Open Access Article
N.
Moore
,
D.
Pousty
,
D.
Ma
,
R.
Hofmann
,
A.
Pras
,
R. E.
Higbee
,
H.
Mamane†
* and
S. E.
Beck†
*
International Ultraviolet Association, Chevy Chase, Maryland 20815, USA. E-mail: nathan.moore@ouce.ox.ac.uk; dana.poustylakritz@colorado.edu; madt@cdmsmith.com; ron.hofmann@utoronto.ca; asafpras@mail.tau.ac.il; rehigbee@purdue.edu; hadasmg@tauex.tau.ac.il; sara.beck@ubc.ca
First published on 7th October 2025
Water disinfection using ultraviolet (UV) light is an emerging tool for improving access to safely managed drinking water in rural areas and low-resource regions. However, there is little information comparing existing UV systems in those contexts, towards improving the effectiveness of future UV systems. This work presents 19 case studies of small, decentralized UV water disinfection systems being used during the last 30 years to improve water access. The case studies cover a wide range of project types, including schools, hospitals, communities, households and healthcare facilities, spanning four continents. A variety of energy sources, water sources and social environments are also reviewed. In general, the use of UV immediately improved the microbiological quality of the water; however, long-term tracking of system performance is largely missing. UV system effectiveness was limited by several factors, including the potential for recontamination after UV disinfection, insufficient maintenance, and the absence of regulatory frameworks that allow the more widespread adoption of UV disinfection compared to more conventional disinfectants. This paper is intended to be supporting evidence for the utility of UV technologies for improving safe water access in low-resource settings, and to support practitioners in improving UV system design and implementation.
Water impactUltraviolet (UV) light is a promising technology for water and wastewater disinfection in rural and low-resource contexts; however, there is little published information to guide the design of UV installations in those settings. We present 19 decentralized UV disinfection case studies, covering 30 years of implementations across a variety of scales, water sources and geographies, and review the disinfection efficacy, implementation challenges, and future considerations. |
000 annual deaths, including 297
000 deaths of children under five years, from diarrhea that results from unsafe drinking water, sanitation and hand hygiene.6,7 While there has been an increase in access to safely managed sanitation and handwashing facilities with soap and water from 2015 to 2020, progress will need to quadruple to achieve SDG 6 by 2030.7
One of the biggest problems directly leading to waterborne diseases caused by bacteria, viruses, and protozoa is the lack of water treatment and, specifically, disinfection. Conventional water treatment approaches emphasize centralized systems, rely on intensive capital, and do not address social barriers to water access. Common decentralized water treatment methods implemented at the household or community level include boiling, coagulation and settling, filtration (including biosand filters, ceramic pots, membranes and activated carbon) and disinfection with chemicals such as chlorine.8,9 Some communities may rely on truck delivery of treated water; however, the transportation tanks often are not adequately cleaned, and deliveries may be unreliable.10,11 Some areas also face the challenge of satisfying cultural and taste requirements. While the commonly-accepted dose of free residual chlorine is 2.0 mg L−1, taste studies indicate that tolerated chlorine thresholds are lower than this value.12,13 Additionally, household water storage practices in low- to middle-income countries often result in the recontamination of drinking water after it has been collected,14–16 reinforcing the case for treatment systems at the point of use. Point-of-use systems for both treatment and storage of water are designed to protect some of the world's most vulnerable populations from preventable waterborne diseases.17 As the world continues to work toward achieving UN SDG 6 to provide safe water access and sanitation for all, reliable and innovative disinfection has become increasingly important.
After commonly being used for disinfection in centralized systems in high-income contexts, ultraviolet (UV) lamps and UV light emitting diodes (LEDs) have recently emerged as promising alternatives for water and wastewater disinfection in decentralized systems in rural areas and low- to middle-income countries as well. UV disinfection functions as a broad-spectrum antimicrobial agent, effectively inactivating protozoan, bacterial and viral pathogens, without chemical addition or taste and odor challenges, with no harmful effects from overdosing and with little to no disinfection byproduct formation.18–25 Traditional low-pressure (LP) UV lamps are low-cost, long lasting, and energy-efficient but also are fragile, contain trace levels of mercury, and must typically be left on continuously, whereas UV LEDs can be more expensive, but have a much smaller architecture and have the ability to be instantly turned on and off according to flow, thereby theoretically increasing service life. In recent years, the science of using UV sources for low-cost and remote disinfection applications has steadily advanced. Today, UV technologies are being considered, if not used, in many such contexts around the world.26–33
Despite the promise of UV disinfection to help to provide water security to decentralized low-income communities, there are no standard engineering practices nor official protocols to guide the installations. There are also very few published reports on such UV installations in either the peer-reviewed or the grey literature. As such, new installations are currently being designed on an ad hoc basis, without addressing the shortcomings or reflecting the strengths of previous installations. The objective of this work is to begin to address this important information gap so that each new generation of UV installations can build on the lessons learned from their predecessors. Nineteen case studies spanning over 30 years are presented, which cover a wide range of projects at multiple scales, including schools, hospitals, communities, households, and healthcare facilities. Moreover, the studies demonstrate the utilization of a variety of UV-based systems with different specifications of flow rates and energy sources, addressing different water sources and social environments, including manually-collected and streamed water from wells, groundwater, rainwater, ponds, rivers, storage tanks and more. The case studies were contributed by researchers, equipment manufacturers, government agencies, and non-governmental organizations, and the contributors were often part of the implementation or management process. Each case study describes the project's background and objectives, the UV technology specifications and, most importantly, the outcomes and lessons learned. In the Conclusion section of this work, cross-cutting considerations for the sustainability of UV systems are summarized across all of the case studies. The Conclusion section also contains an analysis of key aspects of UV water systems, such as water quality impacts and maintenance considerations; as well as future research needs, recommendations for implementation, and implementation challenges that must be overcome. A map (Fig. 1) and database of decentralized UV disinfection systems around the world, containing details about the case studies described in this work, is also available at https://www.iuva.org/UN-Sustainable-Development-Goals-Task-Force.34 It is hoped that this work will serve as a resource for engineers, practitioners, researchers and decision makers who may be working with UV disinfection. Furthermore, it is hoped that it will inspire others to report their own experiences with this emerging technology.
| Section | Country | Scale | Water source and pretreatment | UV system specifications and performance | Power source and consumption | System controls | Period of operation | UV implementation challenges | Select solutions to implementation challenges |
|---|---|---|---|---|---|---|---|---|---|
| LP = low-pressure. LI = log inactivation. | |||||||||
| 1 | Canada | 38 LPM | Source: surface water (creek), concentration of total coliform in raw water was between 100–3000 CFU per 100 mL | LP UV, VIQUA UV-MAx Pro10, 40 mJ cm−2 at 38 LPM, maximum ∼3.5 log-inactivation observed for total coliform |
Grid power, 120 W, battery provides 1 hour backup power for continuous use | Emergency solenoid shut-off valve in normally closed position, closes when UV dose <40 mJ cm−2, when system loses power, unplugged, or UV lamp not on. Sensor included for monitoring UV intensity | November 2016 – present | Turbidity spikes during spring snowmelt | Robust pre-filtration |
| System 1: two residences | |||||||||
| Alarms and back-up electricity source | |||||||||
| Building community trust | |||||||||
| System 2: three residences | |||||||||
| Trained community operators leading operations and maintenance (O&M) | |||||||||
| Regular community outreach and monitoring | |||||||||
| Pretreatment: multi-media filter, two 1 μm cartridge filters | |||||||||
| 2 | Dominican Republic | 24 LPM | Source: well and harvested rainwater, concentration of E. coli in raw rainwater >100 MPN per 100 mL | LP UV, Viqua S5Q-PA, ∼30 mJ cm−2 at 24 LPM, maximum ∼2 LI observed for E. coli | Solar panels, 30 W consumption by UV system | None specified | 2012 – present | Intermittent usage schedule | A full-time trained operator and advocate |
| Four primary schools | Staff turnover, training, and community awareness | A sustainable business model whereby the systems are implemented and maintained | |||||||
| Pretreatment: sand filtration, 1 μm cartridge filter | Irregular maintenance and testing | A clear process for the systems to acquire regulatory approval or certification from a locally trusted source | |||||||
| No sustainable business model | |||||||||
| 3 | India | 1.5 LPM | Source: Krishna River taps (well or river) | 280 nm UV LED (Pearl Aqua Micro 6B), design dose was 30 mJ cm−2 | Grid power, 9 W consumption by UV LED | None specified | August 2022 | Poor supply chain for parts replacement | Designed a tool to promote safe water handling and train analysis by local water ambassadors |
| Four households | |||||||||
| Intermittent electricity | |||||||||
| RO systems, E. coli and total coliform were detected in source water (presence/absence results only) | |||||||||
| Diversified electricity sources | |||||||||
| Distance from water point means possible recontamination with storage | |||||||||
| Pretreatment: none | |||||||||
| Lack of community awareness and skilled technicians | |||||||||
| 4 | India | 1 L batch reactor | Source: Oorani – dug out rainwater pond, concentration of E. coli in source water 133 ± 8 CFU mL−1 | Custom built 275 nm UV LED reactor, ∼2.1 LI of E. coli observed in field corresponding to UV dose of <5 mJ cm−2, no E. coli detected in UV effluent | Mechanical energy, 6VDC battery | None specified | 2018–2020 | Funding and local people to be trained for O&M | Improved awareness of the technology |
| Used pretreatment filters for ooranies with high turbidity | |||||||||
| One village of 1050 people | |||||||||
| Costs for scale-up of UV LED technology is high | |||||||||
