Emergence and re-emergence of four types of severely infectious viruses have claimed significant numbers of lives when anthropogenic activities contribute to the mutagenesis of these pathogens and infectivity of these pathogens has been noticeably altered. However, both point and non-point sources can transport these viruses in water treatment and resource recovery facilities (RRF) where the presence of these pathogens in aerosolized form or in suspension can cause astronomical public health concerns. Hence, numerous scientific studies have been reviewed to comprehend the possible inactivation mechanisms of those viruses in aqueous phase where thermal-, photo-, and chemical-inactivation have confirmed their effectiveness in restraining those viruses and inactivation mechanisms are the major focuses to apprehend the quick and cost-effective virus removal process from water and RRF. Although practical applications of nano-sized disinfectants have challenged researchers, those disinfectants can completely kill the viruses and hamper RNA/DNA replication without any sign of reactivation or repair. Moreover, limitations and future research potential are discussed so that efficacious strategic management for a treatment facility can be developed at the forefront of fighting tactics against an epidemic or a pandemic. Enumerations, besides state-of-the-art detection techniques with gene sequences, are mentioned for these viruses.

  • UV and FUVC can effectively inactivate corona- and ebolaviruses.

  • Nanostructured disinfectants have potential to inactivate the emerging viruses by forming ROSs in both solid and liquid phase.

  • Disintegration of capsid protein and nucleic acid is imperative to inactivate viruses.

  • A strategic framework to develop early warning in the community should be established.

  • This kind of review manuscript is extremely rare.

Graphical Abstract

Graphical Abstract
Graphical Abstract

Owing to changing climate and deforestation (Tollefson 2020), excess or unintentional anthropogenic disposal of mutagens and teratogens in the environment have facilitated the emergence of severe infectious diseases caused by a number of pathogens, e.g., Coronavirus, Ebola virus, Zika virus, and Lassa virus, that have claimed a myriad number of innocent lives and adversely impacted the socio-economic environment. Different strains of Coronaviruses (CoV), i.e., Middle East Respiratory Syndrome CoV (MERS-CoV), Severe Acute Respiratory Syndrome CoV (SARS-CoV), and SARS-CoV-2 claimed about 1,294,815 lives out of 52,743,880 confirmed cases from 2002 to 2020 (WHO 2003; JHU 2020). Five Ebola viruses, i.e., Zaire Ebola virus (ZEBOV), Sudan virus (SUDU), Reston virus (RESTV), Tai Forest virus (TAFV), and Bundibugyo virus (BDBV), including other members of the Filoviridae family, i.e., Marburgvirus genus (MARV and RAVV) (Kuhn et al. 2010) claimed about 15,697 lives of 35,215 confirmed cases since 1967 (WHO 2020), when about 87.2% deaths occurred after 2015 through various exposure routes. Although Zika virus (ZIKV) is not extremely deadly, there were 50 fatalities reported until 2019 (Cardona-Ospina et al. 2019) and Lassa virus mortality rate is about 5,000 deaths/year (Ogbu et al. 2007). Whatever the exposure routes of these pathogens, extensive cleaning or washing of infected surfaces and wastes by a universal solvent or cleaning agent, i.e. water, can convey those pathogens in water reclamation facilities (WRF) or resource recovery facilities (RRF) or other surface water that may be later reclaimed as potable water. Thus, environmental engineers have a leading role in developing early awareness through wastewater-based epidemiology (WBE) about the occurrence of an epidemic or a pandemic.

Waste from diverse sources can exacerbate the situation in an RRF; however, inactivation of pathogens by some well-known disinfectants may manage the initial trigger of an outbreak. Careful application of disinfectants is a task of the utmost importance because of the possibility of disinfection by-products’ (DBPs) formation through excessive use of disinfectants in the system. DBPs’ formation can not only impose some extra treatment costs but also activate some chemical carcinogens in the presence of natural organic matter (NOM) in secondary or tertiary treatment levels, causing deterioration of the situation.

Moreover, enumeration of viable cells by cell culture may not be fully realized at this moment as a laboratory equipped with bio-safety level 3/4 (BSL-3/4) cabinet is not available in all facilities or laboratories. Although reverse transcription quantitative polymerase chain reaction (RT-qPCR) has been applied to extract deoxyribonucleic acid (DNA)/ribonucleic acid (RNA) from different aliquots, viability of cells may not be confirmed from the extracted DNA/RNA. The presence of DNA/RNA can deliver a clue about the presence/absence of specific pathogens but infectiousness may, nonetheless, not be comprehended. Thus, researchers have been employing significant effort in enumeration and inactivation of pathogens causing emerging infectious diseases so that wastewater-based early alertness can be effectively developed. Although enumeration will develop awareness about the presence of certain viruses in the environment and aqueous phase, inactivation may ensure the extent of effectiveness of available disinfectants and possible prevention of dispersion of cells in both gaseous and aqueous phases.

Although it is comparatively stress-free to remove and inactivate those pathogens from a surface as few factors may influence the removal process, inactivation of those pathogens from water and wastewater, where myriad number of factors may affect the removal process, is an arduous task because some inactivation processes may not be pragmatic with presently available resources. Some published review papers are dedicated to discussing the inactivation of SARS-CoV-2, but a concrete review report on transport, dispersion, and inactivation of SARS-CoV, MARS-CoV, Ebola virus, Zika virus, and Lassa virus in aqueous phase is not available; inactivation mechanisms, the most important subject to successfully tackle an outbreak, are not elaborately discussed in those review papers. This report covers inactivation techniques of all the above-mentioned emerging viruses with richly depicted inactivation mechanisms of those viruses with possible impact of climate change on the evolution of those viruses. The main objectives of this report are to discuss the possible sources of four emerging pathogens’ contaminated wastewater, their enumeration process with currently available resources, inactivation mechanisms by disinfectants and other physicochemical inactivation techniques in aqueous phase so that quality potable water can be supplied to the end consumers and community awareness can be built on some rationales.

Filoviridae, the family of filamentous (length >1,000 nm) negative-sense single-stranded RNA virions, includes five major species of enveloped Ebola viruses (average diameter 80 nm; length 130–2,300 nm), responsible for diseases in humans and primates. Coronaviridae, the family of enveloped (coated by lipid bi-layer) positive-sense single-stranded RNA Coronaviruses, i.e., alphacoronavirus (α-CoV), betacoronavirus (β-CoV), gammacoronavirus (γ-CoV), and deltacoronavirus (Δ-CoV) (ICTV 2019), is responsible for diseases of birds, mammals, and amphibians. Among these, α-CoV and β-CoV species are basically accountable for mammal diseases. ZIKV (average diameter 40 nm), an enveloped virus from the family Flaviviridae and genus Flavivirus, with positive-sense, single-stranded RNA, can cause diseases in humans, birds, reptiles, and mammals. Lassa virus (average diameter 70–150 nm), a member of the Arenaviridae family with negative-sense, single-stranded RNA with envelope, can be transmitted from rats’ feces, urine, saliva, blood, and respiratory secretion to humans (Ogbu et al. 2007).

The first two families end up in wastewater through zoonotic spillover and oral–fecal route of transmission, and prominent sources of both families in water bodies are shown in Figure 1. Although non-enveloped viruses are more stable in water compared to enveloped viruses, enveloped RNA viruses have conspicuous survivability in water from 96-h to 720-h (Judson et al. 2015). ZIKV transmission is possible not only by mosquitoes, i.e., Aedes aegypti and Aedes albopictus (Du et al. 2019), or tick bites or zoonotic spillover but also by vertical (i.e., from mother to child) or horizontal (i.e., from one person to another) transmission, sex, blood transfusion, accidental exposure; the virus can contaminate aquatic environments or wastewater through discharging of semen, urine (0.7–220 × 106 genome copies/ml) (Gourinat et al. 2015), saliva, breast milk, amniotic fluid, and cerebrospinal fluid (Du et al. 2019). Lassa virus has been detected in infected people's blood, feces, urine, vomit, semen, and saliva (Ogbu et al. 2007) that can ultimately mix with wastewater and other sources of potable water. A patient infected by Ebola virus discharges about 9 l/d body fluid where virus genome concentration ranges from 2.8 to 7.2 log10 viral RNA copies/ml and Ebola virus is noticeably persistent in blood (Bibby et al. 2017). Ebola virus genome concentration in stool is 7 log10 RNA copies/ml, 5–6 log10 RNA copies/ml in urine, and 2–9 log10 RNA copies/ml in blood (Bibby et al. 2015; Casanova & Weaver 2015). MARS-CoV genome concentration in a patient's blood and serum generally varies from 3.3 to 4.2 log10 genome copies/ml and from 5 to 6 log10 RNA copies/ml, respectively (Keil et al. 2016; Hindawi et al. 2018). SARS-CoV-2 genome concentration in urine, stool, saliva or sputum, wastewater influent and effluent, and primary and secondary sludge can be 52 × 106 genome copies/l (Bardi & Oliaee 2021), 6.8 log10 genome copies/g (La Rosa et al. 2020), 104–1014 genome copies/l (Giacobbo et al. 2021), from 5 × 104 to 3 × 106 genome copies/l (Wurtzer et al. 2020), 7.5 × 103–14.7 × 103 genome copies/l (Zhang et al. 2020), and 1.17–4.02 × 104 genome copies/l (Bardi & Oliaee 2021), respectively. So far, SARS-CoV-2 and its gene have been detected in different types of water, e.g., untreated wastewater in France, Australia, Japan, Spain, USA, UK, Italy, Netherlands, India, UAE, Chile, Slovenia, Czech Republic and many other countries; water contaminated by untreated or partially treated wastewater; urban river water in Ecuador; sea water in Spain, UK, Morocco, and ocean organisms (García-Ávila et al. 2020). Therefore, virus cell inactivation and DNA/RNA disintegration are equally important to achieve total eradication of these viruses in aqueous phase as ruptured virus cells will spill nucleic acid and that nucleic acid may facilitate the replication of those viruses in the environment.

Figure 1

Sources of Ebola virus (dotted line) and Coronavirus (solid line) in wastewater (information from Giacobbo et al. 2021).

Figure 1

Sources of Ebola virus (dotted line) and Coronavirus (solid line) in wastewater (information from Giacobbo et al. 2021).

Close modal

All these pathogen-contaminated wastes can reach water and RRF. However, when these kinds of viruses are identified in water or wastewater, treatment plant operators should not discharge those pathogens with effluent without treatment as accidental inhalation or ingestion (WHO 2018; Yaro et al. 2021) or adsorption through cuts or sores (CDC 2021) can release those viruses into the bloodstream or gastrointestinal tract or nosocomial route and severe complexity may occur after such exposure. Moreover, meat consumption of infected mammals (i.e., bats, rats, and monkeys) and wild birds may be a possible transmission route of those viruses from animals to humans as those wild animals/birds have proven to be hosts of those viruses (Gutiérrez-Bugallo et al. 2019; Yaro et al. 2021); hence, treatment plant operators must take the utmost care to prevent a probable aquatic or gaseous phase transmission route.

Precise and accurate enumerations are very important for quick and early detection and warning to safeguard society, the environment, and eco-system against any outbreak of an epidemic and pandemic caused by emerging pathogens. For this reason, scientists have made significant efforts to develop user-friendly, cost-effective, and efficacious techniques: i.e., microscopic (e.g., scanning electron microscope (SEM); transmission electron microscope (TEM); atomic force microscope (AFM)), cultural (e.g., plating methods; most probable number (MPN); primary and continuous cell culture; cytopathogenic effect (CPE); plaque-forming unit (PFU); 50% tissue culture infectious dose (TCID50)), physiological, immunological (e.g., antibody; immune-affinity chromatographic assay; enzyme-linked immunosorbent assay (ELISA); immunofluorescense assay (IFA)), and nucleic acid-based (e.g., real time-PCR; RT-qPCR; digital PCR (dPCR); integrated cell culture-PCR (ICC-PCR); gene probe) analysis to support WBE, although applications of those techniques are dependent on several aspects, i.e., purpose, species, time-frame, and available resources. Among these technologies, RT-qPCR has been used as the gold standard to detect SARS-CoV-2 infection (Chen et al. 2020). Table 1 shows different enumeration techniques for targeted pathogens in water and wastewater.

