Water distribution networks (WDNs) ensure safe and adequate water, requiring efficient hydraulic performance and water quality management. This study examines challenges in maintaining residual chlorine levels and hydraulic efficiency in IIT Roorkee's WDN. Chlorine dosing at seven overhead tanks (OHTs) at 0.5 mg/L over 24 h (1.775 kg/day) fails to sustain residual chlorine above 0.2 mg/L, leading to microbiological regrowth. A methodology integrating mixed-integer linear programming and WaterGEMS modeling was developed to optimize booster chlorination (BC) stations. Water demand was allocated using the Thiessen polygon method, and the life-cycle cost (LCC) of BC stations was evaluated using the present worth (PW) method. From 93 junctions, eight critical ones were identified. Four optimally placed BC stations (BC1–BC4) at links P-124, P-67, P-9, and P-119, with a chlorine dosage of 1 mg/L, reduced total chlorine mass to 3.075 kg/year and LCC to INR 101.90 million over 30 years while maintaining residual chlorine above 0.2 mg/L. Model calibration and validation yielded R² values of 0.86 (chlorine) and 0.96 (pressure). Pressure analysis revealed suboptimal pressures at 16.13% of junctions during peak demand. This study highlights existing inefficiencies and demonstrates the benefits of optimized booster chlorination.

  • The hydraulic performance of the water distribution network was studied.

  • Optimized BC stations were proposed to improve disinfection and maintain residual chlorine.

  • Measured junction pressure was used for WaterGEMS calibration before hydraulic analysis.

  • Water quality at overhead tank was used for WaterGEMS calibration before chlorine analysis.

  • The life-cycle cost of booster chlorination stations was evaluated using the present worth method.

Water supply and distribution systems are critical infrastructures that provide communities with reliable access to clean and safe water. These systems include water sources, pump stations, treatment plants, service reservoirs, overhead tanks (OHTs), and pipe networks. Their primary function is to supply and distribute potable water from the source to the community for various purposes (Mehta et al. 2017). In addition to meeting the needs of human consumption, effective water supply and distribution systems are essential for sustaining economic activities, ensuring public health, and promoting overall societal well-being (Kadhim et al. 2021). Efficient management of these systems plays a pivotal role in fostering sustainable development and improving the quality of life for populations (Beker & Kansal 2023).

Maintaining water quality in urban water distribution systems (WDS) is crucial, as these systems represent the final before human consumption. Even treated water can become contaminated during distribution, posing significant risks to public health (Islam et al. 2017). Water intended for drinking and food preparations must meet established quality standards and remain free of organic and inorganic contaminants that could cause diseases. Among the various methods used for water disinfection, chlorine is the most commonly employed disinfectant (Mazhar et al. 2020). The efficiency of the disinfections by chlorine depends on residual chlorine concentration ensuring continuous protection of microbial contaminants throughout the distribution networks. In WDS, residual chlorine levels of between 0.2 and 0.3 mg/L are frequently maintained to act as a sentinel for the entry of pollutants and to stop the growth of unwanted bacteria and other organisms (Galal-Gorchev 1996).

The chlorine dosage and the location of injections during disinfections are factors that significantly affect residual chlorine levels in WDS (Javadinejad et al. 2019). However, excessive chlorine concentrations in WDS can lead to several challenges, including pipe corrosion and unpleasant taste and odor for consumers near the entry points of the systems. Moreover, elevated levels of chlorine can result in the formation of harmful disinfection by-products, such as trihalomethanes, which are carcinogenic at high concentrations (Goyal & Patel 2015). For this reason, many national regulations impose strict limits on the maximum allowable residual chlorine concentration (Cmax). Reducing the maximum residual concentration (Cmax) at the treatment plant may alleviate these concerns. Still, it could result in inadequate chlorine levels at distant junctions with longer residence times in large water distribution networks (WDN) (Kansal et al. 2005).

The proper location of booster chlorination (BC) stations emerges as a critical solution to maintain the recommended residual chlorine levels throughout WDN, ensuring both the safety and effectiveness of disinfection. To address the optimal placement, operation, scheduling, number, and chlorine dosage of the BC stations in WDNs, several researchers have developed optimization models using various approaches. While many studies discuss life cycle costs, they typically focus only on capital costs, chlorine dosage, and operation/maintenance costs, without accounting for the replacement costs associated with the BC stations. This study addresses this gap by presenting a novel methodology that integrates LCC analysis, with a particular emphasis on replacement costs, into the optimization of BC station placement and dosage, ensuring the economic feasibility and sustainability of the proposed solutions. Cost and time overruns are common challenges in construction projects worldwide, impacting both efficiency and sustainability (Ugural & Burgan 2021). Similarly, Rahman et al. (2012) emphasize that time and cost efficiency are key indicators of a project's overall success.

Recently, Sime & Kansal (2024) investigated an optimization problem for BC stations using a mixed integer linear programming problem. The aim is to minimize chlorine dosage and life cycle costs by increasing the number of BC stations. However, during cost analysis, the study does not consider the life span of BC stations with the design period of WDN. Similarly, Sert & Altan-Sakarya (2017) proposed a linear programming approach to determine the optimal injection rate of the BC stations by considering two scenarios, with and without initial concentrations as unknown variables. However, this methodology focuses on optimizing disinfectant mass injection and maintaining residual chlorine concentration throughout the WDN without addressing the economic aspects like capital costs, operations/maintenance costs, and replacement costs of BC stations over their lifespan. This omission results in a deficiency in comprehending the long-term economic viability and sustainability of establishing booster disinfection stations.

