This study explored various low-cost water treatment technologies that are used to minimize levels of pathogens and contaminants in raw water. The paper focused on techniques such as cloth filtration, boiling, chlorination, and solar water disinfection. In the communities, cloth filtration is applied as the initial step of treating raw water with the proper choice of cloth fabrics followed by either boiling, chlorination or solar water disinfection. In low-income communities with unclean burning fuel sources, boiling was found to be the preferred method. Chlorination was also a popular technique associated with the challenges of low or high levels of free chlorine at the point of use and disinfection by-products. Solar water disinfection required optimal residence time and detection sensors for microorganism inactivation. Overall, the paper provided valuable insights into the different low-cost water treatment techniques that are commonly used for household applications, particularly in developing countries.

  • Low-cost water treatment technologies were reviewed including cloth filtration, boiling, chlorination and solar water disinfection.

  • Efficiency removal of contaminants were presented from different literature data.

  • Challenges of using low-cost water treatment technologies were presented.

The availability of clean water and sanitation facilities in Sub-Saharan Africa (SSA) has recently improved, leading to a positive change in water governance (Nyika & Dinka 2023). As communities gained better access to clean water and sanitation, they became better equipped to manage their water resources and make decisions about water usage. Unfortunately, indigenous communities were among the hardest hit by the shortage of clean and safe water (Balasooriya et al. 2023). In 2019, only 56% of city-dwellers in SSA countries had access to piped water from water authorities, despite the rapid urbanization and growing population in the area (Armah et al. 2018; Eberhard 2019). Even a slight improvement in safe water access and sanitation facilities had a big difference in reducing the incidence of infectious diseases (Cilliers 2021). In fact, inadequate water, sanitation, and hygiene led to global annual diarrhea deaths of about 58% (Mackinnon et al. 2019).

Africa is rich in water resources available in the ground, such as aquifers, as well as on the surface, such as streams, rivers, springs, and lakes (Mahed 2023). The availability of water sources facilitated various social and economic activities, including household use, irrigation, livestock, and industrial applications. Unfortunately, mostly of social and economic activities contributed to water contamination, which adversely affected water quality. A water contaminant refers to any substance other than water molecules that, when present above a certain threshold, potentially cause harm to humans, animals, or the environment (Sharma & Bhattacharya 2017). Environmental Protection Agency (2023) expressed possible contaminants and infectious diseases, highlighted the importance of protecting water sources and ensured access to clean and safe water for all communities. There are several circumstances in which it may be necessary to treat water at the point-of-use (PoU) or inactivate microbial pathogens, including (i) failure of control measures, including lack of or improper disinfection and unsafe handling and storage; (ii) emergencies and disasters led to inadequate sanitation, hygiene, and protection of water sources (WHO 2015).

Approximately 45.6% of the population in Tanzania lacked access to clean and safe water (Komba et al. 2022). The piped water sources for clean and safe water provision in urban areas were about 60% compared to 28% in rural areas (Musonge et al. 2022). Large parts of urban and rural areas faced acute piped water supply issues due to poor planning, inability to address technical aspects, financial issues, operation, and maintenance (Marobhe 2008). High non-revenue water due to the water losses, high pressure at the nodal junctions, low flow velocity resulting from oversized pipes caused water stagnation, and unreliable water supply services were significant challenges in operations of the water infrastructure of most fast-growing cities in developing countries (Shushu et al. 2021). However, there were initiatives to improve the water supply and reduce the time spent fetching water (Hopewell & Graham 2014).

However, the use of bottled water in developing countries increased rapidly (Cohen et al. 2020). The number of Water Supply and Sanitation Authorities (WSSAs) was 85 in Tanzania, including regional, and national water projects, districts, and townships. The ratio of water production and water demand was still approaching half, with the water production of 393.2 million cubic meters (EWURA 2023). About 396 Certified Bottled Water Companies (CBWCs) scattered within Tanzania partially or fully packed drinking water into bottles of different sizes, i.e., 0.5, 1, 1.5, 3, 10, and 18 L using different water treatment technologies. Again, about 102 water-well drilling companies (WDCs) registered for deep water-well drilling and installation. Twenty-five companies were selling equipment and installation services for water treatment (URT. The United Republic of Tanzania 2023). Figure 1 summarizes the stakeholder's contribution to the water access and availability in Tanzania.
Figure 1

Percentage of water access and availability from different sectors: CBWC = certified bottled water companies; WDC = water-well drilling companies; WSSA = water supply and sanitation authorities; and SEIC = selling equipment and installation companies services.

Figure 1

Percentage of water access and availability from different sectors: CBWC = certified bottled water companies; WDC = water-well drilling companies; WSSA = water supply and sanitation authorities; and SEIC = selling equipment and installation companies services.

