.

Figure 1

HOSP production process.

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Nutrient media, microorganisms, and rainwater

Nutrient medium for the growth/cultivation of B. subtilis was prepared with 5 g of peptone and 3 g of beef extract for a 1 L solution. The pH of the medium was adjusted to 7.0 with phosphate buffer. For agar medium, bacteriological agar was added at 2% to the aforementioned preparation.

B. subtilis (ATCC 6051) endospores were cultured based on a modified protocol described by Morris (2012). Harvested endospore stock was serially diluted using 0.001 M phosphate-buffered saline solution (PBS) and spread on nutrient agar plates to check their quality and quantity. An average of 9.2 × 108CFU/mL was observed in the harvested stock.

Fresh rainwater was harvested locally from the rooftop, funneled, and collected directly into sterile glass containers. Harvested rainwater was then pasteurized at 63 °C for 30 min before storing aseptically for further use. The characteristics of pasteurized rainwater are summarized in Table 1.

Table 1

Physicochemical characteristics of pasteurized rainwater

ParametersUnitResults
Electrical conductivity μS/cm 30.53 
pH – 5.25 
Total organic carbon mg/L 4.81 
Turbidity NTU 3.22 
Total dissolved solids mg/L 16.07 
ParametersUnitResults
Electrical conductivity μS/cm 30.53 
pH – 5.25 
Total organic carbon mg/L 4.81 
Turbidity NTU 3.22 
Total dissolved solids mg/L 16.07 

HOSP treatment against B. subtilis spores

The bactericidal effect of HOSP was examined against B. subtilis endospores in a rainwater test medium. All experiments were performed at 25 ± 1 °C under stagnant conditions in a 15 mL sterile centrifuge tube. Powder slurry was prepared by dissolving HOSP into 10 mL of rainwater. Endospore suspension was pipetted to the slurry aseptically at a concentration of 5.7 log10 (colony-forming units per millimeter [CFU/mL]) (i.e., 5 × 105 CFU/mL). Samples were periodically taken, diluted in sterile 0.001 M PBS, and spread thoroughly over agar plates in duplicates. Colonies were counted as CFU/mL after incubation at 37 °C for 72 h. Antibacterial activity was determined by calculating the log inactivation rate of the test organism using Equation (1):
(1)
where N0 and N are the number of viable bacteria before and after treatment, respectively.

To evaluate the influence of process parameters on the antibacterial activity of HOSP, a combination of RSM and CCD developed by Design-Expert® software version 12.0.7.0 (Stat-Ease, Inc., USA) was adopted. A four-factor, five-level CCD with 30 experimental runs consisting of 16 factorial points, 8 axial points, and 6 replicates at the central point (0, 0, 0, 0) was performed. The inactivation rates of B. subtilis spores were chosen as the dependent variable, whereas the independent variables were OSP heating temperature (X1), OSP heating duration (X2), HOSP concentration (X3), and treatment time (X4). Ranges and values of the independent variables in Table 2 were estimated based on the relevant scientific literature and our preliminary studies.

Table 2

Independent variables and levels used in CCD for the sporicidal activity against B. subtilis spores by HOSP

Factor levels
Factors, Xi− 2− 10+ 1+ 2
OSP heating temperature (°C), X1 600 700 800 900 1,000 
OSP heating duration (min), X2 10 20 30 40 50 
HOSP concentration (mg/mL), X3 0.1 0.5 0.9 1.3 1.7 
Treatment time (h), X4 72 144 216 288 
Factor levels
Factors, Xi− 2− 10+ 1+ 2
OSP heating temperature (°C), X1 600 700 800 900 1,000 
OSP heating duration (min), X2 10 20 30 40 50 
HOSP concentration (mg/mL), X3 0.1 0.5 0.9 1.3 1.7 
Treatment time (h), X4 72 144 216 288 

Experimental data were processed with Design-Expert® software trial version 12.0.7.0 and fitted to a second-order polynomial equation (Cho & Zoh 2007; Younis et al. 2014; Mohammadi et al. 2017):
(2)
where Y represents the response variable (log inactivation); Xi and Xj are the independent coded variables; is the intercept term; and , , and are coefficients of the linear, quadratic, and interaction effects, respectively.