| Pretreatment: sand filtration | |||||||||
| 5 | India | 15 LPM | Source: surface water and groundwater | Custom built LP UV, 120 mJ cm−2, maximum 6-LI of E. coli observed in laboratory testing dechlorinated tap water | Grid power, 60 W consumption for UV system | None specified | 1994–1995 | Device flow rate was higher than necessary | Reduced size of device to deliver lower flow rates at a lower cost |
| 500 to 1500 people | High cost to develop and transport | Placed UV lamp above water to reduce fouling | |||||||
| Pretreatment: slow-sand filtration | Lack of sufficient water pressure for UV reactor | Filtration process replaced with slow-sand filter to increase pressure | |||||||
| Rapid chemical and biological fouling | |||||||||
| Lack of trained personnel for O&M | |||||||||
| 6 | Lao PDR | 50 LPM | Source: treated wastewater | LP UV, 4 Sanitron S50C units in parallel, system designed to achieve at least 30 mJ cm−2 at 50 LPM (manufacturer specified 30 mJ cm−2 at 75 LPM) | Grid power, 65 W consumption per unit, 260 W total consumption | Guardian digital UV light monitor, detects decrease in UV intensity (e.g., quartz fouling, poor water quality, lamp aging) | 2011 – present | Influent water had high turbidity | Improved pretreatment and maintenance of wetlands |
| 70 households, maximum of 700 users | Pretreatment: settler, anaerobic baffled reactor, anaerobic filter, planted gravel filter, aerobic polishing pond | Flow rate exceeded manufacturer recommendations | Additional lamps required to increase disinfection capacity | ||||||
| Excessive fouling and scaling of quartz sleeves | Regular sleeve cleaning protocols and O&M | ||||||||
| Irregular O&M | |||||||||
| 7 | Kenya | 2.8 LPM | Source: rainwater | 265 nm UV LED, Klaran WS Series Retrofit Kit, manufacturer specified 4-LI of Pseudomonas aeruginosa at 2 LPM | Solar or grid power, 10 W consumption by UV LED | None specified | September 2022–July 2023 | Intermittent grid electricity | Household preferred UV compared to chlorine (taste) |
| One household | |||||||||
| High cost | Solar panel for consistent electricity | ||||||||
| Dirt and bird droppings | |||||||||
| Pretreatment: biosand and biochar | |||||||||
| 8 | Kenya | 7.5 LPM | Source: springwater and rainwater | LP UV, VIQUA VT1, manufacturer specified 16 mJ cm−2 at 7 LPM, expected dose is <16 mJ cm−2 at 7.5 LPM | 30 W solar panel, 30 Ah car battery, 12VDC, 9 W consumption by UV lamp | Security boxes requested by schools prevent tampering, window allowed operator to check whether system was on or off | 2017–2020 | Energy surges leading to lamp burnout | Consider the power quality supplying UV |
| Four primary schools (400 people) | |||||||||
| Unavailability of local UV systems or parts | Use local UV equipment supplier | ||||||||
| Pretreatment: slow-sand filtration | |||||||||
| Lacking skilled operators for water testing, operation, and maintenance | |||||||||
| 9 | Mexico | 5 LPM | Source: spring, well, and rainwater | Custom built LP UV, designed to deliver 120 mJ cm−2 at 5 LPM | Grid or solar | None specified | First period: 2006–2014, second period: 2018–2022 | Behavior change – drinking untreated water | Human-centered perspective service delivery approach |
| System1: 400 households | Pretreatment: system 1: none | Need to subsidize systems with government programs | Treatment of water directly into home reduced contamination | ||||||
| System 2: 187 households | System 2: 2 filters (5 μm and 1 μm) and activated carbon | UV does not impact water taste | |||||||
| 10 | Nicaragua | 5.2 LPM | Source: groundwater, E. coli up to 48 MPN per 100 mL detected | LP UV, VIQUA VT4, designed to deliver 40 mJ cm−2 at 5.2 LPM | Diesel generator, 20 W consumption by UV system | None specified | 2018–2022; not constructed | Unavailability of local UV systems or parts | Emphasize community buy-in and communication |
| Two communities | |||||||||
| Political tensions | |||||||||
| Maintain relationships with local communities and NGOs | |||||||||
| Lack of community buy-in | |||||||||
| Pretreatment: prefiltration (100, 10 μm, and 5 μm), reverse osmosis | |||||||||
| Intermittent electricity, 8 hours per day | |||||||||
| 11 | Philippines | 2 LPM | Source: groundwater, E. coli up to 5000 MPN per 100 mL detected | 280 nm UV LED, no dose specified | 150 W solar panel, 12 V, 350 mA | None specified | September 2018 – present | Potential photoreactivation of microorganisms | Solar power as a suitable, alternative power source |
| One community | |||||||||
| Increase contact time, number of LEDs | |||||||||
| Seasonal variation of water quality | |||||||||
| Pretreatment: none | |||||||||
| Insufficient microbial inactivation | Reduce exposure to sun for photoreactivation | ||||||||
| Disinfection of storage tank | |||||||||
| 12 | Rwanda | 5 LPM | Source: rainwater | LP UV, 40 mJ cm−2 at 5 LPM | 80 W solar panel or 12 V car battery | None specified | 2010 – present | Sustainable financing of units and maintenance | Schools prefer UV due to lower costs and less maintenance |
| 23 schools and small hospitals | |||||||||
| Pretreatment: two washable bag filters of 25 μm and 10 μm | |||||||||
| Local attendance for installation, maintenance, service, and education | |||||||||
| 13 | Rwanda | 10 LPM | Source: piped water, rainwater, and surface water, up to 63 CFU mL−1 detected in field | LP UV, up to 1.8-LI achieved (no microorganism specified), no dose specified | 50 W or 102 W solar panel | Sensor and alarm system notify operators of faulty lamp | 2005–2015; maintained and operated for at least 10 years by Engineers without Borders – USA | Community adoption of UV | Coupling system with other technologies – drip irrigation, lighting, biogas generators |
| Two communities | Unavailability of local UV systems or parts | ||||||||
| Pretreatment: gravel filter with self-filling tank for filter back wash, and pressurized sand filter | Training of local personnel to operate system | Strong relationships with community leaders enabled recruitment and training | |||||||
| Liaising with importers for UV lamps | |||||||||
| Free-of-charge system was a component in adoption | |||||||||
| 14 | Rwanda | Up to 100 LPM | Source: piped water, rainwater, and surface water | LP UV, 2 Sterilight UV systems, dose not specified | Solar panels | System includes RealTech UV-transmittance sensor, flowmeter, and control valve. UV lamp operation controlled by flow monitoring system | 2007–2010 | Installation required extensive engineering and project management | Consider ultrafiltration pretreatment |
| One community | |||||||||
| Future potential for sustainable financing through carbon finance as market develops | |||||||||
| Funding through weak carbon credit markets not a sustainable business model to provide sufficient revenue for O&M | |||||||||
| Pretreatment: elevated backwash tank, gravel filter and pressurized sand filter | |||||||||
| 15 | South Africa | 15 LPM | Source: surface water and groundwater | LP UV, maximum 6-LI of E. coli observed in laboratory testing dechlorinated tap water | Grid power, 60 W | Photosensor for monitoring the UV lamp and sensor for UVT controlled flow | 1997 | User O&M | Simplify systems to reduce maintenance requirements |
| Two communities | Public sector mobilization and financing | ||||||||
| Pretreatment: none | |||||||||
| Flow control valve opening when UV system is supplied with power to reduce human error | |||||||||
| Two photo sensors control valve to open when UV is on and UV transmittance is high | |||||||||
| 16 | Tanzania | 5 LPM | Source: rainwater | LP UV (unspecified system) | 125 W solar panel (12 V) charging 12 V battery, 25 W consumed | None specified | 2019 – present | Lamp burnout and damaged electrical wires and components | Improve operation, maintenance and inspection protocols |
| Seven systems at six healthcare facilities | |||||||||
| Pretreatment: first flush, sedimentation | |||||||||
| Training of community operators | |||||||||
| Poor user-focused design: difficult to inspect and clean system and UV lamps | |||||||||
| UV reactor and hardware must be enclosed from environmental factors | |||||||||
| Poor cleaning of rainwater harvesting system and quartz sleeve led to significant fouling | |||||||||
| 17 | Uganda | 3.5 LPM | Source: rainwater and groundwater, E. coli too numerous to count, reduced to 104 CFU per 100 mL by filter | 280 nm UV LED, PearlAqua Automate System, UV dose not specified | Solar or grid, 20 W consumption for UV LED system | Flow meter for detecting flow, alert system for faulty UV LEDs | 2021 – present | Protecting the UV system from damage | UV must be enclosed for protection |
| One healthcare center and one primary school | Inconsistent power supply and potential power surges | Integrate UV LED units into micro-factories to treat great volumes of water | |||||||
| Pretreatment: biofiltration cartridge filters | User safety | ||||||||
| 18 | United States & Ukraine | 38 LPM | Source: piped water or surface water | 280 nm UV LED (Pearl Aqua Deca), estimated 30–40 mJ cm−2 at 45 LPM at up to 38 LPM | Generator or grid, 180 W consumption for UV LED system | None specified | 2021 – present | Awareness, knowledge, acceptance at government level | Better integration into existing emergency protocols of government |
| Deployed in several locations | |||||||||
| Pretreatment: activated carbon filtration | |||||||||
| 19 | United States | 0.5 LPM 300 people | Source: surface water, total coliform concentration up to 325 CFU mL−1 and E. coli concentration up to 7 CFU mL−1 | UV LED (Pearl Aqua Model 25G), challenge testing with MS2 achieved RED >40 mJ cm−2 at 0.5 LPM | Grid, 26 W nominal power consumption | Indicator lights included for status of UV LEDs. Internal current loop – measures lamp life | January 2017–February 2018, Pilot Study | Temporal changes in UV transmittance and flowrate | UV LEDs useful with low mineral water to minimize fouling, reduce chlorine use, and minimize formation of disinfection byproducts |
| Pretreatment: slow-sand filtration, total coliform up to 10 CFU mL−1 and E. coli up to 2 CFU mL−1 in filter effluent | |||||||||
Given the limited published literature on this topic, a broad approach was taken to identify relevant projects. The case studies were sourced through the International Ultraviolet Association (IUVA). A “call to action” was disseminated to IUVA members, specifically targeting researchers, equipment manufacturers, government agencies, and non-governmental organizations with direct experience in implementing or managing decentralized UV disinfection projects. This targeted approach leveraged the expertise within the IUVA community to identify a diverse set of relevant case studies. The IUVA network proved instrumental in identifying relevant case studies and connecting with key practitioners. The selection aimed to include a variety of UV system configurations, including both UV mercury vapor lamps and UV LEDs, and systems utilizing different power sources (e.g., grid electricity, and solar power). Additionally, projects addressing different water sources (groundwater, surface water, rainwater, stored water, and wastewater) were prioritized. Case studies contributors included researchers, equipment manufacturers, and non-governmental organizations that were part of the implementation or management process. Case studies were included if they met the following criteria:
1. Technology: the project included the use of a UV water disinfection system, such as mercury-based UV lamps or LEDs.
2. Setting: the work was implemented in a rural area or a low-resource community.
3. Scale: the water treatment system was designed for a decentralized application serving specific populations (e.g., households, schools, communities, hospitals, and healthcare facilities).
4. Documentation: sufficient information was available to extract relevant data regarding system design, system performance, water quality and health outcomes, and system operation.
A standardized approach was then used to extract relevant information from each case study. Key data points included:
1. Project context: location (country, region), community characteristics, and specific needs addressed.
2. Water source: type of water source (groundwater, surface water, rainwater, etc.) and its initial quality.
3. UV system specifications: type of UV source (lamp or LED), flow rate, power source, and system design.
4. Operational parameters: operating procedures, maintenance requirements, and challenges encountered.
5. Performance data: pre- and post-disinfection water quality data (e.g., indicator organism concentrations, turbidity), where available.
6. Lessons learned: key insights, challenges, and recommendations from the project implementers.
This review is subject to certain limitations. The case studies represent a non-random sample of projects, and the availability of data varied across cases. Due to the nature of field implementations and the nascence of decentralized UV disinfection, rigorous control groups and comprehensive monitoring data were often lacking. The reliance on self-reported data and project reports may introduce biases. Despite these limitations, this review provides a valuable synthesis of practical experiences with decentralized UV disinfection systems, offering insights for improving future implementations and advancing progress toward SDG 6.
161 acres of land, and split by the Fraser River. Though rich in natural resources, the Nation is challenged by the relative remoteness of their individual communities. A decade-long struggle with water advisories led to a community-backed initiative to seek alternative solutions. RESEAU Centre for Mobilizing Innovation (RESEAU CMI) was engaged to provide an innovative solution for two reserves located far from the larger communities within Lytton, which did not qualify for funding of a centralized water system from Indigenous Services Canada (ISC).
IR3 (Spintlum) and IR11 (Yawaucht) consisting of two and three residences, respectively, are supplied by surface creek water, and were on long-standing boil water advisories. Following a course of feasibility work, design, community engagement and site visits, the point-of-entry (POE) pilot project was introduced. Using water quality data collected by the RESEAU team, the project partners designed POE systems to properly treat each community's water source. In this case, both IR3 and IR11 faced significant levels of DOC, turbidity, total coliform, and E. coli counts. All POE systems were designed to each treat water for a single residence. The general characteristics were determined following a thorough sampling program. The results for turbidity, total coliform and E. coli are shown in Table 2 as compared to Health Canada's Guidelines for Canadian Drinking Water Quality.35 Turbidity was measured using a Hach colorimeter at the University of British Columbia.36 Total coliform and E. coli were measured by the First Nation Health Authority with the IDEXX MPN method, following the 9223 enzyme substrate coliform test in the Standard Methods for the Analysis of Water and Wastewater.36
| Parameter | Unit | Guideline valuea | IR11 | IR3 |
|---|---|---|---|---|
| a From the Guidelines for Canadian Drinking Water Quality (February 2017).35 b Treatment limits for individual filters or units: less than or equal to 0.3 NTU in at least 95% of measurements either per filter cycle or per month; never to exceed 1.0 NTU. | ||||
| Turbidity | NTU | ≤0.3b | 3.68 | 0.32 |
| Total coliform | CFU per 100 mL | 0 per 100 mL | 271 | 741 |
| E. coli | CFU per 100 mL | 0 per 100 mL | <1 to 20 | <1 to 5 |
Over the course of preliminary meetings and site visits, the project was successfully introduced. The engagement sessions provided an opportunity for knowledge sharing, but most importantly gave community members a chance to give input and have their questions addressed. One of the key requirements to a successful POE system is an established trust by resident users, and First Nations Health Authority (FNHA) was engaged in the site visits to help mitigate concerns.
On the technical side of the project, the design requirements for POE treatment in IR 3 and IR 11 were established with adherence to Health Canada's Guidelines for Canadian Drinking Water Quality (GCDWQ), ISC Decentralized Protocol, and Occupational Health and Safety Requirements.35 A process flow diagram of the treatment system is in Fig. 2. The entire treatment system, at each location, was contained within a locked enclosure accessible only by the operator. In general, incoming raw water was subject to turbidity reduction media, 1-micron nominal cartridge filtration, 1 micron absolute cartridge filtration, followed by UV disinfection.
![]() | ||
| Fig. 3 The Lytton POE systems, with the low-pressure UV system, were installed in a secured enclosure, placed inside residents' homes. | ||
An emergency solenoid shut-off valve was located downstream of the UV lamp and was normally closed when the water was not in use, preventing water from reaching the consumer. It also closed if the UV dose was less than 40 mJ cm−2 and if the system lost power, was unplugged or if the UV lamp failed to turn on. In response to a power failure, the solenoid valve would close, as it would no longer be powered open. The UV unit had a sensor to detect lamp intensity. If a safe UV dose was not achieved during the warmup cycle (if the intensity went below a set value calculated for the required dose), an alarm occurred, and the solenoid remained closed. A backup battery was available for temporary power (approximately providing up to one hour power for continuous operation) in the case of a power failure.
Following the established protocol for regular and successive water testing, the first five weeks of piloting included a frequent sampling schedule. This was necessary to thoroughly assess the system performance and provide careful oversight. The regulations set by FNHA required three consecutive weeks of clean results (i.e., non-detectable microbial counts) in order to lift the boil water advisories. This target was achieved between mid-December and mid-January 2016, based on a staggered sampling schedule and testing that included weekly bacteriological results. As of January 2017, both Reserve communities and all five participant residences, were off the boil water advisory.
As the project progressed through the first year of installation, the water quality sampling frequency moved to a bi-weekly schedule (Fig. 4). Despite spikes in total coliform counts, which coincided with spikes in turbidity, the bacteria were completely inactivated by the UV light. A number of formal and informal engagement sessions were coordinated, both in the community and via conference calls with the purpose being to facilitate regular communication between the project partners, gather community feedback, and develop strategies to any arising issues. Ongoing follow-up work to assess the operator and resident satisfaction, as well as monitoring system performance and O&M costs, continued throughout the pilot year.
Over eight years later, the system is still in operation. No issues have been reported. Periodic maintenance includes UV lamp replacement and quartz sleeve cleaning approximately every six months.
Since its launch in 2012, the Water Supply course has implemented drinking water treatment systems in four primary schools within the La Vega region of the Dominican Republic. These schools are all located within 10 minutes of one another and often collaborate or work together. Although the COVID-19 pandemic delayed project goals, there are plans to implement a fifth system in the community of Desecho. While this small town lies on a beautiful mountainside, its increased elevation has made it difficult for the town to acquire basic resources, particularly during the rainy season. It is the community in greatest need of potable water and may be provided with both a well and a treatment system for harvested rainwater to satisfy the town's daily water requirements.
Primary and secondary disinfection provided a multi-barrier treatment system for the communities. A UV disinfection system inactivates microbial pathogens, including bacteria, viruses and protozoa, and serves as the primary disinfectant. The VIQUA S5Q-PA unit was selected as an off-the-shelf point-of-use system that would meet the target flow of 24 LPM for delivering at least 40 mJ cm−2. The UV system includes a sensor on the reactor to indicate operation as well as a Sterilight Silver series ballast with a large LCD display that indicates the remaining life of the UV lamp. Zimba (the blue unit on the right of Fig. 5), an autonomous, gravity-based batch chlorinator, dilutes bleach (i.e., sodium hypochlorite) to the desired concentration (unspecified), which provides secondary disinfection during transportation and storage. The Zimba could chlorinate roughly 10 L per batch.