Table 1

Enumeration techniques for targeted pathogens

TechniquesSpeciesGene typesPolynucleotide/oligonucleotide (primer/probe)References
RT-qPCR SARS-CoV-2 N1 gene 5′-GAGCCGAAAATGAGGGAAAT-3′ (forward) Ahmed et al. (2020) and Leung et al. (2020)  
   5′-TGTGGTTAGTGGGAGTTG AATCTG-3′ (reverse)  
   5′-FAM-ACCCCGCATTACGTTTGG TGGACC-BHQ1-3′ (probe)  
  N1 gene 5′-GACCCCAAAATCAGCGAAAT-3′ (forward) Arizti-Sanz et al. (2020)  
   5′-TCTGGTTACTGCCAGTTGAATCTG-3′ (reverse)  
   5′-FAM-ACCCCGCATTACGTTTGGTGGACC-BHQ1-3′ (probe)  
  N gene 5′GGGGAACTTCTCCTGCTAGAAT-3′ (forward) Zhang et al. (2020)  
   5′-CAGACATTTTGCTCTCAAGCTG-3′ (reverse)  
   5′FAM-TTGCTGCTGCTTGACAGATT-TAMRA-3′ (probe)  
  ORF 1ab 5′-CCCTGTGGGTTTTACACTTAA-3′ (forward)  
   5′-ACGATTGTGCATCAGCTGA-3′ (reverse)  
   5′-FAM-CCGTCTGCGGTATGTGGAAAGGTTATGG-BHQ1-3′ (probe)  
  ORF 1ab 5′-GTGCTAAACCACCGCCTG-3′ (forward) La Rosa et al. (2020)  
   5′-CAGATCATGGTTGCTTTGTAGGT-3′ (reverse)  
 SARS-CoV  5′-CTAACATGCTTAGGATAATGG-3′ (forward2) Wang et al. (2005)  
   5′-GCCTCTCTTGTTCTTGCTCGC-3′ (forward3)  
   5′-CAGGTAAGCGTAAAACTCATC-3′ (reverse1)  
 MARS-CoV N1 gene 5′-CAAAACCTTCCCTAAGAA GGAAAAG-3′ (forward) Hindawi et al. (2018)  
   5′-GCTCCTTTGGAGGTTCAGACAT-3′ (reverse)  
   5′-FAM-ACAAAAGGCACCAAAAGAAGAATCAACAGACC-BHQ1-3′ (probe)  
 ZIKV  5′AATGGGAAGGAAAGAAGAGG-3′ (forward) Lamb et al. (2018)  
   5′-GCTGGGGTGATGAGAGTTGT-3′ (reverse)  
 ZEBOV  5′-CAGCCAGCAATTTCTTCCAT-3′ (forward) Cook et al. (2016)  
   5′-TTTCGGTTGCTGTTTCTGTG-3′ (reverse)  
   FAM-5′-ATCATTGGCGTACTGGAGGAGCAG-3′ (probe)  
RT-PCR ZEBOV  5′-GCTTCCACAGTTATCTACCGAGG-3′ (forward) Warfield et al. (2007)  
   5′-CTCTCTCAAGGGGTGTGAGC-3′ (reverse)  
   FAM-5′-TTTCGCTGAAGGTGTCGTTGCA-3′-TAMRA (probe)  
Cell culture (PFU or TCID50SARS-CoV-2   Keil et al. (2020). Jiang et al. (2020), Patterson et al. (2020) and Buonanno et al. (2020)  
 SARS-CoV   Chan et al. (2020), Eickmann et al. (2020), Kariwa et al. (2006), Han et al. (2005), Lai et al. (2005), Wang et al. (2005) and Darnell et al. (2004)  
 MARS-CoV   Eickmann et al. (2018), Hindawi et al. (2018), Keil et al. (2016), Kumar et al. (2015) and Leclercq et al. (2014)  
 ZEBOV   Cutts et al. (2020), Eickmann et al. (2018), Bibby et al. (2015, (2017),Cook et al. (2016),Fischer et al. (2015) and Elliott et al. (1982)  
 Lassa virus   Elliott et al. (1982)  
 ZIKV   Wilde et al. (2016)  
TechniquesSpeciesGene typesPolynucleotide/oligonucleotide (primer/probe)References
RT-qPCR SARS-CoV-2 N1 gene 5′-GAGCCGAAAATGAGGGAAAT-3′ (forward) Ahmed et al. (2020) and Leung et al. (2020)  
   5′-TGTGGTTAGTGGGAGTTG AATCTG-3′ (reverse)  
   5′-FAM-ACCCCGCATTACGTTTGG TGGACC-BHQ1-3′ (probe)  
  N1 gene 5′-GACCCCAAAATCAGCGAAAT-3′ (forward) Arizti-Sanz et al. (2020)  
   5′-TCTGGTTACTGCCAGTTGAATCTG-3′ (reverse)  
   5′-FAM-ACCCCGCATTACGTTTGGTGGACC-BHQ1-3′ (probe)  
  N gene 5′GGGGAACTTCTCCTGCTAGAAT-3′ (forward) Zhang et al. (2020)  
   5′-CAGACATTTTGCTCTCAAGCTG-3′ (reverse)  
   5′FAM-TTGCTGCTGCTTGACAGATT-TAMRA-3′ (probe)  
  ORF 1ab 5′-CCCTGTGGGTTTTACACTTAA-3′ (forward)  
   5′-ACGATTGTGCATCAGCTGA-3′ (reverse)  
   5′-FAM-CCGTCTGCGGTATGTGGAAAGGTTATGG-BHQ1-3′ (probe)  
  ORF 1ab 5′-GTGCTAAACCACCGCCTG-3′ (forward) La Rosa et al. (2020)  
   5′-CAGATCATGGTTGCTTTGTAGGT-3′ (reverse)  
 SARS-CoV  5′-CTAACATGCTTAGGATAATGG-3′ (forward2) Wang et al. (2005)  
   5′-GCCTCTCTTGTTCTTGCTCGC-3′ (forward3)  
   5′-CAGGTAAGCGTAAAACTCATC-3′ (reverse1)  
 MARS-CoV N1 gene 5′-CAAAACCTTCCCTAAGAA GGAAAAG-3′ (forward) Hindawi et al. (2018)  
   5′-GCTCCTTTGGAGGTTCAGACAT-3′ (reverse)  
   5′-FAM-ACAAAAGGCACCAAAAGAAGAATCAACAGACC-BHQ1-3′ (probe)  
 ZIKV  5′AATGGGAAGGAAAGAAGAGG-3′ (forward) Lamb et al. (2018)  
   5′-GCTGGGGTGATGAGAGTTGT-3′ (reverse)  
 ZEBOV  5′-CAGCCAGCAATTTCTTCCAT-3′ (forward) Cook et al. (2016)  
   5′-TTTCGGTTGCTGTTTCTGTG-3′ (reverse)  
   FAM-5′-ATCATTGGCGTACTGGAGGAGCAG-3′ (probe)  
RT-PCR ZEBOV  5′-GCTTCCACAGTTATCTACCGAGG-3′ (forward) Warfield et al. (2007)  
   5′-CTCTCTCAAGGGGTGTGAGC-3′ (reverse)  
   FAM-5′-TTTCGCTGAAGGTGTCGTTGCA-3′-TAMRA (probe)  
Cell culture (PFU or TCID50SARS-CoV-2   Keil et al. (2020). Jiang et al. (2020), Patterson et al. (2020) and Buonanno et al. (2020)  
 SARS-CoV   Chan et al. (2020), Eickmann et al. (2020), Kariwa et al. (2006), Han et al. (2005), Lai et al. (2005), Wang et al. (2005) and Darnell et al. (2004)  
 MARS-CoV   Eickmann et al. (2018), Hindawi et al. (2018), Keil et al. (2016), Kumar et al. (2015) and Leclercq et al. (2014)  
 ZEBOV   Cutts et al. (2020), Eickmann et al. (2018), Bibby et al. (2015, (2017),Cook et al. (2016),Fischer et al. (2015) and Elliott et al. (1982)  
 Lassa virus   Elliott et al. (1982)  
 ZIKV   Wilde et al. (2016)  

Ebola virus

Some inactivation mechanisms of species of Ebola viruses and their surrogates are discussed below with the necessary information shown in Table 2. Casanova & Weaver (2015) evaluated the thermal inactivation rate of bacteriophage Φ6, a double-stranded RNA (ds-RNA) enveloped virus, as a surrogate of Ebola virus in wastewater at 22 °C (psychrophilic condition) and 30 °C (mesophilic condition) where inactivation rate was very fast at 30 °C compared to 22 °C. Inactivation rate was linear at 30 °C but inactivation rate was non-linear and segmented, i.e., different rates at different time periods at 22 °C; and 6–7 log10 inactivation could be achieved within 3–7 days where temperature, virus concentration, virus type, strains, treatment process, holding time, and wastewater composition may be important factors in virus removal. Inactivation rate of virus in surface water was slower than that in wastewater; however, inactivation rate was faster in wastewater than in pure water. Moreover, dsRNA structure of Φ6 contributed more stability in the inactivation process compared to ssRNA Ebola virus and Coronavirus.