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Various water treatment technologies produced different water quality associated with drawbacks (Kiagho et al. 2016). A slow-sand filter combined with sodium silicate and silver nano-materials purified raw water and applied to only a few indigenous communities in the Northern part of Tanzania (Hilonga 2019). Two non-profit organizations allocated in Morogoro and Arusha region made pot ceramic filters with an average of 99.8% efficiency in removing Escherichia coli and other bacteria with the capacity to produce an average of 50 liters of clean drinking water per day (MSABI 2023; WTW. Wine to Water 2023). Generally, cloth filtration, chlorination–water guards, and solar water disinfection (SODIS) were mainly adopted in developing countries for treating raw water (K'oreje et al. 2020). This paper presents cost-effective water treatment techniques for domestic use in developing countries, with a concentration on cloth filtration, boiling, chlorination, and solar water disinfection (SODIS). It also reviews the treatment effectiveness to eliminate the impurities and associated costs of implementing small-scale water treatment facilities.

Overview of water treatment techniques

Water treatment is the process of minimizing the presence of contaminants to reach the minimum level for consumption in social and economic activities (Pakharuddin et al. 2021). Whether physical, chemical, or biological contaminants were removed using different technologies tailored to address the specific type of contaminant. The household water treatment practice was limited due to the lack of educated people or low levels of income within the communities (Unicef 2019; Asefa et al. 2023). Figure 2 shows the techniques for treating raw water from the point source before consumption.
Figure 2

Schematic diagram showing the mechanism of water treatment process from water source to user, modified from Iwuozor (Iwuozor 2019).

Figure 2

Schematic diagram showing the mechanism of water treatment process from water source to user, modified from Iwuozor (Iwuozor 2019).

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Decantation is the process of separating insoluble impurities from raw water by taking advantage of their varying densities, which causes denser contaminants to settle at the bottom of the container (Jorge et al. 2021). The presence of suspended impurities in raw water with a density slightly different or lower than the water density is commonly separated using the flotation technique (Rubio et al. 2007). The injection of air at high pressure into the raw water, forms tiny bubbles, i.e., less than 0.1 mm (Puget et al. 2000). Then, hydrophobic suspended impurities adhere to the bubbles and, moving against the gravitational pull (Kyzas & Matis 2018), rise and accumulate on the surface of the water (Srinivasan & Viraraghavan 2009; Li & Xiao 2023). The flotation technique comprised ejector systems including a pump, heater, mixer, and cooler to generate dissolving air at high pressures in the solid–liquid separation process (Zabel 1984). The application of the flotation technique depended on the quality and nature of effluent particle size down to 10 μm, aerobic sludge, operation flexibility, capital cost, and separation efficiency greater than 90% compared to the sedimentation/decantation technique (Viitasaari et al. 1995).

Filtration is a unit operation that separates suspended impurities in the raw water through a porous medium or membrane (Cheremisinoff 1998). The size of porous media or membrane allows the impurities of the same size to pass and retain larger particle size at a specific time (Ghaedi et al. 2016). A porous media or membrane is a thin interface discrete layer up to the pore size of less than 10−8 m diameter that moderates the permeation of pressured raw water (Baker 2012). Many of the filters are off-the-shelf market manufactured with four different models: (i) cake filtration involved the hard particulate solids and assumed to settle on the top side of the filter with a constant permeability and pressure drop increased linearly; (ii) blocking filtration involved the constant permeability with the pressure drop increased exponentially; (iii) deep bed or depth filtration involved the retaining suspended contaminants depending on the pore size of the media like any related sand or ceramic filters; and (iv) in cross-flow filtration, the engineered filter media, characterized by precise pore size, is subjected to high-velocity raw water flowing tangentially across it, allowing only a fraction of the liquid to pass through (Abd Rahim & Othman 2019). Examples of cross-flow filtration technologies include microfiltration, ultrafiltration, nanofiltration, and reverse osmosis, as detail described in Ripperger et al. (2000).

Coagulation destabilized the suspended contaminants using coagulants to promote impurities to come together. A coagulant is a chemical product from organic or inorganic materials. A coagulant chemical was added to the raw water to neutralize the negative charges of the non-settled contaminants (Sharma & Ahammed 2023). Flocculation refers to the process in which destabilized particles agglomerate to form larger particles known as flocs. (Ghernaout 2020). Water disinfection means inactivating biological contaminants using physical or chemical disinfectants (Gelete et al. 2020). The physical disinfectants include ultraviolet light (UV), heat, sounds, and other radiations. Chemical disinfectants include chlorination, ozonation, hydrogen peroxide, and metal oxidation processes (Ishaq et al. 2018; Gelete et al. 2020).

Cloth filtration

Cloth filter in the same way called fabric filter, is often used to describe a wide range of fabrics, including woven and non-woven materials. Cloth filter is made from cotton, silk, burlap, satin, or saree cloth as available in the off-the-shelf market with pore sizes of about 20 μm (Oza 2019). The cloth filters reduced the turbidity and pathogens by capturing the top layer of the fabric filter (Thompson 2015). Unlike other types of fabric structures, woven fabric with plain, twill, or satin was commonly used for water treatment as it has the same size as the warp and weft, as shown in Figure 3 (Ali et al. 2018). The woven fabric consisted of an interlacing pattern of warp above welf or welf above warp. Knowing that the warp fibers are the threads that run vertically and are loaded onto the desired dimension frame first to create the skeleton of the cloth. While weft fibers are the threads that run horizontally, interlacing with the warp yarns to create the desired fabric pattern or texture (Sutherland & Chase 2011). The twill woven fabric is more flexible and accessible to filter than the plain and satin fabric.
Figure 3

Basic weave patterns of woven plain, twill, and satin from left to right, respectively (Ali et al. 2018).

