The World Health Organization considers water quality aesthetic parameters affecting taste, odor, and appearance as factors to be monitored to determine the overall safety of water. Water safety plans (WSPs) can be used by utilities to proactively identify aesthetic hazards, rank them by likelihood of occurrence and consequence to the utility, generate risk scores, and provide direction on how to monitor, mitigate, and verify that controls are in place. The City of Wichita Falls Public Water System (CWF PWS) used the water safety planning approach to outline how aesthetics may negatively affect the system from source water, in-plant processes, and into the distribution system. By proactively identifying these hazards and outlining what to do using a WSP, the utility has put measures in place to ensure that aesthetically acceptable water is delivered to their customers. This article outlines the water safety planning process for water quality aesthetics and how the CWF PWS developed and implemented its WSP.

  • A water safety plan (WSP) is a tool that utilities can implement as a best management practice.

  • WSPs can complement required government regulations, along with internal operational guidelines.

  • This article highlights a comprehensive WSP for the management of aesthetic water quality and customer satisfaction for the City of Wichita Falls Public Water System (PWS).

The water safety plan (WSP) was introduced by the World Health Organization (WHO) in the 3rd edition of the Guidelines for Drinking-water Quality (WHO 2004) based on comprehensive risk assessment and management approaches to ensure the safety of drinking water (Hrudey et al. 2024). The WSPs are a tool that utilities can implement as a best management practice to complement government regulations, along with internal operational guidelines. The water safety planning framework consists of (1) system assessment to understand the entire water supply system from the source to the customer to identify potential hazards and assess risk, (2) control measures to effectively reduce the risks to acceptable levels, (3) monitoring to check the performance of the control measures, (4) management and communication, and (5) documentation and review (Davison et al. 2005).

The usefulness of WSPs lies in the fact that they are flexible and can be tailored to each individual utility's needs (Burlingame & Bartrand 2023). WSPs incorporate centralized controls (e.g., chemical dosing points within the water treatment process to reduce source water odors) and decentralized controls (e.g., flushing water mains throughout the distribution system to alleviate customer complaints). These controls can be used to mitigate single or multiple issues and risk scores can be assigned to issues that can then be prioritized for effective management of events (Ferrero et al. 2019; Tsitsifli & Tsoukalas 2021; WHO 2023). In the past decades, WSPs have been successfully developed and implemented to control chemical quality (Gunnarsdóttir et al. 2012), to assess and improve microbial quality in rural water utilities (Pundir et al. 2021; Souter et al. 2024), and to evaluate the possibility of improving consumer relations and challenging water quality issues (Rodriguez-Alvarez et al. 2022).

Utilities can use WSPs for health-related contaminants, as well as aesthetic issues, including customer complaints. Burlingame et al. (2024) described how water safety planning can be applied to such guidelines as the United States Environmental Protection Agency secondary maximum contaminant levels (US EPA SMCLs) which include aesthetic and cosmetic parameters, such as aluminum, chloride, odor, and taste in a more integrated manner. The WHO includes aesthetic quality as important for a safe water supply (WHO 2023) and the hazard category ‘Acceptability’ covers aspects that affect customer acceptance of the water (e.g., taste, odor, color, and appearance). These factors are crucial because if consumers find the water unacceptable, it could lead to a lack of confidence and might push them to seek alternative water sources that may not be safe (Turgeon et al. 2004; Doria et al. 2009). Consequently, aesthetic aspects are considered in water safety planning due to their potential indirect health implications. However, to date, there is a lack of case studies describing actual WSPs created and implemented by the water utilities to monitor and improve aesthetic quality and customer confidence (Ferrero et al. 2019).

This article outlines how the City of Wichita Falls Public Water System (CWF PWS) developed a WSP for aesthetic issues ranging from organic taste-and-odor (T&O) compounds to inorganics like chloride and iron. The WSP complements adherence to US EPA SMCLs by providing additional guidance on how to manage and prevent events caused by aesthetic issues. CWF PWS was already addressing aesthetic issues but in silos – not in an integrated way. A water safety planning approach brings together the goals, controls, monitoring, and management of the various aesthetic issues that could affect the water utility, whether currently being addressed or not, into one risk management plan – a WSP. The WSP becomes the standard procedure for controlling aesthetic water quality for the CWF PWS. This paper presents the water safety planning process that was used and shows various elements of the WSP that were developed.