Table 2

Emerging Ebola virus removal rate by different inactivation mechanisms

Pathogen genusDisinfectants or inactivation process (Concentration)% removal/log-removal or TCID50 (Contact time /intensity)Other propertiesReferences
Φ6 (in blood) Hydrogen peroxide vapor (HPV) (>400 mg/l) 5.5-log10 PFU (32-h) Initial virus titer = 5 × 106 PFU/coupon; glass surface Wood et al. (2020)  
  6.5-log10 PFU (32-h) Stainless steel  
  4.9-log10 PFU (32-h) Tile  
  5.6-log10 PFU (32-h) N95 filter medium  
  6.0-log10 PFU (32-h) Painted joint tape (PJT)  
  6.5-log10 PFU (32-h) Wood  
MS2 (in blood) Hydrogen peroxide vapor (HPV) (>400 mg/l) 3.5-log10 PFU (32-h) Initial virus titer = 5 × 106 PFU/coupon; glass surface  
  2.5-log10 PFU (32-h) Stainless steel  
  2.7-log10 PFU (32-h) Tile  
  2.7-log10 PFU (32-h) N95 filter medium  
  3.0-log10 PFU (32-h) Painted joint tape (PJT)  
  2.7-log10 PFU (32-h) Wood  
ZEBOV-Makona Activated hydroger peroxide (AHP) 6.4-log10 TCID50/ml (1-min) Initial virus titer = 8.8-log10 TCID50/ml Cutts et al. (2020)  
 Quaternary ammonium compounds (QACs) 6.6-log10 TCID50/ml (1-min)   
Vesicular stomatitis virus (VSV) AHP 6.2-log10 TCID50/ml (1-min) Initial virus titer = 8.8-log10 TCID50/ml  
 QAC 6.0-log10 TCID50/ml (1-min)   
ZEBOV- Mayinga in platelets Photo inactivation (UVC, 254 nm) >4.5 log10 TCID50/ml (0.2 J/cm2Initial virus titer = 8.11 log10 TCID50/ml Eickmann et al. (2018)  
Methylene blue (MB) in plasma Visible light (LED) >4.7 log10 TCID50/ml (120 J/cm2Initial virus titer = 8.83 log10 TCID50/ml  
ZEBOV NaOCl (1 mg/l) 3.5 log10 TCID50/ml (20 s) Initial virus titer = 105 TCID50/ml; Bibby et al. (2017)  
 NaOCl (5/10 mg/l) 4.18 log10 TCID50/ml (20 s)   
MS2 Absorption/Emission from aeration tank 0.137 log10 (3-h) Initial virus titer = 107 PFU/ml Lin & Marr (2017)  
 Biological emission from sewage pipe 0.071 log10 (3-h)   
Φ6 Absorption/Emission from aeration tank 0.8 log10 (3-h) Initial virus titer = 107 PFU/ml  
 Biological emission from sewage pipe 2.6 log10 (3-h)   
Bacteriophage Φ6 Thermal inactivation 1-log removal (0.31-d) Raw hospital wastewater and fecal waste; Initial virus titer = 107.8 PFU/ml; 37 °C; Strasser (2017)  
  2-log (0.63-d)   
  3-log (0.94-d)   
  4-log (1.3-d)   
  5-log (1.6-d)   
  1-log (1.8-d) 22 °C  
  2-log (3.6-d)   
  3-log (5.5-d)   
  4-log (7.3-d)   
  5-log (9.1-d)   
 Chemical inactivation, NaOCl (400 mg/l) 1-log (10-min)   
 2,800 mg/l 5-log (10-min)   
Coliphage ΦX-174 Thermal inactivation 1-log removal (3.9-d) Initial virus titer = 107.8 PFU/ml; 37 °C  
  2-log (7.7-d)   
  3-log (12.0-d)   
  4-log (15.0-d)   
  5-log (19.0-d)   
  1-log (17.0-d) 22 °C  
  2-log (33.0-d)   
  3-log (50.0-d)   
  4-log (67.0-d)   
  5-log (83.0-d)   
 Chemical inactivation, NaOCl (960 mg/l) 1-log (10-min)   
 3,500 mg/l 5-log (10-min)   
Coliphage MS2 Thermal inactivation 1-log removal (5.0-d) Initial virus titer = 107.8 PFU/ml; 37 °C  
  2-log (10.0-d)   
  3-log (15.0-d)   
  4-log (20.0-d)   
  5-log (25.0-d)   
  1-log (8.3-d) 22 °C  
  2-log (17.0-d)   
  3-log (25.0-d)   
  4-log (33.0-d)   
  5-log (42.0-d)   
 Chemical inactivation, NaOCl (3,800 mg/l) 1-log (10-min)   
 24,000 mg/l 5-log (10-min)   
E. coli Chemical inactivation, 0.05% NaOCl (stable) 90% Rinse water; initial bacteria concentration = 5 × 108 CFU/ml; pH = 11; without OL Wolfe et al. (2017)  
 0.05% NaOCl (freshly generated) 90% pH = 9–11  
 0.05% sodium dichloro-isocyanurate (NaDCC) 85.5% pH = 6  
 High-test hypochlorite (HTH), 65% CaOCl 87% pH = 11  
Φ6 0.05% NaOCl (stable) 51% Rinse water; initial virus titer = 107 PFU/ml; pH = 11; without OL  
 0.05% NaOCl (freshly generated) 51%   
 0.05% NaDCC 52%   
 HTH, 65% CaOCl 49%   
ZEBOV Thermal inactivation 90% (6.6-d) Initial virus titer = 6 log10 TCID50/ml Bibby et al. (2015)  
ZEBOV-Mayinga 70% EtOH 100% (1 min)  Cook et al. (2016)  
 0.05% NaOCl 40.3% (10 min)   
 0.1% NaOCl 70.15% (10 min)   
 0.5% NaOCl 100% (5 min)   
 1.0% NaOCl 100% (5 min)   
ZEBOV-Kikwat 70% EtOH 100% (1 min)   
 0.05% NaOCl 43.3% (10 min)   
 0.1% NaOCl 70.15% (10 min)   
 0.5% NaOCl 100% (5 min)   
 1.0% NaOCl 100% (5 min)   
ZEBOV-Makona 70% EtOH 100% (2.5 min)   
 0.05% NaOCl 28.4% (10 min)   
 0.1% NaOCl 73.1% (10 min)   
 0.5% NaOCl 100% (5 min)   
 1.0% NaOCl 100% (5 min)   
Φ6 Thermal inactivation 2 log10 (24-h) 30 °C Casanova & Weaver (2015)  
  5.2 log10 (48-h)   
  >7.0 log10 (72-h)   
  0.14 log10 (24-h) 22 °C  
  5 log10 (5-d)   
ZEBOV-Makona-WPGC07 Thermal inactivation 100% (4-d) Water; Initial virus titer = 104.5 log10 TCID50/ml; 27 °C Fischer et al. (2015)  
  100% (7-d) Initial virus titer = 104.2 log10 TCID50/ml; 21 °C  
  100% (7-d) Dry blood; Initial virus titer = 105 log10 TCID50/ml; 27 °C; RH = 80%  
  100% (6-d) Initial virus titer = 105 log10 TCID50/ml; 21 °C; RH = 40%  
  7.14% (8-d) Liquid blood; Initial virus titer = 104.2 log10 TCID50/ml; 27 °C  
  17% (8-d) Initial virus titer = 104.7 log10 TCID50/ml; 21 °C  
ZEBOV Photo inactivation by 1,5 iodonaphthylazide (INA, 100 μmol/l) + UV (310–360 nm) 37.5% (10-min, 10 mW/cm2/min) Initial virus titer = 8 × 104 PFU/ml Warfield et al. (2007)  
ZEBOV-Mayinga Thermal inactivation 5-log10 PFU/ml (22-min) Initial virus titer = 106 PFU/ml; 60 °C Mitchell & McCormick (1984)  
ZEBOV Photo-inactivation (gamma irradiation, 60Co) 100% (98 × 104 rads) Initial virus titer = 6.5 log10 TCID50/ml; 4 °C Elliott et al. (1982)  
  100% (140 × 104 rads) −60 °C  
Pathogen genusDisinfectants or inactivation process (Concentration)% removal/log-removal or TCID50 (Contact time /intensity)Other propertiesReferences
Φ6 (in blood) Hydrogen peroxide vapor (HPV) (>400 mg/l) 5.5-log10 PFU (32-h) Initial virus titer = 5 × 106 PFU/coupon; glass surface Wood et al. (2020)  
  6.5-log10 PFU (32-h) Stainless steel  
  4.9-log10 PFU (32-h) Tile  
  5.6-log10 PFU (32-h) N95 filter medium  
  6.0-log10 PFU (32-h) Painted joint tape (PJT)  
  6.5-log10 PFU (32-h) Wood  
MS2 (in blood) Hydrogen peroxide vapor (HPV) (>400 mg/l) 3.5-log10 PFU (32-h) Initial virus titer = 5 × 106 PFU/coupon; glass surface  
  2.5-log10 PFU (32-h) Stainless steel  
  2.7-log10 PFU (32-h) Tile  
  2.7-log10 PFU (32-h) N95 filter medium  
  3.0-log10 PFU (32-h) Painted joint tape (PJT)  
  2.7-log10 PFU (32-h) Wood  
ZEBOV-Makona Activated hydroger peroxide (AHP) 6.4-log10 TCID50/ml (1-min) Initial virus titer = 8.8-log10 TCID50/ml Cutts et al. (2020)  
 Quaternary ammonium compounds (QACs) 6.6-log10 TCID50/ml (1-min)   
Vesicular stomatitis virus (VSV) AHP 6.2-log10 TCID50/ml (1-min) Initial virus titer = 8.8-log10 TCID50/ml  
 QAC 6.0-log10 TCID50/ml (1-min)   
ZEBOV- Mayinga in platelets Photo inactivation (UVC, 254 nm) >4.5 log10 TCID50/ml (0.2 J/cm2Initial virus titer = 8.11 log10 TCID50/ml Eickmann et al. (2018)  
Methylene blue (MB) in plasma Visible light (LED) >4.7 log10 TCID50/ml (120 J/cm2Initial virus titer = 8.83 log10 TCID50/ml  
ZEBOV NaOCl (1 mg/l) 3.5 log10 TCID50/ml (20 s) Initial virus titer = 105 TCID50/ml; Bibby et al. (2017)  
 NaOCl (5/10 mg/l) 4.18 log10 TCID50/ml (20 s)   
MS2 Absorption/Emission from aeration tank 0.137 log10 (3-h) Initial virus titer = 107 PFU/ml Lin & Marr (2017)  
 Biological emission from sewage pipe 0.071 log10 (3-h)   
Φ6 Absorption/Emission from aeration tank 0.8 log10 (3-h) Initial virus titer = 107 PFU/ml  
 Biological emission from sewage pipe 2.6 log10 (3-h)   
Bacteriophage Φ6 Thermal inactivation 1-log removal (0.31-d) Raw hospital wastewater and fecal waste; Initial virus titer = 107.8 PFU/ml; 37 °C; Strasser (2017)  
  2-log (0.63-d)   
  3-log (0.94-d)   
  4-log (1.3-d)   
  5-log (1.6-d)   
  1-log (1.8-d) 22 °C  
  2-log (3.6-d)   
  3-log (5.5-d)   
  4-log (7.3-d)   
  5-log (9.1-d)   
 Chemical inactivation, NaOCl (400 mg/l) 1-log (10-min)   
 2,800 mg/l 5-log (10-min)   
Coliphage ΦX-174 Thermal inactivation 1-log removal (3.9-d) Initial virus titer = 107.8 PFU/ml; 37 °C  
  2-log (7.7-d)   
  3-log (12.0-d)   
  4-log (15.0-d)   
  5-log (19.0-d)   
  1-log (17.0-d) 22 °C  
  2-log (33.0-d)   
  3-log (50.0-d)   
  4-log (67.0-d)   
  5-log (83.0-d)   
 Chemical inactivation, NaOCl (960 mg/l) 1-log (10-min)   
 3,500 mg/l 5-log (10-min)   
Coliphage MS2 Thermal inactivation 1-log removal (5.0-d) Initial virus titer = 107.8 PFU/ml; 37 °C  
  2-log (10.0-d)   
  3-log (15.0-d)   
  4-log (20.0-d)   
  5-log (25.0-d)   
  1-log (8.3-d) 22 °C  
  2-log (17.0-d)   
  3-log (25.0-d)   
  4-log (33.0-d)   
  5-log (42.0-d)   
 Chemical inactivation, NaOCl (3,800 mg/l) 1-log (10-min)   
 24,000 mg/l 5-log (10-min)   
E. coli Chemical inactivation, 0.05% NaOCl (stable) 90% Rinse water; initial bacteria concentration = 5 × 108 CFU/ml; pH = 11; without OL Wolfe et al. (2017)  
 0.05% NaOCl (freshly generated) 90% pH = 9–11  
 0.05% sodium dichloro-isocyanurate (NaDCC) 85.5% pH = 6  
 High-test hypochlorite (HTH), 65% CaOCl 87% pH = 11  
Φ6 0.05% NaOCl (stable) 51% Rinse water; initial virus titer = 107 PFU/ml; pH = 11; without OL  
 0.05% NaOCl (freshly generated) 51%   
 0.05% NaDCC 52%   
 HTH, 65% CaOCl 49%   
ZEBOV Thermal inactivation 90% (6.6-d) Initial virus titer = 6 log10 TCID50/ml Bibby et al. (2015)  
ZEBOV-Mayinga 70% EtOH 100% (1 min)  Cook et al. (2016)  
 0.05% NaOCl 40.3% (10 min)   
 0.1% NaOCl 70.15% (10 min)   
 0.5% NaOCl 100% (5 min)   
 1.0% NaOCl 100% (5 min)   
ZEBOV-Kikwat 70% EtOH 100% (1 min)   
 0.05% NaOCl 43.3% (10 min)   
 0.1% NaOCl 70.15% (10 min)   
 0.5% NaOCl 100% (5 min)   
 1.0% NaOCl 100% (5 min)   
ZEBOV-Makona 70% EtOH 100% (2.5 min)   
 0.05% NaOCl 28.4% (10 min)   
 0.1% NaOCl 73.1% (10 min)   
 0.5% NaOCl 100% (5 min)   
 1.0% NaOCl 100% (5 min)   
Φ6 Thermal inactivation 2 log10 (24-h) 30 °C Casanova & Weaver (2015)  
  5.2 log10 (48-h)   
  >7.0 log10 (72-h)   
  0.14 log10 (24-h) 22 °C  
  5 log10 (5-d)   
ZEBOV-Makona-WPGC07 Thermal inactivation 100% (4-d) Water; Initial virus titer = 104.5 log10 TCID50/ml; 27 °C Fischer et al. (2015)  
  100% (7-d) Initial virus titer = 104.2 log10 TCID50/ml; 21 °C  
  100% (7-d) Dry blood; Initial virus titer = 105 log10 TCID50/ml; 27 °C; RH = 80%  
  100% (6-d) Initial virus titer = 105 log10 TCID50/ml; 21 °C; RH = 40%  
  7.14% (8-d) Liquid blood; Initial virus titer = 104.2 log10 TCID50/ml; 27 °C  
  17% (8-d) Initial virus titer = 104.7 log10 TCID50/ml; 21 °C  
ZEBOV Photo inactivation by 1,5 iodonaphthylazide (INA, 100 μmol/l) + UV (310–360 nm) 37.5% (10-min, 10 mW/cm2/min) Initial virus titer = 8 × 104 PFU/ml Warfield et al. (2007)  
ZEBOV-Mayinga Thermal inactivation 5-log10 PFU/ml (22-min) Initial virus titer = 106 PFU/ml; 60 °C Mitchell & McCormick (1984)  
ZEBOV Photo-inactivation (gamma irradiation, 60Co) 100% (98 × 104 rads) Initial virus titer = 6.5 log10 TCID50/ml; 4 °C Elliott et al. (1982)  
  100% (140 × 104 rads) −60 °C  

Note: PFU/ml = 0.7 TCID50/ml.

Bibby et al. (2015) examined the persistence of Ebola virus in sterilized wastewater where virus titer had decreased due to inactivation, particle aggregation and adsorption on solids in wastewater. All these mechanisms had decreased virus titers in aqueous phase but persistence may increase on solid surfaces if those surfaces act as a shield. Ninety per cent inactivation was identified after 2.1-d including time zero time point and 6.6-d excluding time zero time point. Inactivation was slower in wastewater compared to deionized water where 90% inactivation was observed within 1.8-d at 21 °C but the rate of inactivation was faster than that of in blood as 90% inactivation was achieved in 21-d. Persistence of Ebola virus in wastewater is lower than that of other enteric viruses, i.e., hepatitis A (>17-d), adenovirus (33-d), and poliovirus (5-d). Microbial, i.e., bacteria and protozoan activity may, however, decrease virus titer in wastewater by consuming those viruses as nutrient sources or forming different metabolites that are harmful for virus existence. Again, WHO recommended a holding time of 1 week to aid 3-log virus inactivation.

Fischer et al. (2015) witnessed ZEBOV stability in different inanimate surfaces and aqueous phase with different temperatures and relative humidities (RHs); and ZEBOV was more stable at 21 °C rather than 27 °C with ≈1-log10 removal/d. ZEBOV persistence in liquid blood was longer than that in dry blood because nutrient and metabolite transfer in dry conditions are relatively tough due to hampered biochemical conditions. ZEBOV stability in non-human primate (NHP) blood (14-d) is almost similar to in human blood; and several factors, i.e., virus titer concentration, virus species, sample matrices, parameters related to weather and sterility can influence the virus infectivity and dispersion when zoonotic transformation may be a serious issue.

Disinfection characteristics for three variants of ZEBOV, i.e., 1976 Mayinga, 1995 Kikwat, and 2014 Makona were examined by Cook et al. (2016) by using 70% ethanol (EtOH), 0.05%, 0.1%, 0.5%, and 1.0% sodium hypochlorite (NaOCl) as disinfectants; and Makona variant had higher resistance than that of the other two variants regardless of temperature and RH. Disinfection efficacy was increased with increasing concentration and contact time. Cultured cell inactivation was the most reliable and standard methodology; however, RNA extraction was effectively accomplished rather than recovery of Ebola virus particles from specific media. Evolution of ZEBOV was significantly noticeable as disinfectant resistance developed with time.

Bibby et al. (2017) depicted Ebola virus inactivation in unsterilized and gamma-irradiated wastewater by NaOCl with concentrations of 0, 1, 5, and 10 mg/l and noticed rapid chlorine decay in irradiated wastewater due to the presence of significant chlorine demand in the sample when virus inactivation was very slow in that same sample. Although rapid virus inactivation was observed with a disinfectant dose of 1 mg/l in the first 20-s, no removal was observed later because of the rapid decrease of free chlorine (FC) and no virus recovery was observed for disinfectant doses of 5 and 10 mg/l. 4-log10 virus removal was achieved in concentration time (Ct) value of 1.1 mg-min/l when NaOCl concentration was 5 and 10 mg/L; however, USEPA recommended value for the same removal is 3 mg-min/l. Some factors, i.e., pH, composition of wastewater, mixing, and virus aggregation can affect the inactivation process. No virus removal was detected between pH 4.3 and 6.9 but 1-log10 virus removal was discovered after 193-min at pH 11.2; thus, virus can be killed at elevated pH.

Lin & Marr (2017) investigated aerosolization and removal of two surrogates, i.e., MS2 and Φ6 of ZEBOV, by toilet flushing, converging of pipes and in aeration tank, although it was noticed that 94% of virions generally remain in aqueous phase rather than in gaseous phase or in bio-solids. The number of aerosols produced was high in aeration tank (aerosol diameter: 55–60 nm) compared to toilet flushing (aerosol diameter: 25–52 nm) and pipe converging (aerosol diameter: 130–162 nm), but the volume of aerosol produced was large in toilet flushing rather than in aeration tank and pipe convergence. Aerosolization of MS2 was more efficient than Φ6 due to the absence of lipid bi-layer and small structure (25–80 nm) of MS2. Virus emission in aerosol form was observed from both aeration tank and pipe convergence, although emission from toilet flushing was very slight. However, Φ6 emission was rapid compared to MS2 because Φ6 had high absorption and thermal inactivation rates. Also, virus emission was high from aeration tank and low from pipe convergence; and aeration tank virus emission rate was ten times higher than that of from pipe convergence, where both systems had high potential of inhalation exposure to treatment facility workers. MS2 and Φ6 were used as surrogates of ZEBOV in this experiment, but the icosahedral structure of Φ6 significantly differed from the filamentous structure of ZEBOV. Aerosolization may also differ due to certain factors, i.e., virion size and shape, fluid viscosity, mixing, turbulence, wastewater composition, operation variables, environmental parameters and area open to air.

Strasser (2017) inspected the survivability of three surrogates, i.e., MS2, ΦX-174, and Φ6 of ZEBOV by thermal (i.e., 22 °C and 37 °C) and chemical (i.e., NaOCl) inactivation processes applied in a mixture of raw hospital wastewater (75%) and human fecal waste (25%). Virus survivability decreased with increasing temperature, contact time, and disinfectant dose. The virus can be protected by aggregation (i.e., 2–3 virus particles are attached together), adsorption on another virus particle or on any other particulate matter, and embedded on a surface if disinfectant is not properly mixed with the sample. Therefore, chlorine can inactivate pathogens by penetrating the outer envelope, losing and damaging cell components, oxidizing a number of amino acids in proteins and enzymes, degradation of nucleic acids, altering the structural components, and hampering ATP production process; however, resistance is a factor basically depending on virus species and defense mechanisms. Moreover, ammonia concentration in wastewater with pH varying from 8.0 to 9.3 can also facilitate the virus inactivation process, although duration of the removal process is quite lengthy, but combined chlorine with ammonia by forming mono-chloramine, di-chloramine, and tri-chloramine can effectively inactivate virus with the substantial possibility of DBPs’ formation. Furthermore, inactivation mechanisms, e.g., reactions with amino acids, namely, cysteine, cystine, methionine, and tryptophan; fragmentation of RNA and denaturing the protein structure (Jacangelo et al. 1987) have been observed because of chloramines. Required chlorine concentration can be minimized in water and wastewater by reducing turbidity, oxidizable organic matter, and chlorine demand for other inorganic compounds. Average daily inactivation was 0.12-log, 0.06-log, and 0.55-log removal at 22 °C for MS2, ΦX-174, and Φ6, respectively, and 0.2-log, 0.26-log, and 3.2-log removal at 37 °C for MS2, ΦX-174, and Φ6, respectively; where as Φ6 was most sensitive to thermal treatment as well as to chemical disinfectant. Inactivation was faster in the first 3-min for all species and inactivation rate was 1.7, 4.4, and 5.7 times faster at the temperature of 37 °C for MS2, ΦX-174, and Φ6, respectively.

