Open Access Article
Mariele de Souza Parra Agostinho
*a,
Artur Sass Braga
b,
Benjamin Anderson
b,
Yves Filionb and
Cristovão Vicente Scapulatempo Fernandes
c
aParana Sanitation Company – Sanepar. Federal University of Paraná – UFPR, Curitiba, Paraná, Brazil. E-mail: marielespa@gmail.com
bDepartment of Civil Engineering, Queen's University, Kingston, Ontario, Canada. E-mail: asb9@queensu.ca; ben.anderson@queensu.ca; yves.filion@queensu.ca
cFederal University of Paraná – UFPR, Curitiba, Paraná, Brazil. E-mail: cvs.fernandes@gmail.com
First published on 26th March 2026
Biofilms play a crucial role in drinking water distribution systems (DWDS), as they influence microbial stability and water quality. While the effects of steady-state hydraulic conditions on biofilm formation and adhesion are well documented, the influence of small-amplitude hydraulic transients remains unexplored. This study examines the impact of small-amplitude transients on biofilm development and adhesion to the pipe wall, mobilization behavior during flushing, and microbial activity in the bulk water in a full-scale PVC distribution pipe laboratory. Over a 28 days biofilm conditioning period, biofilms were subjected to steady-state flow and periodic transient events, followed by controlled flushing to evaluate the detachment behavior. The key findings showed that a moderate transient pulse (20 kPa) enhanced biofilm adhesion to the wall and led to a more uniform biofilm distribution along the pipe wall. A stronger transient pulse (40 kPa) inhibited biofilm accumulation and promoted continuous detachment from the wall during the 28-days biofilm conditioning period. Pipe flushing confirmed that biofilms formed under moderate and strong transient conditions exhibited greater wall adhesion and resistance to mobiliation during flushing as compared to those grown under steady-state flow conditions. These findings suggest that controlled hydraulic transients may play a role in biofilm management strategies, offering the potential to optimize DWDS maintenance and reduce microbial mobilization risks. However, further research is needed to assess the long-term effects in real-world systems with diverse pipe materials, nutrient conditions, and disinfection regimes.
Environmental significanceHydraulic transients influence biofilm behavior in water distribution systems. This study demonstrates that controlled, low-amplitude transients can either promote or inhibit biofilm growth. These findings contribute to our understanding of biofilms in drinking water infrastructure and highlight how network operational strategies can influence biofilm development and sediment accumulation on pipe walls, both key factors affecting drinking water quality. |
Hydraulic variability has been shown to shape biofilm architecture and function. Increased flow variability is frequently associated with higher bacterial density but reduced EPS-to-cell ratios and lower microbial diversity.4 Exposure to fluctuating velocities has also been linked to enhanced metabolic activity, indicating that hydraulic stress may act as a selective pressure promoting physiologically resilient communities. Surface properties further modulate these responses, as rougher pipe materials facilitate stronger initial adhesion, whereas sustained high shear conditions may inhibit biofilm accumulation.15
The importance of hydraulic history in determining biofilm structure has been highlighted in experimental DWDS studies. Douterelo et al.1 demonstrated that both habitat type and hydraulic regime significantly influence bacterial community composition. Variable flow conditions promoted the formation of more compact biofilms that exhibited increased resistance to detachment. Such findings underscore the role of hydraulic conditioning in determining long-term biofilm stability. More recent work has reinforced the need to integrate hydraulic management with microbial monitoring, showing that flow regimes interact with environmental factors such as temperature16 and that controlled flushing can effectively limit biofilm accumulation.17 Collectively, these studies establish that biofilm growth dynamics in DWDS are intrinsically linked to the magnitude, variability, and history of applied shear forces.