The systems deliver an average of 24 LPM and are powered by solar panels, which were installed by local trade specialists hired by the team. The solar panel system included a DC–AC converter and battery system. Once installed, the school's designated operator was provided in-person training by Purdue engineering students, a manual written by native Spanish speakers and videos addressing maintenance and troubleshooting. Custom manuals were written for each system and included simple explanations of each component's purpose, manufacturer, price, O&M. Schools were provided with compartment bag tests for E. coli, test strips for free and total chlorine, a UV transmittance (UVT) meter and a probe that measures pH and total dissolved solids (TDS), as well as a turbidimeter that is shared among the four schools. The water treatment system is still used intermittently and the solar panels are used consistently by the school.
| Parameter | Raw rainwater | Treated water |
|---|---|---|
| Turbidity | 8.10 | 1.18 |
| Total dissolved solids (TDS) | 86.8 ppm | 63.2 ppm |
| UV transmittance (UVT) | 82% | 92% |
| E. Coli Most probable number (MPN) | >100/100 mL | 0/100 mL |
Community taps are scattered throughout the village within the living area, with a group of four households living around a tap in the village. The water is not streamed regularly; instead, it is streamed without notice between 4:00 a.m. and 7:00 am (Fig. 7). The water quality is poor and the source of the water is the river or wells. Table 4 details the water quality with high total dissolved solids, TDS, and part of the sources with high turbidity. The water quality at the current taps is also poor. Structurally, the taps are shaky, fragile and unstable; thus, the community must exercise care to avoid damaging them. The water pressure when the tap is open ranges from 0.3 to 0.8 bar, and when the taps are closed the pressure ranges from 1.0 to 1.5 bar. The inner tap diameter is between 1.6 cm and 2.2 cm, and the outer tap diameter is between 1.8 cm and 2.6 cm. For hand pumps, the inner diameter is 4.6 cm and the outer diameter is 5.0 cm (Table 4).
| Source type | Inner diameter (cm) | Outer diameter (cm) | Hach | Sensors | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Free chlorine | Total chlorine | Total hardness (ppm) | Total alkalinity (ppm) | pH | Temp (C) | Conductivity (ms cm−1) | TDS (ppm) | Turbidity (NTU) | OD (mg L−1) | ORP | |||
| a HH = household. b Not applicable. | |||||||||||||
| Control – Mineral water | —b | — | 0 | 0 | 0 | 0 | 6.2 | 29 | 0 | 0 | 0 | 7.72 | 0 |
| RO filter | 2.4 | 2.6 | 0 | 0 | 50 | 40 | 6.2 | 28.6 | 0.3 | 267.2 | 0 | 7.34 | 146 |
| HHa RO | — | — | 0 | 0 | 50 | 0 | 6.8 | 28.7 | 2.1 | 683 | 0 | 7.36 | 153 |
| Community tap #1 | 1.6 | 1.8 | 0 | 0 | 425 | 240 | 7.8 | 28.1 | 0.3 | 195 | 0 | 7 | 158 |
| Chief HHa | 2 | 2.2 | 0 | 0 | 245 | 180 | 8.4 | 28 | 2.2 | 871.5 | 0 | 6.9 | 135 |
| Handpump | 4.6 | 5 | 0 | 0 | 425 | 240 | 8.4 | 29.3 | 2.4 | 924 | 8.6 | 6.9 | 140 |
| Community tap #2 | 1.6 | 1.8 | 0 | 0 | 250 | 120 | 7.8 | 29.7 | 0.3 | 209 | 118 | 7.3 | 160 |
| Community tap #3 | 1.9 | 2.2 | 0 | 0 | 250 | 240 | 8.4 | 28.4 | 0.3 | 201.3 | 46 | 7.1 | 159 |
| Krishna river | — | — | 0 | 0 | 250 | 120 | 8.4 | 28.5 | 1.92 | 1036 | 124 | 6.32 | — |
To obtain bacterial presence or absence for the water source examined, the samples were kept in a custom-built field incubator under conditions that are suitable in terms of duration and temperature, namely 31° to 37 °C for 24 h, which can allow the bacteria to develop and reproduce. The incubator is easy to use, cost-effective and purposely built for rural areas with intermittent electricity supply. The parts of the incubator were purchased in India and built in the field. Fig. 8 shows the field incubator and the Aquagenx field test before incubation. E. coli and total coliform results are shown in Fig. 9.
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| Fig. 9 E. coli and total coliform results before and after UV disinfection, and turbidity levels across water sources. | ||
Moreover, the awareness of sanitation standards is low. For example, the water in the household is commonly stored in water containers that are placed on the floor, are not often cleaned, can be not covered at all, etc. We conducted detailed social surveys from each household to map and identify the behavior and awareness.38 The challenge was to provide a solution that is suitable for the household-level needs, considering the drinking water consumption, electricity hours and the village's social standards. This solution aims to overcome the challenges by providing a point-of-use, affordable and easy-to-use solution that will be integrated into the water tanks, which will be activated by an alternative energy source.
• Consider the entire water journey from source to use. The water sources are not always the problem, as even treated water can get re-contaminated during storage.
• Water should be treated as close as possible to the point of use. The water disinfection process should not be placed at a distance (too much effort for daily use); instead, it should be in a close community tap or at the household level.
• Rely only on the existing energy sources. Solar panels are difficult to install, maintain and operate in these areas; thus, energy harvesting could be from diversified options which are case specific, such as a hydrogenator or a battery.
• Count on intermittent electricity each day. The system cannot be dependent on constant electricity supply but can be based on short-term charged electricity.
With the advent of bore wells, hand pumps, and Community Water Supply Systems (CWSS), ooranies took a back seat and were left without proper care. Due to sparse rainfall and the fast depletion of groundwater, the drinking water supply available through the modern systems in rural areas faced problems. At this juncture, the Secretary to Government, Rural Development Department considered it expedient to renovate the ooranies not only to ensure sustainable water for drinking but also to support the existing bore wells and CWSS. The Secretary of the Government of Tamil Nadu decided to form a task force to renovate the ooranies in a scientific manner to ensure sustainability with people's participation.
The Center for Environmental Studies, Anna University – along with the Ministry of Rural Development – had come forward with an aim to provide clean and safe drinking water for the rural people. In order to achieve drinking water quality for zero coliforms, disinfection studies had to be conducted using UV LED disinfection. For executing the research work, Pattikaddu Oorani (Tamil Nadu, South India) was selected, where oorani is the only source of drinking water for the residents (Fig. 10). Thus, the objective was to disinfect drinking water taken from an oorani at the end-user stage in the rural villages using a zero-energy reactor system for disinfection in rural areas, where a hand pump is the major point-of-use for the small community population.
The hand lever of a hand pump was welded with the necessary support angles at appropriate places to achieve the full rotation of the circular plate, where the plate rotates with the mechanical up and down movement of the hand lever. The circular plate was connected to the large gear wheel, which was connected to the dynamo through a small gear wheel. One rotation of the larger gear wheel induces the smaller gear to rotate 10 times. On average, in one minute, 60 strokes (up and down movement of the lever) can be generated by a person. The mechanical energy of the gear wheel was converted into electrical energy through a dynamo. The dynamo was connected to the 6 V DC battery through a bridge rectifier. The voltage generated by the hand pump lever produced 600 revolutions per minute in the small gear wheel, which was enough to charge a 6 V battery.
E. coli concentrations were measured using the pour plate method, which involved adding 1 mL of the sample to 20 mL of nutrient agar in sterile Petri dishes and mixing, solidifying, and incubating at 30 °C for three days before colony counting (IS 14648:2011). The initial colony count was 133 ± 8 CFU mL−1E. coli inactivation of 100% was observed in six minutes of disinfection time in the UV LED batch annular reactor fitted with the hand pump. With the exposure to UV LED irradiance, the colony counts reduced significantly with time, resulting in <1 CFU mL−1. The system was observed to achieve a maximum inactivating fluence of ∼5 mJ cm−2 for E. coli, which corresponds with 2
log inactivation. The cost of UV LEDs is the major barrier to scalability, followed by the design and large-scale manufacturing of UV LEDs through collaboration with manufacturing companies with a target of zero-energy disinfection technology at the point of use in remote rural villages.
The novelty of the study is its practical applicability of a sustainable point-of-use disinfection technology that might be economically implemented in lower-income, smaller communities. Therefore, an economically feasible and self-sustaining disinfection system is required, which is the reason the wavelength ∼280 nm was chosen for the present study.
The goal was to disinfect communities' drinking water collected by hand from surface sources or from hand pumps fitted on shallow borewells. The water entering the device might have had a pressure of only a few centimeters of water column. The disinfection was required to be highly effective (exceeding USEPA guidelines) and affordable to local low-income community members, and the device needed to perform robustly in the difficult operating environment in remote areas of the developing world.