Wolfe et al. (2017) compared inactivation of two ZEBOV surrogates, i.e., Escherichia coli and Φ6 by chlorine-based disinfectants from rinse water loaded with organic substances (i.e., 7.80 mg/ml bovine serum albumin, 10.92 mg/ml tryptone, 2.52 mg/ml bovine mucin) or without any organic loading (OL) where inactivation rate was high for E. coli rather than Φ6 because virus has high resistance compared to bacteria against chlorine-based disinfectants; and the presence of organic substances can slightly decrease inactivation rate for E. coli but marginally increase Φ6 removal. Stabilized and freshly generated NaOCl had a similar removal rate for both surrogates regardless of OL; however, all chlorine-based disinfectants had significant removal efficacy for bacteria and virus. Chlorine generally oxidizes the outer membrane and peptidoglycan layer of bacteria, whereas lipid membrane and capsid proteins of virus are basically ruptured in the presence of corrosive oxidizing agents.

Wood et al. (2020) studied the inactivation of two well-known surrogates, i.e., MS2 (non-enveloped outer-layer) and Phi6 (enveloped outer-layer) of ZEBOV by hydrogen peroxide vapor (HPV) from six different types of surfaces where non-enveloped viruses had high resistance to disinfectant compared to enveloped viruses and high concentration of HPV (>400 mg/l) had more inactivation efficiency than that of low HPV (≈25 mg/l). Blood was present as organic loading in the system where virus persistence was significantly increased in the presence of blood since blood acted as a shield for the virus particles or blood oxidation decreased disinfectant concentration available to inactivate viruses. However, virus inactivation was more than 3-log reduction within 2-h in the absence of blood and other factors, i.e., temperature, RH, outer-layer structure and types of surfaces can influence removal mechanisms. It is also surmised that ZEBOV may be more stable in blood compared to water. Moreover, H2O2 (≈17 mg/l) alone had insignificant inactivation potential (<0.1-log) against MS2; but 4-log removal was realizable by the combined action of Fe(II) and H2O2 within a very short time and reactive oxygen species’ (ROSs) formation had a major influence on the inactivation process where increasing H2O2 concentration, increasing pH, and the presence of complex forming agents had deleterious impacts on the inactivation process (Kim et al. 2010).

Warfield et al. (2007) inspected inactivation of ZEBOV by combining UV irradiation and a photo-inducible alkylating agent, named 1,5 iodonaphthylazide (INA), without damaging the antigenic function and structural integrity of cells; and no sign of virus infectivity and replication was detected in the system after treatment with UV + INA. No morphological and structural conformation change was observed under TEM after treatment, although significant distortion of structural immunogenic epitopes was identified due to crosslinks of surface glycoprotein (GP) and lipid by-layers where virus infectivity was hindered by spoiling GP fusion activity. However, INA-treated ZEBOV stimulated the adaptive response since some non-crossed antibodies emerged from denatured antigens and a strong immunogenic response can be expected from INA-treated virus. This technique is a better approach to damage virus infectivity but its impact on water and wastewater treatment should be carefully evaluated because of the presence of some mutagenic, teratogenic, and carcinogenic compounds.

Elliott et al. (1982) examined Ebola virus inactivation by gamma irradiation (60Co) at 4 °C and −60 °C. Inactivation in the frozen state needed a greater amount of energy than that in liquid state where the synergistic impact of radiation and heat was responsible for inactivation. Moreover, this method achieved a better inactivation outcome compared to UV light.

Thus, Fenton-like reactions (electro or photo-assisted) have perceptible antimicrobial potential where DBPs’ formation, because of high H2O2 concentration, may be minimized due to organic oxidation, and mineralization of cell debris and remaining DBPs can be achieved. Semiconductor materials in the presence of a photon source can accelerate the degradation process but the presence of OL (except biological cell) in the aliquot can decrease the efficiency of oxidative damage of the pathogen cell and its components. Excess OL, however, is a dilemma in the Fenton-supported process: OL can act as electron source (e) to form OH from H2O2 but formed OH may be consumed to oxidize other organic chemicals. A parallel decontamination process may remove various pollutants from the aqueous phase, even though recalcitrant pollutant formation may be a possibility. Minimization of total organic carbon (TOC) content will be an issue for the advanced oxidation process (AOP)-assisted disinfection process efficiency; otherwise, full potential of ROSs and H2O2 in pathogen inactivation may not be achieved.

Coronavirus

During the deadly outbreaks, a significant number of studies have been conducted and some of their relevant outcomes are critically discussed below, with the removal efficacy of pathogens, e.g., SARS-CoV, SARS-CoV-2, and MARS-CoV, shown in Table 3. Lamarre & Talbot (1989) enthusiastically tried to understand the impacts of pH and temperature on HCoV-229E inactivation when infectivity of different strains of the same family can respond differently to pH and temperature as most Coronaviruses may be inactivated at acidic pH and high temperature, i.e., >25 °C. However, virus viability may not be affected at extreme pH at low temperature, i.e., 4 °C, and virus was the most stable at pH 5.0–8.0. Rapid thawing and freezing of virus particles, however, may not affect the morbidity or mortality of viruses as rapid change of temperature may not distort protein and DNA/RNA structure or hinder enzymatic activity.

