| Literature DB >> 33045227 |
Bashir Adelodun1, Fidelis Odedishemi Ajibade2, Joshua O Ighalo3, Golden Odey4, Rahmat Gbemisola Ibrahim5, Kola Yusuff Kareem6, Hashim Olalekan Bakare7, AbdulGafar Olatunji Tiamiyu7, Temitope F Ajibade8, Taofeeq Sholagberu Abdulkadir9, Kamoru Akanni Adeniran6, Kyung Sook Choi10.
Abstract
Water is an essential resource required for various human activities such as drinking, cooking, and other recreational activities. While developed nations have made significant improvement in providing adequate quality water and sanitation devoid of virus contaminations to a significant percentage of the residences, many of the developing countries are still lacking in these regards, leading to many death cases among the vulnerable due to ingestion of virus-contaminated water and other waterborne pathogens. However, the recent global pandemic of COVID-19 seems to have changed the paradigm by reawakening the importance of water quality and sanitation, and focusing more attention on the pervasive effect of the use of virus-contaminated water as it can be a potential driver for the spread of the virus and other waterborne diseases, especially in developing nations that are characterized by low socioeconomic development. Therefore, this review assessed the socioeconomic inequalities related to the usage of virus-contaminated water and other waterborne pathogens in developing countries. The socioeconomic factors attributed to the various waterborne diseases due to the use of virus-contaminated water in many developing countries are poverty, the standard of living, access to health care facilities, age, gender, and level of education. Some mitigation strategies to address the viral contamination of water sources are therefore proposed, while future scope and recommendations on tackling the essential issues related to socioeconomic inequality in developing nations are highlighted.Entities:
Keywords: Developing countries; Drinking water; Inequality; Socioeconomic; Virus contamination
Mesh:
Year: 2020 PMID: 33045227 PMCID: PMC7546968 DOI: 10.1016/j.envres.2020.110309
Source DB: PubMed Journal: Environ Res ISSN: 0013-9351 Impact factor: 6.498
Fig. 1Topographic map of African River network.
Fig. 2Socioeconomic factors influencing the occurrence of viral waterborne diseases.
Detection of viruses in water environment.
| Virus type | Water Matrix | Concentration in genome (copies/L) | Country | Reference |
|---|---|---|---|---|
| Rotavirus | Wastewater treatment plant (influent and effluent) | 103 to 105 | South Africa | |
| Adenovirus, | Treated wastewater | 4.6 × 104 to 1.2 × 106 | Brazil | |
| Pepper mild mottle | Municipal pond | 1.0 × 103 to 1.0 × 106 | Bolivia | |
| Hepatitis E | Wastewater treatment plant (influent and effluent) | 6.1 × 102 to 5.8 × 105 | Italy | |
| SARS-CoV-2 | Sewage | Low of detection to 5.6 × 104 | Italy | |
| SARS-CoV-2 | River | 2.1 × 103 to 3.2 × 104 | Ecuador | |
| SARS-CoV-2 | Wastewater (treated and untreated) | 105 to 106.5 | France | |
| SARS-CoV-2 | Untreated wastewater | 2.6 × 103 to 2.2 × 106 | The Netherlands | |
| SARS-CoV-2 | Wastewater (treated and untreated) | 3.1 × 103 to 7.5 × 103 | USA | |
| SARS-CoV-2 | Untreated wastewater | 1.9 × 101 to 1.2 × 102 | Australia | |
| SARS-CoV-2 | Wastewater | 1.4 × 105 to 3.4 × 105 | Spain | |
| SARS-CoV-2 | Secondary treated wastewater (before chlorination) | 2.4 × 103 | Japan |
Summary of mitigation strategies for virus contamination of water.