Disinfection kinetics

This study identified an appropriate kinetic model for the inactivation rate of B. subtilis endospores against HOSP in rainwater. Commonly used deceleration kinetic models, i.e., the modified Chick–Watsons model, Homs model, and Selleck–Collins model, were applied and tested to find a suitable fit.

The Chick–Watson model is the most commonly used in water treatment as a classical kinetic equation. Although the model is widely used to describe the inactivation kinetics of chemicals, it has limitations in practical applications where the sterilization rate does not change with time. In such cases, other models are used to explain deviations from the Chick–Watson first-order kinetics (Azzellino et al. 2011; Idris et al. 2017).

To explain a decelerating rate of disinfection, the Collins–Selleck model was developed (Crittenden et al. 2012). The Hom model, an empirical generalization of the Chick–Watson pseudo-first-order rate law, is used to address a curvilinear rate of disinfection (Lambert & Johnston 2000). This model – a linear regression of the concentration of the disinfectant, time of treatment, and the survival – is used to examine disinfection data of different organisms and to explain the effect of disinfection systems. HOSP dosage and treatment time were taken as the predictors, and the log of survival ratio of the indicator organisms was taken as the dependent variable. The experimental data were fit to disinfection models shown below.
(3)
(4)
(5)
where N is the number of viable organisms present at time t; N0 is the number of viable organisms at time 0; k1 and k2 are coefficients of specific lethality; kcs is a log-based coefficient of specific lethality; kh is the inactivation rate constant; b is the lag coefficient; n and m are Hom dilution coefficient and time exponent, respectively; and C is biocide concentration, specifically HOSP concentration.

The model that yields the highest coefficient of determination (adjusted R2) was the best fit for the purpose. To determine the inactivation kinetics and estimate the model parameter, nonlinear multivariate regression analysis was performed using R software for Macintosh, version 3.5.3.

Modeling the bactericidal activity of HOSP

The antibacterial effect of HOSP against B. subtilis endospores, expressed as log inactivation, was investigated under various conditions in accordance with the experimental runs indicated by Design-Expert® software version 12.0.7.0. Table 3 summarizes the results of all 30 runs in the CCD matrix for response surface modeling. The observed inactivation rates for B. subtilis endospores ranged from −0.02 to 4.86 log. The model predictions were consistent with observed log inactivation.

Table 3

Five-level/four-factor CCD matrix along with log inactivation response for B. subtilis endospores