Table 3

Inactivation rate of Coronavirus under different scenarios

Pathogen genusDisinfectants or inactivation process (Concentration)% removal/log-removal or TCID50 (Contact time/intensity)Other propertiesReferences
SARS-CoV-2 AcoD 99.77% Wastewater sludge; Initial virus gene = 20 × 106 copies/l; OL = 1.5 g-VS/l; 20 °C Bardi & Oliaee (2021)  
  99.945% OL = 3.5 g-VS/l; 20 °C  
  99.855% OL = 1.5 g-VS/l; 35 °C  
SARS-CoV-2 Thermal inactivation 5-log10 (25-d) Initial virus titer = 10 TCID50/10 μl; virus in suspension; 25 °C; RH = 50% Chan et al. (2011)  
  5-log10 (25-d) Virus in dry condition  
  3.5-log10 (1-d) 38 °C; RH = >95%  
  1-log10 (1-d) 33 °C; RH = >95%  
  0.75-log10 (1-d) 28 °C; RH = >95%  
  2-log10 (1-d) 38 °C; RH = 85%  
  0.75-log10 (1-d) 33 °C; RH = 85%  
  0.25-log10 (1-d) 28 °C; RH = 85%  
SAES-CoV-2 Chemical inactivation, Ozone (O3, 36 mg/l) 100% (10-min) Initial virus titer = 4.0 × 103 PFU/ml Hu et al. (2021)  
  100% (5-min)   
  100% (1-min)   
 O3 (36 mg/l) 100% (1-min) Initial virus titer = 4.0 × 104 PFU/ml  
 O3 (18 mg/l) 100% (1-min)   
 O3 (4.5 mg/l) 98.25% (1-min)   
SARS-CoV-2 Thermal inactivation of E-Sarbeco gene 50% (16-d) Wastewater; Initial gene concentration = 7.4 log10 copies /100 ml; 4 °C Hokajärvi et al. (2021)  
  90% (52-d)   
  99% (105-d)   
  No decay −20 °C/ − 75 °C  
 Thermal inactivation of N2 gene 50% (11-d) Initial gene concentration = 8.1 log10 copies/100 ml; 4 °C  
  90% (36-d)   
  99% (73-d)   
  No decay −20 °C/ − 75 °C  
HCoV-NL63 Photocatalytic inactivation, UVC (254 nm, 30 W) 93.1–95.0% (1-min) Initial virus titer = 2.1 × 106 TCID50/ml Khaiboullina et al. (2021)  
  100% (5-min)   
  88.89% (0.5-min) Virus in liquid droplet  
  91.76% (0.5-min) Dried virus  
 TiO2 nanoparticles (TNP) + UVC (254 nm, 30 W) 100% (1-min)   
  97.78% (0.5-min) Virus in liquid droplet  
  98.82% (0.5-min) Dried virus  
 TNP + UVC (254 nm, 4,300 μW/cm296.32% (1-min) Irradiation from 50 cm  
 TNP + UVC (254 nm, 13,000 μW/cm2100% (0.5-min)   
 UVC (254 nm, 30 W) 92.81% (1-min) RH = 45%  
  94.50% (1-min) RH = 65%  
  98.00% (1-min) RH = 85%  
 TNP + UVC (254 nm, 30 W) 99.71% (1-min) RH = 45%  
  99.71% (1-min) RH = 65%  
  100.00% (1-min) RH = 85%  
SARS-CoV-2 Photo inactivation (FUVC, 222 nm) 4.4-log10 TCID50/ml (30 mJ/cm2Intermittent irradiation Kitagawa et al. (2021)  
  4.6-log10 TCID50/ml (30 mJ/cm2Continuous irradiation  
SARS-CoV-2 UASB process 1.3-log Wastewater; Initial gene concentration = 3,500 gene copies/L Kumar et al. (2021)  
SARS-CoV-2 Chemical inactivation, QACs (0.2% w/w) >3.19-log10 (15-s) Water; Initial virus titer = 107 PFU/ml; no organic load Ogilvie et al. (2021)  
  >3.02-log10 (30-s)   
  >3.19-log10 (15-s) In hard water  
  >2.72-log10 (30-s)   
  2.09-log10 (15-s) 5% Bovine serum albumin (BSA) as organic load  
  >2.68-log10 (30-s)   
  >2.97-log10 (15-s) 5% Bovine mucin (BM) as organic load  
  >2.93-log10 (30-s)   
SARS-CoV-2 Electro-chemical oxidation (5 V) 99.99% (5-min) Water; Initial virus titer = 2.5 × 107 TCID50/ml; <37 °C Tu et al. (2021)  
 4 V >99% (5-min)   
 2 V 87% (5-min)   
SARS-CoV-2 Thermal inactivation 4.25-log (10-min) Initial virus titer = 105.5 TCID50/0.1 ml; 56 °C Xiling et al. (2021)  
  ≥5.17-log (10-min) 70 °C  
  ≥5.17-log (5-min) 90 °C  
 Chemical inactivation, FC (250 mg/l) 3.25-log (5-min)   
 500 mg/l 3.58-log (0.5-min)   
 1,000 mg/l ≥4.72-log (0.5-min)   
SARS-CoV-2 Thermal inactivation 90% (27.8-d) Untreated wastewater (UWW); Initial genome concentration = 106.03 gene copies/ml; 4 °C Ahmed et al. (2020)  
  90% (20.4-d) 15 °C  
  90% (12.6-d) 25 °C  
  90% (8.04-d) 37 °C  
  90% (43.2-d) Autoclaved wastewater (AWW); 4 °C  
  90% (29.9-d) 15 °C  
  90% (13.5-d) 25 °C  
  90% (5.71-d) 37 °C  
  90% (58.6-d) Tap water (TW); 4 °C  
  90% (51.2-d) 15 °C  
  90% (15.2-d) 25 °C  
  90% (9.40-d) 37 °C  
MHV  90% (56.6-d) UWW; initial genome concentration = 105.84 gene copies/ml; 4 °C  
  90% (28.5-d) 15 °C  
  90% (17.3-d) 25 °C  
  90% (7.44-d) 37 °C  
  90% (43.1-d) AWW; 4 °C  
  90% (33.9-d) 15 °C  
  90% (17.6-d) 25 °C  
  90% (5.58-d) 37 °C  
  90% (43.9-d) TW; 4 °C  
  90% (71.2-d) 15 °C  
  90% (18.6-d) 25 °C  
  90% (10.9-d) 37 °C  
SARS-CoV-2 Thermal inactivation 3.37 log10 TCID50/ml (15-min) Initial virus titer = 6.6 log10 TCID50/ml; 56 °C Batéjat et al. (2020)  
  5.93 log10 TCID50/ml (15-min) 65 °C  
SARS-CoV-2 Photo inactivation (UVC, 254 nm) 3-log10 (3.7 mJ/cm2Initial virus titer = 3 × 105 gene copy number/ml Biasin et al. (2021)  
SARS-CoV-2 Thermal inactivation 90% (1.6-d) and 99% (3.2-d) WW; Initial virus titer = 5 log10 TCID50/ml; 20 °C Bivins et al. (2020)  
  90% (2.1-d) and 99% (4.3-d) WW; Initial virus titer = 3 log10 TCID50/ml; 20 °C  
  90% (2.0-d) and 99% (3.9-d) Tap water (TW); Initial virus titer = 5 log10 TCID50/ml; 20 °C  
  90% (15-min) and 99% (30-min) WW; Initial virus titer = 5 log10 TCID50/ml; 50 °C  
  90% (2.2-min) and 99% (4.5-min) WW; Initial virus titer = 5 log10 TCID50/ml; 70 °C  
HCoV-229E Photo-inactivation (Far-UVC, 12 W 222 nm KrCl excimer lamp) 1-log10 (0.56 mJ/cm2Aerosolized virus; Initial virus titer = 7.5 log10 TCID50/ml; 24 °C; RH = 66%; Buonanno et al. (2020)  
  2-log10 (1.1 mJ/cm2  
  3-log10 (1.7 mJ/cm2  
HCoV-OC43  1-log10 (0.39 mJ/cm2  
  2-log10 (0.78 mJ/cm2  
  3-log10 (1.2 mJ/cm2  
SARS-CoV-2 Thermal inactivation 4.8 log10 TCID50/ml (3-d) Initial virus titer = 106.5 TCID50/ml; 37 °C Chan et al. (2020)  
  4.8 log10 TCID50/ml (3-d) 30 °C  
  4.8 log10 TCID50/ml (14-d) 25 °C  
  2 log10 TCID50/ml (14-d) 4 °C  
 Chemical inactivation, ethanol (75%) >1.83 log10 TCID50/ml (1-min) 25 °C  
 NaOCl (20 mg/l) >2.3 log10 TCID50/ml (1-min) 25 °C  
 NaOCl (100,000 mg/l) >3.25 log10 TCID50/ml (1-min) 25 °C  
 pH based (2, 3, 12, 13) >6.5 log10 TCID50/ml (1-d)   
SARS-CoV Thermal inactivation 5.8 log10 TCID50/ml (3-d) Initial virus titer = 107 TCID50/ml; 37 °C  
  5.8 log10 TCID50/ml (5-d) 30 °C  
  5.8 log10 TCID50/ml (14-d) 25 °C  
  0.4 log10 TCID50/ml (14-d) 4 °C  
SARS-CoV-2 Thermal inactivation of N gene 48.55% (30-min) 56 °C Chen et al. (2020)  
 Thermal inactivation of ORF 56.40% (30-min)   
 N gene 49.96% (20-min) 80 °C  
 ORF 65.96% (20-min)   
 N gene 100.0% (20-min) 100 °C/121 °C  
 ORF 100.0% (20-min)   
 Chemical inactivation (TRIzol), N gene 47.54% (10-min) 22 °C  
 ORF 39.85% (10-min)   
SARS-CoV-Frankfurt 1 in platelets Photo inactivation (UVC) >3.4 log10 TCID50/ml (0.2 J/cm2Initial virus titer = 7.2 log10 TCID50/ml Eickmann et al. (2020)  
MB in plasma Visible light >3.1 log10 TCID50/ml (120 J/cm2Initial virus titer = 7.4 log10 TCID50/ml  
HCoV-OC43 Photo-inactivation (UV-LED) 3.9 log10 removal (267 nm at 10 mJ/cm2Initial virus titer = 8 × 105 PFU/ml Gerchman et al. (2020)  
  3.9 log10 removal (279 nm at 26 mJ/cm2  
  4.4 log10 removal (286 nm at 37 mJ/cm2  
  4.2 log10 removal (297 nm at 54 mJ/cm2  
SARS-CoV-2 Nanostructured Al 6,063 alloy (rough surface) 100% (6-h) Initial virus titer = 105 TCID50/ml; Roughness = 995 nm; Water contact angle = 17.7 ° Hasan et al. (2020)  
 Al 6,063 alloy (smooth surface) 100% (48-h) Water contact angle = 96.3 °  
 Polystyrene tissue culture plate (TCP) 99.85% (48-h)   
SARS-CoV-2 Photo-inactivation; UVA (365 nm, 540 μW/cm2) and UVC (254 nm, 1,940 μW/cm2100% (9-min) Initial concentration = 5 × 106 TCID50/ml; Irradiation dose = 1.94 mJ/cm2 (UVC) and 0.54 mJ/cm2 (UVA) Heilingloh et al. (2020)  
  50% (1.4-min)   
 UVC 100% (9-min) Irradiation dose = 1,048 mJ/cm2  
SARS-CoV-2 Thermal inactivation 5-log (32.5-min) 60 °C Hessling et al. (2020)  
  5-log (3.7-min) 80 °C  
  5-log (0.5-min) 100 °C  
SARS-CoV-2 Photo-inactivation; DUV-LED (250–300 nm) 87.4% (1-s) Initial concentration = 2 × 104 plaque forming unit (PFU)/ml; Irradiation rate = 3.75 mW/cm2 Inagaki et al. (2020)  
  99.9% (10-s)   
  >99.9% (20-s)   
  99.9% (10-s)   
  >99.9% (20-s)   
MHV-A59 Thermal inactivation >6-log (1-s) Initial virus titer = 5 × 107 PFU/ml; 115 °C Jiang et al. (2020)  
  7.7-log (0.5-s) >125 °C  
  5-log (0.25-s) 150 °C  
  Not effective (0.1-s) 170 °C  
SARS-CoV-2 in platelets Photocatalytic inactivation (riboflavin, 500 μmol/L and UV, 6.24 J/mL) ≥4.53 log10 PFU/ml Initial virus titer = 4.77 log10 PFU/ml Keil et al. (2020)  
In plasma  ≥3.40 log10 PFU/ml Initial virus titer = 4.62 log10 PFU/ml  
SARS-CoV-2 Gamma irradiation (60Co source) 6.5 log10 TCID50/ml (1 Mrad) Initial virus titer = 6.5 log10 TCID50/ml Leung et al. (2020)  
  6.45 log10 TCID50/ml (0.16 Mrad)   
SARS-CoV-2 Photo inactivation (UV, 254 nm) 7.5 log10 PFU/ml (0.04 J/cm2Initial virus titer = 7.5 log10 PFU/ml Patterson et al. (2020)  
 Chemical inactivation (methanol, 6.1 log10 TCID50/ml Initial virus titer = 6.6 log10 PFU/ml  
 4%) paraformaldehyde 6.1 log10 TCID50/ml   
SARS-CoV-2 Photo-inactivation (Solar radiation) 90% (27-min) UV flux = 0.26 J/m2.min; In summer Sagripanti & Lytle (2020)  
  90% (>300-min) UV flux = 0.01 J/m2.min; In winter  
  90% (115-min) UV flux = 0.06 J/m2.min; In spring  
  90% (63-min) UV flux = 0.11 J/m2.min; In fall  
Bacteriophage Φ6 Photo-inactivation (LED, 405 nm) 3-log (1,300 J/cm2Initial concentration = 107 PFU/ml; Size = 75 nm Vatter et al. (2020)  
  1-log (430 J/cm2  
SARS-CoV-2 NaOCl (6,700 g/m3100% Medical wastewater Zhang et al. (2020)  
MARS-CoV in platelets Photo inactivation (UVC, 254 nm) >3.8 log10 TCID50/ml (0.2 J/cm2Initial virus titer = 8.12 log10 TCID50/ml Eickmann et al. (2018)  
MB in plasma Visible light (LED) >3.3 log10 TCID50/ml (120 J/cm2Initial virus titer = 7.86 log10 TCID50/ml  
MARS-CoV Photocatalytic inactivation (amotosalen and UVA 4.67 log10 PFU/ml Initial virus titer = 7.8 log10 PFU/ml Hindawi et al. (2018)  
  7.13 log10 RNA copies/ml Initial genome titer = 10.51 log10 RNA copies/ml  
Coliphage MS2 Photocatalytic inactivation, VUV (185 + 254 nm) 100% (0.125-s) Initial virus titer = 1.7 × 103 PFU/ml; RH = 40% Kim & Jang (2018)  
 UV (254 nm) 49% (0.125-s)   
 O3 100% (0.125-s)   
 UV (254 nm) + O3 100% (0.125-s)   
 VUV (185 + 254 nm) 100% (0.052-s)   
 UV (254 nm) 32% (0.052-s)   
 O3 98% (0.052-s)   
 UV (254 nm) + O3 96% (0.052-s)   
 VUV (185 + 254 nm) 100% (0.026-s)   
 UV (254 nm) 12% (0.026-s)   
 O3 95% (0.026-s)   
 UV (254 nm) + O3 95% (0.026-s)   
 VUV (185 + 254 nm) 61% (0.009-s)   
 O3 10% (0.009-s)   
 UV (254 nm) + O3 9% (0.009-s)   
 VUV (185 + 254 nm) 50% (0.004-s)   
 TiO2 plate + VUV 58% (0.009-s)   
 Pd-TiO2 plate + VUV 60% (0.009-s)   
 Pd-TiO2 plate (5 mm) + VUV 66% (0.009-s)   
 Pd-TiO2 spiral + VUV 43% (0.009-s)   
 Pd-TiO2 (2 mm) + VUV 69% (0.009-s)   
 Pd-TiO2 (2 mm) + VUV + UV 68% (0.009-s)   
 Pd-TiO2 (2 mm) + VUV 66% (0.009-s) RH = 10%  
  68% (0.009-s) RH = 40%  
  58% (0.009-s) RH = 70%  
 Pd-TiO2 (2 mm) 44% (0.009-s) 4 °C; RH = 40%  