| Process | Target viruses | Key findings | Reference |
|---|---|---|---|
| Coagulation-sedimentation | Pepper mild mottle virus and JC polyomavirus | The process was able to achieve a Log 10 reduction value of 0.41 and 1.91 for Pepper mild mottle virus and JC polyomavirus (wet season). | |
| Rapid sand filtration | Pepper mild mottle virus and JC polyomavirus | The process was able to achieve a Log 10 reduction value of 1.26 and 0.49 for Pepper mild mottle virus and JC polyomavirus (wet season). | |
| Chlorination | Noroviruses, rotaviruses and hepatitis E virus | At a 4 mg/L dosage of chlorine, Log 10 reduction value of ≥6 was achieved for all three viruses. | |
| Ceramic water filter | Enteric virus | Though the process was efficient, increasing the turbidity of the influent water using bentonite helped to improve the viral decontamination efficiency. | |
| Chlorination | Hepatitis E virus and human adenovirus 2 | A Log reduction of value of 0.41 was achieved. | |
| Cold atmospheric-pressure plasma and plasma-activated water | Bacteriophages T4, ɸ174 and MS2 | The mechanism of virus deactivation was a singlet oxygen attack on the nucleic acid and other proteins. | |
| Iron electrocoagulation | Adenovirus, echovirus, and feline calicivirus and bacteriophage surrogates (Fr, MS2, P22 and ɸ174) | The viruses were effectively removed by the physical coagulation process but less susceptible to iron inactivation. | |
| Sequential electrocoagulation-electrooxidation by boron-doped diamond electrodes | Bacteriophages ɸ174 and MS2 | The results were not that positive as the sequential process alone did not give any major advantage in comparison with using the only electrocoagulation. | |
| Combined ozonation, coagulation and ceramic membrane | Bacteriophage MS2 | Introducing ozonation to the process improves the performance of the process. | |
| Ceramic pot filter with silver | Bacteriophage MS2 | Pot characteristics were observed not to affect the virus decontamination process nor the contact time in the filtration phase. The important effect of silver came at contact time with silver during storage. | |
| Silver-doped titanium oxide photocatalytic degradation | Bacteriophage MS2 | The higher silver content in the photocatalytic adsorbent improved the inactivation efficiency of the virus. | |
| Silica-modified titanium oxide photocatalytic degradation | Bacteriophage MS2 | Modification improved viral deactivation by about 270%. | |
| Micro-filtration membrane | Foot-and-mouth disease (type O) and Infectious bovine respiratory disease | The fuzzy inference system was successfully used to model the experimental data to predict virus removal based on operational parameters. | |
| Aluminum-based coagulation | Bacteriophages T4, Qβ and MS2 | The viruses were effectively decontaminated due to interactions with the coagulant. | |
| Adsorption by super-powdered activated carbon | Bacteriophages Qβ and MS2 | In contrast with the ordinary activated carbon (AC), the super-powdered AC was more effective in virus removal due to its higher hydrophobicity, the greater portion of nano-pores and lesser electrophoretic repulsion. | |
| Microfiltration | Norovirus | It was unsuitable for virus removal (pore size 0.1 μm). | |
| Ultrafiltration | Norovirus | The process was able to achieve a virus reduction value in the Log 4 region. | |
| Hybrid pre-coagulation – microfiltration process | Norovirus | A first-stage coagulation process helped to improve the efficiency of the microfiltration. | |
| Ultraviolet (UV) irradiation | Adenovirus, feline calicivirus, coxsackievirus, echovirus, poliovirus and bacteriophage | The process was more efficient in the decontamination of adenoviruses than for the others. | |
| Titanium oxide photocatalytic degradation | Adenovirus, feline calicivirus, coxsackievirus, echovirus, poliovirus and bacteriophage | The process was more efficient in the decontamination of bacteriophages than for the others. | |
| Ferric chloride coagulation | Adenovirus, feline calicivirus, coxsackievirus, echovirus, poliovirus and bacteriophage | The process was more efficient in the decontamination of coxsackievirus, bacteriophage MS2 and adenovirus than for the others. | |
| Nano-filtration by carbon nanotubes | Bacteriophage MS2 | At an 8–11 bar pressure, virus removal was effectively achieved. | |
| Solar water disinfection | Hepatitis A virus, norovirus surrogate and murine norovirus | UV from solar irradiation was effective for virus inactivation albeit to a greater extent than the temperature of the process. | |
| Polysulfone membrane coated with magnetite | Bacteriophage MS2 | Coating with magnetite improves treatment performance up to 99.99% in the Log 4 region. | |
| Advanced bardenpho as a secondary treatment in a water plant | Pepper mild mottle virus, Aichi virus, noroviruses, enterovirus, sapovirus, rotavirus, adenovirus and polyomaviruses | When the advanced bardenpho was used as a secondary treatment in a water treatment plant, most pathogenic viruses were removed and it compared better to the conventional process. | |
| Activated carbon modified with silver and copper oxide nanoparticles | Bacteriophage T4 | The modified porous media was able to achieve virus reduction in the region of Log 3. | |
| Iron electrocoagulation – microfiltration | Bacteriophage MS2 | The primary mechanism was by sweep flocculation which was assisted by charge neutralization. | |
| Nano-Titanium oxide membrane adsorption | Bacteriophage F2 | PAN (0.05 μm) membrane had higher removal efficiency than PVDF (0.20 μm) membrane. | |
| Photocatalytic membrane separation process | Bacteriophage F2 | At an optimum condition of 40 L/(m2h) intermittent suction mode, virus removal of over 5 log was achieved in 24 h. | |
| Iron coagulation – microfiltration | Bacteriophage MS2 | The process was able to achieve over 4-log virus removal at optimum conditions. |
Fig. 3Schematic of a ceramic water filter (Farrow et al., 2014).