Water is vital for human life, socioeconomic development, and environmental conservation. Access to safe drinking water and sanitation is a human right recognized by the United Nations’ 2030 Agenda in its Sustainable Development Goal No. 6. In this context, fluoride in groundwater at concentrations of 0.6–0.9 mg L−1 is essential for dental health. However, at higher levels (>1.5 mg L−1), it is harmful to health. Thus, this study evaluated the removal of excess fluoride from groundwater in defluoridation systems installed in rural schools using activated bone charcoal as an adsorbent. The performance results of the campus defluoridation system indicate that the system can meet the consumption needs of a school with up to 39 people consuming 2 L day−1, with a minimum flow rate of 3.3 L h−1, for a minimum period of 90 days. Regarding the efficiency of fluoride removal from water in rural schools A, B, and C, the results indicated a value higher than 97%, meeting potability standards. The technology is sustainable, improves sanitation conditions, and ensures safe and accessible drinking water for all.

  • In southern Brazil, specifically in the central region of Rio Grande do Sul, groundwater has high fluoride concentrations.

  • Bone charcoal is an effective adsorbent in water defluoridation.

  • The efficiency in removing fluoride from water in rural schools A, B, and C, the results indicated a value greater than 97%.

  • The economic viability of adsorption technology contributes to improving sanitation in rural schools.

Water is essential for human life, socioeconomic development, and environmental protection. However, population growth in recent decades, climate change, and inefficient natural resource management have raised global concerns about water resource availability (Mujtaba et al. 2024). Among the 17 Sustainable Development Goals (SDGs) of the UN Agenda, SDG 6 aims explicitly to ensure safe drinking water and sanitation by 2030 (Shaji et al. 2024).

In this context, fluoride in groundwater at concentrations of 0.6–0.9 mg L−1 is essential for dental and bone health (State Health Department 1999). However, at elevated levels (>1.5 mg L−1), it is harmful to health (Protocol GM/MS N° 888 2021), causing problems such as skeletal and dental fluorosis, increased insulin resistance, decreased estrogen and testosterone levels, and neurological damage (Rathnayake et al. 2022; Gu et al. 2024).

Fluoride is naturally found in groundwater, and contamination occurs due to volcanic eruptions, atmospheric deposition, and the dissolution of fluoride-containing rocks (Lacson et al. 2021; Tong et al. 2023). Fluoride in water can also be attributed to human activities through industrial emissions, fertilizers, and waste disposal (El Messaoudi et al. 2024).

Thus, the World Health Organization (WHO 2011) has set the maximum acceptable fluoride limit for drinking water at 1.5 mg L−1 (Lacson et al. 2021). The United States Environmental Protection Agency (USEPA) has set it at 2.0 mg L−1 (Podgorski & Berg 2022), the European Union (EU) between 0.7 and 1.5 mg L−1 (Deng et al. 2024), and in China, the maximum allowed fluoride concentration in drinking water is 1.0 mg L−1 (Tong et al. 2023).

In Rio Grande do Sul, particularly in the central region, in the municipalities of Restinga Seca, Agudo, Paraíso do Sul, and Novo Cabrais, high fluoride concentrations have been observed in groundwater, with values of 5.6, 4.2, 5.0, and 3.6 mg L−1, respectively (Luiz et al. 2018).

Due to the adverse effects caused by elevated fluoride levels, removing fluoride from groundwater and surface water has been a challenge in water resource management (Mohandas et al. 2023). Various technologies for drinking water treatment have been proposed for defluoridation, such as adsorption, biosorption, ion exchange, coagulation/precipitation, membrane processes (reverse osmosis and nanofiltration), electrodialysis, electrocoagulation (Halder et al. 2023; Shaji et al. 2024), and phytoremediation (Weerasooriyagedara et al. 2020). Adsorption for fluoride removal using activated bone charcoal offers the best cost–benefit ratio (Lacson et al. 2021) due to its simple operation and wide availability of adsorbents (Kimambo et al. 2019). It allows the development of sustainable, low-cost, and easily maintained technologies, which are also innovative for implementation in emerging countries to ensure drinking water safety (Gao et al. 2022; Medellín Castillo et al. 2023; Shimabuku et al. 2023).

Therefore, this study aimed to evaluate the defluoridation system of groundwater in rural schools of the Taquari-Antas Watershed in the municipality of Venâncio Aires, RS, Brazil, using activated bone charcoal as the adsorbent medium, applying a sustainable, low-cost technology that is easy to implement, operate, and maintain.

Materials and methods

Data collection on the number of students, teachers, administrative staff, collection points, water consumption sources, and water supply networks was conducted in collaboration with the school administrations through the Department of Education of Venâncio Aires, RS, Brazil. Five rural schools (A–E) were pre-selected. After sample collection and analysis of all institutions' natural water supply networks, only three rural schools (A, B, and C) showed concentrations exceeding the maximum permitted in Rio Grande do Sul, Brazil (State Health Department 1999).