Overview of the CWF PWS

The CWF is located in north-central Texas, USA, with a population of approximately 104,000 people. It is situated near the Texas-Oklahoma border, about 140 miles northwest of Dallas. The CWF PWS has a surface water system that consists of four surface water sources, including Lake Arrowhead, Lake Kickapoo, and the Lake Kemp/Lake Diversion system. These sources are treated at two locations, which include three conventional and one microfiltration/reverse osmosis advanced treatment plants at Cypress Water Treatment Facility (CWTF), and two conventional treatment plants at Jasper Water Treatment Facility (JWTF). The maximum capacities of CWTF and JWTF are approximately 26 and 54 million gallons per day or 98,000 and 204,000 m3/day, respectively, and serve around 150,000 people including surrounding communities that purchase raw and/or finished water. The CWF PWS also maintains a water distribution system with a total length of 579 miles (932 km) as shown in Figure 1. The water distribution system includes three pumping stations, nine ground storage tanks, and seven elevated storage tanks. The CWF PWS uses chloramine as a secondary disinfectant. The Texas Commission on Environmental Quality (TCEQ) is the primary regulatory agency in the State of Texas. The TCEQ enforces compliance with all US EPA regulations but has not set regulatory limits for aesthetics. The CWF PWS has an effective program for monitoring and mitigating T&O events (Adams et al. 2023b). This T&O management program for all aesthetic-related issues that CWF PWS faces was expanded to create a formal WSP in this study.
Figure 1

The CWF PWS with monitoring locations and controls generally indicated: control locations are where processes are in place to treat or manage hazards and monitoring locations are where tests are made to make sure the controls are being effective or operating as intended.

Figure 1

The CWF PWS with monitoring locations and controls generally indicated: control locations are where processes are in place to treat or manage hazards and monitoring locations are where tests are made to make sure the controls are being effective or operating as intended.

Close modal

Summary of the developing process of a WSP

The development of a WSP (i.e., water safety planning) follows certain steps in an organized manner, from identifying the hazards (in this case, the aesthetic concerns or SMCLs) and the means for managing or controlling them to the validation that controls actually work (WHO 2023). This can be summarized in the following steps as used for this WSP for the CWF PWS:

  • 1. Identify and list the hazards (contaminants) to be included in the WSP, covering both actual and potential hazards.

  • 2. Inventory the conditions or events that result in hazardous events, such as customer complaints.

  • 3. Assign ratings of the likelihood of occurrence and consequence of occurrence for each hazardous event in #2 above.

  • 4. Calculate risk scores based on the ratings for #3 above, for each hazardous event.

  • 5. Prioritize the risk scores to identify where improvement plans can reduce either the likelihood or consequence ratings and thus the risk scores.

  • 6. For each hazardous event, identify the critical controls that are in place to prevent an event or mitigate an event. Also identify control limits, monitoring plans, and response plans.

  • 7. Design validation monitoring to confirm that the controls are working as intended (such as actual measurement of SMCL parameters in the treated drinking water).

  • 8. Finalize the WSP and provide periodic reviews and updates.

The CWF PWS began building its WSP by using contaminants listed in Table 1 to create a risk matrix, drawing from decades of customer complaints that have been collected and stored. These strengthened the WSP, building it based on real water quality issues over time. However, no PWS can predict every possible scenario, so WSPs must be reviewed and revised accordingly as new data are collected. Aesthetic hazards were identified for each process step from source to distribution, along with the type of event the hazard could cause. The hazardous events that result in a contaminant causing a water quality problem were rated based on their likelihood of occurrence versus the severity of their consequence if they did occur. The inventory of hazardous events was combined with risk scores and ranked to determine where any immediate focus should be given. Then controls were identified for each hazardous event, as well as how to monitor each control and verify the controls' effectiveness at mitigating/reducing the hazard by the use of internally established action levels. The following sections describe how each part of the WSP was developed using examples from the CWF PWS.