Figure 3

Basic weave patterns of woven plain, twill, and satin from left to right, respectively (Ali et al. 2018).

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Still, all types have been used to develop filters ranging from 6 to 300 μm as applied in all grades, from coarse to ultrafine filtering (Eyvaz et al. 2017). Paper filters came from a slurry of cellulose fibers, or pulp laying on woven wire bands, emerging from textile fabrics manufactured from natural and synthetic materials or a felt filter as a cloth type manufactured by condensing, matting, and pressing fiber materials. Figure 4 shows typical performance curves of the papers and cloth filters.
Figure 4

Filtration performance comparison of cloth and paper filters (Sutherland 2008).

Figure 4

Filtration performance comparison of cloth and paper filters (Sutherland 2008).

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The use of a non-woven fabric filter to the conventional-slow-sand filter improved the removal performance of contaminants in the raw water (Mondal et al. 2007). The innovative approach of applying non-toxic polymer coatings to cotton fabric (Kawabata et al. 1992; Zahid et al. 2017), along with the use of engineered fabrics such as Bidim A8 and A10 (Siwila & Brink 2019), and the integration of fabric materials into traditional filters (Siwila 2019), enhanced the adoption of fabric-based materials for cost-effective water treatment in household settings. However, the filter selection depended on the amount of water treated, investment capital, residual discharge, chemical resistance, swelling, heat, pressure, wear, hydraulic and retention rate (Eyvaz et al. 2017).

Boiling process

Boiling small quantities of water into a stove or heater to remove the contaminants has been practiced for many years (Dinkel et al. 2020). The boiling method was the most common means of treating water against alternative household-based filtration methods and disinfection (Clasen et al. 2008). Boiling water effectively neutralized contaminants in the water (WHO 2015); however, this method was not adequately highlighted or consistently implemented within communities. The piped and tap water was safe and potable for drinking whether normal boiled, prolonged boiling, or repeatedly boiled water (Zhai et al. 2020). Boiling water before consumption improved health within communities and reduced the incidence of non-waterborne digestive (Li & Xiao 2023). However, traditional belief that water was typically boiled solely for children, while such boilers acknowledged that boiled water was freed from germs, but not ready to drink (Juran & MacDonald 2014).

The boiling method had the advantage of being widely practiced in households to improve water quality (Zhang 2013). However, it has challenges regarding the cost of energy sources, i.e., wood, charcoal, electricity, or gas (Rosa et al. 2010) or recontamination during storage (Brown & Sobsey 2012), causing accidents to children and burnt houses (Juran & MacDonald 2014). Some pathogens like bacteria, protozoa, and viruses are destroyed at a temperature above 60 °C with a resident time of up to 20 min (Ghaudenson et al. 2021). The boiling process was reported only to remove a small amount of chlorine residual (Bayne et al. 1965). As practiced in boiling or thermal disinfection, pathogens were killed at the temperature ranging from 20 to 90 °C (Espinosa et al. 2020). However, some contaminants including amino acids and nucleotides, are killed at high temperatures above 200 °C (Brock 1985).

Chlorination process

Introduction

Chlorination is the process of adding chlorine to disinfect contaminants in the water. The suspended matter with turbidity below 5 NTU in the water increased the ability of chlorine to react with the pathogens, molds, and algae common in water reservoirs and tanks. Chlorine was applied into the water in several forms as chlorine gas – elemental, sodium hypochlorite solution – bleach, and dry calcium hypochlorite. Chlorine is characterized by versatile and low-cost disinfectant. Chlorination applied to different locations: (i) point-of-delivery – chlorine added into the water truck tank, but care should be taken to avoid corrosion; (ii) in-line chlorination involves continuously discharging chlorine into the water network as distributed to the users; (iii) POU-chlorine was introduced into the clay pot, jerrican, or plastic container, resulting in a chlorine concentration that reached as high as 10 mg/L (Branz et al. 2017). Again, POU treatment is utilized in drilled wells or boreholes (Reed et al. 2013), although the chlorine levels may not remain consistent or diminish quickly (Verkerk & McNicholl 2018).