Defluoridation systems for groundwater were constructed and installed, using activated bone charcoal as the adsorbent (20 × 50 mesh, internal surface area of 120 m2 g−1, pore size range from 7.5 to 60,000 nm), acquired from Bonechar (Carvão Ativado do Brasil LTDA, Maringá, Brazil).

Description of the study area

The Taquari-Antas is a sub-watershed located within the hydrographic region of the Guaíba watershed, RS, covering an area of 26,430 km2 and with an estimated population of 1,383,442 inhabitants (2020), including 1,081,261 in urban and 302,181 in rural areas (SEMA 2024).

Venâncio Aires belongs to the Taquari-Antas watershed, with a total area of 773.2 km2 (SEMA 2024). It is located in the central-eastern mesoregion of Rio Grande do Sul and in the Santa Cruz do Sul microregion, between the Rio Pardo Valley and Taquari Valley (IBGE 2024). The study area consists of rural schools A, B, and C, as shown in Figure 1, developed using QGIS software version 3.24.
Figure 1

Area of rural schools A, B, and C in Venâncio Aires, RS, Brazil, where the public water supply defluoridation systems were installed.

Figure 1

Area of rural schools A, B, and C in Venâncio Aires, RS, Brazil, where the public water supply defluoridation systems were installed.

Close modal

Sizing of the defluoridation system

The groundwater defluoridation system was sized for installation at the point of consumption to remove excess fluoride only from direct consumption water. Thus, the daily water consumption volume, the initial fluoride concentration in natural water, and activated bone charcoal adsorption capacity were considered. Other relevant considerations for sizing are the following:

  • I. The activated bone charcoal used in the filter has the following specifications: 20 × 50 mesh, density of 0.675 g, porosity of 65%, and adsorption capacity of 1,200 mg kg−1.

  • II. The full concentration of fluoride ions in natural water is 4.0 mg L−1.

  • III. The contact time ranges from 8.5 to 250 min, with the ideal time being 60 min (Fo = 1).

Equations (1)–(3) were applied to quantify the minimum flow rate of the supply system (Qmin), the total volume of treated water (Vt), and the removed fluoride load, respectively:
(1)
where Qmin is the minimum flow rate (L h−1); N is the total number of consumers; D is the daily consumption per capita (L); and 24 represents h day−1:
(2)
where Vt is the volume of treated water (L); N is the total number of consumers; D is the daily consumption per capita (L); and T is the operating time (days):
(3)
where Load is the removed fluoride load (mg); Vt is the volume of treated water (L); Fi is the initial fluoride concentration (mg L−1); and Ft is the final fluoride concentration (mg L−1).

Based on all considerations, calculations were performed to size the groundwater defluoridation systems for schools (A, B, and C), as shown in Table 1. To meet the needs of rural schools, the system was designed with the premise of a daily consumption of 2 L day−1 per consumer and an average fluoride concentration of 0.8 mg L−1. The estimated mass of activated bone charcoal ranged from 5 to 12 kg, covering 4,320 to 7,020 L of defluoridated water. Thus, the rural schools' defluoridation systems were sized with 14 kg of activated bone charcoal.

Table 1

Calculations for sizing groundwater defluoridation systems for schools A, B, and C

SizingSymbolUnitRural schools
ABC
Operation conditions Total consumers N  31 24 39 
Per capita daily consumption D 
Minimum flow Qmin L h−1 2.6 2.0 3.3 
Operating time (cycle) T days 90 90 90 
Volume of water treated Vt 5,580 4,320 7,020 
Initial concentration (FFi mg L−1 2.51 2.24 2.85 
Final concentration (FFt mg L−1 0.8 0.8 0.8 
Characteristics Removed fluoride load Load mg 9,542 6,221 14,391 
Minimum contact time Tc min 60 60 60 
Adsorption capacity Qa mg kg−1 1,200 1,200 1,200 
Porosity P  0.65 0.65 0.65 
Density D kg L−1 0.675 0.675 0.675 
Operation factor Fo  1.0 1.0 1.0 
Results Coal mass M kg 12 
Column volume CV 12 18 
SizingSymbolUnitRural schools
ABC
Operation conditions Total consumers N  31 24 39 
Per capita daily consumption D 
Minimum flow Qmin L h−1 2.6 2.0 3.3 
Operating time (cycle) T days 90 90 90 
Volume of water treated Vt 5,580 4,320 7,020 
Initial concentration (FFi mg L−1 2.51 2.24 2.85 
Final concentration (FFt mg L−1 0.8 0.8 0.8 
Characteristics Removed fluoride load Load mg 9,542 6,221 14,391 
Minimum contact time Tc min 60 60 60 
Adsorption capacity Qa mg kg−1 1,200 1,200 1,200 
Porosity P  0.65 0.65 0.65 
Density D kg L−1 0.675 0.675 0.675 
Operation factor Fo  1.0 1.0 1.0 
Results Coal mass M kg 12 
Column volume CV 12 18 

Sample collection followed the Standard methods for the examination of water and wastewater guidelines (Miner 2006). The initial water flow was discarded at a slow rate for 2 min. Then, 500 mL of water was collected in a polypropylene (PP) bottle, stored in thermal boxes with ice, and transported to the laboratory for analysis, following APHA guidelines.