In addition to this gap, several studies are investigating the hydraulic performance of existing WDN using EPANET, WaterCAD, and WaterGEMS software. For example, Mekonnen (2023) and Jeong & Kang (2020)) evaluate the hydraulic performance of existing WDS. However, most studies aim to determine the pressure and velocity in WDN without effectively addressing how to allocate node water demand. Similarly, Agunwamba et al. (2018) and Nasrollahi et al. (2021) have focused on hydraulic modeling and pressure management but often rely on simplified demand allocation methods. Proper demand allocation is critical to accurately representing the hydraulic and chlorine dynamics in the network, and its neglect can compromise the accuracy of simulation results and optimization outcomes. This study employs the Thiessen polygon approach to spatially allocate junction water demand and integrates it with WaterGEMS hydraulic modeling to simulate pressure, velocity, and chlorine distribution across the WDN.

The methodology uses mixed-integer linear programming and water quality modeling WaterGEMS software to determine the optimal BC stations for effective disinfection and the present worth (PW) method was applied to evaluate the LCC of BC stations. Minimizing the chlorine dosage and number of BC is the objective function, and maintaining residual chlorine in WDN is a constraint during the optimization of BC.

Description of study area

The study area is the Indian Institute of Technology Roorkee, one of India's premier engineering institutes, located in the Hardwar district of Uttarakhand, India (Figure 1). The campus encompasses 23 departments, 2 senior secondary schools, and one hospital, covering 147.71 hectares. Situated at the foothills of the Himalayas along the banks of the Ganges River, the campus is geographically positioned between a latitude of 29°51′52ʺN and a longitude of 77°53′47ʺE, with an elevation range of 260–275 m and an average elevation of 268 m above mean sea level. The climate of Roorkee is classified as humid subtropical, characterized by hot summers, cool winters, and heavy rainfall during the monsoon season. According to Indian temperature zoning, summer spans from April to June with temperatures ranging from 25 to 45 °C, the monsoon season occurs from July to September with temperatures between 25 and 35 °C, and winter lasts from December to February with temperatures ranging from 5 to 20 °C. The annual precipitation in Roorkee varies between 1,000 and 12,000 mm, predominantly occurring during the monsoon season.
Figure 1

Study area map.

Proposed framework to analyze hydraulic performance and optimal BC

Figure 2 illustrates and explains the proposed framework for analyzing hydraulic performance and optimal BC in the existing urban WDN step-by-step.
Figure 2

Proposed framework to analyze hydraulic performance and optimal BC (numbers indicate the order of steps).

Figure 2

Proposed framework to analyze hydraulic performance and optimal BC (numbers indicate the order of steps).

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Step 1. Data collection

The following information parameters are needed to model and simulate any urban area's existing WDN. (1) Pipe information (length, diameter, and roughness); (2) OHT data (elevation and diameter); (3) pump data (discharge rate and pump head); and (4) junction data (demand, pressure, and water quality), and population data. These datasets were collected through various methods, including field observations, experimental tests, historical records, and interviews with field workers. These data were also collected using a pressure gauge, magnetic flow meter, and plastic jerrycan.

Step 2. Mapping the existing WDN using Google Earth Pro, ArcGIS, and WaterGEMS software

The existing system was mapped using Google Earth Pro to identify OHT, tube wells, road patterns, building types (institution, public, or residential area), and pipeline networks Figure 3(a). The data were then exported to ArcGIS software for Thiessen polygon preparation Figure 3(b)). Finally, the data were imported into WaterGEMS to simulate chlorine concentration and hydraulic parameters during peak and minimum hourly consumption (MHC) Figure 3(c).
Figure 3

Layout of the existing WDN using three different platforms. (a) Google Earth (b) ArcGIS, and (c) WaterGEMS.

Figure 3

Layout of the existing WDN using three different platforms. (a) Google Earth (b) ArcGIS, and (c) WaterGEMS.

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Step 3. Allocation of node water demand using the Thiessen polygon approach

Junction water demand allocation refers to the demand at a specific point in a WDN, typically at junctions. WDN models simplify by assuming that water is drawn only from a limited number of junctions, ignoring the numerous actual service connections along the pipelines. As suggested by Mulatu (2017), the water demand at a particular junction can be estimated by dividing the total population by the number of junctions and multiplying by a standard per capita water demand rate. However, this method does not accurately represent the actual allocation of junction water demand, as it assumes an even distribution of users across junctions without considering the spatial variation of users. Similarly, grouping existing water users solely based on demand requirements overlooks the geographical proximity of users to specific junctions, potentially leading to an inaccurate distribution of localized demand patterns. Therefore, the Thiessen polygon approach is more suitable, as it delineates the service area of each junction spatially, providing an equitable distribution of water demand based on the proximity of users to the nearest junction, which is particularly useful in areas with high population density.

Additionally, the Thiessen polygon approach ensures that each junction's area of influence is clearly defined, making it more appropriate for network analysis and hydraulic modeling. Tufa & Abate (2022) state that the Thiessen polygon creates a polygon around each demand junction to define the area it influences. These polygons must incorporate population data and per capita water demand to ensure the accurate allocation of junction water demand. In this study, the per capita water demand was set at 200 liters per capita per day (l/s) for residential areas and 45 liters per capita per day (lpcd) for institutional areas to allocate junction water demand. The university population density was estimated at one person per room for unmarried hostels and four persons per room for married hostels. The demand at each junction within the distribution system is calculated using the following equation:
(1)
where Qi represents the junction water demand in (l/s), pi is the population distribution at junction i, qi is the per capita water demand (l/s) at junction i, and 86,400 is the number of seconds in a day.

Step 4. WaterGEMS model calibration to hydraulic parameters and chlorine

According to Mekonnen (2023), it is essential to calibrate and validate a model to ensure that its results accurately reflect the values observed in the field. Similarly, Kassahun & Dargie (2024) state that model calibration continuously evaluates and adjusts parameters by comparing the simulated outcomes with the observed values. This study uses WaterGEMS software for two purposes:

  • (1) Hydraulic analysis in the WDN to assess pressures at various nodes and velocities in various pipelines during the various hourly demands.