 Pd-TiO2 (2 mm) + VUV 64% (0.009-s)   
 Pd-TiO2 (2 mm) 44% (0.009-s) 25 °C; RH = 40%;  
 Pd-TiO2 (2 mm) + VUV 68% (0.009-s)   
Bacteriophage Φ6 FC (2 mg/l) 6-log (8-s) Initial virus concentration = 4.5 × 1010 PFU/ml Ye et al. (2018)  
 UV254 6-log (215 mJ/cm2Irradiation intensity = 0.14 mW/cm2  
MARS-CoV Photocatalytic inactivation (riboflavin, 500 μmol/L and UV, 6.24 J/mL) 4.25-log Initial virus titer = 3.6 × 107 PFU/ml Keil et al. (2016)  
MARS-CoV Photo inactivation (Gamma irradiation, 60Co) 100% (2 Mrad) Initial virus titer = 1.6 × 1010 PFU/ml Kumar et al. (2015)  
  83.3% (1 Mrad) Initial virus titer = 106 PFU/ml  
MARS-CoV Thermal inactivation 4.67 log10 TCID50/ml (0.5-min) Initial virus titer = 5.59 log10 TCID50/ml; 56 °C Leclercq et al. (2014)  
  3.67 log10 TCID50/ml (0.5-min) 65 °C  
TGEV Thermal inactivation 8-log (38-d) PSWW; Initial concentration = 5.8 log10 MPN/ml; 25 °C Casanova et al. (2009)  
  1.25-log (35-d) PSWW; Initial concentration = 5.5 log10 MPN/ml; 4 °C  
  2.6-log (14-d) Lake water; Initial concentration = 5.0 log10 MPN/ml; 25 °C  
  1-log (14-d) Lake water; Initial concentration = 5.2 log10 MPN/ml; 4 °C  
  4.2-log (49-d) Pure water; Initial concentration = 4.5 log10 MPN/ml; 25 °C  
  No removal (49-d) Pure water; Initial concentration = 6.5 log10 MPN/ml; 4 °C  
MHV  8-log (28-d) PSWW; Initial concentration = 6.6 log10 MPN/ml; 25 °C  
  0.75-log (35-d) PSWW; Initial concentration = 6.8 log10 MPN/ml; 4 °C  
  2.5-log (14-d) Lake water; Initial concentration = 6.9 log10 MPN/ml; 25 °C  
  No removal (14-d) Lake water; Initial concentration = 6.6 log10 MPN/ml; 4 °C  
  5.6-log (49-d) Pure water; Initial concentration = 6.5 log10 MPN/ml; 25 °C  
  0.2-log (49-d) Pure water; Initial concentration = 6.5 log10 MPN/ml; 4 °C  
HCoV Thermal inactivation 99% and 99.9% after 6.76-d and 10.1-d, respectively Filtered tap water at 23 °C Gundy et al. (2009)  
  99% and 99.9% after 8.09-d and 12.1-d, respectively Unfiltered tap water at 23 °C  
  99% and 99.9% after 392-d and 588-d, respectively Unfiltered tap water at 4 °C  
  99% and 99.9% after 1.57-d and 2.35-d, respectively Filtered primary effluent 23 °C  
  99% and 99.9% after 2.36-d and 3.54-d, respectively Unfiltered primary effluent at 23 °C  
  99% and 99.9% after 1.85-d and 2.77-d, respectively Secondary effluent  
PV  99% and 99.9% after 43.3-d and 64.9-d, respectively Filtered tap water at 23 °C  
  99% and 99.9% after 47.5-d and 71.3-d, respectively Unfiltered tap water at 23 °C  
  99% and 99.9% after 135-d and 203-d, respectively Unfiltered tap water at 4 °C  
  99% and 99.9% after 23.6-d and 35.5-d, respectively Filtered primary effluent at 23 °C  
  99% and 99.9% after 7.27-d and 10.9-d, respectively Unfiltered primary effluent at 23 °C  
  99% and 99.9% after 3.83-d and 5.74-d, respectively Secondary effluent  
SARS-CoV-Hanoi Thermal inactivation 5.81-log (5-min) Initial virus titer = 2.6 × 107 TCID50/ml; 56 °C Kariwa et al. (2006)  
  6.41-log (30-min)   
  100% (60-min)   
 Photo inactivation (UV) 5.32-log (15-min, 134 μW/cm2Initial virus titer = 3.8 × 107 TCID50/ml  
  6.31-log (30-min, 134 μW/cm2  
 Chemical inactivation, 100% methanol 6.02-log (30-min) Initial virus titer = 2.1 × 107 TCID50/ml  
 100% acetone 5.81-log (5-min) Initial virus titer = 1.3 × 107 TCID50/ml  
 2.5% glutaraldehyde 4.14-log (5-min) Initial virus titer = 2.2 × 106 TCID50/ml  
 3.5% paraformaldehyde 3.7-log (5-min) Initial virus titer = 1.6 × 106 TCID50/ml  
SARS-CoV- P9 Catalytic oxidation (Ag/Al2O3105.5 TCID50/ml (5-min) Initial virus titer = 106 TCID50/ml; 20 °C Han et al. (2005)  
 Cu/Al2O3 105.25 TCID50/ml (5-min)   
 Al2O3 100.25 TCID50/ml (5-min)   
SARS-CoV- GVU6109 NaOCl (500 mg/l) >3-log (5-min) Initial virus titer = 107 TCID50/ml; 20 °C Lai et al. (2005)  
 NaOCl (1,000 mg/l) >3-log (5-min)   
SARS-CoV-Urbani Photo-catalytic inactivation (amotosalen-HCl, 150 μmol/L and UVA, 320–400 nm) 105.5 PFU/ml (4-min, 3 J/cm2Initial virus titer = 105.5 PFU/ml Lin et al. (2005)  
SARS-CoV Chemical inactivation, NaOCl (5 mg/l); FC (0.11 mg/l) 68.38% (30-min) Wastewater; Initial virus titer = 101.75 TCID50/ml; 20 °C Wang et al. (2005)  
 NaOCl (10 mg/l); FC (0.4 mg/l) 100% (30-min)   
 NaOCl (20 mg/l); FC (0.5 mg/l) 100% (30-min)   
 NaOCl (40 mg/l); FC (0.82 mg/l) 100% (30-min)   
E. coli NaOCl (20 mg/l); FC (0.5 mg/l) 100% (30-min) Wastewater; Initial bacteria concentration = 1.3 × 106 CFU/l  
 NaOCl (40 mg/l); FC (0.82 mg/l) 100% (30-min)   
f2 phage NaOCl (5 mg/l); FC (0.11 mg/l) 30.91% (30-min) Wastewater; Initial virus titer = 1.1 × 105 PFU/l  
 NaOCl (10 mg/l); FC (0.4 mg/l) 27.27% (30-min)   
 NaOCl (20 mg/l); FC (0.5 mg/l) 79.09% (30-min)   
 NaOCl (40 mg/l); FC (0.82 mg/l) 100% (30-min)   
SARS-CoV NaOCl (10 mg/l); FC (0.39 mg/l) 43.77% (1-min) Wastewater; Initial virus titer = 101.6 TCID50/ml; 20 °C  
 NaOCl (10 mg/l); FC (0.33 mg/l) 68.38% (5-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 100% (10-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 100% (20-min)   
 NaOCl (10 mg/l); FC (0.35 mg/l) 100% (30-min)   
E. coli NaOCl (10 mg/l); FC (0.39 mg/l) 0.0% (1-min) Wastewater; Initial bacteria concentration = 4.6 × 105 CFU/l  
 NaOCl (10 mg/l); FC (0.33 mg/l) 0.0% (5-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 14.29% (10-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 26.09% (20-min)   
 NaOCl (10 mg/l); FC (0.35 mg/l) 20.21% (30-min)   
f2 phage NaOCl (10 mg/l); FC (0.39 mg/l) 15.79% (1-min) Wastewater; Initial virus titer = 1.9 × 105 PFU/l  
 NaOCl (10 mg/l); FC (0.33 mg/l) 15.79% (5-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 18.32% (10-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 21.05% (20-min)   
 NaOCl (10 mg/l); FC (0.35 mg/l) 31.58% (30-min)   
SARS-CoV NaOCl (20 mg/l); FC (0.59 mg/l) 100% (1-min) Wastewater; Initial virus titer = 101.75 TCID50/ml; 20 °C  
 NaOCl (20 mg/l); FC (0.57 mg/l) 100% (5-min)   
 NaOCl (20 mg/l); FC (0.51 mg/l) 100% (10-min)   
 NaOCl (20 mg/l); FC (0.50 mg/l) 100% (20-min)   
 NaOCl (20 mg/l); FC (0.53 mg/l) 100% (30-min)   
E. coli NaOCl (20 mg/l); FC (0.59 mg/l) 23.09% (1-min) Wastewater; Initial bacteria concentration = 5.5 × 105 CFU/l  
 NaOCl (20 mg/l); FC (0.57 mg/l) 99.97% (5-min)   
 NaOCl (20 mg/l); FC (0.51 mg/l) 99.99% (10-min)   
 NaOCl (20 mg/l); FC (0.50 mg/l) 99.9998% (20-min)   
 NaOCl (20 mg/l); FC (0.53 mg/l) 100% (30-min)   
f2 phage NaOCl (20 mg/l); FC (0.59 mg/l) 0.0% (1-min) Wastewater; Initial virus titer = 2.9 × 105 PFU/l  
 NaOCl (20 mg/l); FC (0.57 mg/l) 13.78% (5-min)   
 NaOCl (20 mg/l); FC (0.51 mg/l) 23.46% (10-min)   
 NaOCl (20 mg/l); FC (0.50 mg/l) 48.67% (20-min)   
 NaOCl (20 mg/l); FC (0.53 mg/l) 78.24% (30-min)   
SARS-CoV ClO2 (5 mg/l); FC (0.00 mg/l) 0.0% (30-min) Wastewater; Initial virus titer = 101.75 TCID50/ml; 20 °C  
 ClO2 (10 mg/l); FC (0.00 mg/l) 94.38% (30-min)   
 ClO2 (20 mg/l); FC (0.00 mg/l) 82.22% (30-min)   
 ClO2 (40 mg/l); FC (2.19 mg/l) 100% (30-min)   
E. coli ClO2 (5 mg/l); FC (0.00 mg/l) 0.0% (30-min) Wastewater; Initial bacteria concentration = 1.3 × 106 CFU/l  
 ClO2 (10 mg/l); FC (0.00 mg/l) 0.0% (30-min)   
 ClO2 (20 mg/l); FC (0.00 mg/l) 0.0% (30-min)   
 ClO2 (40 mg/l); FC (2.19 mg/l) 99.46% (30-min)   
f2 phage ClO2 (5 mg/l); FC (0.00 mg/l) 0.0% (30-min) Wastewater; Initial virus titer = 1.1 × 105 PFU/l  
 ClO2 (10 mg/l); FC (0.00 mg/l) 32.73% (30-min)   
 ClO2 (20 mg/l); FC (0.00 mg/l) 42.73% (30-min)   
 ClO2 (40 mg/l); FC (2.19 mg/l) 60.0% (30-min)   
SARS-CoV ClO2 (10 mg/l) 43.77% (1-min) Wastewater; Initial virus titer = 101.6 TCID50/ml; 20 °C  
 ClO2 (10 mg/l) 68.38% (5-min)   
 ClO2 (10 mg/l) 68.38% (10-min)   
 ClO2 (10 mg/l) 68.38% (20-min)   
 ClO2 (10 mg/l) 55.33% (30-min)   
E. coli ClO2 (10 mg/l) 0.0% (1-min) Wastewater; Initial bacteria concentration = 4.6 × 105 CFU/l  
 ClO2 (10 mg/l) 17.39% (5-min)   
 ClO2 (10 mg/l) 0.0% (10-min)   
 ClO2 (10 mg/l) 14.29% (20-min)   
 ClO2 (10 mg/l) 21.74% (30-min)   
f2 phage ClO2 (10 mg/l) 42.11% (1-min) Wastewater; Initial virus titer = 1.9 × 105 PFU/l  
 ClO2 (10 mg/l) 26.32% (5-min)   
 ClO2 (10 mg/l) 17.79% (10-min)   
 ClO2 (10 mg/l) 26.32% (20-min)   
 ClO2 (10 mg/l) 47.37% (30-min)   
SARS-CoV ClO2 (40 mg/l); FC (19.10 mg/l) 94.37% (1-min) Wastewater; Initial virus titer = 101.75 TCID50/ml; 20 °C  
 ClO2 (40 mg/l); FC (17.59 mg/l) 100% (5-min)   
 ClO2 (40 mg/l); FC (13.99 mg/l) 100% (10-min)   
 ClO2 (40 mg/l); FC (10.91 mg/l) 100% (20-min)   
 ClO2 (40 mg/l); FC (5.86 mg/l) 100% (30-min)   
E. coli ClO2 (40 mg/l); FC (19.10 mg/l) 100% (1-min) Wastewater; Initial bacteria concentration = 5.5 × 105 CFU/l  
 ClO2 (40 mg/l); FC (17.59 mg/l) 99.999% (5-min)   
 ClO2 (40 mg/l); FC (13.99 mg/l) 99.99% (10-min)   
 ClO2 (40 mg/l); FC (10.91 mg/l) 99.99% (20-min)   
 ClO2 (40 mg/l); FC (5.86 mg/l) 100% (30-min)   
f2 phage ClO2 (40 mg/l); FC (19.10 mg/l) 13.78% (1-min) Wastewater; Initial virus titer = 2.9 × 105 PFU/l  
 ClO2 (40 mg/l); FC (17.59 mg/l) 23.46% (5-min)   
 ClO2 (40 mg/l); FC (13.99 mg/l) 17.65% (10-min)   
 ClO2 (40 mg/l); FC (10.91 mg/l) 48.97% (20-min)   
 ClO2 (40 mg/l); FC (5.86 mg/l) 68.78% (30-min)   
SARS-CoV-Urbani Photo inactivation (UVC, 254 nm) 4.75 log10 TCID10/ml (15-min, 4,016 μW/cm2Initial virus titer = 6.33 log10 TCID10/ml Darnell et al. (2004)  
 UVA, 365 nm 0.45 log10 TCID10/ml (15-min, 2,133 μW/cm2  
 Gamma irradiation (60Co source) 0.9 log10 TCID10/ml (15,000 rads)   
 Thermal inactivation 5.33 log10 TCID10/ml (20-min) 56 °C  
  4.70 log10 TCID10/ml (10-min) 65 °C  
  6.33 log10 TCID10/ml (45-min) 75 °C  
 Chemical inactivation (formaldehyde) 5.0 log10 TCID10/ml (24-h) 25 °C/35 °C  
 Glutaraldehyde 5.33 log10 TCID10/ml (24-h) 25 °C/35 °C  
 pH based (1, 12, 14) 5.33 log10 TCID10/ml (24-h) 4 °°C/25 °C/37 °C  
HCoV-229E Drying 100% (12-h) Initial virus titer = 5.5x × 105 TCID50/ml; aluminum; 21 °C; RH = 55–70% Sizun et al. (2000)  
  100% (12-h) Sterile sponges  
  100% (12-h) Latex surgical gloves  
 Thermal inactivation 65% (6-d) Phosphate buffer saline (PBS); 37 °C  
  100% (6-d) Earle's minimal essential medium (EMEM)  
HCoV-OC43 Drying 100% (3-h) Initial virus titer = 5.15 × 105 TCID50/ml; aluminum; 21 °C; RH = 55–70%  
  100% (1-h) Sterile sponges  
  100% (1-h) Latex surgical gloves  
 Thermal inactivation 54% (6-d) PBS; 37 °C  
  90% (6-d) EMEM  
HCoV-229E Thermal inactivation 0.6 log10 PFU/ml (6-h) Initial virus titer = 6.1 log10 PFU/ml; 4 °C; pH = 9.0 Lamarre & Talbot (1989)  
  >4.8 log10 PFU/ml (6-h) pH = 4.0  
  0.0 log10 PFU/ml (6-h) pH = 7.0  
  >4.8 log10 PFU/ml (6-h) 33 °C; pH = 9.0  
  >4.8 log10 PFU/ml (6-h) pH = 4.0  
  0.6 log10 PFU/ml (6-h) pH = 7.0  
  0.6 log10 PFU/ml (14-d) 4 °C; pH = 6.0  
  >4.8 log10 PFU/ml (14-d) 22 °C; pH = 6.0  