Table 1

List of aesthetic hazards for consideration in the WSP

Parameter (units)Limit as per SMCLsUpdated limitaAesthetic issueStatus of the parameter for CWF
Parameters controlled centrally 
 Ammonia-N (mg/L) None 0.1 Odor Potential 
 Chloride (mg/L) 250 200 Taste Actual 
 Corrosivity Non-corrosive Needs to be updated Color, taste, staining, sediment Potential 
 Fluoride (mg/L) 2.0 Same Discoloration of teeth Potential 
 Geosmin (ng/L) None 5–15 based on local conditions Odor Actual 
 Hardness (mg/L as calcium) None 100 Taste, sediment, scaling Potential 
 2-Methylisoborneol (MIB) (ng/L) None 5–15 based on local conditions Odor Actual 
 pH (units) 6.5–8.5 Adjust according to local corrosion control treatment Taste, scaling Potential 
 Silver (mg/L) 0.1 Same Skin discoloration N/A 
 Sodium (mg/L) None 50 Taste Potential 
 Sulfate (mg/L) 250 200 Taste Potential 
 TDS (mg/L) 500 Same Taste, sediment, scaling Potential 
Parameters controlled by multiple, distributed means 
 Aluminum (mg/L) 0.05–0.2 Same Color, sediment Potential 
 Color (color units) 15 Same Color, sediment Potential 
 Copper (mg/L) 1.0 0.5 as soluble copper Taste, color, staining Potential (copper plumbing is used, but not historically an issue for the system) 
 Iron (mg/L) 0.3 0.15 as ferrous iron Taste/flavor, color, staining Actual 
0.15 as particulate iron (iron oxides) Sediment, staining, color 
 Manganese (mg/L) 0.05 0.02 Sediment, color, staining N/A (manganese is not an issue in source water) 
 Odor (threshold odor number) Develop specific odorant limits Odor Actual 
 Turbidity (NTU) None 1.0 Sediment, appearance Potential 
 Zinc (mg/L) Same Taste, color Potential (galvanized pipe and brass fittings/fixtures are used, but are not historically an issue for the system) 
Parameter (units)Limit as per SMCLsUpdated limitaAesthetic issueStatus of the parameter for CWF
Parameters controlled centrally 
 Ammonia-N (mg/L) None 0.1 Odor Potential 
 Chloride (mg/L) 250 200 Taste Actual 
 Corrosivity Non-corrosive Needs to be updated Color, taste, staining, sediment Potential 
 Fluoride (mg/L) 2.0 Same Discoloration of teeth Potential 
 Geosmin (ng/L) None 5–15 based on local conditions Odor Actual 
 Hardness (mg/L as calcium) None 100 Taste, sediment, scaling Potential 
 2-Methylisoborneol (MIB) (ng/L) None 5–15 based on local conditions Odor Actual 
 pH (units) 6.5–8.5 Adjust according to local corrosion control treatment Taste, scaling Potential 
 Silver (mg/L) 0.1 Same Skin discoloration N/A 
 Sodium (mg/L) None 50 Taste Potential 
 Sulfate (mg/L) 250 200 Taste Potential 
 TDS (mg/L) 500 Same Taste, sediment, scaling Potential 
Parameters controlled by multiple, distributed means 
 Aluminum (mg/L) 0.05–0.2 Same Color, sediment Potential 
 Color (color units) 15 Same Color, sediment Potential 
 Copper (mg/L) 1.0 0.5 as soluble copper Taste, color, staining Potential (copper plumbing is used, but not historically an issue for the system) 
 Iron (mg/L) 0.3 0.15 as ferrous iron Taste/flavor, color, staining Actual 
0.15 as particulate iron (iron oxides) Sediment, staining, color 
 Manganese (mg/L) 0.05 0.02 Sediment, color, staining N/A (manganese is not an issue in source water) 
 Odor (threshold odor number) Develop specific odorant limits Odor Actual 
 Turbidity (NTU) None 1.0 Sediment, appearance Potential 
 Zinc (mg/L) Same Taste, color Potential (galvanized pipe and brass fittings/fixtures are used, but are not historically an issue for the system) 

aUpdated limits are based on the review provided by Dietrich & Burlingame (2015) and Sain & Dietrich (2015).

Identification of aesthetic hazards

The US EPA's list of SMCLs, as well as several additional parameters, was compared with CWF PWS's experience and history with aesthetic issues and challenges to identify the existing hazards to be addressed by a water safety planning approach (Table 1). Each parameter is listed with its associated SMCL, including updates and customer complaint issues that are routinely observed. Many of these parameters are in need of update by the US EPA, as detailed in Dietrich & Burlingame (2015). Parameters that are known aesthetic issues for CWF PWS are labeled ‘Actual’. Parameters that have not caused issues but could be a concern are labeled ‘Potential’ and parameters that are unlikely to become issues are labeled ‘N/A’.