The primary objectives of the field test (Fig. 12) were to: 1) identify and correct any design problems and unanticipated technical flaws in the device, get feedback from an illustrative user community and from focus groups, and ensure the device's compatibility with the user preferences and requirements in South Asian communities; 2) evaluate and document the field performance of the device and its effectiveness in limiting the occurrence of waterborne biological contaminants in drinking water; 3) determine appropriate media and delivery systems for a) community placement and acceptance of the device, b) the necessary user education to assure sanitary and exclusive use of disinfected water for drinking and food preparation, and c) relevant community education in public hygiene and sanitary practices; and 4) determine the content and delivery systems for technical training of maintenance personnel, local management systems for community ownership and operation of the device to ensure its ongoing functioning.
The revised compact design (“UV Waterworks 2.0”) was pilot tested in the Lily of the Valley children's hospice in the rural area adjacent to Durban in South Africa, as described in case study #15.
log reduction in E. coli CFU (colony forming units). UV Waterworks was tested by third-party laboratories to ensure it could kill 15 different pathogenic bacteria (including Campylobacter jejuni, Shigella, Salmonella typhi, Vibrio cholerae and Escherichia coli) and multiple pathogenic viruses (including rotavirus and poliovirus), and also cysts of Giardia. Specific capabilities of the device include:
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| Fig. 13 UV waterworks, built with a glass cover for exhibits and displays to explain how the technology works. | ||
1. Can operate with unpressurized water.
2. Demonstrated inactivation of pathogenic bacteria and viruses in water with turbidity of up to 30 NTU.
3. Does not require a trained operator.
4. Requires maintenance every 6 months.
5. Fast-acting disinfection (hydraulic residence time = 12 seconds).
The initial design was constructed of welded stainless steel, at a cost of $900 USD, consumed 40 W and reduced the bacterial colony forming units (CFU) per 100 mL at 30 LPM from 100
000 to less than one, i.e., disinfection that meets WHO and EPA standards.
After a second workshop in India in May 1994, the design was field tested at several sites in India, including at Bhupalpur, from 1994 to 1995. A hand pump was used to supply contaminated well water to the UV Waterworks unit, which was powered by a 12 V car battery. The Indian communities reported that the flow capacity of the device (60 LPM) was far higher than necessary, and the devices were bulky and costly. In response, a revised prototype was developed that still used 40 W but disinfected 15 LPM. This new design was better matched to the flow rate of the widely used UNICEF India Mark-II hand pump, was more compact and had a substantially lower manufacturing cost. This design, completed in December 1995, exhausted all project funding. The design has seen only minor modifications since then, as the project effort has shifted to testing, troubleshooting and promotion.
The Indian communities informed us that the flow capacity of the device was much higher than necessary, and the devices were too bulky and costly. In response, a revised version was delivered with lower flow rates and lower costs. Socially, the lack of trained personnel on-site and the difficulty in traveling the large distances required in rural India presented a skill deficiency challenge.
In 2011, BORDA installed a UV disinfection system for decentralized wastewater treatment at the site of an existing wastewater treatment plant at the Staff Operator Village of the Theun-Hinboun hydropower generation plant. The original wastewater treatment system, which was in use from 1995 to 2009 and used a mechanical-activated sludge system, had stopped functioning due to high costs and a lack of O&M knowledge and capabilities. As a result, the system had high odors and was no longer meeting effluent wastewater quality discharge standards. The company requested support from BORDA to upgrade the plant in 2010. The upgraded plant, which became operational in October of 2011, included a pretreatment system (Fig. 14) with a grease trap, settler, anaerobic baffled reactor, anaerobic filter, planted gravel filter, and aerobic polishing pond prior to UV disinfection, before discharge into a natural stream. At the start of operation, the wastewater plant was serving over 70 households and a maximum of 700 users with a treatment capacity of 70 m3 per day.
One suggestion for improving pretreatment of the water prior to UV disinfection was to install a tube settler in the aerobic pond so that particles would attach to it and settle down. Sand filters and membrane filters also would reduce the influent turbidity; however, they would require routine maintenance. Another suggestion from colleagues at the Asian Institute of Technology was to better maintain the wetlands in the planted gravel filter by harvesting, for example. Since it had been operating for four and a half years, solids would have accumulated on the media, which increases the contaminants flowing through. Maintenance would require cutting the plants, removing sludge that had accumulated on the top surface, and washing or replacing the media.
Another suggestion to increase UV exposure was to route the four lamps in series instead of in parallel; however, the flow rate with the lamps operating in parallel already was exceeding that recommended by the manufacturer. Therefore, routing them in series would not have been sufficient for meeting the treatment demand. Adding more lamps would have been one solution to increase the disinfection capacity while maintaining or lowering the flow rate.
The low-pressure UV lamps used were designed to last for 10
000 hours, or 14 months of continuous operation. BORDA recommended that they be replaced every year to be conservative. The THPC operators confirmed that the lamps were only six months old; therefore, their output was not the source of the problem. It was recommended that the operators use a solution to clean the lamp sleeves including citric acid, phosphoric acid or Lime Away to dissolve calcium and magnesium deposits or another solution recommended by the UV reactor manufacturer that is consistent with the NSF/ANSI (the Public Health and Safety Organization/American National Standards Institute) Standard 60 on Drinking Water Treatment Chemicals – Health Effects. Pilot studies lasting five to 12 months using UV reactors with low-pressure and medium-pressure lamps found that standard cleaning protocols and wiper frequencies (one to 12 cleaning cycles per hour) have been sufficient to overcome the effect of sleeve fouling with water that had total and calcium hardness levels less than 140 milligrams per liter (mg L−1) and iron less than 0.1 mg L−1.44,45
The collected rainwater is commonly stored in polystyrene tanks, metal jerry cans, clay pots and other water storage containers. Galvanized corrugated iron sheets are the commonly-used housing roofing material for most communities in Kenya, including the rural communities at Nyamesocho village (Fig. 16). Therefore, the rainwater is often collected from such roofs. Notably, if not filtered, the collected and stored rainwater is contaminated by dirt found in the rooftops originating from bird and some animal droppings, tree leaves, etc. In the past, visible worms frequently have been seen in the stored rainwater (Fig. 16), which is a confirmation of the reports on the growth of microbial contaminants within water storage containers.46,47 Also, if the water is stored for long periods of time, it can produce an unpleasant smell, which can prevent people from drinking it. Therefore, this project was designed to collect, filter and disinfect rainwater by ultraviolet light-emitting diodes (UV LED) for use at household point of use. Future work in the area will involve designing and building similar but larger water treatment systems to serve more people in the community, including systems in community schools within the rural villages as well as within more densely populated poverty-stricken areas within Nairobi.
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| Fig. 17 (Left) Rainwater collection, filtration and disinfection system. (Right) Biosand and biochar layers within the filtration system. | ||
For continuous operation of the UV LED system, it was powered by automatic interchangeable electricity from both solar panels and grid lines. Although the cost of the treatment system seemed expensive, the installation and operation were relatively easy.
Local plumbers and electricians were hired to install the systems, and a welder built solar panel roof brackets and boxes to contain the systems and prevent tampering (Fig. 18). The boxes to prevent tampering, which were requested by the schools, were designed with a window to allow the operator to easily check whether the system was on or off. The systems were designed to cost around $250 USD, including all components and installation costs. This system was installed directly before the drinking water taps for immediate consumption or use after treatment (the water was not stored post-UV treatment). Therefore, it was only available on demand, because the stored water could become contaminated post-treatment with no residual disinfectant in the water.50
All of the UV system components were functional in 2020, but they were not being used consistently due to technical constraints. One major barrier was a problem with energy surges that were not properly mitigated by the charge controller in the system. There were issues with both locally and United States-sourced low-cost charge controllers. As a result, lamps would frequently burn out and need to be replaced. A surge protector was installed (which was unavailable locally), but the surges were frequent, requiring that an operator check the system before each use, which was not practical. Further, parts for the VIQUA VT1 system were not available locally and needed to be sourced from a company in Uganda (which needed to order them from Canada). Alternate UV systems were available at the local water equipment supplier, Davis and Shirtliff. Rigorous testing of locally available supplies and design of treatment systems using only these supplies would have prevented many of the technical issues encountered.
Challenges with system testing and maintenance were also encountered. Testing was set up to be conducted by the school maintenance worker and a science teacher. They would then use WhatsApp to send pictures of the results weekly. Unfortunately, they did not feel comfortable conducting Aquagenx compartment bag tests, which is a field test to detect E. coli in water samples. Further, the UV transmittance readings we received proved unreliable due, it is believed, to the continual need for calibration of the low-cost UVT instrument. Thus, many of the important tests needed to maintain system compliance were difficult to obtain.
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| Fig. 19 Mesita Azul household water treatment system with an open-channel UV reactor (silver cylinder) fed by gravity. | ||
A second iteration of UV installations was undertaken from 2018 to 2022 through Cantaro Azul's SAFEWATER program. Here, 187 treatment units were installed in rural households in the state of Chiapas, Mexico. The SAFEWATER system consists of a point-of-entry water treatment unit that includes a 250 L raw water container located in the bottom level of the support structure and a 250 L container for treated water at the top level (Fig. 20). The bottom container can receive water from multiple sources, including piped water (e.g., a nearby spring or well), a hose from a storage tank (e.g., rainwater harvesting) or poured in directly when manually collected. Water is pumped from this container, through the treatment components and into the top container for safe storage. The treatment process consists of two pleated filters with nominal pore sizes of 5 μm and 1 μm, an activated carbon filter and a UV disinfection chamber (either the same open-channel system as the Mesita Azul or a common pressurized system). The key element of the SAFEWATER system is that it uses gravity to distribute water from the top container through 1/2′′ PVC pipes to two to five taps installed within the home.