  • (2) To assess the residual chlorine concentration at various nodes; identify the nodes with less than min. Chlorine concentration, and identify/suggest the booster chlorine concentration stations.

However, the model is calibrated and validated through the observed and simulated pressures and residual chlorine concentration at several nodes of the WDN to ensure the accuracy of the model. According to Tufa & Abate (2022), 2–10% of the samples are sufficient for calibration and validation. In this study, four dead-end locations (J-56, J-82, J-84, and J-91) were selected (out of the total 93 locations) (4% of the total nodes) for calibration and validation of pressures at the peak hourly demand and pressure is measured by the use of a pressure gauge. The residual chlorine is calibrated and validated through the three overhead tanks (OHT-1, OHT-2, OHT-3, and OHT-7) by assessing residual chlorine using the 4500-Cl B Iodometric Method. Therefore, the statistical correlation coefficient (R2) was used to evaluate the model's accuracy.

Step 5. Simulation of hydraulic parameters and residual chlorine levels

The calibrated and validated WaterGEMS model was run to simulate pressure, velocity, and residual chlorine levels. To evaluate the pressure and velocity of the existing WDN, the WaterGEMS model was run under peak and MHC scenarios. For residual chlorine levels, the model was run for 24 h starting from the time of chlorine dosage injection.

Step 6. Proposed methodology for optimizing BC stations

Traditionally, municipal drinking WDNs are disinfected by adding chlorine at the source, typically in water treatment plants. However, this method often requires a higher chlorine dosage to ensure sufficient residual chlorine concentration at distant nodes within the network (Sert & Altan-Sakarya 2017). In an extensive municipal WDN with long water retention time, certain areas of the network may experience insufficient chlorine residual levels. Proper placement of BC stations in WDN can help maintain adequate residual chlorine concentrations across the entire network while minimizing chlorine dosage (Javadinejad et al. 2019). However, determining the optimal location and dosage of BC stations is one of the most significant factors. The following flowchart illustrates the step-by-step methodology for determining the optimal placement and number of BC stations in a WDN, integrating performance evaluation, LCC analysis, and tradeoff considerations (Figure 4).
Figure 4

Optimization framework for BC: steps for placement, cost analysis, and feasibility assessment.

Figure 4

Optimization framework for BC: steps for placement, cost analysis, and feasibility assessment.

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Step A: Problems formulation for optimization of BC stations in WDN

The primary objectives of optimizing BC stations are to minimize the chlorine dosage required for disinfection, reduce the number of BC stations, and ensure safe and efficient water distribution. This study proposed an optimization approach to address the operational and economic challenges associated with disinfection by chlorine, as outlined below.

Minimum total chlorine dosage injection
During chlorination, chlorine dosage must be carefully optimized to maintain the recommended residual chlorine levels throughout networks. Consider a WDN where there is m number of links which is suitable for BC stations, n is the total number of junctions in WDN, chlorine dosage added to water at link j, flow through links, is minimum allowable chlorine concentration, is maximum allowable chlorine concentration, is chlorine concentration at node i, and Dt is the total mass dosage required (kg/day), the objective function can be stated as follows:
(2)
Subject to:
(3)
(4)
Minimizing the number of booster stations
BC stations are strategically placed at selected links to achieve optimal chlorine coverage, while the number of stations is minimized to reduce the life cycle costs. Assume NB is the number of BC stations in the network, and Xi is a binary variable representing whether a booster station is placed at link j.
Objective function:
(5)
(6)

Step B: Evaluate the current performance of chlorine levels

Maintaining chlorine residuals within a WDN is crucial to protecting users from microbial contamination (Avvedimento et al. 2022). The regulatory requirement for residual chlorine at the consumer end in India is a minimum of 0.2 mg/l to prevent microorganism contamination at various points in the water distribution (Goyal & Patel 2015). However, many countries practice chlorination at the source or service reservoirs to meet these regulatory requirements without considering the size of the network and chlorine decay in WDN.

This approach often results in under-dosing, thereby exposing the users to microbial growth, or over-dosing, which can increase the economic burden of disinfection and cause taste and odor issues (Haider et al. 2015). In the IIT Roorkee WDN, chlorine is applied to the OHTs at a concentration of 0.5 mg/l over 24 h, with a total chlorine dosage of 1.775 kg/day across seven OHTs (Figure 5). However, this application method fails to maintain adequate residual chlorine levels throughout the network. The regulatory requirement for residual chlorine at the consumer end in India is a minimum of 0.2 mg/l to prevent microbial contamination at various points in the distribution system.
Figure 5

Existing chlorine application system in the OHT.

Figure 5

Existing chlorine application system in the OHT.

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Step C: Find the optimal placement and number of BC stations

According to Avvedimento et al. (2022), installing BC stations is the best solution to address issues of under-dosing and over-dosing effectively and maintain residual chlorine levels across the WDN. This study analyzed five scenarios to determine the ideal location and the number of BC stations, as well as the chlorine dosage needed for effective disinfection. In scenario 1, only the chlorine dosage was increased from 0.5 to 4 mg/l to assess its impacts on residual chlorine levels across the WDN before proposing BC stations. Scenario 2 proposed installing one BC station, followed by scenario 3 with two BC stations. Scenario 4 analyzed the performance with three BC stations, and finally, scenario 5 evaluated the residual chlorine across the full network with four BC stations.