Although flushing represents an intentional high-shear intervention, routine steady flow variations during normal operation can also generate shear stresses sufficient to destabilize biofilms. The structural properties developed during the growth phase determine the susceptibility of biofilms to such perturbations. Biofilms formed under steady hydraulic regimes often exhibit EPS-rich matrices that enhance cohesion and adhesion, conferring resistance to moderate shear stress, yet allowing substantial biomass accumulation that may mobilize during high-shear flushing.
Experimental evidence suggests that hydraulic conditioning influences detachment behavior. So et al.19 reported that rougher biofilms were more prone to detachment under fluctuating shear forces, whereas Lemos et al.20 found that biofilms developed under steady conditions exhibited greater shear resistance. These findings indicate that the detachment response is governed not only by instantaneous WSS magnitude but also by the prior hydraulic environment under which the biofilm was formed. Consequently, steady flow regimes can simultaneously promote structural resilience and increase the risk of episodic biomass release during operational disturbances.
Early modeling work by Brunone and Berni demonstrated that transient flows produce fluctuating wall shear stresses distinct from those observed under steady conditions.22 Subsequent experimental investigations by Wang et al.23 provided empirical evidence linking local WSS variations during transient events to biofilm detachment and altered growth dynamics. Further experimental work by Weston et al.24 indicated that the initial surge phase of a transient is particularly effective in mobilizing biofilm material. Complementary findings by Khu et al.25 showed that fluctuating velocities and flow reversals can modify biofilm thickness, adhesion strength, and bacterial density, thereby influencing detachment behavior.
Together, these studies demonstrate that biofilm mobilization is governed not only by extreme hydraulic interventions but also by the dynamic shear variability inherent to distribution systems. Nevertheless, most transient-focused investigations have examined large-amplitude pressure waves capable of exceeding biofilm shear strength and posing structural risk to infrastructure.
Existing transient-related studies have largely treated hydraulic transients as acute disturbance events characterized by high-amplitude pressure waves associated with pipe burst risk or catastrophic failure. In contrast, the potential role of small-amplitude transients as repetitive mechanical conditioning stimuli has received little attention. In this study, small-amplitude hydraulic transients are defined as pressure fluctuations in the range of 20–40 kPa that induce localized WSS variations without approaching structural failure thresholds. These conditions reflect typical operational fluctuations rather than extreme events.
It is hypothesized that repeated small-amplitude WSS oscillations may influence biofilm structural development, adhesion strength, and adaptive responses to shear, thereby affecting resilience to subsequent high-shear events such as flushing. To date, no study has systematically evaluated the impact of such operationally representative transients on biofilm formation and stability in a full-scale, controlled laboratory pipe system.
The overarching aim of this study is to examine the effects of small-amplitude hydraulic transients on biofilm development in a full-scale laboratory PVC pipe rig under controlled conditions. Specifically, this work seeks to determine how these transients affect biofilm growth and spatial distribution along the pipe wall, biofilm mechanical resilience under elevated WSS during flushing, and microbial activity within the bulk water phase.
A total of three experiments were performed. In the first experiment (Exp A), a steady-state flow rate of 0.6 L s−1 was maintained at 280 kPa without induced transients during the 28-days period. In the second experiment (Exp B), a steady-state flow rate of 0.6 L s−1 was maintained at the same pressure but a small-amplitude 20 kPa positive transient pressure wave was generated with a solenoid valve installed at the outlet of a pipe loop (Fig. 1). During the 28 days biofilm conditioning phase, the solenoid valve was partially closed once every hour to temporarily reduce the flow rate to 0.54 L s−1 for a duration of 30 seconds. Following this period, the valve was reopened to restore the steady-state flow condition of 0.6 L s−1 within the pipe loop. During the 28-days biofilm conditioning phase, a total of 672 initial positive transient pressure pulses (20 kPa) were generated with the solenoid valve. A third experiment (Exp C) was performed where the solenoid valve was partially closed and then re-opened to generate a 40 kPa initial positive transient pressure pulse at every hour of the 28-days biofilm conditioning period. The solenoid valve operations in Exp B and C were calibrated to ensure controlled, reproducible wall shear stress (WSS) fluctuations in the pipe loop. The initial positive transient pressure pulses of 20 kPa and 40 kPa generated in Exp B and C produced flow variations of 10% and 20% in the pipe loop. These flow variations are representative of transient events frequently encountered in operational DWDSs due to routine activities such as pump startups, valve closures, and demand fluctuations.27,28 Unlike major transient events caused by pump failures or sudden valve closures that produce large pressure waves and flow accelerations and decelerations, the controlled solenoid valve operations were designed to produce small, repeatable pressure waves and flow accelerations/decelerations in the pipe loop.