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| Fig. 20 The 250 L SAFEWATER system (left) with the encased LP UV lamp and activated carbon filters (right). | ||
The second phase of the study (the SAFEWATER project from 2018 to 2022) was designed to deliver treated water for all uses in the household to minimize the risk from access to untreated stored water. During the study of 187 installations, the rate of positive E. coli incidences was reduced from 80% in the untreated control group to 20% in the treated systems. It was observed that only 16% of the households showed evidence of people sporadically drinking from non-treated stored water.
Cantaro Azul reported that scaling UV disinfection in rural communities requires efforts to reduce production costs, increase the lifetime of the products and integrate such treatment methods into government programs that partially or fully subsidize water treatment solutions in marginalized communities. To achieve this goal, it is important to form alliances that support all dimensions of the implementation of UV, from research and innovation to product design, capacity building, supply chain development, community mobilization and public policy advocacy.
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| Fig. 21 The multi-barrier treatment train includes prefiltration, reverse osmosis (RO), UV disinfection and calcite filters. | ||
A pressure tank maintains water pressure (15 psi) for the RO unit and is controlled by a 15 psi pressure switch. Electrical controls are in place to detect when the storage tank is full, and a float switch shuts off the RO unit with a solenoid valve. CPVC piping was selected for the UV system inlet and outlet to prevent pipes from melting during periods of no flow in the UV reactor. No chlorine residual was provided in this system design. The ambient temperature in Rama Cay is between 72 °F and 93 °F throughout the year, so bacteria could propagate in the storage tank. The design assumes the community uses nearly all the water in the tank to prevent excessive water from stagnating overnight. The entire system (RO and UV) shuts down when the generator is shut off each night.
The capital cost of each individual water system was approximately $9400 USD, including RO ($4500 USD), UV disinfection ($325 USD), calcite contactors ($375 USD), tanks and plumbing ($3000 USD) and electrical components ($1150 USD). For each system, the replacement costs are $345 USD every two years for RO pre-filters and membranes, $84 USD per year for UV lamps and $90 USD per year for calcite filter media. This is planned to be funded by the Friends in Action Organization. The final system will be housed in a concrete building and community members will be able to collect potable water from tanks.
A team from the University of Tokyo worked with the University of San Agustin and the Philippine Science High School Western Visayas Campus to install a solar-powered UV LED system (Yu Jeco, Larroder and Oguma, 2019). Since the island has no access to the commercial power grid, the solar-powered UV LED disinfection system was introduced by the team as a feasible technology (Fig. 22). The team set a long-term goal to let the residents learn how to operate and maintain the system by themselves; therefore, community members were encouraged to join a free workshop to learn the basics of public health and UV disinfection.
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| Fig. 22 Pilot setup of solar-powered UV LED water disinfection system in Panobolon Island, Guimaras, Philippines. The UV LED module is enclosed in the yellow circle. | ||
log-inactivation of E. coli (K-12 IFO3301) at a flow rate of 2 LPM. The test matrix in PBS had an initial concentration of E. coli of 106 CFU mL−1 and a UVT at 280 nm of 96%.
Water quality conditions in the field were as follows (mean ± SD): turbidity = <0.1 degree (Japanese turbidity unit), color = 0.8 ± 0.1 degree (Japanese color unit), hardness = 46.4 ±1.3 mg L−1, iron = <0.02 mg L−1, manganese = <0.005 mg L−1, temperature = 17.1 ± 1 °C, pH = 7.7 ± 0.02, conductivity = 11.0 ± 0.25 mS m−1. Concentrations of microorganisms in the raw water were as follows: E. coli up to 1.5 CFU mL−1, total coliform up to 2.5 CFU mL−1, standard plate count up to 16 CFU mL−1, and heterotrophic plate count up to 2500 CFU mL−1. E. coli and total coliform were not detected in the UV LED effluent for the duration of the pilot testing (n = 21 samples, 12 months), except for one detection of E. coli after UV disinfection. The average log-inactivation of heterotrophic plate count was 0.77 and 1.83 for 2 LPM and 10 LPM operation, respectively.
The UV LED was rated to operate at 12 V and 350 mA, which was powered by a 150 W commercial silicon solar panel generating approximately 325 Wh per day with a battery storage of 50 Ah (Fig. 23). The region has an estimated annual mean of 4.3 kWh m−2 per day, as detected at Iloilo City. The system was only operated during the period of piloting.
1. The UV LED flow-through module adapted in the initial trial was not enough for inactivation performance, as treated water was still occasionally positive with E. coli. Modifying the current prototype module, or using different modules with higher inactivation performance, would be necessary. Alternatively, UV LED exposure during storage, instead of flow-through treatment, would be an option.
2. Photoreactivation of microorganisms under strong sunlight could be an issue in the field, as this was slightly observed during this field testing. Sunlight protection measures should be taken. For example, light-screening containers are recommended to bring the treated water back home.
3. Seasonal variations of both groundwater quality and solar radiation should be considered in the treatment design process as these can affect system performance. These factors also should be monitored over a long period of time.
After prefiltering with two washable bag filters of 25 and 10 microns (Fig. 24), disinfection is achieved with use of a 20 watt UV254 lamp (dose of 40 mJ cm−2). A solar panel of 80 W is used so that it can perform independently even in a remote area without access to grid energy. The unit has a total weight of 44 kg with dimensions of 54 × 75 × 140 cm (excluding solar panel). Flow rate is approximately 5 LPM. Storage capacity is 100 L. A regular 12 V car battery can be used for backup power during the night and is charged by the system's solar panel.
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| Fig. 25 A Naïade (on the left) and rainwater harvesting tank on a primary school in Kigali, serving 240 children and 20 staff members. | ||
The biggest challenge is financing the purchase of units and maintenance. This has been the case in all countries where Naïade systems were installed, within Africa, Asia and South America. Neighboring schools using chlorine have indicated that they have a strong wish to switch over to UV, due to costs and work instructions.
log removal”.
At some schools, it was reported that within two weeks after installation of a Naïade system, approximately 40% more children attended school because of a decreased incidence of chronic diarrhea.
In Rwanda, units are installed in Gisenyi, Musasa, Kigali, Muhanga, Musanze, Huye, Kayonza, Umutara, Kibungo, Nyabihu, Nyirangarama, Nemba, Nyamata and Rwamagana, serving treated water to over 27
300 students.
The most challenging topics remaining include:
• Financing units and maintenance.
• Local attendance for installation, maintenance, service and education.
Both Muramba and Mugonero were faced with frequently contaminated and untreated water from a range of sources, including piped water, harvested rainwater and surface water. All water sources were shown in initial testing to be contaminated with coliforms, some of them with E. coli, indicating human and animal fecal contamination, with levels of contamination fluctuating seasonally as a result of heavy rainfall. Testing also showed turbidity above advised values, which can be associated with higher levels of disease-causing organisms attached to particulates. The goal was to reduce exposure to contaminated water causing diarrheal illnesses by treating the water using the BYOW system.
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| Fig. 26 A schematic of the BYOW system (left) and photo of the system installed in Mugonero (right). | ||
The BYOW system is capable of treating water at 10 LPM, as was shown in long-term testing in Houston, Texas, where activated sludge from a sewage plant was used as an input. In this extreme case, the system was capable of reducing turbidities of 70 NTU to below 1 NTU, and 3000 CFU mL−1 to below 2 CFU mL−1. In the field, a maximum of 4.65 NTU was reduced to below 2.25, and a maximum of 63 CFU mL−1 to zero, with the exception of one case, where CFU mL−1 was reduced to one.
The lamps in the UV system are rated for 365 days of constant use, so if the system is used for less than six hours per day, it can be inferred that each lamp will last four years (neglecting lamp cycling impacts). The lamp is installed within a quartz sleeve.
In order to ensure the technology adoption by the local community, local community leaders were recruited to organize the installation of the system, and the BYOW units were implemented alongside other technological solutions, such as drip irrigation, solar-powered lighting and computers, and biogas generators. In Mugonero, the installation of the BYOW system was supplemented with the installation of six 10 m3 rainwater collection tanks. The relationship with community leaders also ensured reliable recruitment and attendance for maintenance training sessions conducted by the engineers.
To ensure minimal reliance on non-local materials, a trade study was carried out as part of the design phase, wherein alternative solutions were compared with respect to (among other parameters) the local source-ability of the required materials. By liaising with an importer in Kigali (near the communities) with whom community leaders have an existing commercial relationship, the means of sourcing replacement UV lamps was secured – by far the most challenging of the components to source.
The systems were installed for free-of-charge use, although future BYOW systems could operate a pay-per-use business model. Assuming the worst-case situation in the replacement of a lamp every six months at a cost of ∼$100, the running cost per liter for each BYOW system was $0.027. The initial installation of the system cost about $5000 and it was designed to operate for 10 years before it would require major refurbishing, rendering the likely cost per liter at $0.10. If a typical worker earns $1 and uses 4 L of clean drinking water per day, the cost of drinking water from the BYOW system is less than 0.3% of income. However, users reported that the free-of-charge aspect of the BYOW systems implemented was a strong component in their adoption of the technology.