  >4.8 log10 PFU/ml (12-d) 33 °C; pH = 6.0  
  >4.8 log10 PFU/ml (5-d) 37 °C; pH = 6.0  
Pathogen genusDisinfectants or inactivation process (Concentration)% removal/log-removal or TCID50 (Contact time/intensity)Other propertiesReferences
SARS-CoV-2 AcoD 99.77% Wastewater sludge; Initial virus gene = 20 × 106 copies/l; OL = 1.5 g-VS/l; 20 °C Bardi & Oliaee (2021)  
  99.945% OL = 3.5 g-VS/l; 20 °C  
  99.855% OL = 1.5 g-VS/l; 35 °C  
SARS-CoV-2 Thermal inactivation 5-log10 (25-d) Initial virus titer = 10 TCID50/10 μl; virus in suspension; 25 °C; RH = 50% Chan et al. (2011)  
  5-log10 (25-d) Virus in dry condition  
  3.5-log10 (1-d) 38 °C; RH = >95%  
  1-log10 (1-d) 33 °C; RH = >95%  
  0.75-log10 (1-d) 28 °C; RH = >95%  
  2-log10 (1-d) 38 °C; RH = 85%  
  0.75-log10 (1-d) 33 °C; RH = 85%  
  0.25-log10 (1-d) 28 °C; RH = 85%  
SAES-CoV-2 Chemical inactivation, Ozone (O3, 36 mg/l) 100% (10-min) Initial virus titer = 4.0 × 103 PFU/ml Hu et al. (2021)  
  100% (5-min)   
  100% (1-min)   
 O3 (36 mg/l) 100% (1-min) Initial virus titer = 4.0 × 104 PFU/ml  
 O3 (18 mg/l) 100% (1-min)   
 O3 (4.5 mg/l) 98.25% (1-min)   
SARS-CoV-2 Thermal inactivation of E-Sarbeco gene 50% (16-d) Wastewater; Initial gene concentration = 7.4 log10 copies /100 ml; 4 °C Hokajärvi et al. (2021)  
  90% (52-d)   
  99% (105-d)   
  No decay −20 °C/ − 75 °C  
 Thermal inactivation of N2 gene 50% (11-d) Initial gene concentration = 8.1 log10 copies/100 ml; 4 °C  
  90% (36-d)   
  99% (73-d)   
  No decay −20 °C/ − 75 °C  
HCoV-NL63 Photocatalytic inactivation, UVC (254 nm, 30 W) 93.1–95.0% (1-min) Initial virus titer = 2.1 × 106 TCID50/ml Khaiboullina et al. (2021)  
  100% (5-min)   
  88.89% (0.5-min) Virus in liquid droplet  
  91.76% (0.5-min) Dried virus  
 TiO2 nanoparticles (TNP) + UVC (254 nm, 30 W) 100% (1-min)   
  97.78% (0.5-min) Virus in liquid droplet  
  98.82% (0.5-min) Dried virus  
 TNP + UVC (254 nm, 4,300 μW/cm296.32% (1-min) Irradiation from 50 cm  
 TNP + UVC (254 nm, 13,000 μW/cm2100% (0.5-min)   
 UVC (254 nm, 30 W) 92.81% (1-min) RH = 45%  
  94.50% (1-min) RH = 65%  
  98.00% (1-min) RH = 85%  
 TNP + UVC (254 nm, 30 W) 99.71% (1-min) RH = 45%  
  99.71% (1-min) RH = 65%  
  100.00% (1-min) RH = 85%  
SARS-CoV-2 Photo inactivation (FUVC, 222 nm) 4.4-log10 TCID50/ml (30 mJ/cm2Intermittent irradiation Kitagawa et al. (2021)  
  4.6-log10 TCID50/ml (30 mJ/cm2Continuous irradiation  
SARS-CoV-2 UASB process 1.3-log Wastewater; Initial gene concentration = 3,500 gene copies/L Kumar et al. (2021)  
SARS-CoV-2 Chemical inactivation, QACs (0.2% w/w) >3.19-log10 (15-s) Water; Initial virus titer = 107 PFU/ml; no organic load Ogilvie et al. (2021)  
  >3.02-log10 (30-s)   
  >3.19-log10 (15-s) In hard water  
  >2.72-log10 (30-s)   
  2.09-log10 (15-s) 5% Bovine serum albumin (BSA) as organic load  
  >2.68-log10 (30-s)   
  >2.97-log10 (15-s) 5% Bovine mucin (BM) as organic load  
  >2.93-log10 (30-s)   
SARS-CoV-2 Electro-chemical oxidation (5 V) 99.99% (5-min) Water; Initial virus titer = 2.5 × 107 TCID50/ml; <37 °C Tu et al. (2021)  
 4 V >99% (5-min)   
 2 V 87% (5-min)   
SARS-CoV-2 Thermal inactivation 4.25-log (10-min) Initial virus titer = 105.5 TCID50/0.1 ml; 56 °C Xiling et al. (2021)  
  ≥5.17-log (10-min) 70 °C  
  ≥5.17-log (5-min) 90 °C  
 Chemical inactivation, FC (250 mg/l) 3.25-log (5-min)   
 500 mg/l 3.58-log (0.5-min)   
 1,000 mg/l ≥4.72-log (0.5-min)   
SARS-CoV-2 Thermal inactivation 90% (27.8-d) Untreated wastewater (UWW); Initial genome concentration = 106.03 gene copies/ml; 4 °C Ahmed et al. (2020)  
  90% (20.4-d) 15 °C  
  90% (12.6-d) 25 °C  
  90% (8.04-d) 37 °C  
  90% (43.2-d) Autoclaved wastewater (AWW); 4 °C  
  90% (29.9-d) 15 °C  
  90% (13.5-d) 25 °C  
  90% (5.71-d) 37 °C  
  90% (58.6-d) Tap water (TW); 4 °C  
  90% (51.2-d) 15 °C  
  90% (15.2-d) 25 °C  
  90% (9.40-d) 37 °C  
MHV  90% (56.6-d) UWW; initial genome concentration = 105.84 gene copies/ml; 4 °C  
  90% (28.5-d) 15 °C  
  90% (17.3-d) 25 °C  
  90% (7.44-d) 37 °C  
  90% (43.1-d) AWW; 4 °C  
  90% (33.9-d) 15 °C  
  90% (17.6-d) 25 °C  
  90% (5.58-d) 37 °C  
  90% (43.9-d) TW; 4 °C  
  90% (71.2-d) 15 °C  
  90% (18.6-d) 25 °C  
  90% (10.9-d) 37 °C  
SARS-CoV-2 Thermal inactivation 3.37 log10 TCID50/ml (15-min) Initial virus titer = 6.6 log10 TCID50/ml; 56 °C Batéjat et al. (2020)  
  5.93 log10 TCID50/ml (15-min) 65 °C  
SARS-CoV-2 Photo inactivation (UVC, 254 nm) 3-log10 (3.7 mJ/cm2Initial virus titer = 3 × 105 gene copy number/ml Biasin et al. (2021)  
SARS-CoV-2 Thermal inactivation 90% (1.6-d) and 99% (3.2-d) WW; Initial virus titer = 5 log10 TCID50/ml; 20 °C Bivins et al. (2020)  
  90% (2.1-d) and 99% (4.3-d) WW; Initial virus titer = 3 log10 TCID50/ml; 20 °C  
  90% (2.0-d) and 99% (3.9-d) Tap water (TW); Initial virus titer = 5 log10 TCID50/ml; 20 °C  
  90% (15-min) and 99% (30-min) WW; Initial virus titer = 5 log10 TCID50/ml; 50 °C  
  90% (2.2-min) and 99% (4.5-min) WW; Initial virus titer = 5 log10 TCID50/ml; 70 °C  
HCoV-229E Photo-inactivation (Far-UVC, 12 W 222 nm KrCl excimer lamp) 1-log10 (0.56 mJ/cm2Aerosolized virus; Initial virus titer = 7.5 log10 TCID50/ml; 24 °C; RH = 66%; Buonanno et al. (2020)  
  2-log10 (1.1 mJ/cm2  
  3-log10 (1.7 mJ/cm2  
HCoV-OC43  1-log10 (0.39 mJ/cm2  
  2-log10 (0.78 mJ/cm2  
  3-log10 (1.2 mJ/cm2  
SARS-CoV-2 Thermal inactivation 4.8 log10 TCID50/ml (3-d) Initial virus titer = 106.5 TCID50/ml; 37 °C Chan et al. (2020)  
  4.8 log10 TCID50/ml (3-d) 30 °C  
  4.8 log10 TCID50/ml (14-d) 25 °C  
  2 log10 TCID50/ml (14-d) 4 °C  
 Chemical inactivation, ethanol (75%) >1.83 log10 TCID50/ml (1-min) 25 °C  
 NaOCl (20 mg/l) >2.3 log10 TCID50/ml (1-min) 25 °C  
 NaOCl (100,000 mg/l) >3.25 log10 TCID50/ml (1-min) 25 °C  
 pH based (2, 3, 12, 13) >6.5 log10 TCID50/ml (1-d)   
SARS-CoV Thermal inactivation 5.8 log10 TCID50/ml (3-d) Initial virus titer = 107 TCID50/ml; 37 °C  
  5.8 log10 TCID50/ml (5-d) 30 °C  
  5.8 log10 TCID50/ml (14-d) 25 °C  
  0.4 log10 TCID50/ml (14-d) 4 °C  
SARS-CoV-2 Thermal inactivation of N gene 48.55% (30-min) 56 °C Chen et al. (2020)  
 Thermal inactivation of ORF 56.40% (30-min)   
 N gene 49.96% (20-min) 80 °C  
 ORF 65.96% (20-min)   
 N gene 100.0% (20-min) 100 °C/121 °C  
 ORF 100.0% (20-min)   
 Chemical inactivation (TRIzol), N gene 47.54% (10-min) 22 °C  
 ORF 39.85% (10-min)   
SARS-CoV-Frankfurt 1 in platelets Photo inactivation (UVC) >3.4 log10 TCID50/ml (0.2 J/cm2Initial virus titer = 7.2 log10 TCID50/ml Eickmann et al. (2020)  
MB in plasma Visible light >3.1 log10 TCID50/ml (120 J/cm2Initial virus titer = 7.4 log10 TCID50/ml  
HCoV-OC43 Photo-inactivation (UV-LED) 3.9 log10 removal (267 nm at 10 mJ/cm2Initial virus titer = 8 × 105 PFU/ml Gerchman et al. (2020)  
  3.9 log10 removal (279 nm at 26 mJ/cm2  
  4.4 log10 removal (286 nm at 37 mJ/cm2  
  4.2 log10 removal (297 nm at 54 mJ/cm2  
SARS-CoV-2 Nanostructured Al 6,063 alloy (rough surface) 100% (6-h) Initial virus titer = 105 TCID50/ml; Roughness = 995 nm; Water contact angle = 17.7 ° Hasan et al. (2020)  
 Al 6,063 alloy (smooth surface) 100% (48-h) Water contact angle = 96.3 °  
 Polystyrene tissue culture plate (TCP) 99.85% (48-h)   
SARS-CoV-2 Photo-inactivation; UVA (365 nm, 540 μW/cm2) and UVC (254 nm, 1,940 μW/cm2100% (9-min) Initial concentration = 5 × 106 TCID50/ml; Irradiation dose = 1.94 mJ/cm2 (UVC) and 0.54 mJ/cm2 (UVA) Heilingloh et al. (2020)  
  50% (1.4-min)   
 UVC 100% (9-min) Irradiation dose = 1,048 mJ/cm2  
SARS-CoV-2 Thermal inactivation 5-log (32.5-min) 60 °C Hessling et al. (2020)  
  5-log (3.7-min) 80 °C  
  5-log (0.5-min) 100 °C  
SARS-CoV-2 Photo-inactivation; DUV-LED (250–300 nm) 87.4% (1-s) Initial concentration = 2 × 104 plaque forming unit (PFU)/ml; Irradiation rate = 3.75 mW/cm2 Inagaki et al. (2020)  
  99.9% (10-s)   
  >99.9% (20-s)   
  99.9% (10-s)   
  >99.9% (20-s)   
MHV-A59 Thermal inactivation >6-log (1-s) Initial virus titer = 5 × 107 PFU/ml; 115 °C Jiang et al. (2020)  
  7.7-log (0.5-s) >125 °C  
  5-log (0.25-s) 150 °C  
  Not effective (0.1-s) 170 °C  
SARS-CoV-2 in platelets Photocatalytic inactivation (riboflavin, 500 μmol/L and UV, 6.24 J/mL) ≥4.53 log10 PFU/ml Initial virus titer = 4.77 log10 PFU/ml Keil et al. (2020)  
In plasma  ≥3.40 log10 PFU/ml Initial virus titer = 4.62 log10 PFU/ml  
SARS-CoV-2 Gamma irradiation (60Co source) 6.5 log10 TCID50/ml (1 Mrad) Initial virus titer = 6.5 log10 TCID50/ml Leung et al. (2020)  
  6.45 log10 TCID50/ml (0.16 Mrad)   
SARS-CoV-2 Photo inactivation (UV, 254 nm) 7.5 log10 PFU/ml (0.04 J/cm2Initial virus titer = 7.5 log10 PFU/ml Patterson et al. (2020)  
 Chemical inactivation (methanol, 6.1 log10 TCID50/ml Initial virus titer = 6.6 log10 PFU/ml  
 4%) paraformaldehyde 6.1 log10 TCID50/ml   
SARS-CoV-2 Photo-inactivation (Solar radiation) 90% (27-min) UV flux = 0.26 J/m2.min; In summer Sagripanti & Lytle (2020)  
  90% (>300-min) UV flux = 0.01 J/m2.min; In winter  
  90% (115-min) UV flux = 0.06 J/m2.min; In spring  
  90% (63-min) UV flux = 0.11 J/m2.min; In fall  
Bacteriophage Φ6 Photo-inactivation (LED, 405 nm) 3-log (1,300 J/cm2Initial concentration = 107 PFU/ml; Size = 75 nm Vatter et al. (2020)  
  1-log (430 J/cm2  
SARS-CoV-2 NaOCl (6,700 g/m3100% Medical wastewater Zhang et al. (2020)  
MARS-CoV in platelets Photo inactivation (UVC, 254 nm) >3.8 log10 TCID50/ml (0.2 J/cm2Initial virus titer = 8.12 log10 TCID50/ml Eickmann et al. (2018)  
MB in plasma Visible light (LED) >3.3 log10 TCID50/ml (120 J/cm2Initial virus titer = 7.86 log10 TCID50/ml  
MARS-CoV Photocatalytic inactivation (amotosalen and UVA 4.67 log10 PFU/ml Initial virus titer = 7.8 log10 PFU/ml Hindawi et al. (2018)  
  7.13 log10 RNA copies/ml Initial genome titer = 10.51 log10 RNA copies/ml  
Coliphage MS2 Photocatalytic inactivation, VUV (185 + 254 nm) 100% (0.125-s) Initial virus titer = 1.7 × 103 PFU/ml; RH = 40% Kim & Jang (2018)  
 UV (254 nm) 49% (0.125-s)   
 O3 100% (0.125-s)   
 UV (254 nm) + O3 100% (0.125-s)   
 VUV (185 + 254 nm) 100% (0.052-s)   
 UV (254 nm) 32% (0.052-s)   
 O3 98% (0.052-s)   
 UV (254 nm) + O3 96% (0.052-s)   
 VUV (185 + 254 nm) 100% (0.026-s)   
 UV (254 nm) 12% (0.026-s)   
 O3 95% (0.026-s)   
 UV (254 nm) + O3 95% (0.026-s)   
 VUV (185 + 254 nm) 61% (0.009-s)   
 O3 10% (0.009-s)   
 UV (254 nm) + O3 9% (0.009-s)   
 VUV (185 + 254 nm) 50% (0.004-s)   
 TiO2 plate + VUV 58% (0.009-s)   
 Pd-TiO2 plate + VUV 60% (0.009-s)   
 Pd-TiO2 plate (5 mm) + VUV 66% (0.009-s)   
 Pd-TiO2 spiral + VUV 43% (0.009-s)   
 Pd-TiO2 (2 mm) + VUV 69% (0.009-s)   
 Pd-TiO2 (2 mm) + VUV + UV 68% (0.009-s)   
 Pd-TiO2 (2 mm) + VUV 66% (0.009-s) RH = 10%  
  68% (0.009-s) RH = 40%  
  58% (0.009-s) RH = 70%  