Although the maximum fluoride limit in public water supply is 1.5 mg L−1 according to the WHO (2011) and the GM/MS Protocol No. 888 (2021), for this study, the maximum in treated water was set at 0.9 mg L−1. This value corresponds to the maximum limit stipulated by the legislation of the State of Rio Grande do Sul, which determines the range of 0.6–0.9 mg L−1 as ideal for dental and bone health (State Health Department 1999). Thus, for the dimensioning of this system, the ideal value (final concentration) was determined to be 0.8 mg L−1.

Structuring the assembly of the defluoridation system

Based on the data collected during the sizing stage, the defluoridation system was structured to treat water at the point of consumption, considering the flow of visitors in the schools and the possibility of increasing the number of consumers. Thus, the defluoridation system was assembled using 14 kg of activated bone charcoal (with a particle diameter of 20 × 50 mesh) in fiberglass-reinforced polymer (FRP) tanks of 7″ × 44″, as shown in Figure 2, with a volumetric capacity of 24.3 L. A manual three-way valve controlled the water flow. An auxiliary 5″ filter with a 1 μm filter element completed the treatment process. The description of the components, purpose, and quantity of the groundwater defluoridation system are given in Supplementary material 1.
Figure 2

Structure of the groundwater defluoridation system installed in schools A, B, and C.

Figure 2

Structure of the groundwater defluoridation system installed in schools A, B, and C.

Close modal

Identical defluoridation systems were structured, with one unit installed to perform preliminary tests on the University of Santa Cruz do Sul (UNISC) campus and the other units in rural schools (A, B, and C).

Defluoridation system diagnostics

The defluoridation system was evaluated in three stages. In the first stage, the equilibrium time in the adsorption process and the adsorption capacity were determined in bench tests using a jar test agitator (Quimis, model Q-305D23, Diadema, SP, Brazil). In the second stage, a prototype of the defluoridation system was installed and monitored on the UNISC campus. In the third stage, the defluoridation systems were installed in the three rural schools and continuously monitored to assess the efficiency of the treated water under actual usage conditions.

Bench tests

The tests were conducted with samples of activated bone charcoal with a particle diameter of 20 × 50 mesh, which were previously dried in an oven (Quimis, model Q-317B-22, Diadema, SP, Brazil) at 100 °C for 3 h. The evaluation was done with three distinct bench tests (1, 2, and 3). In tests 1 and 2, naturally fluoridated water was used, with a fluoride concentration of 2.24 mg L−1, using 2 g (test 1) and 4 g (test 2) of activated bone charcoal, respectively. For test 3, an artificially fluoridated solution was prepared using deionized water and sodium fluoride P.A. (NaF) (Nuclear brand, Diadema, SP, Brazil), with a fluoride concentration of 2.9 mg L−1 and 2 g of activated bone charcoal. The three adsorption tests were monitored for 480 min in a jar test at 120 rpm.

The equilibrium time of the adsorption process was determined through the adsorption kinetics curve, which corresponds to the point where no significant reduction in the fluoride concentration in the solution is observed. The adsorption capacity of activated bone charcoal in g−1 was calculated according to Equation (4):
(4)
where CA is the adsorption capacity (mg g−1); C0 is the initial fluoride concentration (mg L−1); Ci is the final fluoride concentration (mg L−1); V is the volume of treated water (L); and M is the weight of activated bone charcoal (g).

Campus defluoridation system prototype

The prototype of the defluoridation system was installed on the UNISC campus. It was monitored daily for 25 days until the fluoride concentration in the treated water reached values equal to that of the natural water (meaning the complete saturation of the adsorbent medium). Thus, the lifespan of this prototype was established when the filtered water results reached fluoride concentration values greater than 0.9 mg L−1.

Rural school defluoridation systems

The defluoridation systems were structured with all the necessary components for assembly, using 14 kg of activated bone charcoal, and installed and monitored in the rural schools (A, B, and C) through physicochemical, pH, turbidity, total dissolved solids (TDS), and fluoride analysis for 60 days.