The design solution is installed in-line with existing water pipes and included an elevated backwash tank, a gravel filter and a pressurized sand filter, followed by a solar photovoltaic-powered UV disinfection system (Fig. 27).
The UV system included two Sterilight UV lamps, a RealTech UVT sensor, a flowmeter and a valve. The electronic controller, designed by Manna Energy Limited and Portland State University engineers, monitored UVT and flowrate. It turned the smaller UV lamp on for low flowrates and clear water and the larger UV lamp on for higher flows and lower water quality; the flowrate was controlled with a valve to maintain a minimum UV residence time (Fig. 28).
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| Fig. 29 UV Waterworks 2.0 unit installed on the exterior wall of the kitchen at the Lily of the Valley HIV-Hospice near Durban, South Africa. | ||
log inactivation). UV Waterworks was tested by third-party laboratories to ensure it can kill 15 different pathogenic bacteria (including Campylobacter jejuni, Shigella, Salmonella typhi, Vibrio cholerae and Escherichia coli) and multiple pathogenic viruses (including rotavirus and poliovirus), and also cysts of Giardia. Specific capabilities of the device include:
1. Works with unpressurized water.
2. Deactivates pathogenic bacteria and viruses in water with turbidity of up to 30 NTU.
3. Does not need a trained operator.
4. Maintenance is minimal and infrequent (every six months).
5. Rapid disinfection (water passes through the unit in 12 seconds).
It turned out that once, prior to opening the device for routine maintenance, the local electrician had disconnected the power to UV Waterworks; however, the electrician overlooked reconnecting the power when the maintenance was completed. Since the hydraulics (water inlet and outlet) were decoupled from the power supply to the lamp, the kitchen staff continued to use the device, mistakenly thinking that the water emerging from the faucet was disinfected. This problem was discovered and corrected upon a subsequent visit to the hospice.
The corrective design change immediately implemented in the design (now called UV Waterworks 2.1, Fig. 30) was the addition of an electrically controlled flow control valve at the inlet, which was normally off and would open only when the device was supplied with power. Additionally, two photo sensors added inside the UV Waterworks also controlled this valve. One photosensor monitored the UV lamp itself, and the other monitored the UV transmittance of the water being treated. Unless the UV lamp was on and the UV transmittance of the water also was adequately high, the inlet valve would remain closed. This large electromagnetic valve consumed an additional 20 W of electrical power, raising the total power consumption from 40 W to 60 W. This is the design that was mass produced by the industrial licensee after the year 2000 for commercial implementation.
In sharp contrast, the business model undertaken to bring the device to market through the private sector was highly successful. Leveraging the inventors' novelty through a patent-licensing agreement and technical expertise through a continued development partnership, funding has been secured in an amount that is an order of magnitude higher than the initial public funding. Obstacles to deployment in the hands of commercial partners in this case are beyond the scope of this paper.
The technical benefits of simplifying a device in order to reduce maintenance requirements were evident from the first case study; results that teach elegance over complexity in design. Similarly, appropriately strong community engagement was highly successful in effectively adapting the technology, presenting yet another positive lesson in collaborative development.
In conclusion, an innovative UV disinfection technology adapted for the under-developed economy was developed, tested, patented and licensed. The contribution to the general field has been significant, but public sector organizational challenges have hindered widespread deployment.
Without adequate WASH treatment, homes, schools and health centers become breeding grounds for diseases that kill children and threaten their ability to grow. Tanzania is one of seven countries with the highest disease burden caused by cholera in Africa.59 The country suffers from late detection of cholera and outbreaks due to non-existent water treatment and weak surveillance systems, particularly in HCFs.60
000 people (Table 5). This was funded by an international agency and implemented by an NGO in 2019.
| Health clinic | Population |
|---|---|
| Kharumwa | 27 093 |
| Nkome | 44 003 |
| Kashishi | 20 866 |
| Nyangh'wale | 15 323 |
| Nyugwa | 15 502 |
| Bukwimba | 18 415 |
| Total |
141 202
|
In this instance, rainwater harvesting (RWH) was used as a water source due to the lack of available groundwater and surface water in the area. Rainwater is known to be subject to contamination from collection surfaces and storage – bird and animal feces, tree waste and air pollution. At each hospital, rainwater was collected from a large rooftop catchment area. Through a series of gutters, the rainwater passed through a first flush diverter and wash-out chamber, which removed dirt, debris and leaves. The water was then stored in a 100 m3 underground storage tank. A solar-powered pump brought the rainwater into a 10 m3 raised storage tank. Water then flowed through a 25 W low-pressure UV lamp into the hospital facility for multiple uses for staff and patients in operation rooms, doctors' offices, bathrooms, etc. (Fig. 31). The UV lamp was powered by a 125 W, 12 V solar panel, which charged a 12 V lead-acid battery.
After 18 months, an inspection of the six healthcare facilities observed that three of seven lamps were not functional at the time of visit; one lamp had burnt out while two were not functioning due to electrical issues. Two of the malfunctions were due to poorly designed electrical components. Poor housing, protection and monitoring of the systems resulted in damaged wire connections and hardware caused by birds and overheating of components due to poor cleaning. The plumbing design was not conducive for regular cleaning and inspection of the UV lamps. Furthermore, the UV lamps themselves did not provide clear user feedback of their status. This resulted in lamps that overheated from being always on or lamps that were not functioning due to burn out or simply being switched off.
The majority of the lack of functioning was due to poor technology transfer to staff throughout turnover, missing maintenance protocols and lack of awareness and understanding of UV function. This oversight was primarily seen through poor cleaning of rooftops and gutter systems, which may have contributed to the significant dirt and fouling on the quartz sleeve and interference with UV transmittance.
ASEI is exploring the opportunity to integrate the UV LED units into modular micro-factories, each with the ability to produce about 1500 L per day of treated water. These micro-factories can be leased to water vendors to supply treated water from central locations in communities.
The consumers in this case study region are health conscious and had concerns with the use of chlorine. This case study demonstrates that, when integrated into an appropriately designed water treatment and dispensing system, UV disinfection can provide an effective treatment option free of oxidative chemicals.
The water-on-wheels mobile emergency water treatment system (WOW Cart, Fig. 33) is designed to provide treated water during such a response and recovery period. It is designed for deployment anywhere in the world and can provide potable water using sources ranging from raw water to compromised water from distribution systems. Oftentimes, deployments are conducted in conjunction with local nonprofit organizations from the impacted community. WaterStep, a Louisville, KY nonprofit and fabricator of the WOW Cart often works with State or Federal agencies coordinating deployments with local/nearby water utilities or other nonprofits.
Recent deployments of the WOW Cart include:
• Western Kentucky, following multiple tornadoes in December 2021.
○ Graves County Public Health Department
○ Mercy Chef Mobile Kitchen
○ Dawson Springs 4H Camp
• Eastern Kentucky, following flooding in multiple communities in August 2022.
○ Perry County, HomePlace Community Center
○ Perry County, Buckhorn Children's Home
○ Letcher County, Mayking Fire Department
○ Breathitt County, River Caney Staging Area
• Ukraine in Summer 2022.
The WOW cart's design minimizes the footprint and weight, which can enable transportation in the back of a pickup truck and movement on-site by two people. The UV LED system also adds to the robustness of the system, minimizing any risk of damaging the device during transportation and operation. The on-site treatment of water also reduces the dependence on bottled water, which creates a solid waste disposal problem. Additionally, the WOW cart fills a niche that bottled water cannot address in terms of providing safe water for showers (Fig. 34), laundry, food preparation/clean-up and general sanitation, which could also include medical triage. It is also envisioned that WOW carts could be pre-deployed to critical institutions such as nursing homes, hospitals and prisons, where relocating residents presents a considerable health and financial risk.
The WOW Cart is 30′′ wide × 48′′ long × 42′′ tall, weighs less than 500 pounds and produces up to 38 LPM (typically operated at 31 LPM, depending on the conditions of the filters). It can be operated off the grid using the supplied dual-fuel gasoline/propane generator or by plugging it into a normal wall outlet. There is no complicated mixing of chemicals, filter backwashing or large volumes of media to dispose of. The UV LED system (Pearl Deca) is manufactured in Kentucky, United States by AquiSense Technologies. It consists of multiple UV LEDs with a nominal wavelength of 280 nm and operates from a 24 VDC input. The UV disinfection capability provides an additional level of disinfection at a UV dose of 30–40 mJ cm−2 (wavelength unspecified), which complements the chlorination step in its ability to inactivate microbial contaminants (such as Cryptosporidium spp.) that chlorine is unable to address. The UV LED technology fits perfectly into this concept with a small footprint and simply monitors flow rate to turn instantly on at full power with flowing water, thus limiting fouling potential and ensuring an extended lamp replacement interval.
Volunteers without water treatment expertise can be trained quickly to operate the WOW cart. The UV LED system has NSF material compliance certification and requires almost no maintenance, thus adding to the ability of volunteers to provide safe water. It is expected that following deployment, the WOW Cart will be warehoused following complete drainage and drying out until needed for the next response. It can be purchased by government agencies, water utilities or other nonprofits from WaterStep. Monetary donations to the organization following disasters allows them to donate WOW Carts to impacted communities and other nonprofits.
