| Literature DB >> 35700262 |
Megan Lindmark1, Katya Cherukumilli2, Yoshika S Crider3,4,5, Perrine Marcenac6, Matthew Lozier6, Lee Voth-Gaeddert6,7, Daniele S Lantagne8, James R Mihelcic9, Qianjin Marina Zhang10, Craig Just1, Amy J Pickering2,11.
Abstract
The world is not on track to meet Sustainable Development Goal 6.1 to provide universal access to safely managed drinking water by 2030. Removal of priority microbial contaminants by disinfection is one aspect of ensuring water is safely managed. Passive chlorination (also called in-line chlorination) represents one approach to disinfecting drinking water before or at the point of collection (POC), without requiring daily user input or electricity. In contrast to manual household chlorination methods typically implemented at the point of use (POU), passive chlorinators can reduce the user burden for chlorine dosing and enable treatment at scales ranging from communities to small municipalities. In this review, we synthesized evidence from 27 evaluations of passive chlorinators (in 19 articles, 3 NGO reports, and 5 theses) conducted across 16 countries in communities, schools, health care facilities, and refugee camps. Of the 27 passive chlorinators we identified, the majority (22/27) were solid tablet or granular chlorine dosers, and the remaining devices were liquid chlorine dosers. We identified the following research priorities to address existing barriers to scaled deployment of passive chlorinators: (i) strengthening local chlorine supply chains through decentralized liquid chlorine production, (ii) validating context-specific business models and financial sustainability, (iii) leveraging remote monitoring and sensing tools to monitor real-time chlorine levels and potential system failures, and (iv) designing handpump-compatible passive chlorinators to serve the many communities reliant on handpumps as a primary drinking water source. We also propose a set of reporting indicators for future studies to facilitate standardized evaluations of the technical performance and financial sustainability of passive chlorinators. In addition, we discuss the limitations of chlorine-based disinfection and recognize the importance of addressing chemical contamination in drinking water supplies. Passive chlorinators deployed and managed at-scale have the potential to elevate the quality of existing accessible and available water services to meet "safely managed" requirements.Entities:
Keywords: chlorine disinfection; drinking water treatment; low- and middle-income countries; passive in-line chlorination; resource-constrained settings; safely managed water supply
Mesh:
Substances:
Year: 2022 PMID: 35700262 PMCID: PMC9261193 DOI: 10.1021/acs.est.1c08580
Source DB: PubMed Journal: Environ Sci Technol ISSN: 0013-936X Impact factor: 11.357
Characteristics of Passive Chlorinators Identified in Literature Review and NGO Surveya
| passive chlorinator | chlorine dosing mechanism | flow regime | current system compatibility | dosing control mechanism | associated costs (USD, inflation adjusted) |
|---|---|---|---|---|---|
| Tablet | |||||
| ADEC Clorador/Adapted CTI-8*** | dissolution | gravity or pressurized | prior to storage tank | manual bypass valve | device: $150–200.00 |
| chlorine refill: 10 tablets
included in device cost[ | |||||
| A’jin Chlorinator*** (not reported) | dissolution | not reported (evaluation underway) | not reported (evaluation underway) | not reported (evaluation underway) | device: cost not reported, evaluation underway |
| AkvoTur (self-constructed) | dissolution | gravity | after storage tank, pretap | number of slits in the tablet chamber exposed | device:
$7.00[ |
| Arch Chemical Pulsar 1 (commercially available) | dissolution + Venturi | gravity or pressurized | not reported | manual bypass valve + internal slit position | no costs reported |
| Aquatabs Flo (commercially available) | dissolution | gravity | prior to storage tank | screw restricting outflow | device: $20.00[ |
| Aquatabs Inline*** (commercially available) | dissolution | gravity or pressurized | prior to storage tank or tap | manual bypass valve | device: $58.00[ |
| Aquaward (commercially available) | dissolution | gravity or pressurized | prior to storage tank | manual bypass valve | device: $608.35[ |