Chlorination mechanism

Any form of chlorine was gently added to the water to form hydrochloric acid and hypochlorous acids (HOCl). The dissolution of HOCl into H+ and hypochlorite ion (OCl) depended on the pH level in the water (Treacy 2019). The formation of HOCl was completed in the solution with a pH above 4 and left little Cl2 existing, as shown in Figure 5 (Deborde & Von Gunten 2008). Depending on the temperature at a pH of 7.3, the formation of HOCl and OCl is equal to the 50% chlorine present or a higher pH level will increase the OCl (BSDW. Bureau of Safe Drinking Water 2016). Hypochlorous acid was dominant at low pH levels and more effective in chlorinated water.
Figure 5

Reaction distribution of Cl2, HOCl, and ClO with an increase in the pH level at a temperature of 25 °C and 177.5 mg/L of chlorine concentration (Deborde & Von Gunten 2008).

Figure 5

Reaction distribution of Cl2, HOCl, and ClO with an increase in the pH level at a temperature of 25 °C and 177.5 mg/L of chlorine concentration (Deborde & Von Gunten 2008).

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Disinfection by-products

Chlorine residuals were typically maintained between 0.2 and 0.5 mg/L in commercial water supplies or tap water to ensure the preservation of water quality throughout distribution and storage (WHO World Health Organization). But, it produced challenges of odor and taste concerns for some users (ACC. American Chemistry Coucil 2019). Combining hypochlorous acid and hypochlorite ions made free chlorine (SDWF. Safe Drinking Water Foundation 2023). The interaction of free chlorine with humic and fulvic substances in the water presented an additional issue of forming trihalomethanes (THMs) and other halo-compounds, such as haloacetic acids (HAAs), which are disinfection byproducts (DBPs). However, the best option is to avoid the formation of these compounds, as regular consumption of DBPs can pose health risks to humans (Nair et al. 2023). Following the regulations set by the USA, which limit HAAs to 60 μg/L and THMs to 80 μg/L in tap water, is a good practice to adopt (USEPA US Environmental Protection Agency 2006). As natural organic matter as the major contributor to DBP, other factors like salt composition and concentration increase the formation (Hao et al. 2017). Balancing between the chlorine dosage and reagents helped to minimize the formation of DBPs (Ding et al. 2019) or reduce them to a lower level (Ghernaout 2017).

High formation of DBPs during chlorination requires use of the carbon adsorption treatment plant before water is distributed to the users (Spirenkova et al. 2021). The kinetics formation of the DBPs during chlorination detail described in Cheng, et al. (Cheng et al. 2023). The use of granular activated carbon, quartz and sand treatment (Qiao et al. 2022), advanced oxidation processes (Patton et al. 2022), or ultraviolet/hydrogen peroxide (UV/H2O2), and ultraviolet/peroxymonosulfate (UV/PMS) improved the removal of the DBPs in the chlorinated water (Huang et al. 2022). The five commercial sensors such as free chlorine, oxidation-reduction potential, pH, turbidity, and ultraviolet absorbance at 254 nm used to monitor the DBP levels (Reynaert et al. 2023). Again, a lot of literature indicated granular activated carbon was very effective in removing DPB, much more than 25% (Stefán et al. 2019). However, adding TiO2 and ZnO into the treated water to remove DBPs was possible after exposing to solar radiation (Pérez-Lucas et al. 2022).

Solar water disinfection

Introduction

The SODIS method has been applied to treat drinking water for more than 40 years with much recognition of its ability to inactivate microorganisms (Akpan & Udom 2023; Phiri et al. 2023). The extensive adoption of SODIS for water treatment ensured the provision of clean drinking water at the household level (Ferdous & Hasan 2014; Chaúque et al. 2022; Hobbins). The SODIS method comprised transparent plastic or glass containers of capacity ranging from 1 to 2 L, and the bottom support (Meierhofer & Landolt 2009). Figure 6 shows the solar radiation transmitted to the raw water in the bottles (Ubomba-Jaswa et al. 2009; Xia et al. 2022). The SODIS technique was simple, low-cost, and safe to apply in geographical areas with high sunshine time, especially in sub-Saharan African countries (Dessie et al. 2014). However, the bottle must be exposed to solar radiation to the extent all pathogens are inactivated, or no re-growth of microorganisms is observed in the treated water (Karim et al. 2021). The exposure times varied from 6 to 48 h depending on the intensity of solar radiation and pathogens sensitivity (McGuigan et al. 2012). Treating water with the SODIS method saved the life of people by preventing diseases such as diarrhea, cholera, and other waterborne diseases (García-Gil et al. 2021).
Figure 6

Closed bottle filled with raw water exposed to solar radiation: (1) solar radiation, (2) crossing through the bottle; (3) crossing through the raw water; (4) inactivation pathogens with solar radiation (Schute et al. 2011).

Figure 6

Closed bottle filled with raw water exposed to solar radiation: (1) solar radiation, (2) crossing through the bottle; (3) crossing through the raw water; (4) inactivation pathogens with solar radiation (Schute et al. 2011).