A UV LED water disinfection reactor (the PearlAqua by AquiSense Technologies) was studied over a year-long demonstration test, and performance was compared side-by-side with an existing chlorination system at a small water treatment plant in Colorado serving about 300 people. As detailed further in Hull et al.,28 the UV LED disinfection system was validation tested using MS2 bacteriophage inactivation over a range of flow rates and water UV transmittances. The reactor also was challenge-tested with MS2 periodically during the year-long demonstration. Over the bench testing and during the demonstration study in challenging conditions without any maintenance, the reactor demonstrated viral and bacterial disinfection efficacy and resilience, providing proof of concept for application of UV LED for municipal treatment.
Light-emitting diodes (LEDs) are non-mercury sources of polychromatic UV emission with promise as a sustainable solution for drinking water disinfection in small communities. Manufacturers and researchers have produced LEDs capable of emitting wavelengths across the UVC spectrum (200 nm to 280 nm) as low as 220 nm.61 UV LEDs could be more sustainable than traditional UV lamps because they do not contain mercury, have lower power requirements, are more compact and are becoming more efficient as materials science advances.23,26 Additionally, LEDs are capable of nearly instantaneous power-up, do not suffer from unlimited cycling, have long lifespans, are small in size and have higher power density than conventional mercury UV lamps.62
One objective of this research was to validate UV LED reactor disinfection performance at bench scale across a range of flow rates and UV transmittances to develop a predictive model for disinfection (Fig. 35). In the second objective, the LED reactor was installed in the first long-term disinfection demonstration in a small drinking water system. The validation model was used to assess disinfection performance over time through periodic challenge testing.
psi and a pressure drop at maximum flow (12 LPM) of 1.3 psi.63 It is rated for operating in water temperatures ranging from 0 °C to 50 °C, connects with 1/2-in. (outer diameter female national pipe thread [FNPT]) fittings, weighs 3.3 lb, and measures roughly 6 × 6 × 6 in. for the entire system. The reactor operates in upflow orientation where water passes through an internal diffuser before irradiation, can be mounted with a spring-loaded bracket and is powered by a single cable from the UVinaire LED module to a standard outlet (120
V and 60
Hz). The power cable has a converter that supplies 12
V DC to the UVinaire, with 2.5 A maximum current and 26 W nominal power consumption. The UVinaire houses the internal electronics, fan, heat sink and array of LEDs that irradiate through a quartz window to the reactor interior. The outside of the UVinaire has two visible LED indicator lights coded for various electronic warnings to indicate the status of the system and LEDs. The UVinaire has an internal 4–20
mA current loop that can be used to measure the lamp life remaining or for remote monitoring and operation. Before testing, the total output power of the UVinaire was approximately 0.25
W.
The field site for the demonstration study was the drinking water treatment plant in the small mountain town (population ∼300 and elevation ∼7000 ft) of Jamestown, CO, United States. Surface water directly from James Creek or from a shallow infiltration gallery was slow-sand filtered before chlorination and distribution of approximately 38 to 208 m3 per day, depending on seasonal demand. The UV reactor was installed on the outlet of the slow-sand filter and operated at 0.5 LPM in parallel to the existing chlorination system.
Most case studies described resulted in outcomes that immediately improved the water quality and positively impacted the population; however, in almost all cases studied, the long-term effectiveness of the UV intervention (i.e., over years) was not tracked nor reported. Furthermore, several insights and persistent limitations were uncovered and should be considered and addressed in future projects. In general, the challenges, considerations, and limitations can be summarized into five categories, described in more detail below (Table 6): availability, water quality, system design, operation and maintenance, and social factors.
| Availability |
|---|
| • Affordability and funding |
| • Supply chain for replacement parts |
| • Costs for scaling up |
| Water quality |
|---|
| • Turbidity spikes |
| • Chemical and biological fouling |
| • Water quality monitoring |
| System design |
|---|
| • Location of the water system |
| • Inadequate user-focused design |
| • Necessity of a reliable energy source |
| Operation and maintenance |
|---|
| • Insufficient training and staff turnover |
| • Irregular maintenance and testing |
| • Little to no project follow-up |
| Social factors |
|---|
| • Building community trust and buy-in |
| • Community consultation |
| • Water supply institutions and regulations |
Water projects in low-income and rural settings are often financed by private, donor and governmental funding (case studies 7, 10, 12, 14). These projects have also been driven through establishing partnerships and applying innovative business models (case studies 4, 13). Water supply and treatment systems can require a significant initial investment; however, it is also important to consider the long-term financing mechanisms required to operate and maintain the UV systems.
Ensuring that UV disinfection is effective often requires effective pre-treatment. The water treatment processes upstream of the UV device must condition the water for effective UV treatment, particularly for reducing turbidity and increasing UVT. This may include using pretreatment technologies such as filtration and ensuring the UV systems apply sufficient irradiance over time (case studies 2, 3, 5–11, 13–20).
Additionally, while UV disinfection inactivates microorganisms, post-treatment recontamination is a concern. Factors such as sublethal UV doses, shielding by particulates, and the lack of residual disinfectants can contribute to microbial regrowth. Bacteria may recover through reactivation from a viable but nonculturable state, DNA repair, or reproduction of surviving cells.64 UV systems require a continuous power supply, and failures or reduced intensity can compromise disinfection, increasing contamination risk. Without residual disinfection, treated water is vulnerable to recontamination, especially in non-sterile or containers or unsanitary conditions. A substantial increase in E. coli contamination in treated water taken from storage containers and drinking glasses compared to water taken directly from the UV system effluent has been found.50 Additionally, UV treatment does not remove suspended solids, which can shield microorganisms, reducing disinfection efficacy.65 Pre-filtration can be used to ensure water clarity. Certain bacteria, such as Listeria monocytogenes, have shown recovery post-UV treatment under favorable conditions.66 To reduce these risks, proper storage, regular maintenance of UV systems, and integration with residual disinfection methods like chlorination can help to maintain water quality.
Another challenge that was observed is the lack of monitoring of the system's operation and performance over time due to the cost of water quality analysis, especially microbiological counts. These rely on correct sampling procedures and proximity to an external laboratory. The tests are tedious as they involve sampling, transporting the samples to the laboratory, and analyzing and reporting the results, all of which can take more than 24 hours. Regular testing activities and training can also be a burden for the community and local operators. According to WHO guidelines and the EU Drinking Water Directive,67,68 the E. coli and FC parametric value should be zero colony-forming units (CFU) per 100 mL, which is complex to analyze in many settings (case studies 1, 2, 8, 11 15). Nevertheless, in some of the case studies, researchers used field kits which were able to measure inactivation of E. coli and fecal coliforms in the field (case studies 2, 3, 7).
Additionally, the energy required for powering the UV reactors can be sourced from a range of power sources, including grid, solar, and battery (case study 5). Some locations might have access to a consistent energy supply from an electrical grid; however, some case studies reported intermittent electricity which could result in a shutdown of the UV source (case studies 7 and 10) unless backup battery power was available (case study 1). In these cases, alternative energy supplies should be considered, such as solar panels, gasoline generators, batteries or using a hand pump to charge a battery. The maintenance and assurance of energy should be considered in the initial design and in the operation and maintenance plan (case studies 4, 5, 8, 9, 11, 12, 16, 18).
In general, across the 19 case studies, there was a lack of consistency in how the UV systems were characterized and in the metrics that were used to demonstrate that the systems were performing adequately. For example, UV lamp intensity and UV dose (or Reduction Equivalent Dose, RED), log-inactivation and the target microorganism, lamp fouling and scaling, and validation testing protocols are commonly-used to characterize the efficacy of large centralized UV systems.25 However, this information was either not tracked or not made available in several case studies. This may be a result of how new UV technology is compared to more established forms of disinfection (such as chlorination), the complexity of UV disinfection systems, and the lack of available guidance on UV system design and operation for decentralized systems.
In some cases, however, the challenges discussed in the previous section can be overcome with an effective Operation and Maintenance strategy. Examples of required regular maintenance activities include inspections, lamp replacement, quartz sleeve cleaning, and pretreatment servicing. It is also important to consider all factors of maintenance and properly define protocols, roles and responsibilities, professional servicing as well as sustainable financing for operation and maintenance costs (case studies 1, 2, 4–6, 8, 12–16, 18).
Various UV LED water treatment systems incorporate flow control valves managed by UV dose, UVT or water flow rate to optimize disinfection (case studies 1, 15, 17). UV monitoring systems detect decreases in UV intensity and lamp failures through UV light monitors, sensors, and alarm systems (case studies 6, 8, 13, 15). Internal current loops provide real-time system status and lamp life tracking (case study 19). These integrated control and monitoring mechanisms enhance system efficiency, reliability, and fault detection, ensuring effective decentralized water treatment.
It is important to follow up on the project post-implementation, not only from the technical side, but also by conducting interviews or surveys with users to address pain points at the intersection of the technology and the users (case studies 1, 2, 16).
This manuscript serves as introductory material for program managers who are considering UV as a technology; referencing these examples may provide inspiration while also preventing some of the common mistakes. This compilation, along with the associated map at http://www.iuva.org/UN-Sustainable-Development-Goals-Task-Force,34 could also serve as a point of connection between future practitioners. We intend for the map to be an evolving document to which more case studies will be added over time. We hope that this paper and the case studies within will provoke discussions on what the water sector needs to advance in the adoption of UV technologies in low-resource settings.
Footnote |
| † These authors contributed equally to the manuscript. |
| This journal is © The Royal Society of Chemistry 2026 |