Step-D: Life cycle cost (LCC) of selected BC stations

The LCC of each BC station is calculated using the PW method, a financial evaluation technique used to determine the value of a series of cash flows at a single point in time, typically at the present, using a specified discount rate (Krupnick 1998). This calculation considers the BC station life span of 30 years, from 2025 to 2055. In this method, three cost components are considered for LCC analysis: Fixed costs (capita and chlorine costs), operational/maintenance (O&M) costs, and replacement costs (rc). The money required to replace a component of BC stations during the life cycle of a project is classified as replacement costs, with replacements occurring every 10 years (Jena & Kansal 2025). According to Islam et al. (2013) and Sime & Kansal (2024), land acquisition, house construction, and securing initial utilities are associated with capital costs. In contrast, operators and utilities are considered part of O&M costs. In this study, the annual O&M costs are calculated as 5% of the present worth of fixed cost (PWfc), while replacement costs are projected at 15 and 30% of PWfc for 2035 and 2045, respectively (Table 1). The present worth of fixed costs (PWfc), present worth of operation and maintenance costs (PWo&m), and present worth of replacement costs (PWrc) are calculated as follows.
(7)
(8)
(9)
(10)
where n is the design period which is 30 years, A is the fixed cost for 30 years, and, i is the discount rate (8%).
Table 1

Economic assessment criteria for LCC analysis

ScenariosCost criteria (the base year of 2025)DescriptionPW of the cost (INR in millions)
Existing system Fixed cost Only the chlorine cost 0.15 
O&M cost (annual) 5% of fixed cost (0.01 million per year) 0.001 
Total PW of the chlorination  0.15 
Capital recovery factor (annual)  0.01 
Benefit-cost ratio (B/C)  1.02 
Scenario 1 Fixed cost Capital cost + chlorine cost 1.17 
O&M cost (annual) 5% of fixed cost (0.06 million per year) 0.01 
Total PW of the chlorination  1.18 
Capital recovery factor (annual)  0.11 
Benefit-cost ratio (B/C)  1.02 
Scenario 2 Fixed cost Capital cost + chlorine cost 100.5 
O&M cost (annual) 5% of fixed cost (5.02 million per year) 0.50 
Replacement cost after 10 years 15% of PW of the fixed cost in 2035, 15.08 M 0.6 
Replacement cost after 20 years 30% of PW of the fixed cost in 2045, 30.15 M 0.6 
Total PW for one booster station  102.19 
Capital recovery cost  9.08 
Benefit-cost ratio (B/C)  1.02 
Scenario 3 Fixed cost Capital cost + chlorine cost 100.49 
O&M cost (annual) 5% of fixed cost (5.02 million per year) 0.50 
Replacement cost after 10 years 15% of PW of the fixed cost in 2035, 15.07 M 0.62 
Replacement cost after 20 years 30% of PW of the fixed cost in 2045, 30.14 M 0.57 
Total PW for two booster stations  102.18 
Capital recovery cost  9.08 
Benefit-cost ratio (B/C)  1.02 
Scenario 4 Fixed cost Capital cost + chlorine cost 100.47 
O&M cost (annual) 5% of fixed cost (5.02 million per year) 0.50 
Replacement cost after 10 years 15% of PW of the fixed cost in 2035, 15.07 M 0.62 
Replacement cost after 20 years 30% of PW of the fixed cost in 2045, 30.14 M 0.57 
Total PW for the three booster stations  102.16 
Capital recovery cost  9.07 
Benefit-cost ratio (B/C)  1.02 
Scenario 5 Fixed cost Capital cost + chlorine cost 100.21 
O&M cost (annual) 5% of fixed cost (5.01 million per year) 0.50 
Replacement cost after 10 years 15% of PW of the fixed cost in 2035, 15.03 M 0.62 
Replacement cost after 20 years 30% of PW of the fixed cost in 2045, 30.06 M 0.57 
Total PW for four booster stations  101.90 
Capital recovery cost  9.05 
Benefit-cost ratio (B/C)  1.02 
ScenariosCost criteria (the base year of 2025)DescriptionPW of the cost (INR in millions)
Existing system Fixed cost Only the chlorine cost 0.15 
O&M cost (annual) 5% of fixed cost (0.01 million per year) 0.001 
Total PW of the chlorination  0.15 
Capital recovery factor (annual)  0.01 
Benefit-cost ratio (B/C)  1.02 
Scenario 1 Fixed cost Capital cost + chlorine cost 1.17 
O&M cost (annual) 5% of fixed cost (0.06 million per year) 0.01 
Total PW of the chlorination  1.18 
Capital recovery factor (annual)  0.11 
Benefit-cost ratio (B/C)  1.02 
Scenario 2 Fixed cost Capital cost + chlorine cost 100.5 
O&M cost (annual) 5% of fixed cost (5.02 million per year) 0.50 
Replacement cost after 10 years 15% of PW of the fixed cost in 2035, 15.08 M 0.6 
Replacement cost after 20 years 30% of PW of the fixed cost in 2045, 30.15 M 0.6 
Total PW for one booster station  102.19 
Capital recovery cost  9.08 
Benefit-cost ratio (B/C)  1.02 
Scenario 3 Fixed cost Capital cost + chlorine cost 100.49 
O&M cost (annual) 5% of fixed cost (5.02 million per year) 0.50 
Replacement cost after 10 years 15% of PW of the fixed cost in 2035, 15.07 M 0.62 
Replacement cost after 20 years 30% of PW of the fixed cost in 2045, 30.14 M 0.57 
Total PW for two booster stations  102.18 
Capital recovery cost  9.08 
Benefit-cost ratio (B/C)  1.02 
Scenario 4 Fixed cost Capital cost + chlorine cost 100.47 
O&M cost (annual) 5% of fixed cost (5.02 million per year) 0.50 
Replacement cost after 10 years 15% of PW of the fixed cost in 2035, 15.07 M 0.62 
Replacement cost after 20 years 30% of PW of the fixed cost in 2045, 30.14 M 0.57 
Total PW for the three booster stations  102.16 
Capital recovery cost  9.07 
Benefit-cost ratio (B/C)  1.02 
Scenario 5 Fixed cost Capital cost + chlorine cost 100.21 
O&M cost (annual) 5% of fixed cost (5.01 million per year) 0.50 
Replacement cost after 10 years 15% of PW of the fixed cost in 2035, 15.03 M 0.62 
Replacement cost after 20 years 30% of PW of the fixed cost in 2045, 30.06 M 0.57 
Total PW for four booster stations  101.90 
Capital recovery cost  9.05 
Benefit-cost ratio (B/C)  1.02 
Finally, the LCC of the proposed BC stations is calculated as the sum of the PW of all cost components.
(11)
Additionally, 20 rupees/kg is assumed for chlorine cost. The cash flow diagram for each PW of cost components is shown in Figure 6.
Figure 6

Cash flow diagram for LCC analysis of a BC station (30-year projection).