The biofilm conditioning phase was set to 28 days based on previous full-scale laboratory studies in which biofilms reached structural and metabolic stability within this timeframe.1,4 Biofilm development was categorized into three stages: an initial phase (days 0–7), characterized by bacterial attachment and EPS production; an intermediate phase (days 7–21), where biofilms developed three-dimensional structures and increased microbial diversity; and a stabilization phase (days 21–28), during which biofilm adhesion strengthened and resistance to shear stress increased.
To facilitate rapid microbial colonization of the pipe wall surfaces, an Initial Bacterial Broth (IBB) was prepared using effluent from a Granular Activated Carbon (GAC) filter combined with a nutrient supplement. Specifically, 18 L of GAC effluent water was mixed with 1.5 L of NutriSelect® Plus No. 3 nutrient broth (13 g L−1) and incubated at 16 °C under continuous agitation for seven days to promote microbial growth. Before application, the bacterial concentration of the IBB was assessed in triplicate using flow cytometry, yielding an average of 2.3 × 105 cells mL−1. To initiate the experiment, 2 L of the IBB was added to the inlet of each tank that supplied the pipe loops. This inoculation step enabled the establishment of biofilms on the internal surfaces of the pipe loops. To support biofilm growth, Nutrient Broth No. 3 was continuously added to the tanks that supply the pipe loops at a rate of 0.60 mg L−1 per day.
Table 1 summarizes the water quality characteristics observed both in the Kingston municipal distribution system, which supplies the DWDL, and within the pipe-loop setups used during the 28 days biofilm conditioning phase in Experiments A, B, and C. Water temperature was kept stable at 16 °C, a value representative of summer conditions commonly observed in Canadian drinking water networks.11 The specific conductivity data, as shown in Table 1, reflect the ionic concentration of the water supplemented with nutrient broth. To facilitate biofilm growth, oxygen was introduced into the storage tanks via aeration, as detailed in Table 1.
| Water quality parametera | Kingston systemc | Experiment A | Experiment B | Experiment C |
|---|---|---|---|---|
| a Water quality parameters are averages of measurements taken during the 28-days biofilm conditioning period in Pipe Loops A and B, unless otherwise specified.b Dissolved oxygen values reported correspond to average, minimum, and maximum values measured during 28-d biofilm conditioning period.c Source water quality parameters taken from 2023 King Street Water Treatment Plant Annual Report, Utilities Kingston.d Measured in Kingston distribution system.e Measured at discharge works of Kingston King St. WTP. | ||||
| pH | 7.20–8.15d | 7.75 | 7.92 | 8.10 |
| Water temperature (°C) | 12.3e | 16.7 | 16.9 | 16.1 |
| Dissolved oxygen (mg L−1)b | N/A | 13.1 | 13.1 | 13.0 |
| Specific conductivity (uS per cm) | 303–324d | 313 | 275 | 286 |
| Turbidity (NTU) | 0.056–0.197e | 0.287 | 0.342 | 0.226 |
Kingston's potable water originates from Lake Ontario, near the confluence with the St. Lawrence River (Utilities Kingston 2023).