The parameters in Table 1 that are listed as centrally controlled are the parameters that are managed by source water controls or water treatment processes. Parameters that are controlled by multiple, distributed means include parameters controlled centrally but also within the distribution system, such as by valve operations, flushing, storage tank management, and corrosion control strategies.

Using a risk matrix

Water safety planning uses terminology and procedures as used in risk management programs (Alberta Environment and Parks 2013; WHO 2023). For example, a hazardous event is an event that could happen due to a hazard being present, such as a chemical contaminant in the water source due to an industrial spill. The hazard is a quantifiable parameter that poses a risk such as the concentration of a chemical contaminant. A risk is determined by the likelihood of exposure to the hazard and the consequence of exposure, such as skin irritation or sickness. The risk factors that lead to a hazardous event could be extrinsic (imposed by conditions outside of the utility's control such as a flood) or intrinsic (due to conditions or actions within the utility's control such as a transmission main break or a loss of chlorine residual in a storage tank due to failure in following proper tank operations). The following items were used to quantify and prioritize the risks:

  • Likelihood: A rating of the estimated or quantified frequency of occurrence of a hazardous event. The likelihood scoring is shown in Table 2 (Alberta Environment and Parks 2013).

  • Consequence: A rating of the impact or quantifiable result of a hazardous event.

  • Uncertainty: The confidence that the above two factors are accurately reflected.

Table 2

Terminology for the rating of likelihood

LikelihoodDefinitionRating
Not applicable Does not apply in this water system 
Rare Extremely small chance of happening 
Unlikely It is possible but unlikely to happen 
Possible It could happen 
Likely It is likely to happen 
Almost certain Has already happened or is about to happen 16 
LikelihoodDefinitionRating
Not applicable Does not apply in this water system 
Rare Extremely small chance of happening 
Unlikely It is possible but unlikely to happen 
Possible It could happen 
Likely It is likely to happen 
Almost certain Has already happened or is about to happen 16 

Uncertainty expresses the level of confidence in the likelihood or consequence rating. One way to change a risk score is to gather better data and information by which to show that a likelihood or consequence rating should be changed. For example, the likelihood of a geosmin odor event happening for a reservoir supply may be based on cyanobacterial bloom occurrence data. Therefore, the likelihood rating has a good degree of uncertainty associated with it since not all cyanobacterial blooms produce geosmin. The collection of actual geosmin concentrations during blooms will better determine the likelihood that any particular bloom produces geosmin, and therefore will better determine the likelihood of a hazardous event due to geosmin which could adjust the risk score for this aesthetic hazard.

The consequence scoring is shown in Table 3 (Alberta Environment and Parks 2013). These ratings have been adjusted because Texas has no regulatory requirements for SMCLs. For systems in locations that do, they would need to include regulatory and possible public health-related requirements.

Table 3

Terminology for the rating of consequence

ConsequenceDefinitionRating
Not applicable Does not apply in this water system 
Insignificant Notification of operational staff for possible alert and action 
Minor Notification of operational staff for actual alert and action 
Moderate Customer complaints related to event result in follow-up sampling and reporting, adjustments in operations 
Major Customer complaints related to event >5 complaints/day result in increased sampling and operational adjustments as needed 
Severe Public notification and corrective action taken with widespread customer complaints causing media attention and regulatory review 16 
ConsequenceDefinitionRating
Not applicable Does not apply in this water system 
Insignificant Notification of operational staff for possible alert and action 
Minor Notification of operational staff for actual alert and action 
Moderate Customer complaints related to event result in follow-up sampling and reporting, adjustments in operations 
Major Customer complaints related to event >5 complaints/day result in increased sampling and operational adjustments as needed 
Severe Public notification and corrective action taken with widespread customer complaints causing media attention and regulatory review 16 

The risk severity score is the product of the consequence rating multiplied by the likelihood rating. This score is used to prioritize the risks (Alberta Environment and Parks 2013). The risk score matrix is shown in Table 4.

Table 4

Risk matrix with risk severity scores as used in CWF PWS's WSP

 
 

Note. The scores reflect priorities that should be given to the hazardous events and the colors represent the actions that should be taken: Green represents review periodically; Yellow represents introduce actions to manage the risk or monitor for changes; and Red represents act to reduce the risk. The priority placed on a hazardous condition would follow the color code with red representing high priority for attention. This list of priorities and scores should be evaluated annually and updated.