Comparison of defluoridation systems in the global context

Due to the effects on human health caused by high fluoride concentrations, removal from groundwater has been a challenge in water resource management (Mohandas et al. 2023). Thus, traditional and effective techniques for water defluoridation, such as adsorption, biosorption, ion exchange, precipitation, membrane processes (reverse osmosis and nanofiltration), electrodialysis, and electrocoagulation are managed. Some techniques have disadvantages; for example, the ion exchange process has been tested in India, and it has been shown that its efficiency is affected by other ions such as carbonate, sulfate, alkalinity, and phosphate. In addition, it is not economically viable due to the high cost of synthetic resins. Nanofiltration is highly efficient at removing excess fluoride from water, while membrane separation technology removes high levels of ions, some of which are vital for human health (Halder et al. 2023). Compared with existing studies, among the technologies mentioned, in the global context, adsorption on activated bone carbon presents the best cost–benefit ratio (Lacson et al. 2021), allowing for the development of low-cost, sustainable technologies that are easy to maintain and innovative enough to be implemented in emerging countries (Medellín Castillo et al. 2023).

Kinetic study and adsorption mechanism of bench tests

Table 2 presents the values obtained in the bench tests. Figures 3 and 4 show the graphs of the adsorption kinetics and capacity of activated bone charcoal, respectively.
Table 2

Results of the bench tests for determining activated bone charcoal kinetics and adsorption capacity

AssayTime (min)
01020406090120240300360420480
 Fluoride concentration, mg L−1 
2.24 2.12 2.03 1.94 1.91 1.85 1.79 1.54 1.52 1.46 1.43 1.35 
2.24 1.99 1.91 1.76 1.68 1.54 1.49 1.20 1.15 1.05 0.99 0.92 
2.90 2.66 2.60 2.52 2.47 2.35 2.23 1.83 1.69 1.61 1.48 1.39 
 Adsorption capacity, mg g−1 
0.000 0.061 0.104 0.150 0.164 0.198 0.229 0.350 0.361 0.389 0.407 0.446 
0.000 0.062 0.082 0.121 0.141 0.175 0.189 0.260 0.273 0.298 0.314 0.331 
0.000 0.121 0.150 0.190 0.216 0.279 0.337 0.537 0.606 0.649 0.712 0.759 
AssayTime (min)
01020406090120240300360420480
 Fluoride concentration, mg L−1 
2.24 2.12 2.03 1.94 1.91 1.85 1.79 1.54 1.52 1.46 1.43 1.35 
2.24 1.99 1.91 1.76 1.68 1.54 1.49 1.20 1.15 1.05 0.99 0.92 
2.90 2.66 2.60 2.52 2.47 2.35 2.23 1.83 1.69 1.61 1.48 1.39 
 Adsorption capacity, mg g−1 
0.000 0.061 0.104 0.150 0.164 0.198 0.229 0.350 0.361 0.389 0.407 0.446 
0.000 0.062 0.082 0.121 0.141 0.175 0.189 0.260 0.273 0.298 0.314 0.331 
0.000 0.121 0.150 0.190 0.216 0.279 0.337 0.537 0.606 0.649 0.712 0.759 
Figure 3

Adsorption kinetics results from tests 1, 2, and 3.

Figure 3

Adsorption kinetics results from tests 1, 2, and 3.

Close modal
Figure 4

Adsorption capacity (Q) results from tests 1, 2, and 3.

Figure 4

Adsorption capacity (Q) results from tests 1, 2, and 3.

Close modal

The results indicate that the equilibrium time for the adsorption process occurs after 360 min of contact. It is observed that in the artificial sample (test 3), the adsorption process extends until the end of the contact time of the tests.

Considering the principle of adsorption (Costa et al. 2013; El Messaoudi et al. 2024), which involves adsorbate ions on solid surfaces, reducing the concentration in water, the results in this study showed maximum adsorption capacity values of 0.446, 0.331, and 0.759 mg g−1 for tests 1, 2, and 3, respectively (Table 2).

Prototype defluoridation system diagnostics on campus

Table 3 presents the operational results of the defluoridation system.

Table 3

Operational results of the defluoridation system

General propertiesUnitResults
Coal mass kg 14 
Total volume of filtered water 11,048 
Average filtration flow L h−1 7.9 ± 18.1 
Total testing time 147 
Total volume of filtered water up to a limit of 0.9 mg L−1 7,099 
Adsorption capacity up to a limit of 0.9 mg L−1 mg kg−1 1,096 
Adsorption capacity up to a limit of 0.9 mg L−1 mg kg−1 1,286 
General propertiesUnitResults
Coal mass kg 14 
Total volume of filtered water 11,048 
Average filtration flow L h−1 7.9 ± 18.1 
Total testing time 147 
Total volume of filtered water up to a limit of 0.9 mg L−1 7,099 
Adsorption capacity up to a limit of 0.9 mg L−1 mg kg−1 1,096 
Adsorption capacity up to a limit of 0.9 mg L−1 mg kg−1 1,286 

Figure 5 presents the results of the monitoring of natural and filtered water, showing that the fluoride concentration in natural water had an average value of 2.41 ± 0.20 mg L−1 (n = 19), which is 2.7 times the maximum state-permitted value (State Health Department 1999), of 0.9 mg L−1, and 1.6 times the maximum limit established by federal regulations (Protocol GM/MS N° 888 2021), as well as by the WHO (2011) of 1.5 mg L−1 of fluoride, for potable water standards.
Figure 5

Results of the monitoring of fluoride concentration from the campus prototype defluoridation system. The dotted line indicates the maximum permissible value (MPV = 0.9 mg L−1).