The King Street Water Treatment Plant—located within a 5 km radius of the DWDL—employs multiple treatment steps including pre-chlorination, screening, coagulation/flocculation, filtration, and final chlorination. After treatment, sodium hypochlorite is dosed into a clear well to establish an average residual chlorine concentration of 0.17–2.97 mg L−1, which is maintained throughout the distribution network.29 The treated water reaches the DWDL through a 150 mm cast iron main installed in the 1970s.
Following the biofilm conditioning phase, each pipe loop was flushed at a flow rate of 6.5 L s−1, corresponding to a wall shear stress of 1.2 Pa 1.2 Pa (calculated via the Darcy–Weisbach equation). This step assessed the biofilm's adhesion strength and resistance to detachment developed under the different hydraulic regimes.
During flushing, fresh drinking water was continuously supplied to the tanks at the inlet of the pipe loops to ensure that mobilized biofilm materials were flushed out rather than reintroduced into the loops.
Microbial analysis was conducted by monitoring bacterial cell concentration (BCC), adenosine triphosphate (ATP) concentrations, and volatile suspended solids (VSS) in the bulk water to assess microbial metabolic activity. The BCC of the bulk water samples was assessed using a flow cytometer model SH800 from SONY. Samples were fixed with a 5% glutaraldehyde solution, stained with SYTO BCTM fluorescent dye that targets DNA of bacterial cells, and counted with the equipment against a standard suspension of reference beads with a known concentration. The rate of bioactivity of the bulk water was assessed using rapid ATP tests from Lumina Ultra. VSS was determined by filtering, drying, and weighing the solid fraction of the sample. The solid fraction was autoclaved at a temperature of 550 °C to determine the mass of the volatile fraction.
A removable pipe coupon30 system was used to obtain representative biofilm samples from five locations along both longitudinal and circumferential positions of the pipe loops (Fig. 1). To characterize bacterial cell density (BCD) and ATP density at the pipe wall, biofilms were retrieved from the pipe coupons with a sterile cotton swab. The swabs were immersed in an aqueous solution, and the biofilm material was resuspended through centrifugation for 1 minute. Following this, bacterial cell count and ATP analyses were performed on the biofilm material suspended in solution in a similar manner to those performed on the bulk water samples.
At 28 days, BCD remained highest in Exp A (4.67 × 104 cells cm−2), suggesting that steady-state conditions favor biofilm accumulation over time. In contrast, Exp B exhibited a slight reduction in BCD (4.45 × 104 cells cm−2), possibly due to periodic detachment caused by the transients. Pipe-loop C had the lowest BCD at 28 days (2.79 × 104 cells cm−2), indicating extensive removal of loosely attached cells. This is further illustrated in Fig. 2, where the decrease in cell density between day 28 and the flush step FS is smallest for Exp C. This confirms that while fewer cells persisted on the pipe wall during the biofilm conditioning in Exp C, those that remained exhibited stronger adhesion.
After flushing step FS, Exp B retained the highest BCD (2.73 × 104 cells cm−2), which highlights the resilience of biofilms formed under the 20 kPa transients. By contrast, Exp A exhibited the lowest BCD (1.25 × 104 cells cm−2) after flushing and experienced the greatest level of detachment from flushing. Despite experiencing greater material detachment during the biofilm conditioning phase, the biofilms in Exp C (40 kPa transients) exhibited higher BCD than those in the steady-state Exp A after the flushing step FS. This suggests that while stronger transients initially caused more disruption in the biofilm conditioning phase, the biofilms that remained on the pipe wall developed a higher shear strength, and were more resistant to subsequent detachment.
Fig. 3 indicates a time series of turbidity measured at the outlet of the pipe loop during the flushing stage of Experiments A, B, and C. Exp A exhibited the highest turbidity peak (0.9 NTU) and the greatest level of detachment. This further suggests that the steady-state conditioning imposed in Exp A produced weakly adhered biofilms. Exp B reached a lower turbidity peak (0.6 NTU) which suggests a controlled detachment during flushing. The moderate transients (20 kPa) imposed in the biofilm conditioning phase of Exp B may have enhanced biofilm adhesion and controlled detachment in flushing. By contrast, Exp C exhibited the lowest turbidity (0.3 NTU) which suggests that the strong transient conditions (40 kPa) imposed during the biofilm conditioning phase may have produced the most adhesive biofilms with the least detachment during the flushing phase.