Figure 6

Cash flow diagram for LCC analysis of a BC station (30-year projection).

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Allocation of node water demand using the Thiessen polygon approach

In this study, the demand for residential (R), institutional (I), and public (P) areas is allocated to the nearest junctions (J) using the Thiessen polygon method. This method divides the areas into polygons and assigns each polygon to the nearest junction, ensuring efficient demand distribution. It requires two polygon layers. The first polygon layer is related to the polygons allocated to each junction. The second polygon layer, the consumption layer with demand types (like Residential/institutional), included a specified population density (Momenzadeh et al. 2018). For instance, the demand for R1, R2, R3, and R4 is obtained from J-65, while R5, R6, R7 and R23 are served by J-64. Similarly, R8, R9, and R13 are connected to J-63 and R10, R11, and R12 derive their supply from J-62. Furthermore, R14, R15, R16, R17, and R18 are linked to J-61, and the demand for R19, R20, R21, and R22 are fulfilled by J-66 (Figure 7(a) and 7(b)). The calculated junction demands (l/s) are then imported into the WaterGEMS software for hydraulic and residual chlorine simulation (Figure 7(c)). The institutions can be classified into eight zones denoted by letters A through H, to allocate junction water demand with 93 junctions and 124 pipes.
Figure 7

Thiessen polygon junction water demand allocation.

Figure 7

Thiessen polygon junction water demand allocation.

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Simulation of hydraulic parameters

Result of pressure analysis

Pressure is crucial for ensuring water's reliable and efficient delivery to consumers. Proper pressure levels guarantee that water reaches all parts of the town/city without causing damage to the systems or risking supply interruption (Nasrollahi et al. 2021). According to Agunwamba et al. (2018), high-pressure head systems directly impact pipe bursts and energy demand in WDS. The minimum and maximum pressures in the distribution network are 15–60 m under normal conditions and 15–70 m under exceptional conditions, respectively, Kassahun & Dargie (2024). According to the WaterGEMS junctions report, the pressure distribution result during peak hourly consumption (PHC) indicates that out of 93 junctions in WDN, 16.13% (15 junctions) experience pressure levels below 15 m of water, 66.67% (62 junctions) have pressure between 15 and 25 m, and 17.20% (16 junctions) are in the 25–35 m range (Figure 8). Similarly, during MHC, 78.49% of junctions (73 junctions) have a pressure between 25 and 35 m, while 10.75% (10 junctions) have a pressure of 15–25 m, and another 10.75% (10 junctions) are in the 35–5 m range (Figure 9). Therefore, based on the pressure standard for WDS, the system performs well overall in terms of pressure, except for the low-pressure junctions during PHC, which require attention for improvement.
Figure 8

Pressure contour map during PHC.

Figure 8

Pressure contour map during PHC.

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Figure 9

Pressure contour map during MHC.

Figure 9

Pressure contour map during MHC.

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Velocity results analysis

The velocity of water flow in the pipe is one of the most important parameters for analyzing the hydraulic performance of WDS. The recommended minimum and maximum velocities in the distribution network are 0.6–2 m/s, respectively (Tufa & Abate 2022). A velocity below 0.6 m/s can cause the growth of bacteria and the deposition of sediment in pipes. On the other hand, a velocity in the pipe greater than 2 m/s can cause water hammer and head loss in the WDN. Results show that 14.29% (18 pipes) and 18.25% (23 pipes) fall below the desirable minimum velocity during peak and MHC, respectively. Conversely, 0.79% (1 pipe) and 1.59% (2 pipes) exceed the maximum desirable velocity during peak and minimum hourly demand, respectively (Figures 10 and 11).
Figure 10

Velocity distribution during PHC.

Figure 10

Velocity distribution during PHC.

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Figure 11

Velocity distribution during MHC.

Figure 11

Velocity distribution during MHC.

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Optimization of BC placement and dosage

To evaluate chlorine concentration levels across the WDN and determine the optimal placement of BC stations, eight junctions (J-1, J-4, J-49, J-50, J-55, J-56, J-70, and J-72) were selected from the study area boundary for simulation (Figure 12). These junctions were strategically chosen based on their susceptibility to low chlorine residual concentrations, ensuring a thorough evaluation of the effectiveness of different booster station placements. The selection process focused on identifying critical points within the distribution network where chlorine decay was most likely to occur, allowing for a comprehensive assessment of water quality and the efficiency of BC. Five scenarios were analyzed by adjusting chlorine dosage and implementing BC stations (Table 2).
Table 2