Figure 5

Results of the monitoring of fluoride concentration from the campus prototype defluoridation system. The dotted line indicates the maximum permissible value (MPV = 0.9 mg L−1).

Close modal

The results obtained from the filtered water show an immediate reduction in fluoride concentration, maintaining below 0.1 mg L−1 until reaching 4,300 L of treated water. Fluoride concentration increased in the filtered water, reaching 0.9 mg L−1 with 7,100 L of treated water.

The filtration process continued to be monitored until the fluoride concentration in the water reached values equivalent to those of the natural water, indicating the complete saturation of the adsorbent medium. However, this prototype's lifespan was determined when the fluoride concentration in the filtered water exceeded 0.9 mg L−1, indicating the saturation of the adsorbent medium. At this point, the ratio Ci/C0 corresponded to approximately 0.39, where C0 is the initial average fluoride concentration (2.41 ± 0.20 mg L−1, n = 19) and Ci is the fluoride concentration at time i (0.9 mg L−1). Thus, the lifespan of this system is reached after the filtration of 7,100 L of natural water (Ci of 2.41 ± 0.20 mg L−1; n = 19). The breakthrough point was reached after the filtration of 4,300 L. At that point, Ci/C0 = 0.1, i.e., when the fluoride concentration in the treated water reached 10% of the initial concentration (C0).

The performance of the campus defluoridation system aligns with the design for the sizing, intended for the consumption of a school unit with up to 39 people consuming 2 L day−1 for a minimum period of 90 days.

The results of monitoring pH, turbidity, and TDS by the campus prototype of the defluoridation system are presented in Figure 6 for both natural and filtered water.
Figure 6

pH, turbidity, and TDS results from the campus prototype defluoridation system. The dotted line indicates the maximum permissible value (MPV = 0.9 mg L−1).

Figure 6

pH, turbidity, and TDS results from the campus prototype defluoridation system. The dotted line indicates the maximum permissible value (MPV = 0.9 mg L−1).

Close modal

The evaluation of the monitoring of natural water indicates alkaline properties (pH = 9.0 ± 0.1, n = 18), absence of turbidity (<0.05, n = 18), and an average TDS concentration of 340 ± 27 mg L−1, n = 18. In the filtered water, an initial increase in alkalinity was observed due to the alkaline properties of the adsorbent medium, activated bone charcoal. This pH increase is due to the natural water having high values, as evidenced by the results at the beginning of the filtration process. At the beginning of the filtration process, the TDS concentration is above the maximum allowable limit (Protocol GM/MS N° 888 2021). This occurs due to the leaching of dissolved salts in the activated bone charcoal. As for the turbidity results, only in the first sampling were the values above the maximum permissible value (MPV), corresponding to when the defluoridation system was installed (State Health Department 1999).

Upon reaching a volume of 1,218 L of filtered water from the campus prototype defluoridation system, natural and filtered water samples were collected and analyzed as stipulated in Protocol GM/MS N° 888 (2021). The results are presented in Supplementary material 2.

The results showed that pH (9.35) and ammonia concentration (1.7 mg L−1) did not comply with Protocol GM/MS N° 888 (2021). As previously discussed, the alkaline properties of the natural water and the adsorbent medium resulted in filtered water with values close to the permissible limit for public water supply. This interference in pH at high levels in the natural water is minimized using the defluoridation system.

The ammonia results (1.7 mg L−1) in the filtered water exceeded the maximum permissible limit set by Protocol GM/MS N° 888 (2021) of 1.2 mg L−1, while (WHO 2011) considers that groundwater can have concentrations of up to 3 mg L−1, as ammonia in water is due to bacterial contamination, effluents, or animal excrement (Seben et al. 2021).

Diagnostics of defluoridation systems in rural schools

The monitoring results of the defluoridation systems indicated average fluoride values in the natural water supplying schools A, B, and C of 2.6 ± 0.29 mg L−1, n = 13, 2.4 ± 0.20 mg L−1, n = 10, and 3.3 ± 0.14 mg L−1, n = 14, respectively. After filtration, the average values were less than 0.1 mg L−1. The operational data of the system can be viewed in Supplementary material 3.