Development of the inventory of hazards, risk scores, and hazardous events

Based on the identification of aesthetic hazards or parameters of concern, the next step was for the CWF PWS to identify the conditions under which the aesthetic hazards would create a potential event, such as customer complaints. Such events can be actual ones that have been experienced or near misses, or ones that could theoretically occur but have not yet been experienced. Table 5 provides an inventory of hazards and hazardous events pertinent to CWF PWS.

Table 5

Inventory of hazards and hazardous events

Process stepPotential hazardHazardous event
Source Geosmin, MIB Algae/cyanobacteria bloom occurs in source water, releasing odorants at levels that cause customer complaints 
Source Chloride Source water drought results in an increase in chloride which is not removed by water treatment 
Source Sodium Source water drought results in an increase in sodium which is not removed by water treatment 
Source Sulfate Source water drought results in an increase in sulfate which is not removed by water treatment 
Source Hardness Source water drought results in an increase in hardness which has limited removal by water treatment 
Source Total dissolved solids Source water drought results in an increase in TDS which is not removed by water treatment 
Treatment Corrosivity Source water drought results in an increase in chloride, sulfate, and TDS which are not removed by water treatment 
Treatment Fluoride Source water drought results in an increase in fluoride which is not removed by water treatment 
Treatment Geosmin, MIB Lysing of cyanobacterial cells and the release of geosmin or MIB within treatment due to the entry of a cyanobacterial bloom into the treatment process 
Treatment Turbidity Filtration failure leading to increased turbidity 
Treatment Ammonia Water treatment chemical overfeed 
Storage Odor Microbiological activity in a storage facility that has gone stagnant or lost water quality control 
Distribution Ammonia Accidental increase in the ammonia residual due to a chemical overfeed 
Distribution Color Disturbance of cast iron mains due to main breaks, valve operations 
Distribution Iron Disturbance of cast iron mains due to main breaks, valve operations 
Distribution Turbidity Disturbance of cast iron mains due to main breaks, valve operations 
Process stepPotential hazardHazardous event
Source Geosmin, MIB Algae/cyanobacteria bloom occurs in source water, releasing odorants at levels that cause customer complaints 
Source Chloride Source water drought results in an increase in chloride which is not removed by water treatment 
Source Sodium Source water drought results in an increase in sodium which is not removed by water treatment 
Source Sulfate Source water drought results in an increase in sulfate which is not removed by water treatment 
Source Hardness Source water drought results in an increase in hardness which has limited removal by water treatment 
Source Total dissolved solids Source water drought results in an increase in TDS which is not removed by water treatment 
Treatment Corrosivity Source water drought results in an increase in chloride, sulfate, and TDS which are not removed by water treatment 
Treatment Fluoride Source water drought results in an increase in fluoride which is not removed by water treatment 
Treatment Geosmin, MIB Lysing of cyanobacterial cells and the release of geosmin or MIB within treatment due to the entry of a cyanobacterial bloom into the treatment process 
Treatment Turbidity Filtration failure leading to increased turbidity 
Treatment Ammonia Water treatment chemical overfeed 
Storage Odor Microbiological activity in a storage facility that has gone stagnant or lost water quality control 
Distribution Ammonia Accidental increase in the ammonia residual due to a chemical overfeed 
Distribution Color Disturbance of cast iron mains due to main breaks, valve operations 
Distribution Iron Disturbance of cast iron mains due to main breaks, valve operations 
Distribution Turbidity Disturbance of cast iron mains due to main breaks, valve operations 

Table 6 expands upon the inventory of hazardous events to provide the ratings for the likelihood and consequence of each event, which are then used to derive the risk scores. These are listed in order from high to low in risk scores. The ratings are based on both expert opinion from tenured staff and consulting scientists and actual historical experience, and a confidence rating is shown for how confident CWF PWS is with the ratings that were given. Confidence levels can be based on professional opinion, historical data within the utility, or data from utilities within the watershed or region. For example, a high level of confidence in the ratings for likelihood and consequence shows that CWF PWS has experienced these hazardous events and has information associated with them. A low level of confidence would suggest that research or evaluations should be done to better determine the ratings in order to estimate a reliable risk score.