Run orderCoded values
Real values
Log inactivation (log10(N/N0))
X1X2X3X4OSP heating temperature (°C)OSP heating duration (min)HOSP conc. (mg/mL)Treatment time (h)ObservedPredicted
−2 600 30 0.9 144 0.66 0.76 
−1 −1 −1 +1 700 20 0.5 216 0.49 1.35 
−1 +1 +1 +1 700 40 1.3 216 3.75 3.51 
−1 −1 −1 −1 700 20 0.5 72 0.18 −0.08 
−1 +1 −1 +1 700 40 0.5 216 1.83 1.81 
−1 +1 +1 −1 700 40 1.3 72 2.36 2.08 
−1 −1 +1 −1 700 20 1.3 72 1.07 1.63 
−1 +1 −1 −1 700 40 0.5 72 0.73 0.38 
−1 −1 +1 +1 700 20 1.3 216 3.37 3.05 
10 800 30 0.9 144 3.57 3.31 
11 −2 800 10 0.9 144 2.73 2.32 
12 800 30 0.9 144 3.57 3.31 
13 −2 800 30 0.9 −0.02 0.21 
14 +2 800 50 0.9 144 2.96 3.23 
15 −2 800 30 0.1 144 1.05 0.76 
16 +2 800 30 1.7 144 4.01 4.16 
17 800 30 0.9 144 3.57 3.31 
18 +2 800 30 0.9 288 4.36 3.99 
19 800 30 0.9 144 3.12 3.31 
20 800 30 0.9 144 3.25 3.31 
21 800 30 0.9 144 2.80 3.31 
22 +1 +1 +1 +1 900 40 1.3 216 4.43 5.19 
23 +1 −1 +1 −1 900 20 1.3 72 2.77 2.39 
24 +1 +1 +1 −1 900 40 1.3 72 2.99 2.85 
25 +1 −1 +1 +1 900 20 1.3 216 4.86 4.74 
26 +1 −1 −1 −1 900 20 0.5 72 0.49 0.69 
27 +1 +1 −1 +1 900 40 0.5 216 3.95 3.49 
28 +1 −1 −1 +1 900 20 0.5 216 2.61 3.04 
29 +1 +1 −1 −1 900 40 0.5 72 0.82 1.15 
30 +2 1000 30 0.9 144 3.44 3.21 
Run orderCoded values
Real values
Log inactivation (log10(N/N0))
X1X2X3X4OSP heating temperature (°C)OSP heating duration (min)HOSP conc. (mg/mL)Treatment time (h)ObservedPredicted
−2 600 30 0.9 144 0.66 0.76 
−1 −1 −1 +1 700 20 0.5 216 0.49 1.35 
−1 +1 +1 +1 700 40 1.3 216 3.75 3.51 
−1 −1 −1 −1 700 20 0.5 72 0.18 −0.08 
−1 +1 −1 +1 700 40 0.5 216 1.83 1.81 
−1 +1 +1 −1 700 40 1.3 72 2.36 2.08 
−1 −1 +1 −1 700 20 1.3 72 1.07 1.63 
−1 +1 −1 −1 700 40 0.5 72 0.73 0.38 
−1 −1 +1 +1 700 20 1.3 216 3.37 3.05 
10 800 30 0.9 144 3.57 3.31 
11 −2 800 10 0.9 144 2.73 2.32 
12 800 30 0.9 144 3.57 3.31 
13 −2 800 30 0.9 −0.02 0.21 
14 +2 800 50 0.9 144 2.96 3.23 
15 −2 800 30 0.1 144 1.05 0.76 
16 +2 800 30 1.7 144 4.01 4.16 
17 800 30 0.9 144 3.57 3.31 
18 +2 800 30 0.9 288 4.36 3.99 
19 800 30 0.9 144 3.12 3.31 
20 800 30 0.9 144 3.25 3.31 
21 800 30 0.9 144 2.80 3.31 
22 +1 +1 +1 +1 900 40 1.3 216 4.43 5.19 
23 +1 −1 +1 −1 900 20 1.3 72 2.77 2.39 
24 +1 +1 +1 −1 900 40 1.3 72 2.99 2.85 
25 +1 −1 +1 +1 900 20 1.3 216 4.86 4.74 
26 +1 −1 −1 −1 900 20 0.5 72 0.49 0.69 
27 +1 +1 −1 +1 900 40 0.5 216 3.95 3.49 
28 +1 −1 −1 +1 900 20 0.5 216 2.61 3.04 
29 +1 +1 −1 −1 900 40 0.5 72 0.82 1.15 
30 +2 1000 30 0.9 144 3.44 3.21 

In CCD studies, model adequacy check is an integral part to guarantee that it gives an adequate estimation for real analysis systems (Arslan-Alaton et al. 2009; Ivanescu et al. 2016; Arslan & Kara 2017). Approximating model functions would yield inaccurate or misleading results if the fit were poor (Körbahti 2007; Arslan & Kara 2017). The quality of the proposed model was evaluated by constructing a diagnostic plot between the predicted and actual log inactivation values. As shown in Supplementary Material, Figure S1(a), no significant difference was found since the data points were very close to the diagonal line. In other words, the predicted values from the developed model agreed well with the observed values in the experimental data. The plot of residuals versus predicted responses is indicated in Supplementary Material, Figure S1(b). The distributions of residuals were random without any trends. Furthermore, a one-way analysis of variance (ANOVA) was tested to check the adequacy of the suggested model, and the results are described in Table 4. The model's F-value of 31.62 reveals that the model is statistically fit. A p-value less than 0.05 means that the model parameters are highly significant, whereas values greater than 0.1 indicate insignificant terms. In this case, X1, X2, X3, X4, X1X4 (interaction between X1 and X4), X12 (second-order effect of X1), X32 (second-order effect of X3), and X42 (second-order effect of X4) are important model terms, and X22 (second-order effect of X2) is negligible. The large R2 of 0.9343 shows a high degree of consistency between the observed and calculated results. The quality of fit estimates from the coefficients R2 represents a reasonable agreement between the predicted R2 and the adjusted R2 (the difference is less than 0.2), implying that the model provides an adequate fit for the data. A signal-to-noise ratio of 20.7114 provides an adequate signal, demonstrating that the chosen model can be used to navigate the design space. Consequently, the proposed reduced quadratic model represents the best approach for the relationship between variables and responses and is sufficient to assess the effects of variables.