| chlorine dosing bucket (self-constructed) | dissolution | gravity | at the tap | manual bypass valve | device: $50.00[ |
| CTI-8 (self-constructed) | dissolution | gravity or pressurized | prior to storage tank | manual bypass valve | device: $267.06[ |
| device: $49.50[ | |||||
| floating chlorinator (not reported) | dissolution | N/A | floating in well or storage tank | no. of tablets, slit position | device:
$7.00[ |
| Fluidtrol Process Technologies Chlorinator (research grade) | dissolution | pressurized | prior to full distribution system | not reported | no costs reported |
| MINSA (Panama) chlorinator (self-constructed) | dissolution | gravity or pressurized | prior to storage tank | none | device: $32.95[ |
| device: $15.00[ | |||||
| Norweco (commercially available) | dissolution | gravity | prior to storage tank | manual bypass valve | eevice: $82.50[ |
| PurAll 50H (commercially available) | dissolution | gravity | handpumps | none | eevice: $60.00[ |
| PurAll 100 (commercially available) | dissolution | gravity or pressurized | prior to storage tank or tap | manual bypass valve | device: $662.00[ |
| installation: Cost of full installation + installation hardware included | |||||
| T-shaped erosion chlorinator (self-constructed) | dissolution | gravity or pressurized | prior to storage tank | manual bypass valve | no costs reported |
| Waterway + OceanBlue (commercially available) | dissolution | gravity | prior to storage tank | none | device: $168.24[ |
| Water Mission Erosion Chlorinator*** (commercially available) | dissolution | gravity or pressurized | not reported | linear flow control valve | no costs reported |
| Vulcano Code 102200*** (commercially available) | dissolution | gravity or pressurized | prior to storage tank | manual bypass valve | no costs reported |
| Water4 NuPump*** (not reported) | dissolution | not reported | not reported | not reported | no costs reported |
| Liquid | |||||
| AguaClara (research grade) | linear chemical dose controller[ | gravity | multi-stage water treatment plant | linear chemical
dose controller[ | device: $49063.00–83382.00[ |
| Blue Tap (research grade) | Venturi + patented hydraulic control | gravity or pressurized | prior to storage tank | needle valve regulator | device: $160 |
| Nirapad Pani (research grade) | suction | pressurized | handpump (inlet) | internal regulator | device: $26.12[ |
| Stanford-MSR Venturi (research grade) | Venturi | gravity or pressurized | at tap | needle valve regulator | device: $34.00[ |
| Zimba (commercially available) | suction | gravity | handpump | not reported | device: $112.16[ |
| Granular | |||||
| hypochlorinator (self-constructed) | dissolution | gravity or pressurized | prior to storage tank | manual bypass valve | no costs reported |
| pot chlorinator (self-constructed) | dissolution | N/A | floating in well or storage tank | none | device: $3.12[ |
An unnamed chlorinator evaluated by Ali et al.[35] was not included in the table because the device name was not reported or known by the original authors. The evaluation of this device is summarized in Table .
Chlorinators reported via a practitioner survey are indicated with asterisks (***).
Research grade specifically denotes a device that has only been designed or utilized within a research context. These devices are therefore not currently commercially available.
Evaluations Conducted on Passive Chlorinators Identified in Peer-Reviewed Literature
| effectiveness
metrics | |||||||
|---|---|---|---|---|---|---|---|
| chlorinator | evaluation reference | country | implementation scale | system type and location (within distribution or water delivery network) | population served | FCR(mg/L) mean (SD) [range] (%) sample target | FIB log reduction (%) sample target |
| Tablet | |||||||
| AkvoTur | Dossegger et al.[ | Uganda | communities | gravity-driven membrane filtration kiosks | not reported | 2.1 (0.5) [0.8–3.6] | not reported |
| 67% @ 1.5–2.5 | |||||||
| Arch Chemical Pulsar 1 | Fitzpatrick[ | Ghana | lab and noncommunity field site | N/A | N/A | [0.5–7.0] | not reported |
| With system modifications | |||||||
| Aquatabs Flo | Dossegger et al.[ | Uganda | communities | gravity-driven membrane filtration kiosks | not reported | 1.1 (0.6) [1.7–3.6] | not reported |