The results of fluoride concentration in the natural water of the rural schools show high values, with rural school C presenting the highest values (3.4 ± 0.1 mg L−1; n = 14), corresponding to 3.8 times the MPV (0.9 mg L−1) (State Health Department 1999).

In Protocol GM/MS N° 888 (2021), the MPV for fluoride is 1.5 mg L−1, 2.3 times the maximum limit. The natural occurrence is due to the interaction and weathering between water and rocks. Seben et al. (2022) reported a variation of 0.8–39.5 mg L−1 in fluoride concentration in groundwater in Malawi, Africa. Similar results have been reported in other studies in which other techniques were used for defluoridation (Hadoudi et al. 2023). Thus, the chemical processes involved in fluoride removal are complex and have been widely studied in research (Zaki et al. 2023).

The evaluation of fluoride concentration in the filtered water showed values below 0.1 mg L−1 throughout the monitoring period of the defluoridation systems. The volumes of filtered water in rural schools A, B, and C were 5,660, 2,612, and 4,805 L, respectively. This variation is due to the number of consumers, 31, 24, and 39, respectively, over 60 days. The defluoridation efficiency results were >97.4, >98.3, and >97.6%, respectively. The average results were above 97%, guaranteeing the supply of water with fluoride levels suitable for human consumption. More recent innovations in water treatment technology have shown excellent results, with 90–100% removal of fluoride from groundwater (Fraiha et al. 2024).

Although the State Health Department (1999) defines acceptable fluoride concentration levels in the water supply to be between 0.6 and 0.9 mg L−1, the near-complete removal of fluoride by defluoridation systems does not compromise the water's potability standards. The sustainability of these systems is of great importance, especially in rural areas, as highlighted in recent research (Hadoudi et al. 2021).

Implementing large-scale defluoridation systems is challenging, but they can be scaled up regionally and nationally. However, installation and operating costs must be considered, as well as the replacement of activated bovine bone charcoal and parts and equipment used to size the system.

The long-term viability and maintenance requirements of defluoridation systems in areas with limited resources involve various factors, such as operating costs, financial resource availability, infrastructure, maintenance, and adsorbent material supply. Simpler technologies, such as adsorption with cheap and easily accessible materials, tend to be more viable in resource-limited locations, although they still require ongoing attention to ensure safe and efficient operation.

The study on the defluoridation system, using activated bone charcoal as the adsorbent medium, provided promising information for implementing effective and sustainable methods in groundwater treatment.

The performance results of the campus defluoridation system aligned with the sizing structure. Thus, this system can meet the consumption needs of a school with up to 39 people consuming 2 L day−1, with a minimum flow rate of 3.3 L h−1, for a minimum period of 90 days.

This study demonstrates the removal of excess fluoride from natural water using activated bone charcoal as the adsorbent and its adsorption efficiency in rural schools A (>97.4%), B (>98.3%), and C (>97.6%) throughout the entire operation period, meeting potability standards.

The adsorption process for removing fluoride ions is the most sustainable method due to its main characteristics: practicality, wide availability of adsorbents, efficiency in removing fluoride ions, operational cost feasibility, and sustainability. Indeed, the system developed by adsorption with activated bone charcoal presented an investment cost of US$115.

The adsorption system for groundwater defluoridation implemented in this study features an easy-to-apply technology. It is low cost to implement, operate, and maintain, contributing to improving sanitation conditions in rural schools.

The authors thank the National Council for Scientific and Technological Development (CNPQ) – protocols 306216/2022-1 and 302816/2023-2, Coordination for the Improvement of Higher Education Personnel (CAPES) – code 001, 88881.710390/2022-1, Senai Institute of Leather and Environmental Technology, and Philip Morris Brasil.

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

The authors declare there is no conflict.

