| Literature DB >> 33967299 |
Abstract
The COVID-19 pandemic disturbed the world from the beginning of 2020. The high excessive number of patients and the presence of the SARS-CoV-2 in human excreta and urine even after the infected person's respiratory tests were negative, results in a heavy load of viral in various water bodies and mostly untreated wastewaters. In the present study, the reliability of using small-scale solar thermal desalination systems (solar stills) during a situation like the COVID-19 pandemic is discussed. Pollution of water bodies through the SARS-CoV-2 via numerous routes increases the risk of contaminating the feed water and subsequently the whole structure of solar stills. Since the transmission of pathogens (particle size: 0.5-3 μm) via droplets of water in solar still is reported before, transmitting of SARS-CoV-2 via droplets of water which multiple times smaller (particle size: 60-140 nm) than those pathogens is a concern. The most important issue which must be highlighted is that solar stills worked at low-temperature while the viability and survival of the SARS-CoV-2 in various water matrices in the temperature range (4-37 °C) for several days is reported. In this regard, using solar stills during the COVID-19 pandemic need further consideration by all researchers and people around the world.Entities:
Keywords: COVID-19; Environmental contamination; Pathogens; Solar desalination; Wastewater treatment; Waterborne disease
Year: 2021 PMID: 33967299 PMCID: PMC8096177 DOI: 10.1016/j.desal.2021.115106
Source DB: PubMed Journal: Desalination ISSN: 0011-9164 Impact factor: 9.501
Fig. 1Schematic of solar still.
Fig. 2application of solar still for separation of various impurities.
Productivity of various solar stills at different temperature range.
| Type | Modified/integrate by | Productivity/TWater “for 15–20 °C" | Productivity/TWater “for 20–25 °C" | Productivity/TWater “for 25–30 °C" | Productivity/TWater “for 30–35 °C" | Productivity/TWater “for 35–40 °C" | Productivity/TWater “for 40–45 °C" | Productivity/TWater “for 45–50 °C" | Productivity/TWater “for 50–55 °C" | Ref |
|---|---|---|---|---|---|---|---|---|---|---|
| Stepped/ Passive | Wick & Reflector | – | – | – | – | – | – | – | 54 °C/180 mL | [ |
| Single slope/ Passive | – | – | – | – | – | 37 °C/40 mL | 41 °C/48 mL | 46 °C/80 mL | 50.5 °C/100 mL | [ |
| Single slope/ Passive | Carbon foam & porous absorber | – | – | – | – | – | – | 49.2 °C/100 mL 48.6 °C/40 mL 47.6 °C/40 mL | 54.2 °C/136 mL 54 °C/180 mL51.6 °C/64 mL | [ |
| Double slope/ Passive | Multi Wicks | 19 °C/77 mL | 24 °C/162 mL | 29 °C/445 mL | 33 °C/623 mL | 37 °C/743 mL | – | – | – | [ |
| Double slope/ Passive | Multi Wicks | 18 °C/62 mL | 24 °C/234 mL | 27 °C/398 mL | 31 °C/563 mL | 35 °C/688 mL | – | – | – | [ |
| Single slope/ Active | PV/T | – | 24 °C/50 mL | 27.7 °C/60 mL | 30.9 °C/89 mL | 37.7 °C/99 mL | 42.5 °C/123 mL | 48.2 °C/208 mL | 54.4 °C/311 mL | [ |
| Single slope/ Active | PV/T | – | – | 26 °C/80 mL | 30.7 °C/90 mL | 36.5 °C 152 mL | 42.5 °C/353 mL | 47.5 °C/523 mL | – | [ |
| Single slope/ Passive | – | 15 °C/40 mL | 20.1 °C/37 mL | 29.5 °C/15 mL | 32.3 °C/5 mL | 39.2 °C/5 mL | 40.1 °C/5 mL | 46.2 °C/22 mL | 50.3 °C/58 mL | [ |