| 57% @ 1.5–2.5 | |||||||
| Voth-Gaeddert and Schrank[ | N/A | N/A | lab (flow rates 2–21 Lpm; modification for POU/POC) | N/A | Normal: [1.5 to >3.5] | not reported | |
| @ 2 Lpm 2.1 | |||||||
| @ 10 Lpm 2.3 | |||||||
| @ 18 Lpm 3.5 | |||||||
| modified for POU/POC: [0.3–2.3] | |||||||
| @ 2 Lpm 0.5 | |||||||
| @ 10 Lpm 0.3 | |||||||
| @ 18 Lpm 1.2 | |||||||
| Pickering et al.[ | Bangladesh | Urban compounds | Shared taps served via municipal piped supply | 50 communal water points | 0.33 (0.28) | 0.84 log | |
| 80% >0.1 | |||||||
| control: 5.49 CFU/100 mL | |||||||
| treatment: 0.8 CFU/100 mL | |||||||
| no E. coli detected in 85% of samples | |||||||
| Marcenac et al.[ | Tanzania | rural health care facilities | Rainwater harvest tank taps, standpipe taps, and elevated storage tank inlets | 9 healthcare Facilities | rainwater
harvest tank tap ( | not reported | |
| standpipe tap ( | |||||||
| elevated tank
inlet ( | |||||||
| Crider et al.[ | Nepal | rural community | at inlet of storage tank, predistribution network | 28 households | 74–86% > 0.1 | 1.02 log CFU | |
| upstream: 0.83 log CFU/100 mL | |||||||
| Smith et al.[ | Bangladesh | low-income informal housing settlements + middle-income apartments | at inlet of storage tank, predistribution network or tap | ∼65 landlords and respective housing units | 0.42 (0.48) | not reported | |
| 89% ≥0.1 | |||||||
| Aquaward | Brignoni[ | Puerto Rico | rural community | at inlet of storage tank, predistribution network | 1000 people | 1.06 [0.5–1.7] | total coliform % reduction: [75–100%] |
| initial total coliform concentration, pretreatment: 0–9000 cfu/100 mL | |||||||
| final total coliform concentration, post-treatment: 0–20 cfu/1000 mL | |||||||
| fecal coliform % reduction: [82–100%] | |||||||
| initial fecal coliform concentration, pretreatment: 0–110 cfu/100 mL | |||||||
| final fecal coliform concentration, post-treatment: 0–20 cfu/1000 mL | |||||||
| chlorine dosing bucket | Dossegger et al.[ | Uganda | communities | gravity-driven membrane filtration kiosks | not reported | 1.7 (0.9) [.3–3.5] | not reported |
| 40% @1.5–2.5 | |||||||
| CTI-8 | Taflin[ | Nicaragua + Guatemala | rural communities | at inlet of storage tank, predistribution network | 32 communities | not reported | not reported |
| EOS, Ministry of Health
report[ | Nicaragua | rural communities | at inlet of storage tank, predistribution network | 21 communities | not reported | not reported | |
| CTI report[ | Nicaragua | rural communities | at inlet of storage tank, predistribution network | 70 communities | not reported | not reported | |
| floating chlorinator | Dossegger et al.[ | Uganda | communities | gravity-driven membrane filtration kiosks | not reported | 1.5 (0.9) [0.1–3.1] | not reported |
| 37% @ 1.5–2.5 | |||||||
| Garandeau et al.[ | Liberia | internally displaced persons camp | floating in well | not reported | [0.2–1.0] (modified floating chlorinator) | not reported | |
| Fluidtrol Process Technologies Chlorinator | Martin[ | Haiti | large community | predistribution network (not specified) | 3000 | 69% >0.5 | not reported |
| MINSA (Panama) Chlorinator (“T-Chlorinator”) | Orner et al.[ | Panama | rural indigenous community | at inlet of storage tank, predistribution network | 325 people | 1 tablet: [0.02–0.24]** | not reported |
| 3 tablets: [0.02–0.44] | |||||||
| Yoakum[ | Panama | rural indigenous community | at inlet of storage tank, predistribution network | 183 people | 2 tablets: [0.02–0.2]** | not reported | |
| 3 tablets: [0.27–0.63] | |||||||
| Dossegger et al.[ | Uganda | communities | gravity-driven membrane filtration kiosks | not reported | 2.0 (0.3) [1.1–3] | not reported | |
| 90% @ 1.5–2.5 | |||||||
| Norweco | Rayner et al.[ | Haiti | natural disaster/complex emergency, community setting | at inlet of storage tank, predistribution network | not reported | 0% detectable chlorine | 28% <1 CFU |
| 47% 1–10 CFU | |||||||
| 23% 11–100 CFU | |||||||
| 2% 101–1000 CFU | |||||||
| PurAll 50H | Sikder et al.[ | Cox’s Bazaar, Bangladesh | 2 refugee camps | shared handpump | 44000 | 0.9 (1.3) | 89% <10 CFU/100 mL |
| 44% > 0.2 | |||||||
| PurAll 100 | Crider et al.[ | Nepal | rural community | at inlet of storage tank, predistribution network | 27 households | 90–100% >0.1 | 1.32 log CFU |