Costa
A. B. D.
,
Lobo
E. A.
,
Soares
J.
&
Kirst
A.
(
2013
)
Desfluoretação de águas subterrãneas utilizando filtros de carvão ativado de osso
,
Águas Subterrâneas
,
27
(
3
).
doi:10.14295/RAS.V27I3.27382
.
Deng
L.
,
Wang
Y.
,
Yang
H.
,
Zhang
R.
&
Huang
T.
(
2024
)
New insights into defluoridation via induced crystallization: Implications of phosphate species regulation for process efficiency and economics
,
Separation and Purification Technology
,
348
,
127706
.
doi:10.1016/J.SEPPUR.2024.127706
.
El Messaoudi
N.
,
Franco
D. S. P.
,
Gubernat
S.
,
Georgin
J.
,
Senol
Z. M.
,
Cigeroglu
Z.
,
Allouss
D.
&
El Hajam
M.
(
2024
)
Advances and future perspectives of water defluoridation by adsorption technology: A review
,
Environmental Research
,
252
(
PT 1
),
118857
.
doi:10.1016/J.ENVRES.2024.118857
.
Fraiha
O.
,
Hadoudi
N.
,
Najlae
Z.
,
Salhi
A.
,
Amhamdi
H.
,
Mourabit
F.
&
Ahari
M. H.
(
2024
)
Comprehensive review on the adsorption of pharmaceutical products from wastewater by clay materials
,
Desalination and Water Treatment
,
317
,
100114
.
Gao
Y.
,
You
K.
,
Fu
J.
,
Wang
J.
&
Qian
W.
(
2022
)
Manganese modified activated alumina through impregnation for enhanced adsorption capacity of fluoride ions
,
Water
,
14
(
17
), 2673.
doi:10.3390/W14172673
.
Gu
M.
,
Wu
Y.
,
Jiang
Z.
&
Xu
H.
(
2024
)
Integrated method for grading diagnosis of dental fluorosis combined with segmentation and classification
,
Biomedical Signal Processing and Control
,
96
,
106510
.
doi:10.1016/J.BSPC.2024.106510
.
Hadoudi
N.
,
Amhamdi
H.
&
Ahari
M. H.
(
2021
) ‘
Sorption of bisphenol A from aqueous solutions using natural adsorbents: Isotherm, kinetic and effect of temperature
',
E3S Web of Conferences, EDP Sciences
.
Hadoudi
N.
,
Charki
A.
,
El Ouarghi
H.
,
Salhi
A.
&
Amhamdi
H.
(
2023
)
Sorption of bisphenol A from aqueous solutions by acid activated bentonite clay
,
Desalination and Water Treatment
,
285
,
121
128
.
Halder
S.
,
Maiti
P.
,
Karmakar
S.
,
Roy
M. B.
&
Roy
P. K.
(
2023
)
Enhanced fluoride removal from groundwater using red and white kaolinite lithomarge to develop a low cost eco-friendly defluoridation unit in rural areas of Shilabati River Basin, West Bengal
.
Journal of Water Process Engineering
,
53
,
103698
.
https://doi.org/10.1016/J.JWPE.2023.103698
.
IBGE
(
2024
)
Instituto Brasileiro de Geografia E Estatística – Venâncio Aires. Retrieved from 23 January 2024. Available at: https://cidades.ibge.gov.br/brasil/rs/venancio-aires/panorama.
Kimambo
V.
,
Bhattacharya
P.
,
Mtalo
F.
,
Mtamba
J.
&
Ahmad
A.
(
2019
)
Fluoride occurrence in groundwater systems at global scale and status of defluoridation – State of the art
,
Groundwater for Sustainable Development
,
9
,
100223
.
doi:10.1016/J.GSD.2019.100223
.
Lacson
C. F. Z.
,
Lu
M.-C.
&
Huang
Y.-H.
(
2021
)
Fluoride-containing water: A global perspective and a pursuit to sustainable water defluoridation management – An overview
,
Journal of Cleaner Production
,
280
,
124236
.
https://doi.org/10.1016/J.JCLEPRO.2020.124236
.
Luiz
T. B. P.
,
Silva
J. L. S.
&
Filho
L. L. V. D.
(
2018
)
Hydrochemical investigation of fluoride high contents in groundwaters in portion of guarani aquifer system, southern Brazil
,
Anuário do Instituto de Geociências – UFRJ
,
41
(
1
),
52
65
.
doi:10.11137/2018_1_52_65
.
Medellín Castillo
N. A.
,
González fernández
L. A.
,
Thiodjio-Sendja
B.
,
Aguilera-Flores
M. M.
,
Leyva-Ramos
R.
,
Reyes-López
S. Y.
,
De León-Martínez
L. D.
&
Dias
J. M.
(
2023
)
Bone char for water treatment and environmental applications: A review
,
Journal of Analytical and Applied Pyrolysis
,
175
,
106161
.
https://doi.org/10.1016/J.JAAP.2023.106161
.
Miner
G.
(
2006
)
Standard methods for the examination of water and wastewater
,
American Water Works Association Journal
,
98
(
1
),
130
.
Mohandas
S. A.
,
Janardhanan
S.
,
Rasheed
P. A.
&
Gangadharan
P.
(
2023
)