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The SODIS method improved water quality in a society of low-income levels (Graf et al. 2008; García-Gil et al. 2021). Households situated nearer to water sources were more likely to adopt SODIS at the household level, in contrast to those farther away, which generally had less sanitary conditions, and were less affluent (Du Preez et al. 2010; Christen et al. 2011). The presence of suspended materials with turbidity greater than 30 NTU-Nephelometric turbidity units reduced the solar radiation penetration into raw water (Meierhofer & Wegelin 2002). Raw water filled into transparent plastic bottles or piped systems (Figure 7) and exposed to solar energy. Raw water flowed by gravity to allow continuous water treatment in the pipe system (Mac Mahon & Gill 2018) after being heated to approximately 60 °C, and maintained for 30 min to destroy micro organisms (Lundgren 2014). Using sensors to measure temperature helped to control the water quality (Vivar et al. 2015; Reynaert et al. 2023).
Figure 7

Water treatment technique under solar radiation: (a) stacking bottles (McGuigan et al. 2012) and (b) piped system for continuous flow (Mac Mahon & Gill 2018).

Figure 7

Water treatment technique under solar radiation: (a) stacking bottles (McGuigan et al. 2012) and (b) piped system for continuous flow (Mac Mahon & Gill 2018).

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Containers or pipe systems with storage were loaded with untreated water and exposed to sunlight to deactivate pathogens. The system of flowing raw water, combined with parabolic concentrated solar power, was engineered to enhance the daily volume of water purified (Meierhofer & Landolt 2009; Preez 2011). Positioning the bottles on a black surface (Haider 2017) and corrugated metal sheets (Karim et al. 2021) created a temperature gradient that boosts the efficiency of pathogen inactivation.

Solar radiation

The visible light from the solar radiation ranged from 400 to 700 nm and the Ultraviolet light ranged from 100 to 400 nm (Figure 8). The SODIS method required UV-A radiation to inactive the pathogens ranging from 315 to 400 nm (Heri 2006). The cloud condition ranged from 40 to 60% (Van Hoesen et al. 2023) or 50% (Cristinel et al. 2011) to provide enough energy for damaging the microorganisms in the closed bottles or pipe systems. The amount of UV-A radiation that reached the earth's surface depended on the specific geographic location (Berney et al. 2006) and did not alter the water chemistry (Nwankwo & Agunwamba 2021).
Figure 8

Illustration of the spectrum of sunlight energy from ultraviolet to infrared wavelength (Heri 2006).

Figure 8

Illustration of the spectrum of sunlight energy from ultraviolet to infrared wavelength (Heri 2006).

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The microorganism cells inactivated when exposed to global sunlight intensity of about 530 W/m2 corresponding to greater than 1,500 kJm−2 for 6 h (Amin et al. 2014; García-Gil et al. 2020a, 2020b). Solar collector disinfection (SOCODIS) concentrated solar radiation for about 20% more than the just exposed filled water bottles on the insulated surface (Xie et al. 2023). Figure 9(a) shows the SODIS and (b) SOCODIS systems. Simulation analysis of the bottle indicated the distribution of the solar radiation as shown in Figure 9(c) (Brockliss et al. 2022).
Figure 9

Solar energy radiates (a) bottles; (b) bottles stacking on the concentrated collector (Xie et al. 2023); and (c) simulated bottles filled with raw water. Red color denotes to high value of solar radiation, and blue color indicates a low value of solar radiation (Brockliss et al. 2022).

Figure 9

Solar energy radiates (a) bottles; (b) bottles stacking on the concentrated collector (Xie et al. 2023); and (c) simulated bottles filled with raw water. Red color denotes to high value of solar radiation, and blue color indicates a low value of solar radiation (Brockliss et al. 2022).

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Water depth

The water height per surface area of the bottle in the SODIS process was a very important parameter (Spuhler & Meierhofer 2020). The experiment of 1-L bottles and a bucket of 20-liter with 290 mm diameter and height of 330 mm were conducted as shown in Figure 10(a), and the same conditions with the amount of solar energy radiated to the two vessels, micro-organisms in the bucket were not inactivated (Kalt et al. 2014). The variation of remaining UV-A radiation against water depth is shown in Figure 10(b). Advised to have bottles relatively flat or not go beyond a height of 10 cm (Meierhofer 2006), subjected to sunlight for over 4 h, with a minimum residence time of 30 min (O'Dowd et al. 2023).
Figure 10

Solar water disinfection: (a) stack of bottles and 20-L bucket (Kalt et al. 2014) and (b) variation of remaining UV-A against water depth in the container adopted from Meierhofer & Wegelin (Meierhofer & Wegelin 2002).

Figure 10

Solar water disinfection: (a) stack of bottles and 20-L bucket (Kalt et al. 2014) and (b) variation of remaining UV-A against water depth in the container adopted from Meierhofer & Wegelin (Meierhofer & Wegelin 2002).