Table 4

ANOVA for the reduced quadratic model

SourceSum of squaresdfMean squareF-valuep-valueRemark
Model 55.27 6.14 31.62 <0.0001 *** 
X1 9.00 9.00 46.36 <0.0001 *** 
X2 1.25 1.25 6.44 0.0196 *** 
X3 17.37 17.37 89.45 <0.0001 *** 
X4 21.36 21.36 109.96 <0.0001 *** 
X1X4 0.8464 0.8464 4.36 0.0498 *** 
X12 3.05 3.05 15.69 0.0008 *** 
X22 0.4968 0.4968 2.56 0.1254 
X32 1.25 1.25 6.43 0.0197 *** 
X42 2.52 2.52 12.99 0.0018 *** 
Residual 3.88 20 0.1942    
Lack of fit 3.38 15 0.2255 2.24 0.1902 
Pure error 0.5025 0.1005    
Cor total 59.15 29     
Fit statistics 
Standard deviation 0.4407  R2 0.9343  
Coefficient of variation (%) 17.45  Adjusted R2 0.9048  
Adeq precision 20.7114  Predicted R2 0.8403  
SourceSum of squaresdfMean squareF-valuep-valueRemark
Model 55.27 6.14 31.62 <0.0001 *** 
X1 9.00 9.00 46.36 <0.0001 *** 
X2 1.25 1.25 6.44 0.0196 *** 
X3 17.37 17.37 89.45 <0.0001 *** 
X4 21.36 21.36 109.96 <0.0001 *** 
X1X4 0.8464 0.8464 4.36 0.0498 *** 
X12 3.05 3.05 15.69 0.0008 *** 
X22 0.4968 0.4968 2.56 0.1254 
X32 1.25 1.25 6.43 0.0197 *** 
X42 2.52 2.52 12.99 0.0018 *** 
Residual 3.88 20 0.1942    
Lack of fit 3.38 15 0.2255 2.24 0.1902 
Pure error 0.5025 0.1005    
Cor total 59.15 29     
Fit statistics 
Standard deviation 0.4407  R2 0.9343  
Coefficient of variation (%) 17.45  Adjusted R2 0.9048  
Adeq precision 20.7114  Predicted R2 0.8403  

Note: *Not significant (p ≥ 0.1).

**Significant (0.05 ≤ p < 0.1).

***Highly significant (p < 0.05).

Once high dependability was established, predictions about the antibacterial efficacy of HOSP disinfectant could be obtained through the reduced second-order polynomial equations with coded and actual variables as Equations (6) and (7), respectively.

Final equation in terms of coded factors:
(6)
where Y is the log inactivation response for B. subtilis endospores; X1, X2, X3, and X4 are OSP heating temperature, OSP heating duration, HOSP concentration, and treatment time, respectively.
Final equation in terms of actual factors are as follows:
(7)

The regression model provides the preferred effects of the selected variables as X4 (treatment time) > X3 (HOSP concentration) > X1 (OSP heating temperature) > X2 (OSP heating duration).

Effects of selected variables on the bactericidal activity of HOSP

Three-dimensional surface plots and two-dimensional contours of the responses – where one variable was fixed at the center point, and the others varied over the experimental ranges – were applied to determine the relative effects of selected variables on the bactericidal activity of HOSP. OS particle heating temperature and duration, HOSP concentration, and treatment time could all have a positive or negative effect on B. subtilis endospores removal rate, as shown in Figures 2 and 3. Peak performance with 5.58 log inactivation was predicted at Theating OSP = 926 °C, theating OSP = 34 min, [HOSP] = 1.39 mg/mL, and ttreatment = 271 h.
Figure 2

3D response surface (a) and contour (b) plots for B. subtilis inactivation as a function of oyster shell particle heating temperature and duration. HOSP concentration and treatment time were kept constant at 0.9 mg/mL and 144 h, respectively. B. subtilis log inactivation ranges from −0.02 to 4.86, where warmer (colder) colors indicate higher (lower) values. Please refer to the online version of this paper to see this figure in colour: http://dx.doi.org/10.2166/wh.2023.278.