Scenario analysis for BC stations in IIT Roorkee WDN

Scenario no.DescriptionsOHTsBooster 1
Booster 2
Booster 3
Booster 4
Flow through the link (m3/day)Total yearly mass dosage required (kg)
Dosage (mg/l)LocationDosage (mg/l)LocationDosage (mg/l)LocationDosage (mg/l)LocationDosage (mg/l)
S1 Increase the dosage of chlorine in the current application method N/A N/A N/A N/A Volume = 3,550m3 5,183 
S2 One booster station is placed at the center N/A P-124 N/A N/A N/A 2,990.34 4,366 
S3 Two booster stations were used N/A P-124 P-67 N/A N/A 1,407.97 4,302 
S4 Three booster stations were used N/A P-124 P-67 P-9 N/A 1,390.60 4,226 
S5 Four booster stations were used N/A P-124 P-67 P-9 P-119 2,634.969 3,075 
Scenario no.DescriptionsOHTsBooster 1
Booster 2
Booster 3
Booster 4
Flow through the link (m3/day)Total yearly mass dosage required (kg)
Dosage (mg/l)LocationDosage (mg/l)LocationDosage (mg/l)LocationDosage (mg/l)LocationDosage (mg/l)
S1 Increase the dosage of chlorine in the current application method N/A N/A N/A N/A Volume = 3,550m3 5,183 
S2 One booster station is placed at the center N/A P-124 N/A N/A N/A 2,990.34 4,366 
S3 Two booster stations were used N/A P-124 P-67 N/A N/A 1,407.97 4,302 
S4 Three booster stations were used N/A P-124 P-67 P-9 N/A 1,390.60 4,226 
S5 Four booster stations were used N/A P-124 P-67 P-9 P-119 2,634.969 3,075 

N/A, not available; S, scenarios; P, pipe/link.

Figure 12

Proposed BC stations and sampled locations in IIT Roorkee WDN.

Figure 12

Proposed BC stations and sampled locations in IIT Roorkee WDN.

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Scenario analysis

In scenario 1, the chlorine dosage was increased from 0.5 to 4 mg/L before the proposed BC stations, requiring a total chlorine mass dosage of 5,183 kg/year for a total water volume of 3,550 m3 (Table 2). Despite this increase, chlorine levels remained effectively zero across the WDN, except around the OHT where it was applied. Many locations showed residual chlorine concentrations below the acceptable minimum threshold within 2–4 h, highlighting the limitations of the existing chlorination approach (Figure 13(a)). Scenario 2 introduced a single BC1 station at P-124 with a chlorine dosage of 4 mg/l, reducing the total chlorine mass dosage to 4,366 kg/year. However, residual chlorine levels remained below the recommended threshold, with junctions J-49, J-50, J-55, and J-56 showing 0 mg/l throughout the 24-hour simulation period (Figure 13(b)).
Figure 13

Simulated residual chlorine concentration across the network for (a) scenario 1, (b) scenario 2, (c) scenario 3, (d) scenario 4, and (e) scenario 5.

Figure 13

Simulated residual chlorine concentration across the network for (a) scenario 1, (b) scenario 2, (c) scenario 3, (d) scenario 4, and (e) scenario 5.

Close modal

Scenario 3 implemented two booster stations (BC1 at P-124 and BC2 at P-67), with chlorine dosages of 3 and 2 mg/l, respectively, reducing the total dosage requirement to 4,302 kg/year. Although chlorine distribution improved, J-49 and J-50 still exhibited concentrations below 0 mg/l (Figure 13(c)). Scenario 4 further optimized chlorine distribution by introducing three booster stations (BC1, BC2, and BC3), each with a chlorine dosage of 2 mg/l, reducing the total chlorine mass dosage to 4,226 kg/year. Most junctions showed effective chlorine maintenance, except for J-49, where levels remained unchanged (Figure 13(d)). Finally, scenario 5 implemented four booster stations (BC1, BC2, BC3, and BC4) strategically placed at P-124, P-67, P-9, and P-119, respectively, each with a chlorine dosage of 1 mg/l, significantly lowering the total chlorine dosage to 3,075 kg/year. This scenario ensured that residual chlorine concentrations across all observed junctions exceeded the minimum threshold of 0.2 mg/l, demonstrating the effectiveness of optimized BC in maintaining chlorine levels while minimizing overall chlorine usage (Figure 13(e)).

Life cycle cost of the booster stations

The cost analysis for all scenarios evaluates BC stations' PW for the base year 2025, including annual O&M costs, replacement costs over 20 years, and fixed costs (E). In scenario 1, the analysis focuses solely on the cost of the existing chlorination method by increasing the chlorine dosage from 0.5 to 4 mg/l without installing BC stations. As no capital and replacement costs are involved, the assessment centered on the annual chlorine costs, which amount to 103,660 INR/year (Table 3), with a PW of 1.17 million INR. Additionally, the annual O&M cost for this scenario is 0.06 million INR/year, contributing a PW of 0.01 million INR.

Table 3

Summarized total chlorine dosage required and LCC for selected BC stations

ScenariosLocation of chlorine injectionsChlorine dosage for selected booster station (mg/l)Total mass dosage required (kg/year)Chlorine cost (INR/year)LCC of BC (INR/30 years in million)
Existing system (OHTs) [0.5] 648 12,960 0.15 
Scenario-1 [OHTs] [4] 5,183 103,660 1.20 
Scenario-2 [BC1] [4] 4,366 87,318 102.20 
Scenario-3 [BC1, BC2] [3,2] 4,302 86,045 102.18 
Scenario-4 [BC1, BC2, BC3] [2,2,2] 4,226 84,518 102.16 
Scenario-5 [BC1, BC2, BC3, BC4] [1,1,1,1] 3,075 61,494 101.90 
ScenariosLocation of chlorine injectionsChlorine dosage for selected booster station (mg/l)Total mass dosage required (kg/year)Chlorine cost (INR/year)LCC of BC (INR/30 years in million)
Existing system (OHTs) [0.5] 648 12,960 0.15 
Scenario-1 [OHTs] [4] 5,183 103,660 1.20 
Scenario-2 [BC1] [4] 4,366 87,318 102.20 
Scenario-3 [BC1, BC2] [3,2] 4,302 86,045 102.18 
Scenario-4 [BC1, BC2, BC3] [2,2,2] 4,226 84,518 102.16 
Scenario-5 [BC1, BC2, BC3, BC4] [1,1,1,1] 3,075 61,494 101.90 