Improved defluoridation and energy production using dimethyl sulfoxide modified carbon cloth as bioanode in microbial desalination cell
,
Heliyon
,
9
(
6
),
E16614
.
https://doi.org/10.1016/j.heliyon.2023.e16614
.
Mujtaba
G.
,
Shah
M. U. H.
,
Hai
A.
,
Daud
M.
&
Hayat
M.
(
2024
)
A holistic approach to embracing the United Nation's Sustainable Development Goal (SDG-6) towards water security in Pakistan
,
Journal of Water Process Engineering
,
57
,
104691
.
https://doi.org/10.1016/j.jwpe.2023.104691
.
Podgorski
J.
&
Berg
M.
(
2022
)
Global analysis and prediction of fluoride in groundwater
,
Nature Communications
,
13
(
1
),
4232
.
doi:10.1038/S41467-022-31940-X
.
Protocol GM/MS N° 888
(
2021
)
Altera O anexo Anexo XX N°5, De 28 De Setembro De 2017, Para Dispor Sobre OS Procedimentos De Controle E Vigilância Da Qualidade Da Água Para Consumo Humano E Seu Padrão De Potabilidade. https://www.in.gov.br/en/web/dou/-/portaria-gm/ms-n-888-de-4-de-maio-de-2021-318461562.
Rathnayake
A.
,
Hettithanthri
O.
,
Sandanayake
S.
,
Mahatantila
K.
,
Rajapaksha
A. U.
&
Vithanage
M.
(
2022
)
Essence of hydroxyapatite in defluoridation of drinking water: A review
,
Environmental Pollution
,
311
,
119882
.
doi:10.1016/J.ENVPOL.2022.119882
.
Seben
D.
,
Toebe
M.
,
Wastowski
A. D.
,
Hofstätter
K.
,
Volpatto
F.
,
Zanella
R.
,
Prestes
O. D.
&
Golombieski
J. I.
(
2021
)
Water quality variables and emerging environmental contaminant in water for human consumption in Rio Grande Do Sul, Brazil
.
Environmental Challenges
,
5
,
100266
.
doi:10.1016/J.ENVC.2021.100266
.
Seben
D.
,
Toebe
M.
,
Wastowski
A. D.
,
Da Rosa
G. M.
,
Prestes
O. D.
,
Zanella
R.
&
Golombieski
J. I.
(
2022
)
Association patterns among physical, chemical and microbiological indicators of springs in Rio Grande Do Sul, Brazil
,
Water
,
14
(
19
),
3058
.
doi:10.3390/W14193058
.
SEMA
(
2024
)
Secretaria do Meio Ambiente e Infraestrutura - G040 - Bacia Hidrográfica Do Rio Taquari-Antas. Retrieved from 23 January 2024. Available at: https://sema.rs.gov.br/g040-bh-taquari-antas.
Shaji
E.
,
Sarath
K. V.
,
Santosh
M.
,
Krishnaprasad
P. K.
,
Arya
B. K.
&
Babu
M. S.
(
2024
)
Fluoride contamination in groundwater: A global review of the status, processes, challenges, and remedial measures
,
Geoscience Frontiers
,
15
(
2
),
101734
.
https://doi.org/10.1016/j.gsf.2023.101734
.
Shimabuku
K. K.
,
Baumgardner
M. E.
,
Bahr
R. B.
,
Frojelin
N. R.
,
Kennedy
A. M.
,
Nolan
K. T.
&
Stanton
N. E.
(
2023
)
Fluoride removal in batch and column systems using bonechar produced in a top-lit updraft drum gasifier and furnace
,
Water Research
,
244
,
120332
.
doi:10.1016/J.WATRES.2023.120332
.
State Health Department
(
1999
)
Portaria N° 10 -, Define Teores de Concentração do Íon Fluoreto Nas Águas Para Consumo Humano Fornecidas Por Sistemas Públicos de Abastecimento. https://saude.rs.gov.br/upload/arquivos/202303/21163658-portaria-10-1999.pdf.
Tong
L.
,
Liu
X.
,
Liu
Y.
,
Zhou
K.
,
Zhang
S.
,
Jia
Q.
,
Lu
W.
,
Huang
Y.
&
Ni
G.
(
2023
)
Accumulation of high concentration fluoride in the Ulungur lake water through weathering of fluoride containing rocks in Xinjiang, China
,
Environmental Pollution
,
323
,
121300
.
doi:10.1016/J.ENVPOL.2023.121300
.
Weerasooriyagedara
M.
,
Ashiq
A.
,
Rajapaksha
A. U.
,
Wanigathunge
R. P.
,
Agarwal
T.
,
Magana-Arachchi
D.
&
Vithanage
M.
(
2020
)
Phytoremediation of fluoride from the environmental matrices: A review on its application strategies
,
Groundwater for Sustainable Development
,
10
,
100349
.
doi:10.1016/J.GSD.2020.100349
.
WHO
(
2011
)
Guidelines for drinking-water quality
,
WHO Chronicle
,
38
(
4
),
104
108
.
Zaki
N.
,
Hadoudi
N.
,
Charki
A.
,
Bensitel
N.
,
Ouarghi
H. E.
,
Amhamdi
H.
&
Ahari
M. H.
(
2023
)
Advancements in the chemical treatment of potable water and industrial wastewater using the coagulation–flocculation process
,
Separation Science and Technology
,
58
(
15–16
),
2619
2630
.
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