Table 6

Development of risk scores

 
 

1Likelihood of occurrence rating: (1) rare, (2) unlikely, (4) possible, (8) likely, and (16) almost certain.

2Level of confidence: high, moderate, and low. States the level of confidence with which the rating can be given. Consider: Confidence level might be based on professional opinion, historical data within the utility, or data from utilities within the watershed or region.

3Consequence of occurrence rating: (1) Insignificant, (2) Minor, (4) Moderate, (8) Major, and (16) Severe.

4Explanation of consequence: Based on SMCL explanations and customer complaints.

5The risk score is the product of the likelihood and consequence ratings.

Table 7 provides possible improvement plan actions to reduce the risk scores for six of the highest hazardous events. Such action could reduce the likelihood that an event would occur, or the consequence when an event does occur, or both. The reduction in one or both ratings would then lower the risk score.

Table 7

Improvement plans to consider for reducing higher risk scores focused on aesthetic quality risk management

 
 

Identification of controls that are in place and their verification

The next step was to list all the controls that are in place within the water utility for managing aesthetic quality (Table 8). Controls can be water treatments, standard operating procedures, flushing of mains, cross-connection control, valve inspection, and water main disinfection practices as laid out in AWWA C651 Standard (AWWA 2023). Table 8 shows examples of contaminant controls, and how each control is monitored, or itself controlled. Examples include dosing a reservoir with copper sulfate (the control) to reduce blooms of alga/cyanobacteria (the hazardous event), which would reduce the production of geosmin or 2-methylisoborneol (MIB) (the hazards). How the effectiveness of the control is monitored is accomplished by performing organism counts before and after dosing copper sulfate. Finally, verification that this control works would be demonstrated by low to non-detectable levels of geosmin or MIB in the water entering the treatment plants.

Table 8

Hazardous event treatment processes and controls

Water system component or processPertinent control of hazardous eventMonitoring of the control
Source water Copper sulfate addition to the reservoir for control of cyanobacteria that produce geosmin and MIB Algae/cyanobacteria counting by flow imaging microscopy to identify concentrations of T&O-producing organisms; monitor T&O compounds by sensory analysis and GC-MS 
Aeration of source water at intake structures to ensure lakes are well-mixed Continuous monitoring using data sondes at the intake for dissolved oxygen and temperature to determine if control is mitigating lake from stratifying 
Selection or switching of source waters for optimum quality Monitoring each lake for T&O-producing organisms and T&O compounds by sensory analysis and/or GC-MS 
Water treatment processes PAC addition as needed for treating geosmin and MIB Monitoring T&O compounds by sensory analysis and/or GC-MS 
KMnO4 addition continuously for treating T&O Monitoring T&O compounds by sensory analysis and/or GC-MS 
pH adjustment to optimize corrosivity indices for slightly scale-forming water quality Monitoring pH at the entry point 
Disinfect full column of filter media and backwash for plants out of service for a period of several months to reduce the potential for biogenic T&O production (Adams et al. 2021Monitoring disinfectant residual 
Optimization of chlorine dioxide generation to ensure limited excess free chlorine is available to reduce the potential for brominated phenol and haloanisole production (Adams et al. 2023aWeekly monitoring of chlorine dioxide generators for yield and purity 
Finished water storage facilities Cycling storage tanks and towers to ensure water age stays low to prevent chloramine degradation and changes in corrosivity Monitoring corrosivity parameters: pH, monochloramine, alkalinity, TDS, temperature, calcium hardness, chloride, sulfate 
Distribution system water mains Adequate flushing after system repair/maintenance work to ensure turbidity, color, and iron are at normal levels Monitoring disinfectant residuals, turbidity, color, and/or iron 
Valves and hydrants Valve management for minimizing unknown dead-ends where water stagnates and odors and sediment and rust collect Distribution crews record when valves are closed for work so that they are reopened when work is completed 
Dead-ends and pressure district boundaries Routine chloramine and free ammonia analysis, as well as monthly flushing to minimize the extent of stagnant water, sediment, odor development, and iron corrosion Monitoring disinfectant residual and free ammonia–nitrogen to trigger action when the water is becoming stagnant 
Water system component or processPertinent control of hazardous eventMonitoring of the control
Source water Copper sulfate addition to the reservoir for control of cyanobacteria that produce geosmin and MIB Algae/cyanobacteria counting by flow imaging microscopy to identify concentrations of T&O-producing organisms; monitor T&O compounds by sensory analysis and GC-MS 
Aeration of source water at intake structures to ensure lakes are well-mixed Continuous monitoring using data sondes at the intake for dissolved oxygen and temperature to determine if control is mitigating lake from stratifying 
Selection or switching of source waters for optimum quality Monitoring each lake for T&O-producing organisms and T&O compounds by sensory analysis and/or GC-MS 
Water treatment processes PAC addition as needed for treating geosmin and MIB Monitoring T&O compounds by sensory analysis and/or GC-MS 
KMnO4 addition continuously for treating T&O Monitoring T&O compounds by sensory analysis and/or GC-MS 
pH adjustment to optimize corrosivity indices for slightly scale-forming water quality Monitoring pH at the entry point 
Disinfect full column of filter media and backwash for plants out of service for a period of several months to reduce the potential for biogenic T&O production (Adams et al. 2021Monitoring disinfectant residual 
Optimization of chlorine dioxide generation to ensure limited excess free chlorine is available to reduce the potential for brominated phenol and haloanisole production (Adams et al. 2023aWeekly monitoring of chlorine dioxide generators for yield and purity 
Finished water storage facilities Cycling storage tanks and towers to ensure water age stays low to prevent chloramine degradation and changes in corrosivity Monitoring corrosivity parameters: pH, monochloramine, alkalinity, TDS, temperature, calcium hardness, chloride, sulfate 
Distribution system water mains Adequate flushing after system repair/maintenance work to ensure turbidity, color, and iron are at normal levels Monitoring disinfectant residuals, turbidity, color, and/or iron 
Valves and hydrants Valve management for minimizing unknown dead-ends where water stagnates and odors and sediment and rust collect Distribution crews record when valves are closed for work so that they are reopened when work is completed 
Dead-ends and pressure district boundaries Routine chloramine and free ammonia analysis, as well as monthly flushing to minimize the extent of stagnant water, sediment, odor development, and iron corrosion Monitoring disinfectant residual and free ammonia–nitrogen to trigger action when the water is becoming stagnant 