Thus, the total LCC of the chlorination system is calculated to be 1.18 million INR. There was no significant difference between the LCC in scenarios 2, 3, and 4; the chlorine costs were 87,318 INR/year, 86,045 INR/year, and 84,518 INR/year, respectively. The slight reduction in chlorine costs in those scenarios does not significantly impact the overall costs. In those scenarios, the LCC was approximately 102.20 INR/30 years (Table 1). Scenario 5 has the lowest LCC of 101.9 INR/30 years among scenarios 2–5 due to the reduced chlorine dosage requirement (3,074.7 kg/year), which lowers the chlorine costs. The annual O&M cost of this scenario is 5.1 million, which is higher than the existing system's annual O&M cost of 0.01 million. Despite the higher O&M costs, the new approach ensures better maintenance of residual chlorine levels throughout the system, significantly improving water quality and meeting water safety standards. The cash flow diagrams for all scenarios are shown in Figure 14.
Figure 14

Cash flow diagrams for (a) scenario 1, (b) scenario 2, (c) scenario 3, (d) scenario 4, and (e) scenario 5 over a 30-year projection.

Figure 14

Cash flow diagrams for (a) scenario 1, (b) scenario 2, (c) scenario 3, (d) scenario 4, and (e) scenario 5 over a 30-year projection.

Close modal

Calibration and validation of the WaterGEMS model for pressure simulation

Before simulating pressure, the hydraulic model was calibrated and validated to ensure its accuracy. The calibrated process involved adjusting model parameters to match observed pressure readings at key junctions (Figure 15). The pressure in the WDN was measured during peak hourly demand using a pressure gauge at J-56, J-82, J-84, and J-91. These observed values were then compared with the simulated results from the WaterGEMS hydraulic model to validate the model's accuracy before proceeding with further simulations (Figure 16).
Figure 15

Calibration results for; (a) J-56, (b) J-82, (c) J-84, (d) J-91.

Figure 15

Calibration results for; (a) J-56, (b) J-82, (c) J-84, (d) J-91.

Close modal
Figure 16

Observed and simulated pressure.

Figure 16

Observed and simulated pressure.

Close modal
Figure 17

Relation between observed and simulated pressure.

Figure 17

Relation between observed and simulated pressure.

Close modal
Figure 18

Calibration results for (a) OHT-1; (b) OHT-2; (c) OHT-3; (d) OHT-7.

Figure 18

Calibration results for (a) OHT-1; (b) OHT-2; (c) OHT-3; (d) OHT-7.

Close modal
Figure 19

Relation between experimental and simulated residual chlorine results.

Figure 19

Relation between experimental and simulated residual chlorine results.

Close modal

Calibration and validation of the WaterGEMS model for chlorine simulation

For model calibration and validation purposes, samples were taken during chlorine injection and throughout 24 hours for laboratory tests. Table 4 compares the simulated residual chlorine levels and the experimental measured in the laboratory. This comparison ensures the accuracy and reliability of the WaterGEMS model in predicting chlorine decay over time.

Table 4

Experimental and simulated residual chlorine (mg/l)

SampleInjection day and timeTime of sample takenSimulated residual chlorine (mg/l)Experimental chlorine residual (mg/l)
OHT-3 26/11/2024
10:00 am 
10:16 AM 0.50 0.49 
11:33 AM 0.47 0.42 
4:13 PM 0.10 0.00 
9:43 PM 0.06 0.00 
OHT-2 26/11/2024
10:50 am 
11:18 AM 0.36 0.35 
3:58 PM 0.28 0.25 
9:57 PM 0.21 0.18 
9:50 AM 0.00 0.00 
OHT-1 27/11/2024
10:45 am 
11:25 AM 0.46 0.49 
3:00 PM 0.10 0.11 
7:13 PM 0.08 0.09 
9:00 PM 0.06 0.03 
OHT-7 27/11/2024
10:00 am 
10:30 AM 0.49 0.46 
1:00 PM 0.27 0.28 
4:00 PM 0.10 0.11 
9:30 AM 0.06 0.04 
SampleInjection day and timeTime of sample takenSimulated residual chlorine (mg/l)Experimental chlorine residual (mg/l)
OHT-3 26/11/2024
10:00 am 
10:16 AM 0.50 0.49 
11:33 AM 0.47 0.42 
4:13 PM 0.10 0.00 
9:43 PM 0.06 0.00 
OHT-2 26/11/2024
10:50 am 
11:18 AM 0.36 0.35 
3:58 PM 0.28 0.25 
9:57 PM 0.21 0.18 
9:50 AM 0.00 0.00 
OHT-1 27/11/2024
10:45 am 
11:25 AM 0.46 0.49 
3:00 PM 0.10 0.11 
7:13 PM 0.08 0.09 
9:00 PM 0.06 0.03 
OHT-7 27/11/2024
10:00 am 
10:30 AM 0.49 0.46 
1:00 PM 0.27 0.28 
4:00 PM 0.10 0.11 
9:30 AM 0.06 0.04 

Statistical analysis and performance evaluation

The statistical analysis and performance evaluation of the WaterGEMS model for the IIT Roorkee WDN revealed strong agreement between observed and simulated values for both pressure and residual chlorine. Key statistical metrics, such as minimum, maximum, mean, median, standard deviation, and coefficient of variation, were calculated to assess the data distribution and variability. The model performance was evaluated using metrics like root mean squared error (RMSE), mean absolute error (MAE), Nash–Sutcliffe efficiency, and R-squared (R2). For pressure, the RMSE was 1.90, MAE was 1.43, and R2 was 0.86, indicating reliable hydraulic predictions (Figure 17). Figure 18 presents the calibration results for chlorine residuals at selected overhead tanks: (a) OHT-1, (b) OHT-2, (c) OHT-3, and (d) OHT-7. The simulated results closely align with observed values, demonstrating the model's calibration accuracy across different locations. The RMSE, MAE, and R² were 0.04, 0.03, 0.96 respectively (Figure 19), indicating exceptional accuracy in water quality simulations (Table 5). These results highlight the model's robustness and its potential for optimizing network operations and ensuring compliance with safety standards.