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Container materials

The SODIS process used cheap and re-use containers such as polyethylene tephthalate (PET), polypropylene (PP) bottles or glass with a lid (García-Gil et al. 2019; García-Gil et al. 2020a, 2020b; Sawant et al. 2023). The potential materials for manufacturing SODIS packaging devices were identified by considering polymethylmethacrylate (PMMA), polyethylene terephthalate (PET), Polyvinyl Chloride (PVC), polypropylene (PP). The higher the transmittance of solar radiation into the raw water, the better the materials for manufacturing the bottles with the order of PMMA > PET > PP > PVC, as shown in Figure 11 (Mounaouer & Abdennaceur 2014).
Figure 11

Material selection for filling raw water in the SODIS technique (Mounaouer & Abdennaceur 2014).

Figure 11

Material selection for filling raw water in the SODIS technique (Mounaouer & Abdennaceur 2014).

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Pathogens inactivation models

The computational fluid dynamics (CFD) software and kinetic mechanisms were used in the compound parabolic collectors (CPCs) to predict the performance of SODIS process, the mechanism of inactivating the microorganism, and the operating time (Moreno-SanSegundo et al. 2021). A number of kinetic models exist to characterize the disinfection mechanism during solar radiation, including Chick-Watson, amended Chick-Watson, and Collin-Selleck to guarantee good disinfection (Verma & Prasad 2013; Castro-Alférez et al. 2018). Model for E. coli inactivation was developed in different conditions with the 2–22.5 L Bottle, and turbidity ranged from 5 to 300 NTU (Minzu et al. 2021) and predicted the range of experimental results for E. coli inactivation (Nalwanga et al. 2014; Ouelhazi et al. 2017; Nalwanga et al. 2018; Aboushi et al. 2021). Table 1 shows the measured temperature of destroying different pathogens. Figure 12 shows the comparison of the simulation of the dynamic model based on the empirical transfer matrix and experimental data under the same conditions (Carielo et al. 2017). Table 2 shows the removal efficiency of microbial based on the type of water container, time duration and amount of solar radiation.
Table 1

Type of pathogen, destruction time, and temperature adopted from Lundgren (Lundgren 2014)

PathogenDestruction time, minDestruction temperature, °C
Salmonella – Typhoid, Paratyphoid 20 60 
Vibrio cholera – Cholera 55 30 
E. coli – Diarrhoea 60 20 
Shigella – Dysentery 55 60 
Rotavirus – Child diarrhoea 60 30 
PathogenDestruction time, minDestruction temperature, °C
Salmonella – Typhoid, Paratyphoid 20 60 
Vibrio cholera – Cholera 55 30 
E. coli – Diarrhoea 60 20 
Shigella – Dysentery 55 60 
Rotavirus – Child diarrhoea 60 30 
Table 2

Summary of the, type of water container, time duration,amount of solar radiation, and removal efficiency of microbials

Material of the containerAmount of solar radiationSunlight exposure durationType of microbialRemoval efficiency, %Source
Simply a transparent bottle – 150 min Total coliform E. coli Aeruginosa 95.9
97.2
90 
Aboushi et al. (Teksoy & Çalışkan Eleren 2017
Flat mirror inserted below a transparent bottle Total coliform E. coli Aeruginosa 96.8
99.6
96 
Concave mirror inserted below a transparent bottle Total coliform E. coli Aeruginosa 96
99.2
95 
Polyethylene terephthalate (PET) and low density polyethylene (LDPE) plastic bags 1,509 W-hr/m2 6–8 h E. coli 99 Karim et al. (2021)  
– 6.6 MJ/m2 day 1 Day Total coliforms 100 Carielo et al. (Tedeschi et al. 2014
E. coli 100 
Pseudomon asaeruginosa 100 
Heterotrophic bacteria 98.7 
Plastic bags, plastic bottles and glass bottles 1.34 kJ/cm 2 6 h Campylobacter jejuni, Enterococcus sp., E. coli, Mycobacterium avium, P. aeruginosa, S. typhi and V. cholerae, are inactivated – Teksoy and Eleren (Mohamed et al. 2014
Polyethylene terephthalate (PET), nalgene and platypus – 6 h Total coliforms and E. coli were removed – Tedeschi et al. (Boyle et al. 2008
Polyethylene terephthalate (PET) – 7 h Cysts of Giardia 95 Mohamed et al. (Méndez-Hermida et al. 2007
Entamoeba 97 
Polyethylene terephthalate (PET) Maximum global irradiance ∼ 1,050 W m−2 ± 10 W m−2 8 h C. jejuni, S. epidermidis, E. coli and Y. enterocolitica inactivation 99.9 Boyle et al. (Chaúque et al. 2023
Borosilicate glass and transparent polypropylene 830 W m−2 8 and 12 h Cryptosporidium parvum oocyst 98 Méndez-Hermidaet al. (Hirtle 2008
Material of the containerAmount of solar radiationSunlight exposure durationType of microbialRemoval efficiency, %Source
Simply a transparent bottle – 150 min Total coliform E. coli Aeruginosa 95.9
97.2
90 
Aboushi et al. (Teksoy & Çalışkan Eleren 2017
Flat mirror inserted below a transparent bottle Total coliform E. coli Aeruginosa 96.8
99.6
96 
Concave mirror inserted below a transparent bottle Total coliform E. coli Aeruginosa 96
99.2
95 
Polyethylene terephthalate (PET) and low density polyethylene (LDPE) plastic bags 1,509 W-hr/m2 6–8 h E. coli 99 Karim et al. (2021)  
– 6.6 MJ/m2 day 1 Day Total coliforms 100 Carielo et al. (Tedeschi et al. 2014
E. coli 100 
Pseudomon asaeruginosa 100 
Heterotrophic bacteria 98.7 
Plastic bags, plastic bottles and glass bottles 1.34 kJ/cm 2 6 h Campylobacter jejuni, Enterococcus sp., E. coli, Mycobacterium avium, P. aeruginosa, S. typhi and V. cholerae, are inactivated – Teksoy and Eleren (Mohamed et al. 2014
Polyethylene terephthalate (PET), nalgene and platypus – 6 h Total coliforms and E. coli were removed – Tedeschi et al. (Boyle et al. 2008
Polyethylene terephthalate (PET) – 7 h Cysts of Giardia 95 Mohamed et al. (Méndez-Hermida et al. 2007
Entamoeba 97 
Polyethylene terephthalate (PET) Maximum global irradiance ∼ 1,050 W m−2 ± 10 W m−2 8 h C. jejuni, S. epidermidis, E. coli and Y. enterocolitica inactivation 99.9 Boyle et al. (Chaúque et al. 2023
Borosilicate glass and transparent polypropylene 830 W m−2 8 and 12 h Cryptosporidium parvum oocyst 98 Méndez-Hermidaet al. (Hirtle 2008
Figure 12