PAC, powdered activated carbon; GC-MS, gas chromatography-mass spectrometry.

Verification monitoring can be seen in Table 9, which shows how the WSP keeps the hazard below action levels. For example, algal/cyanobacteria-related T&O verification monitoring would include quantification of T&O compounds (geosmin/MIB/haloanisoles) to ensure they are kept below action levels. If action levels are exceeded, controls and their monitoring should be re-evaluated to ensure the best methods are being utilized.

Table 9

Verification monitoring for hazardous event controls

Potential hazardMonitoringFrequencyAction levels triggering further investigationa
Known T&O (geosmin, MIB, and haloanisoles) Specific T&O compounds by GC-MS Seasonal (3 × /week in summer, 2 × /week in spring and fall, 1 × /week in winter) at lake intakes Geosmin or MIB > 10 ng/L
Haloanisoles > 2 ng/L 
Chloride, sodium, sulfate, fluoride Analysis by IC Daily at entry points Chloride/sodium/sulfate > 200 mg/L for individual ions
Fluoride > 1 mg/L 
TDS Filtration followed by gravimetric analysis 3 × /week at entry points TDS > 350 mg/L 
Corrosivity Analysis by Langelier Saturation Index (LSI), Ryznar Index, Precipitation Potential Daily at entry points, weekly at RTCR/NAP sites LSI < 0.0 
Odor T&O sensory analysis Seasonal (3 × /week in summer, 2 × /week in spring and fall, 1 × /week in winter) at lakes and entry points Any detectable odor category
TON ≥ 2 
Turbidity and color Analysis by spectrophotometry Daily at entry points and as needed for customer complaints Turbidity > 0.150 NTU
Color > 5 CU 
pH Analysis by pH electrode Hourly at entry points, every 2 h at process control points in the treatment plant pH 8.8–9.2 
Ammonia Analysis by ISE Daily at entry points, weekly at RTCR/NAP sites Ammonia–nitrogen > 0.2 mg/L 
Iron Analysis by ICP-MS or colorimetry Daily at entry points and, as needed for customer complaints Total iron > 0.2 mg/L 
Potential hazardMonitoringFrequencyAction levels triggering further investigationa
Known T&O (geosmin, MIB, and haloanisoles) Specific T&O compounds by GC-MS Seasonal (3 × /week in summer, 2 × /week in spring and fall, 1 × /week in winter) at lake intakes Geosmin or MIB > 10 ng/L
Haloanisoles > 2 ng/L 
Chloride, sodium, sulfate, fluoride Analysis by IC Daily at entry points Chloride/sodium/sulfate > 200 mg/L for individual ions
Fluoride > 1 mg/L 
TDS Filtration followed by gravimetric analysis 3 × /week at entry points TDS > 350 mg/L 
Corrosivity Analysis by Langelier Saturation Index (LSI), Ryznar Index, Precipitation Potential Daily at entry points, weekly at RTCR/NAP sites LSI < 0.0 
Odor T&O sensory analysis Seasonal (3 × /week in summer, 2 × /week in spring and fall, 1 × /week in winter) at lakes and entry points Any detectable odor category
TON ≥ 2 
Turbidity and color Analysis by spectrophotometry Daily at entry points and as needed for customer complaints Turbidity > 0.150 NTU
Color > 5 CU 
pH Analysis by pH electrode Hourly at entry points, every 2 h at process control points in the treatment plant pH 8.8–9.2 
Ammonia Analysis by ISE Daily at entry points, weekly at RTCR/NAP sites Ammonia–nitrogen > 0.2 mg/L 
Iron Analysis by ICP-MS or colorimetry Daily at entry points and, as needed for customer complaints Total iron > 0.2 mg/L 