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| Fig. 3 Times series plot of turbidity measured at the outlet of the pipe loop during the flushing stage of Experiments A, B, and C. | ||
Fig. 4. Bacteria cell density (BCD) at pipe walls at 14 days and 28 days of the conditioning phase and the flushing step (FS) of Experiments A, B and C. The BCD values are averages calculated with measurements taken in triplicate at the invert (INV) pipe position. The error bars represent the variance from the average by ± 1 standard deviation.
Fig. 4 also indicates that in Exp A (steady state), the BCD measured at the inlet (INLT) increased markedly to reach 9.17 × 104 cells cm−2 at 28 days. This suggests that biofilm was able to grow and accumulate in a localized manner near the pipe–loop entry point. In Exp B, the biofilm showed a more uniform distribution, with BCD values ranging from 3.88 × 104 cells cm−2 at the inlet (INLT) to 5.49 × 104 cells cm−2 at the outlet (OUTLT). This suggests that moderate transients (20 kPa) contributed to a more uniform biofilm growth and presence along the pipe. In Exp C, low levels of BCD were measured at the outlet (OUTLT; 2.13 × 104 cells cm−2), which reinforces the hypothesis that a higher transient pressure pulse (40 kPa) led to more frequent detachment during the conditioning phase and hindered the development and stability of the biofilm.
To assess the biofilm resistance to detachment, a quantitative analysis of the relative change in BCD between Day 28 and FS was performed. At the inlet (INLT), Exp A saw a reduction in BCD of 90.7% after flushing, Exp B saw an increase of 55.6% in BCD, and Exp C saw a reduction of 60.2% in BCD. At the midpoint (MIDPT), Exp A saw a reduction in BCD of 55.9%, Exp B saw a reduction in BCD of 51.7%, and Exp C saw a reduction in BCD of 34.2%. At the outlet (OUTLT), Exp A saw a reduction in BCD of 74.7%, Exp B saw a reduction in BCD of 33.3%, and Exp C saw an increase in BCD of 52.3%. These results confirm that biofilms conditioned under moderate (20 kPa) and strong (40 kPa) transient events developed stronger adhesion properties than those formed under steady-state. The increases in BCD between Day 28 and after the flush may reflect a localized biomass accumulation during flushing. This phenomenon may be attributed to the mobilization and subsequent re-deposition of detached biofilm clusters downstream, resulting in a localized increase in BCD at downstream sampling locations.
Fig. 5 also shows that by 28 days, biofilm distribution was more uniform across all circumferential positions in Exp A, B and C. Specifically, in Exp B the biofilm had a relatively uniform BCD distribution, while in Exp A the biofilm showed localized growth at the obvert (OBV, 4.10 × 104 cells cm−2). The results suggest that the steady-state flow imposed in Exp A promoted biofilm accumulation at the obvert position, whereas in Exp B and C the transients promoted growth at the invert and springline positions.
Fig. 5 shows that, following the flushing step FS, biofilm detachment occurred at all circumferential positions in Exp A, B and C, but to varying degrees. Quantitative analysis of the relative change in BCD between Day 28 and FS indicates that at the invert (INV) the reductions were 55.9% in Exp A, 51.7% in Exp B and 34.2% in Exp C. At the springline (SPRGLN), the reductions were 62.0%, 79.4% and 32.5% for Exp A through C. While at the obvert (OBV), the reductions amounted to 49.9%, 83.0% and 19.1% for Exp A through C. After the flush FS, Exp B showed high BCD levels of 2.47 × 104 cells cm−2 at the invert (INV) and BCD levels of 2.47 × 104 cells cm−2 at the springline (SPRGLN). Similarly, Exp C showed high levels of BCD of 2.73 × 104 cells cm−2 at the invert (INV) and BCD levels of 1.04 × 104 cells cm−2 at the obvert (OBV).