| upstream: 1.02 log CFU/100 mL | |||||||
| T-Shaped Erosion Chlorinator | Henderson
et al.[ | Honduras | rural communities | at inlet of storage tank, predistribution network | 5 communities | 1.2 (0.06) ** | not reported |
| 90.3% >0.2 | |||||||
| Waterway + OceanBlue | Blair et al.[ | Dominican Republic | rural community | in-line prestorage tank | not reported | [0.05–1.74] | not reported |
| Ngo et al.[ | Dominican Republic | rural community | in-line prestorage tank | not reported | [0.62–1.89] * | not reported | |
| Liquid | |||||||
| AguaClara | Brooks et al.[ | Honduras | large communities (5) | full scale water treatment plant | 11400 (total) | 5 separate AguaClara systems:* | 5 separate AguaClara systems:* |
| 0.9 | |||||||
| 0.14 | >99.5% | ||||||
| 0.01 (limit of detection, system was not chlorinating during study period) | >99.0% | ||||||
| >97.6% | |||||||
| >97.8% | |||||||
| >91.5% | |||||||
| 0.27 | initial | ||||||
| 0.2 | |||||||
| final | |||||||
| Nirapad Pani | Pickering et al.[ | Bangladesh | urban compounds | at inlet of storage tank | 10 compounds (average 19 households/compound) | 0.66 (0.57) | 78% <1 CFU |
| 80% >0.2 | |||||||
| Stanford-MSR Venturi | Powers et al.[ | Kenya | rural and urban communities | at the tap of community water kiosks | not reported | 0.55 (0.29) | not reported |
| [0.0–1.59] | |||||||
| 88% >0.2 | |||||||
| 86.2% @ 0.2–1.2 | |||||||
| Zimba | Amin et al.[ | Bangladesh | neighborhoods (6) | shared handpumps | not reported | 1.3 (0.54) | 0.43 log CFU |
| 100% @ 0.2–2.0 | |||||||
| Control: 3.47 CFU/100 mL | |||||||
| Treatment: 1.29 CFU/100 mL | |||||||
| 72% < 1 CFU | |||||||
| un-named liquid chlorinator | Ali et al.[ | South Sudan | refugee camps (3) | in-line, pre storage tank | camp 1: 15500 | camp 1: 0.9 (1.2) [0.01–4.60] | not reported |
| camp 2: 37200 | camp 2: 1.2 (0.3) [0.6–2.3] | ||||||
| camp 3: 15800 | camp 3: 1.4 (1.2) [0.1–5.2] | ||||||
| Granular | |||||||
| hypochlorinator | Henderson et al.[ | Honduras | rural communities | at inlet of storage tank, predistribution network | 8 communities | 0.67 (0.50) | not reported |
| pot chlorinator | Cavallero et al.[ | Guinea Bissau | cholera outbreak, community | suspended in well | 6 neighborhoods | 24 h post-installation: 62% @ 0.2–5.0 | not reported |
| 48 h: 15% @ 0.2–5.0 | |||||||
| 72 h: 4% @ 0.2–5.0 | |||||||
| Garandeau et al.[ | Liberia | internally displaced persons camp | suspended in well | not reported | [0–10] | not reported | |
Free chlorine values are typically reported in the following format: mean (sd) [range], % at target value, in mg/L. E. colimeasurements are typically reported in the following format: log reduction, % within target range cfu/100 mL or [range of % reduction]. Log reduction is calculated as follows: log reduction = log10(initial concentration of bacteria/final concentration of bacteria). % reduction is calculated as follows: % reduction = (initial concentration of bacteria-final concentration of bacteria) × 100/initial concentration of bacteria.
Testing of an early Stanford-MSR Venturi prototype doser in Dossegger et al.[21] was not included in this table. Evidence from the paper suggests that it was installed incorrectly with operational flows below the intended flow rates.
Blair et al.[29] and Ngo et al.[47] evaluated two types of chlorinators, but the results were reported in aggregate for both chlorinators.
Evaluations where water samples for FCR andE. coli were not from the POC are denoted by *(POU samples) and **(storage tank samples, upstream of POC).
Figure 1Pathways to address the current limitations of passive chlorination and achieve expected outcomes at scale. The scaling framework suggests methods to strengthen chlorine supply chains, develop and evaluate financial and business models, apply remote sensing and monitoring technologies, and improve chlorine dosing.
Recommended Standard Indicators for Reporting Future Evaluations of Passive Chlorinatorsa
Legend: (*) all of the recommended indicators may not be relevant for every evaluation or study; (**) although we recommend measuring user satisfaction as an indicator, we recognize that user and operator surveys may not always be feasible and thus will be a lower priority in some cases.