GC-MS, gas chromatography-mass spectrometry; IC, ion chromatography; ISE, ion-selective electrode method; ICP-MS, inductively coupled plasma-mass spectrometry; RTCR, revised total coliform rule; NAP, nitrification action plan.

aCustomer complaints serve as verification that aesthetic issues are under control and when they exceed 3/day, then this triggers investigation into the cause.

Although this article addresses maintaining aesthetic water quality within the utility, when fully implemented, WSPs on aesthetic quality should include safeguarding aesthetic quality all the way to the ultimate customer. Meeting this goal will be challenging because many aesthetic water quality issues arise in premise plumbing systems that are outside the control of water utilities. As such, safeguarding aesthetic water quality all the way to the customer and ultimate user involves cooperation between the water supplier and the building owners/operator since all have a stake in providing high-quality water to the consumer. This is an emerging area that requires the cooperation of organizations and professionals who often operate independently. The International Association of Plumbing and Mechanical Officials is working in conjunction with utilities and the drinking water industry to produce guidance on reopening building water systems after extended stagnation (Rhoads et al. 2020) and guidance on water management during construction with an appendix on water quality for plumbers and plumbing engineers (IAPMO 2024). Collaborations such as these are the key to meaningfully addressing water quality aspects for safe and aesthetically pleasing water quality at the customer's tap and to comprehensively implementing water safety planning for aesthetics.

The CWF PWS has completed the key documentation for water safety planning covering aesthetic water quality and US EPA SMCLs, namely known T&O compounds, taste-related metals and ions, turbidity, total dissolved solids (TDS), color, pH, and ammonia. The resultant integrates the various source water, water treatment, and distribution system preventive and mitigative controls, providing context and perspective on why the controls are necessary. Water quality staff also have clear explanations as to why analyses and reporting are done and why the triggers for action are in place. As water quality events that affect aesthetic parameters occur, whether successfully managed or not, the WSP will be reviewed for updates. As improvement plans are acted on, the WSP will be a living document that is reviewed and updated regularly.

While not a regulatory requirement in the US, proactive utilities use water safety planning to strengthen monitoring programs already in place and build rapport with customers by ensuring the production and delivery of safe and aesthetically pleasing water. A WSP integrates information and the management of controls from across a water utility, providing knowledge transfer and information exchange, which helps to build cooperation and unity within the water utility. For WSPs to be effective tools, PWSs must continue to develop and revise them as infrastructures and treatment changes are made to maintain them. Response to customer complaints and ongoing research with the PWS must also be included as the WSP is revised over time.

H. A.: Conceptualization, methodology design, project administration, writing – review and editing; G. A. B.: Conceptualization, methodology design, writing – review and editing; and M. S., A. M. D., T. B., and K. I.: Writing – review and editing.

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

The authors declare there is no conflict.

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