| Single slope/ active | PV/T | 19.4 °C/62 mL | – | 27.7 °C/22 mL | 30.3 °C/20 mL | – | 40.7 °C/16 mL | 45.7 °C/255 mL | – | [ |
| Single slope/active | FPC | – | – | – | – | – | – | – | [ | |
| Single slope/ passive | – | - | - | - | - | 49.9 °C/75 mL | 45 °C/10 mL | 51 °C/30 mL | [ | |
| Single slope/ passive | Inverted absorber | – | – | – | 34.6 °C/60 mL | – | 42.3 °C/30 mL | 46.4 °C/60 mL | 52.3 °C/22 mL | [ |
| Single slope/ Active | PVT-FPC | 9.25 °C/1.4 mL | – | 28.46 °C/18.9 mL | – | 37.57 °C/39.2 mL | 44.4 °C/110.5 mL | 49.26 °C/149.5 mL | 52.25 °C/168.6 mL | [ |
| Single slope/ Active | PVT-FPC | 9.31 °C/1.5 mL | 20.16 °C/7.3 mL | 29.4 °C/21.1 mL | – | 38.84 °C/44.5 mL | – | 45.89 °C/124.3 mL | 50.89 °C/166.4 mL | |
| Single slope/ passive | – | 18.9 °C/80 mL | 21.8 °C/90 mL | 27.9 °C/110 mL | 34.7 °C/120 mL | 38.9 °C/150 mL | – | 45.8 °C/250 mL | 54.9 °C/300 mL | [ |
| Single slope/ Active | PV/T | 18.4 °C/95 mL | 21.8 °C/110 mL | 28.3 °C/150 mL | °C/mL | 35.7 °C/220 mL | - | 46.7 °C/350 mL | 54.4 °C/450 mL | [ |
| Single slope/ Active | PV/T | - | 24.8 °C/120 mL | 28.9 °C/150 mL | - | 35.7 °C/280 mL | 43.6 °C/350 mL | 48.8 °C/500 mL | - | [ |
| Single slope/ Active | PV/T | - | - | 25.3 °C/230 mL | - | 36.3 °C/350 mL | 44.2 °C/480 mL | 49.1 °C/650 mL | - | [ |
| Single slope/ Active | ETC & heat pipe | - | - | - | - | - | - | – | 54.41 °C/320 mL | [ |
| Single slope/ Passive | With/without Reflectors & sun tracking | – | 21.6 °C/1.7 mL | 26.5 °C/16.9 mL | 32.9 °C/21.3 mL | 36.8 °C/172 mL | 42.9 °C/242.8 mL | 45 °C/248 mL | 54.5 °C/290 mL | [ |
| Single slope/ Passive | – | 19.3 °C/30 mL | - | 25.1 °C/38.5 mL | 33.1 °C/54.5 mL | – | 40.9 °C/22.5 mL | 47.05 °C/133.5 mL | 52.1 °C/490 mL | [ |
| Single slope/ Active | FPC | – | – | 26.75C/30 mL | 30 °C/22.5 mL | 39.65 °C/59.5 mL | 44.95 °C/115 mL | – | 51.87 °C/137 mL | [ |
| Double slope/ Active | FPC | – | – | – | – | – | 40.7 °C/40 mL | 48.7 °C/226 mL | 53.4 °C/389 mL | [ |
| Single slope/ Passive | – | 12.2 °C/7 mL | 24 °C/20 mL | 25.1 °C/10 mL | 33.2 °C/21 mL | 36.2 °C/41 mL | 40.4 °C/56 mL | - | - | [ |
| Single slope/ Active | FPC | - | - | 25 °C/16 mL | 32.6 °C/29 mL | - | 42.6 °C/72 mL | 46.4 °C/80 mL | 52.3 °C/250 mL | [ |
| Double slope/ Active | FPC | – | – | 26.6 °C/32 mL | 34.8 °C/37 mL | 35.5 °C/40 mL | 44.1 °C/208 mL | - | 53.1 °C/479 mL | [ |
| Single slope/ Passive | – | – | – | – | 34 °C/33 mL | 39 °C/56 mL | 41 °C/93 mL | 45.9 °C/134 mL | 52 °C/232 mL | [ |
| Single slope/ Passive | Utilizing Fe2O3 micro particle | – | - | – | - | 39 °C/130 mL | 44 °C/161 mL | 48 °C/194 mL | 50 °C/260 mL | [ |
| Single slope/ Passive | Utilizing Fe2O3 nanoparticle | – | – | – | - | 38 °C/80 mL | 44 °C/179 mL | 45 °C/169 mL | 52 °C/210 mL | [ |
Fig. 3Productivity of various solar stills with respect to the temperature.
Fig. 4Possible routes for contamination of water bodies.
Fig. 5Some parameters and methods that affecting the viability of the SARS-CoV-2.
Fig. 6Viability of the SARS-CoV-2 in solution with respect to temperature [163].
Fig. 7The average T90 for the SARS-CoV-2 in tap water [172].
Fig. 8The average T90 for the SARS-CoV-2 in Autoclaved wastewater [172].
Fig. 9The average T90 for the SARS-CoV-2 in untreated wastewater [172].