Comparison of simulation and experimental results of bacterial reduction against time under UV intensity (Carielo et al. 2017).

Figure 12

Comparison of simulation and experimental results of bacterial reduction against time under UV intensity (Carielo et al. 2017).

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Additives materials

The raw water with a high oxygen level increased the chance of microorganisms being inactivated with solar radiation. The bottles were filled with raw water for about three-quarters, shook about 20 seconds for the aeration process, and closed the bottle with the lid before being exposed to solar radiation (Meierhofer & Wegelin 2002). Robust and inexpensive indicators such as photodegradable dye-based, polyoxometalate, and semiconductor photocatalysis were added into the raw water and indicated a significant color change when exposed to solar energy of 389 kJm−2 (Lawrie et al. 2015); equivalent to the energy required to inactivate the pathogens (Martínez-García et al. 2023) and fungi (Farhadi et al. 2022). The indicators show that the raw water is ready for drinking. The use of nanotechnology in the SODIS accelerated the elimination of microorganisms. The performance of SODIS was improved using the photocatalyst of TiO2, silver, copper (Nalwanga et al. 2014), and natural clay (Verma & Prasad 2013).

Advanced oxidation techniques integrated into the SODIS indicated significantly reduced disinfection time for pathogen inactivation, as shown in Table 3. Using photocatalysis technology, such as a metal oxide of Z-scheme heterojunction nanofibers, demonstrated the efficiency of purifying water using solar radiation (Wei et al. 2023). Adding herbs and spices ash such as ginger, thyme, and cumin into the raw water improved the reduction of E. coli instead of using H2O2 as shown in Figure 13. The effort of biodegradable materials toward water disinfection operations enhanced the quality of water and minimize the DBPs (Tang et al. 2022).
Table 3

Summary of additives removal efficiency of microbial into the water treated with solar energy

Method SODISRemoval efficiency of microbialMaterial of the containerAmount of solar radiationSunlight exposure durationSource
SODIS of H2O2 and/or the increment ofdissolved oxygen Inactivation of E. coli, E. faecalis, S. enteritidis, P. aeruginosa and bacteriophage MS2 Borosilicate glass – 5 h Martínez-García et al. (2023)  
Solar photo-Fenton E. coli, Clostridium perfringens, MS2 coliphage, E. faecalis Polyethylene terephthalate (PET) – 24 h Pichel et al. (2023)  
SODIS enhanced with titania-based photocatalysts (TiO2 and BTO–TiO2Bacterial inactivation Polyethylene terephthalate (PET) – 3 h Porley et al. (2020)  
Solar photovoltaic hybrid system E. coli and Enterococcus spp Polyethylene terephthalate (PET) 1,033 W/m2 3 h Vivar et al. (2020)  
SODIS enhanced with photocatalysts coated with TiO2 doped with zinc E. coli by 100%
Enterococcus spp. By 100%
C. perfringens by 99.44% 
Polyethylene terephthalate (PET) – – Gutiérrez-Alfaro et al. (2016)  
Solar photovoltaic hybrid system E. coli, total coliforms, Enterococcus spp. and C. perfringens Polyethylene terephthalate (PET) 979 W/m2 6 h Pichel et al. (2016)  
Method SODISRemoval efficiency of microbialMaterial of the containerAmount of solar radiationSunlight exposure durationSource
SODIS of H2O2 and/or the increment ofdissolved oxygen Inactivation of E. coli, E. faecalis, S. enteritidis, P. aeruginosa and bacteriophage MS2 Borosilicate glass – 5 h Martínez-García et al. (2023)  
Solar photo-Fenton E. coli, Clostridium perfringens, MS2 coliphage, E. faecalis Polyethylene terephthalate (PET) – 24 h Pichel et al. (2023)  
SODIS enhanced with titania-based photocatalysts (TiO2 and BTO–TiO2Bacterial inactivation Polyethylene terephthalate (PET) – 3 h Porley et al. (2020)  
Solar photovoltaic hybrid system E. coli and Enterococcus spp Polyethylene terephthalate (PET) 1,033 W/m2 3 h Vivar et al. (2020)  
SODIS enhanced with photocatalysts coated with TiO2 doped with zinc E. coli by 100%
Enterococcus spp. By 100%
C. perfringens by 99.44% 
Polyethylene terephthalate (PET) – – Gutiérrez-Alfaro et al. (2016)  
Solar photovoltaic hybrid system E. coli, total coliforms, Enterococcus spp. and C. perfringens Polyethylene terephthalate (PET) 979 W/m2 6 h Pichel et al. (2016)  
Figure 13