These results show that biofilms formed under steady-state conditioning (0 kPa, Exp A) exhibited the weakest adhesion, while those formed under moderate and strong transients (20 kPa-Exp B and 40 kPa-Exp C) exhibited the highest strength and ability to resist high shear during the flush. This indicates that biofilms formed under transients, particularly moderate ones, develop stronger adhesion and resist detachment more effectively.
The results demonstrate clear differences in biofilm adhesion and distribution in both the longitudinal locations (INLT, MIDPT, OUTLT) and circumferential positions (INV, SPRGLN, OBV) across all three experiments and their associated conditioning hydraulics. Steady-state conditions (Exp A) promoted localized biofilm accumulation, with notable increases at the inlet (INLT) longitudinal location and obvert (OBV) circumferential position. However, these biofilms demonstrated weaker adhesion overall and were more readily detached during flushing events. Biofilms formed under moderate transients (20 kPa, Exp B) exhibited strong adhesion and uniform distribution along the pipe. These biofilms were characterized by higher BCD values, particularly at the downstream location (OUTLT) and at the invert (INV) and springline (SPRGLN) circumferential positions. They also showed a greater resistance to detachment during flushing than the biofilms in Exp A (steady state). The biofilms grown under strong transients (40 kPa, Exp C) generally showed a uniform distribution, with higher BCD values at the invert (INV) and springline (SPRGLN) positions. These biofilms generally exhibited the greatest level of adhesion and the greatest resistant to detachment during the flushing phase.
Fig. 6a–c indicate a modest increase in BCC and ATP and a more important increase in VSS in the bulk water after the flush for Exp A and C. This result accords with the previous observations that biofilm detachment occurred in the flush for these experiments. As such, this detachment may have introduced new material in the bulk water to increase the value of the biological parameters. Fig. 6a–c also shows that in Exp B, BCC, ATP, and VSS values decreased after flushing. This result is contradictory to what was found in Fig. 2–5, where biofilm detachment was found to occur in the flushing phase. However, this decrease in bulk water parameters may be the result of a combination of factors, including greater structural stability of biofilms formed under moderate transients (reducing the release of viable cells), variations in planktonic populations, or experimental variability.
In this context, the study by Chen et al. (2022) provides a robust conceptual framework for interpreting these observations. Although their work focused on biofilm-bound sandy systems, the authors demonstrated that biofilms exhibit a significant adaptive response to cyclic changes in shear stress, leading to enhanced resilience over time.34 By applying this lens to the present study, the results suggest that the cyclic nature of the small-amplitude transients (20–40 kPa) functioned as a mechanical conditioning agent. This process likely selected for more resilient microbial clusters and stimulated the development of a more cohesive matrix, allowing the biofilm to maintain structural integrity even when subjected to subsequent high-shear flushing events. Interpreting the findings through the lens of biofilm resilience to cyclic hydrodynamic forcing—rather than adhesion strength alone—provides a mechanistic explanation for the reduced detachment observed following conditioning under moderate transients.