Figure 2

3D response surface (a) and contour (b) plots for B. subtilis inactivation as a function of oyster shell particle heating temperature and duration. HOSP concentration and treatment time were kept constant at 0.9 mg/mL and 144 h, respectively. B. subtilis log inactivation ranges from −0.02 to 4.86, where warmer (colder) colors indicate higher (lower) values. Please refer to the online version of this paper to see this figure in colour: http://dx.doi.org/10.2166/wh.2023.278.

Close modal
Figure 3

3D response surface (a) and contour (b) plots for B. subtilis inactivation as a function of HOSP concentration and treatment time. OSP heating temperature and duration were kept constant at 800 °C and 30 min, respectively.

Figure 3

3D response surface (a) and contour (b) plots for B. subtilis inactivation as a function of HOSP concentration and treatment time. OSP heating temperature and duration were kept constant at 800 °C and 30 min, respectively.

Close modal
The interactive effects of oyster shell particle heating temperature (X1) and duration (X2) on the inactivation rate of B. subtilis endospores are shown in Figure 2. The HOSP concentration (X3) and treatment time (X4) were unchanged at 0.9 mg/mL and 144 h, respectively, while other variables were varied in the ranges of 600–1,000 °C with X1 and 10–50 min with X2. As seen in the plots, increasing the calcining temperature positively affected the inactivation rate at all tested conditions. Sterilization efficiency rapidly increased from 0.755 log10 to 3.205 log10 with an increase in OSP calcining temperature from 600 to 1,000 °C, at 30 min heating duration. Meanwhile, the observed change was relatively low with heating duration across all tested heating temperatures. The results correlate well with the previous reports of heat-activated conditions for materials derived from scallop (Sawai 2011) and blood cockle shells (Mohamed et al. 2012a, 2012b). Increasing the temperature during calcination leads to increased conversion of calcium carbonate (CaCO3) to calcium oxide (CaO), Equation (8), producing more CaO per mass of the calcined shell. X-ray diffraction analyses (Supplementary Material, Figure S2) have shown that CaCO3 decomposition in OSs occurs above 600 °C, with XRD peaks for CaO detected above 800 °C – where decomposition mass mainly consists of a mixture of calcium carbonate and crystalline calcium oxide – leading to a complete conversion at 900 °C where all the calcium in the heated mass exists as calcium oxide.
(8)
In aqueous media, both alkalinity and ROS generated from CaO hydration (Equation (9)) have been determined for their bactericidal effects on a wide range of bacterial and fungal organisms (Sawai 2011; Yasue et al. 2011, 2014; Watanabe et al. 2014; Hijikata et al. 2016; Liang et al. 2022). The antimicrobial effect of hydroxyl ions is understood to be protein denaturation and damage to bacterial cytoplasmic membranes and DNA (Mohammadi et al. 2012). A similar effect was observed on MS2 coliphage viral bodies, where capsid damage and partial RNA exteriorization are seen to accompany a pH increase. Meanwhile, alkaline inactivation of Escherichia coli is understood as a process that damages the outer membrane and their enzymatic activities, thereby damaging nucleic acids and/or metabolism (Hijikata et al. 2016). Further studies into CaO-based disinfectants derived from heated surf clam, scallop shell, dolomite (a double salt composed of CaCO3 and MgCO3), and ceramic (a composite of oxides of calcium (CaO), magnesium (MgO), and zinc (ZnO)) have also strongly suggested the involvement of ROS in the microbicidal effect. Yasue et al. (2011) have shown that the sporicidal effect of heated dolomite powder slurry at pH 12.7 was much higher than that of NaOH at pH 13. Chemiluminescence analysis indicated that active oxygen species generated from the slurry was one of the critical factors associated with the sporicidal activity. A similar conclusion was reached in other related studies involving heated scallop shells and ceramic powder (Bae et al. 2006; Sawai 2011; Watanabe et al. 2014). Results predicted in the current study suggest that calcined OSPs are generally identical in characteristics and properties as a potential source for natural disinfectants as calcined scallops, cockle, or clam shells.
(9)