Inactivation of E. coli after combining solar light with ginger, thyme, and ashes without H2O2 (Rodríguez-Chueca et al. 2023).

Figure 13

Inactivation of E. coli after combining solar light with ginger, thyme, and ashes without H2O2 (Rodríguez-Chueca et al. 2023).

Close modal
The production cost of groundwater or surface water sources was greatly increased by the type of water treatment technologies (Horváthová 2022). According to Asefa et al. (2023) presented the most practiced household water treatment method is chlorination (44.9%), followed by boiling (24.5%) and cloth filtration (19.5%). However, the comparison of household water treatment in rural and urban areas (Figure 14) is dominated by boiling followed by cloth filtration (Mohamed et al. 2015). Again, SODIS and filtration showed the potential for water treatment in the future (Zinn et al. 2018). A simplified solar collector, CPC, with a non-tracking system is promised as an alternative to water treatment technologies (Vidal & Diaz 2000).
Figure 14

Comparison of low-cost household water treatments based on the rural and urban areas (Mohamed et al. 2015).

Figure 14

Comparison of low-cost household water treatments based on the rural and urban areas (Mohamed et al. 2015).

Close modal
The SODIS was cheaper than chlorination in the small water treatment systems within the communities at the point-of-use (Dore et al. 2013). The cost per liter for treating water using SODIS with PET is euro 1.4*10−3 with a container life span of 6 months (Keogh et al. 2015). The production costs for treating water gradually increased with the volume of treated water, as shown in Figure 15. The operation cost of SODIS disinfection was lower than chlorination (Moghadam & Dore 2012). But the estimated cost for boiling, flocculation, filtration, and chlorination is $10.56, $4.95, $3.03, and $0.66 per person per year, respectively (Schute et al. 2011). However, the operational expenditure trended with the least cost from filtration, followed by SODIS and chlorination (Tak & Kumar 2017). Chlorine tablets or water guards offered an efficient community-level approach to treating water closer to the point of use or water vendors (Rajasingham et al. 2019; Mazuki et al. 2020; Zafra-Mejía et al. 2020). The communities still used the preferred method of either boiling or cloth filtration with clay pot (Nielsen et al. 2022). The boiling process typically involved the use of charcoal and firewood, which takes longer time than employing chlorination or SODIS techniques. The SODIS technology lacked the water container and awareness to the communities (Dawney et al. 2014; Werner & Fransson 2019; Ngasala et al. 2020) but was suitable for remote areas with low investment costs (Pichel et al. 2019; Sommers 2021; Ghernaout et al. 2023), and preferred to the African countries favored with the solar radiation throughout the year (Rana et al. 2024).
Figure 15

Production cost per expected volume of treated water (Samoili et al. 2022).

Figure 15

Production cost per expected volume of treated water (Samoili et al. 2022).

Close modal

This paper highlights the importance of low-cost household water treatment techniques for developing countries, including cloth filter, boiling, chlorination and solar water disinfection. Low-cost technologies inactivated the microorganisms and related contaminants with simplicity to fit the individual community. This review emphasized the potential of proper choice of cloth materials would improve the initial step of treating high turbidity water using preferable woven fabric with the interlacing pattern. The use of boiling techniques faced the challenges of unclean burning fuels, recontamination and burning of property. The application of chlorination faced the challenges of improper dosage of chlorine with minimum residual level and DBPs at the point-of-use. The use of solar water disinfection faced the challenges of water depth corresponding to the level of turbidity, residence time to expose the bottle on the sunlight, improper water bottle materials, additive costs and detection limits for inactivation of microbials.

The Benjamin W. Mkapa Fund supported this work through the University of Dodoma under the junior research grant category.

Authors originated and conceptualized the idea, O.J.M. designed the research and drafted the paper outline, A.L. and N.S. contributed equally to research design and manuscript compilation.

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

The authors declare there is no conflict.

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