Table 5

Statistical characteristics and model performance metrics

Pressure
Chlorine
Data statisticObserved pressureSimulated pressureObserved residual chlorineSimulated residual chlorine
Minimum (Min) 15 15.56 
Maximum (Max) 30 30.49 0.5 0.49 
Mean (average) 23.7 24.68 0.23 0.21 
Median 25 26.12 0.16 0.15 
Standard deviation 4.156 4.487 0.18 0.19 
Coefficient of variation 17.54% 18.18% 79.90 90.12 
Skewness −1.0004 −0.8776 0.43 0.38 
95% confidence interval (21.75, 25.65) (22.58, 26.78) (0.13, 0.32) (0.11, 0.31) 
Model performance evaluation metrics 
RMSE 1.90 0.04 
MAE 1.43 0.03 
NSE 0.78 0.96 
R2 0.86 0.97 
Pressure
Chlorine
Data statisticObserved pressureSimulated pressureObserved residual chlorineSimulated residual chlorine
Minimum (Min) 15 15.56 
Maximum (Max) 30 30.49 0.5 0.49 
Mean (average) 23.7 24.68 0.23 0.21 
Median 25 26.12 0.16 0.15 
Standard deviation 4.156 4.487 0.18 0.19 
Coefficient of variation 17.54% 18.18% 79.90 90.12 
Skewness −1.0004 −0.8776 0.43 0.38 
95% confidence interval (21.75, 25.65) (22.58, 26.78) (0.13, 0.32) (0.11, 0.31) 
Model performance evaluation metrics 
RMSE 1.90 0.04 
MAE 1.43 0.03 
NSE 0.78 0.96 
R2 0.86 0.97 

The optimization of BC placement and dosage demonstrated the potential for significant improvements in maintaining residual chlorine levels across the WDN. In the IIT Roorkee WDN, the current system applies chlorine to the OHTs at a concentration of 0.5 mg/l over 24 h, with a total chlorine dosage of 1.775 kg/day across seven OHTs. However, this application method fails to maintain adequate residual chlorine levels throughout the network, highlighting a critical limitation of the existing system. This issue underscores the need for a more strategic approach to chlorine dosing and distribution. The proposed methodology for optimizing BC stations was developed using data from the existing system. By simulating various scenarios in WaterGEMS, we compared the existing system's performance with the optimized model. Key metrics chlorine concentration, water pressure, and velocity were evaluated. The results indicate that the optimized approach significantly enhances chlorine distribution, ensuring compliance with safety standards and improving overall system efficiency.

The five scenarios analyzed revealed that increasing chlorine dosage alone (scenario 1) is insufficient to maintain adequate chlorine concentrations throughout the network. However, the strategic placement of BC stations (scenarios 2–5) significantly improved chlorine distribution, with scenario 5 emerging as the most effective approach. By implementing four booster stations with optimized chlorine dosages, scenario 5 ensured that residual chlorine concentrations exceeded the minimum threshold of 0.2 mg/l across all observed junctions while minimizing overall chlorine usage. This approach not only enhances water quality but also reduces operational costs and environmental impacts associated with excessive chlorine use.

The LCC analysis of the BC scenarios provided valuable insights into the economic feasibility of different strategies. While scenario 1 (increased chlorine dosage without booster stations) had the lowest initial cost, its inability to maintain adequate chlorine levels makes it an unsustainable long-term solution. In contrast, scenarios 2–4, which involved the installation of booster stations, offered better performance but at higher costs. Scenario 5, despite having the highest initial investment, emerged as the most cost-effective option over 30 years due to its lower chlorine dosage requirements and improved system performance. The LCC analysis highlights the importance of considering both capital and operational costs when evaluating water distribution system improvements.

The findings underscore the importance of adopting a systematic approach to BC, considering factors such as network topology, flow patterns, and chlorine decay rates. Additionally, practical recommendations for implementing BC stations were provided, considering factors such as cost, feasibility, and population coverage. These recommendations are grounded in the analysis of the existing system, ensuring that the proposed solutions are both technically sound and practically viable.

The main objective of this study was to evaluate the existing chlorination approach and determine the optimal placement and number of BC stations, along with assessing the hydraulic performance of the WDN at IIT Roorkee, India. This was achieved using mixed-integer linear programming and WaterGEMS V8i software. The analysis identified that the existing chlorination approach was unable to maintain the recommended residual chlorine levels throughout the networks. The findings demonstrated that implementing four strategically placed BC stations (BC1, BC2, BC3, and BC4) at links P-124, P-67, P-9, and P-119, with a chlorine dosage of 1 mg/L, effectively addressed the challenges of maintaining residual chlorine levels above the minimum recommended threshold of 0.2 mg/l across the WDN. This configuration reduced the total chlorine mass dosage to 3.075 kg/year and minimized the LCC to INR 101.90 million over 30 years, making it the most efficient and cost-effective solution. Hydraulic performance analysis revealed that most junctions maintained acceptable pressure levels during peak and minimum demand. However, 16.13% of junctions experienced suboptimal pressures (<15 m) during peak demand. Velocity analysis indicated that 14.29% of pipes fell below the minimum threshold, with a minor fraction exceeding the maximum desirable velocity. Despite these deviations, the optimized system improved water quality and operational efficiency significantly. This study provides a replicable framework for addressing disinfection and hydraulic challenges in urban WDNs, promoting robust, cost-efficient, and environmentally sustainable systems. Future research should consider the impacts of seasonal and long-term variations in water demand on pressure, velocity, and residual chlorine levels to refine BC station placement and system performance further.

We thank the IIT Roorkee water supply office for their invaluable support through this study. Their provision of essential data and allocation of labor resources greatly contributed to the successful completion of our research.

Data cannot be made publicly available; readers should contact the corresponding author for details.

The authors declare there is no conflict.

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