These findings have practical implications for the management of biofilms in water distribution systems. There are two opportunities here. First, the generation of controlled hydraulic transients could be strategically applied to periodically mobilize low-strength biofilms and other material in pipes to clean the pipes on a near-continuous basis. Second, the generation of controlled hydraulic transients could be used to promote biofilms with enhanced strength and resistance to detachment. This could potentially reduce the risk of extensive biofilm detachment and release of metals and other toxins anchored in the biofilm during unexpected high-shear events (e.g., pump trip, pipe burst, rapid opening of fire hydrant) and cause serious discolouration episodes. However, the exact magnitude of controlled transients needed to achieve these two goals is likely system-specific and will depend on a number of factors such as pipe material, system configuration, composition and age of biofilms among others. The results also underscore the need for integrated biofilm management strategies that account for both hydraulic and microbial dynamics. Advanced hydraulic and discoloration modelling and monitoring tools could help identify optimal transient regimes that balance biofilm control and system efficiency while minimizing the risk of pipe damage.36
Another limitation concerns the methods used to grow bacteria to inoculate the pipe loops. The experimental setup included two granular activated carbon (GAC) filters—one to remove chlorine and another to provide a surface for bacterial growth before these were introduced into the pipe loops. This approach likely introduced a selection bias by favoring bacteria that thrive in a chlorine-free environment while excluding chlorine-resistant or low-nutrient-adapted species. The absence of these species in the experimental conditions may have influenced the composition and structural properties of the biofilms. In addition to this, the study was performed in a high-nutrient, chlorine-free environment, whereas real distribution systems typically operate under low-nutrient conditions with residual disinfectants that play a crucial role in shaping microbial communities. The absence of these real-world constraints may have affected biofilm growth rates, shear response, and mechanical properties, potentially leading to an overestimation of biofilm resilience under cyclic hydrodynamic forcing relative to operational networks.The representation of hydraulic transients in the experimental setup is another factor to consider. The transient pulses introduced in this study were designed to generate short-lived acceleration and deceleration phases in flow, rather than to precisely replicate transient events that occur in real distribution systems (e.g., pump trips, hydrant operations, and valve closures). While this approach allowed for the isolation of the impact of transient-induced shear stress on biofilm behaviour, the magnitude, frequency, and duration of these laboratory-generated transients may not fully capture the complexity of hydraulic transient fluctuations in real systems. The duration of the experiment, limited to 28 days, is also a constraint. While this timeframe was sufficient to observe an evolution in biofilm formation and adhesion, it may not fully capture the long-term biofilm dynamics and adaptation processes that occur in real distribution systems. Biofilms in operational networks are subjected to seasonal variations, prolonged exposure to fluctuating hydraulic conditions, and interactions with accumulated pipe deposits, all of which could influence their long-term behaviour in ways not accounted for in this study.
Despite these limitations, this study represents a critical first step forward in understanding the impact of hydraulic transients on biofilm development in drinking water distribution systems. Rather than treating hydraulic transients solely as acute disturbance events, this work demonstrates that operational-scale cyclic perturbations can function as mechanical conditioning stimuli that modulate biofilm resilience. By isolating transient effects, this study provides unique evidence of how biofilms respond to dynamic hydraulic conditions, a factor often overlooked in conventional biofilm management strategies. Furthermore, the findings highlight the potential role of controlled hydraulic transients in influencing biofilm stability, which may lead to new strategies to mitigate biofilm-related water quality issues.
The insights gained here establish a foundation for future research, emphasizing the need for field-scale validation and the inclusion of additional variables such as pipe material diversity, and realistic nutrient and disinfection regimes. By framing the results within the concept of biofilm resilience to cyclic hydrodynamic forcing, this work contributes to a more mechanistic understanding of how dynamic hydraulic conditions shape microbial ecosystem development indrinking water distribution networks.
The results have important practical implications for biofilm management in DWDSs. The strategic generation of controlled hydraulic transients may offer a potential approach for regulating biofilm formation while minimizing excessive accumulation or sudden detachment events that could lead to water quality issues such as discoloration and microbial contamination.
Overall, this study advances the understanding of how hydraulic transients influence biofilm development, reinforcing the need for integrated biofilm management strategies that consider both hydraulic and microbial dynamics. By bridging the gap between hydraulic engineering and microbial ecology, these findings contribute to the development of more effective water quality control practices, enhancing the sustainability and safety of drinking water distribution networks.
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