Figure 2 shows the effect of HOSP dosage and treatment time on the inactivation rate at constant shell heating time and temperature of 30 min and 800 °C, respectively. The inactivation rate was predicted to increase steadily with both parameters. Specifically, the bactericidal effects of HOSP rapidly increased from 0.677 log10 to 4.080 log10 with an increase in HOSP dosage from 0.1 to 1.7 mg/mL at 144 h treatment time. The more HOSPs used, the more CaO is generated, resulting in more ROS generation. This assists in a higher inactivation rate of B. subtilis endospores. A similar trend was also observed with the increasing treatment time in the system from 0 to 288 h. The inactivation rate increased from 0.132 log10 to 3.905 log10 at a HOSP concentration of 0.9 mg/mL.

Kinetic analysis of bactericidal activity against B. subtilis

In rainwater medium, the coefficient of determination calculated for the chosen models are presented in Table 5. Here, Hom's empirical model is defined to better describe the experimental data based on R2 best fit.

Table 5

Coefficient determination for tested kinetic models for B. subtilis inactivation in rainwater by OSP heated at 1,000 °C for 10 min

Disinfection kinetic modelR2Adjusted R2
Modified Chick–Watson 0.2551 0.2500 
Collin–Selleck 0.6222 0.6196 
Hom 0.9408 0.9400 
Disinfection kinetic modelR2Adjusted R2
Modified Chick–Watson 0.2551 0.2500 
Collin–Selleck 0.6222 0.6196 
Hom 0.9408 0.9400 

Model parameters k, n, and m for Hom's model determined using multiple linear regression is summarized in Table 6. Both parameters are observed to be statistically very significant with p < 0.05 at 1 × 10−11 and 2 × 10−16. Multiple R2 and adjusted R² were reasonably high at 0.9408 and 0.9400, respectively. Hence, the disinfection kinetic for HOSP against B. subtilis spores in rainwater medium is defined by Equation (10).
(10)
Table 6

Summary of statistics and regression estimates for the best fit Hom's model for B. subtilis inactivation in rainwater

knm
Estimates 0.0017 0.6999 1.6887 
Standard error 0.1725 0.0948 0.0352 
Significance (p < 0.05) 2 × 10−16 10−11 2 × 10−16 
N 148 
R2 0.9408 
knm
Estimates 0.0017 0.6999 1.6887 
Standard error 0.1725 0.0948 0.0352 
Significance (p < 0.05) 2 × 10−16 10−11 2 × 10−16 
N 148 
R2 0.9408 

The relative effects between OS heat activation and treatment conditions on the sporicidal efficacy were determined using a central composited design of the response surface model. The model indicated that the predicted and experimental values were not significantly different. The ANOVA showed that the effects of OS heating temperature, HOSP dosage in the treatment medium, and the treatment time contributed significantly to the sporicidal effects (p < 0.05). Polynomial models fitting the predicted response, i.e., log inactivation of the test organism (B. subtilis), suggested that the yield of active compound (CaO) in calcined OSs and the resulting microbicidal effect increased with the increase in OS heating temperature and HOSP concentration and contact time in rainwater medium. OS heating duration did not significantly increase the active component yield at a given heating temperature. In addition, the inactivation kinetics for HOSP in aqueous media under stagnant storage conditions are in good agreement with Hom's model. The results from this study may be applied to rainwater harvesting tank construction. Incorporating HOSP in rainwater harvesting tank materials, such as submerged bricks or tank inner lining, may prevent water from fouling during long-term storage. Despite their simplicity and low cost, CaO-based disinfectants have some limitations due to alkaline pH and Ca2+ residues in treated rainwater, which presents a major challenge.

This study was supported by the National Science and Technology, Taiwan (Project 109-2221-E-002-079-MY3) and National Taiwan University Core Consortiums (NTUCCP-111L895102 and 112L893902) within the framework of the Higher Education SPROUT Project by the Ministry of Education (MOE) in Taiwan.

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

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Supplementary data