 Pd-TiO2 (2 mm) 44% (0.009-s) 4 °C; RH = 40%  
 Pd-TiO2 (2 mm) + VUV 64% (0.009-s)   
 Pd-TiO2 (2 mm) 44% (0.009-s) 25 °C; RH = 40%;  
 Pd-TiO2 (2 mm) + VUV 68% (0.009-s)   
Bacteriophage Φ6 FC (2 mg/l) 6-log (8-s) Initial virus concentration = 4.5 × 1010 PFU/ml Ye et al. (2018)  
 UV254 6-log (215 mJ/cm2Irradiation intensity = 0.14 mW/cm2  
MARS-CoV Photocatalytic inactivation (riboflavin, 500 μmol/L and UV, 6.24 J/mL) 4.25-log Initial virus titer = 3.6 × 107 PFU/ml Keil et al. (2016)  
MARS-CoV Photo inactivation (Gamma irradiation, 60Co) 100% (2 Mrad) Initial virus titer = 1.6 × 1010 PFU/ml Kumar et al. (2015)  
  83.3% (1 Mrad) Initial virus titer = 106 PFU/ml  
MARS-CoV Thermal inactivation 4.67 log10 TCID50/ml (0.5-min) Initial virus titer = 5.59 log10 TCID50/ml; 56 °C Leclercq et al. (2014)  
  3.67 log10 TCID50/ml (0.5-min) 65 °C  
TGEV Thermal inactivation 8-log (38-d) PSWW; Initial concentration = 5.8 log10 MPN/ml; 25 °C Casanova et al. (2009)  
  1.25-log (35-d) PSWW; Initial concentration = 5.5 log10 MPN/ml; 4 °C  
  2.6-log (14-d) Lake water; Initial concentration = 5.0 log10 MPN/ml; 25 °C  
  1-log (14-d) Lake water; Initial concentration = 5.2 log10 MPN/ml; 4 °C  
  4.2-log (49-d) Pure water; Initial concentration = 4.5 log10 MPN/ml; 25 °C  
  No removal (49-d) Pure water; Initial concentration = 6.5 log10 MPN/ml; 4 °C  
MHV  8-log (28-d) PSWW; Initial concentration = 6.6 log10 MPN/ml; 25 °C  
  0.75-log (35-d) PSWW; Initial concentration = 6.8 log10 MPN/ml; 4 °C  
  2.5-log (14-d) Lake water; Initial concentration = 6.9 log10 MPN/ml; 25 °C  
  No removal (14-d) Lake water; Initial concentration = 6.6 log10 MPN/ml; 4 °C  
  5.6-log (49-d) Pure water; Initial concentration = 6.5 log10 MPN/ml; 25 °C  
  0.2-log (49-d) Pure water; Initial concentration = 6.5 log10 MPN/ml; 4 °C  
HCoV Thermal inactivation 99% and 99.9% after 6.76-d and 10.1-d, respectively Filtered tap water at 23 °C Gundy et al. (2009)  
  99% and 99.9% after 8.09-d and 12.1-d, respectively Unfiltered tap water at 23 °C  
  99% and 99.9% after 392-d and 588-d, respectively Unfiltered tap water at 4 °C  
  99% and 99.9% after 1.57-d and 2.35-d, respectively Filtered primary effluent 23 °C  
  99% and 99.9% after 2.36-d and 3.54-d, respectively Unfiltered primary effluent at 23 °C  
  99% and 99.9% after 1.85-d and 2.77-d, respectively Secondary effluent  
PV  99% and 99.9% after 43.3-d and 64.9-d, respectively Filtered tap water at 23 °C  
  99% and 99.9% after 47.5-d and 71.3-d, respectively Unfiltered tap water at 23 °C  
  99% and 99.9% after 135-d and 203-d, respectively Unfiltered tap water at 4 °C  
  99% and 99.9% after 23.6-d and 35.5-d, respectively Filtered primary effluent at 23 °C  
  99% and 99.9% after 7.27-d and 10.9-d, respectively Unfiltered primary effluent at 23 °C  
  99% and 99.9% after 3.83-d and 5.74-d, respectively Secondary effluent  
SARS-CoV-Hanoi Thermal inactivation 5.81-log (5-min) Initial virus titer = 2.6 × 107 TCID50/ml; 56 °C Kariwa et al. (2006)  
  6.41-log (30-min)   
  100% (60-min)   
 Photo inactivation (UV) 5.32-log (15-min, 134 μW/cm2Initial virus titer = 3.8 × 107 TCID50/ml  
  6.31-log (30-min, 134 μW/cm2  
 Chemical inactivation, 100% methanol 6.02-log (30-min) Initial virus titer = 2.1 × 107 TCID50/ml  
 100% acetone 5.81-log (5-min) Initial virus titer = 1.3 × 107 TCID50/ml  
 2.5% glutaraldehyde 4.14-log (5-min) Initial virus titer = 2.2 × 106 TCID50/ml  
 3.5% paraformaldehyde 3.7-log (5-min) Initial virus titer = 1.6 × 106 TCID50/ml  
SARS-CoV- P9 Catalytic oxidation (Ag/Al2O3105.5 TCID50/ml (5-min) Initial virus titer = 106 TCID50/ml; 20 °C Han et al. (2005)  
 Cu/Al2O3 105.25 TCID50/ml (5-min)   
 Al2O3 100.25 TCID50/ml (5-min)   
SARS-CoV- GVU6109 NaOCl (500 mg/l) >3-log (5-min) Initial virus titer = 107 TCID50/ml; 20 °C Lai et al. (2005)  
 NaOCl (1,000 mg/l) >3-log (5-min)   
SARS-CoV-Urbani Photo-catalytic inactivation (amotosalen-HCl, 150 μmol/L and UVA, 320–400 nm) 105.5 PFU/ml (4-min, 3 J/cm2Initial virus titer = 105.5 PFU/ml Lin et al. (2005)  
SARS-CoV Chemical inactivation, NaOCl (5 mg/l); FC (0.11 mg/l) 68.38% (30-min) Wastewater; Initial virus titer = 101.75 TCID50/ml; 20 °C Wang et al. (2005)  
 NaOCl (10 mg/l); FC (0.4 mg/l) 100% (30-min)   
 NaOCl (20 mg/l); FC (0.5 mg/l) 100% (30-min)   
 NaOCl (40 mg/l); FC (0.82 mg/l) 100% (30-min)   
E. coli NaOCl (20 mg/l); FC (0.5 mg/l) 100% (30-min) Wastewater; Initial bacteria concentration = 1.3 × 106 CFU/l  
 NaOCl (40 mg/l); FC (0.82 mg/l) 100% (30-min)   
f2 phage NaOCl (5 mg/l); FC (0.11 mg/l) 30.91% (30-min) Wastewater; Initial virus titer = 1.1 × 105 PFU/l  
 NaOCl (10 mg/l); FC (0.4 mg/l) 27.27% (30-min)   
 NaOCl (20 mg/l); FC (0.5 mg/l) 79.09% (30-min)   
 NaOCl (40 mg/l); FC (0.82 mg/l) 100% (30-min)   
SARS-CoV NaOCl (10 mg/l); FC (0.39 mg/l) 43.77% (1-min) Wastewater; Initial virus titer = 101.6 TCID50/ml; 20 °C  
 NaOCl (10 mg/l); FC (0.33 mg/l) 68.38% (5-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 100% (10-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 100% (20-min)   
 NaOCl (10 mg/l); FC (0.35 mg/l) 100% (30-min)   
E. coli NaOCl (10 mg/l); FC (0.39 mg/l) 0.0% (1-min) Wastewater; Initial bacteria concentration = 4.6 × 105 CFU/l  
 NaOCl (10 mg/l); FC (0.33 mg/l) 0.0% (5-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 14.29% (10-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 26.09% (20-min)   
 NaOCl (10 mg/l); FC (0.35 mg/l) 20.21% (30-min)   
f2 phage NaOCl (10 mg/l); FC (0.39 mg/l) 15.79% (1-min) Wastewater; Initial virus titer = 1.9 × 105 PFU/l  
 NaOCl (10 mg/l); FC (0.33 mg/l) 15.79% (5-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 18.32% (10-min)   
 NaOCl (10 mg/l); FC (0.4 mg/l) 21.05% (20-min)   
 NaOCl (10 mg/l); FC (0.35 mg/l) 31.58% (30-min)   
SARS-CoV NaOCl (20 mg/l); FC (0.59 mg/l) 100% (1-min) Wastewater; Initial virus titer = 101.75 TCID50/ml; 20 °C  
 NaOCl (20 mg/l); FC (0.57 mg/l) 100% (5-min)   
 NaOCl (20 mg/l); FC (0.51 mg/l) 100% (10-min)   
 NaOCl (20 mg/l); FC (0.50 mg/l) 100% (20-min)   
 NaOCl (20 mg/l); FC (0.53 mg/l) 100% (30-min)   
E. coli NaOCl (20 mg/l); FC (0.59 mg/l) 23.09% (1-min) Wastewater; Initial bacteria concentration = 5.5 × 105 CFU/l  
 NaOCl (20 mg/l); FC (0.57 mg/l) 99.97% (5-min)   
 NaOCl (20 mg/l); FC (0.51 mg/l) 99.99% (10-min)   
 NaOCl (20 mg/l); FC (0.50 mg/l) 99.9998% (20-min)   
 NaOCl (20 mg/l); FC (0.53 mg/l) 100% (30-min)   
f2 phage NaOCl (20 mg/l); FC (0.59 mg/l) 0.0% (1-min) Wastewater; Initial virus titer = 2.9 × 105 PFU/l  
 NaOCl (20 mg/l); FC (0.57 mg/l) 13.78% (5-min)   
 NaOCl (20 mg/l); FC (0.51 mg/l) 23.46% (10-min)   
 NaOCl (20 mg/l); FC (0.50 mg/l) 48.67% (20-min)   
 NaOCl (20 mg/l); FC (0.53 mg/l) 78.24% (30-min)   
SARS-CoV ClO2 (5 mg/l); FC (0.00 mg/l) 0.0% (30-min) Wastewater; Initial virus titer = 101.75 TCID50/ml; 20 °C  
 ClO2 (10 mg/l); FC (0.00 mg/l) 94.38% (30-min)   
 ClO2 (20 mg/l); FC (0.00 mg/l) 82.22% (30-min)   
 ClO2 (40 mg/l); FC (2.19 mg/l) 100% (30-min)   
E. coli ClO2 (5 mg/l); FC (0.00 mg/l) 0.0% (30-min) Wastewater; Initial bacteria concentration = 1.3 × 106 CFU/l  
 ClO2 (10 mg/l); FC (0.00 mg/l) 0.0% (30-min)   
 ClO2 (20 mg/l); FC (0.00 mg/l) 0.0% (30-min)   
 ClO2 (40 mg/l); FC (2.19 mg/l) 99.46% (30-min)   
f2 phage ClO2 (5 mg/l); FC (0.00 mg/l) 0.0% (30-min) Wastewater; Initial virus titer = 1.1 × 105 PFU/l  
 ClO2 (10 mg/l); FC (0.00 mg/l) 32.73% (30-min)   
 ClO2 (20 mg/l); FC (0.00 mg/l) 42.73% (30-min)   
 ClO2 (40 mg/l); FC (2.19 mg/l) 60.0% (30-min)   
SARS-CoV ClO2 (10 mg/l) 43.77% (1-min) Wastewater; Initial virus titer = 101.6 TCID50/ml; 20 °C  
 ClO2 (10 mg/l) 68.38% (5-min)   
 ClO2 (10 mg/l) 68.38% (10-min)   
 ClO2 (10 mg/l) 68.38% (20-min)   
 ClO2 (10 mg/l) 55.33% (30-min)   
E. coli ClO2 (10 mg/l) 0.0% (1-min) Wastewater; Initial bacteria concentration = 4.6 × 105 CFU/l  
 ClO2 (10 mg/l) 17.39% (5-min)   
 ClO2 (10 mg/l) 0.0% (10-min)   
 ClO2 (10 mg/l) 14.29% (20-min)   
 ClO2 (10 mg/l) 21.74% (30-min)   
f2 phage ClO2 (10 mg/l) 42.11% (1-min) Wastewater; Initial virus titer = 1.9 × 105 PFU/l  
 ClO2 (10 mg/l) 26.32% (5-min)   
 ClO2 (10 mg/l) 17.79% (10-min)   
 ClO2 (10 mg/l) 26.32% (20-min)   
 ClO2 (10 mg/l) 47.37% (30-min)   
SARS-CoV ClO2 (40 mg/l); FC (19.10 mg/l) 94.37% (1-min) Wastewater; Initial virus titer = 101.75 TCID50/ml; 20 °C  
 ClO2 (40 mg/l); FC (17.59 mg/l) 100% (5-min)   
 ClO2 (40 mg/l); FC (13.99 mg/l) 100% (10-min)   
 ClO2 (40 mg/l); FC (10.91 mg/l) 100% (20-min)   
 ClO2 (40 mg/l); FC (5.86 mg/l) 100% (30-min)   
E. coli ClO2 (40 mg/l); FC (19.10 mg/l) 100% (1-min) Wastewater; Initial bacteria concentration = 5.5 × 105 CFU/l  
 ClO2 (40 mg/l); FC (17.59 mg/l) 99.999% (5-min)   
 ClO2 (40 mg/l); FC (13.99 mg/l) 99.99% (10-min)   
 ClO2 (40 mg/l); FC (10.91 mg/l) 99.99% (20-min)   
 ClO2 (40 mg/l); FC (5.86 mg/l) 100% (30-min)   
f2 phage ClO2 (40 mg/l); FC (19.10 mg/l) 13.78% (1-min) Wastewater; Initial virus titer = 2.9 × 105 PFU/l  
 ClO2 (40 mg/l); FC (17.59 mg/l) 23.46% (5-min)   
 ClO2 (40 mg/l); FC (13.99 mg/l) 17.65% (10-min)   
 ClO2 (40 mg/l); FC (10.91 mg/l) 48.97% (20-min)   
 ClO2 (40 mg/l); FC (5.86 mg/l) 68.78% (30-min)   
SARS-CoV-Urbani Photo inactivation (UVC, 254 nm) 4.75 log10 TCID10/ml (15-min, 4,016 μW/cm2Initial virus titer = 6.33 log10 TCID10/ml Darnell et al. (2004)  
 UVA, 365 nm 0.45 log10 TCID10/ml (15-min, 2,133 μW/cm2  
 Gamma irradiation (60Co source) 0.9 log10 TCID10/ml (15,000 rads)   
 Thermal inactivation 5.33 log10 TCID10/ml (20-min) 56 °C  
  4.70 log10 TCID10/ml (10-min) 65 °C  
  6.33 log10 TCID10/ml (45-min) 75 °C  
 Chemical inactivation (formaldehyde) 5.0 log10 TCID10/ml (24-h) 25 °C/35 °C  
 Glutaraldehyde 5.33 log10 TCID10/ml (24-h) 25 °C/35 °C  
 pH based (1, 12, 14) 5.33 log10 TCID10/ml (24-h) 4 °°C/25 °C/37 °C  
HCoV-229E Drying 100% (12-h) Initial virus titer = 5.5x × 105 TCID50/ml; aluminum; 21 °C; RH = 55–70% Sizun et al. (2000)  
  100% (12-h) Sterile sponges  
  100% (12-h) Latex surgical gloves  
 Thermal inactivation 65% (6-d) Phosphate buffer saline (PBS); 37 °C  
  100% (6-d) Earle's minimal essential medium (EMEM)  
HCoV-OC43 Drying 100% (3-h) Initial virus titer = 5.15 × 105 TCID50/ml; aluminum; 21 °C; RH = 55–70%  
  100% (1-h) Sterile sponges  
  100% (1-h) Latex surgical gloves  
 Thermal inactivation 54% (6-d) PBS; 37 °C  
  90% (6-d) EMEM  
HCoV-229E Thermal inactivation 0.6 log10 PFU/ml (6-h) Initial virus titer = 6.1 log10 PFU/ml; 4 °C; pH = 9.0 Lamarre & Talbot (1989)  
  >4.8 log10 PFU/ml (6-h) pH = 4.0  
  0.0 log10 PFU/ml (6-h) pH = 7.0  
  >4.8 log10 PFU/ml (6-h) 33 °C; pH = 9.0  
  >4.8 log10 PFU/ml (6-h) pH = 4.0  
  0.6 log10 PFU/ml (6-h) pH = 7.0  
  0.6 log10 PFU/ml (14-d) 4 °C; pH = 6.0  
  >4.8 log10 PFU/ml (14-d) 22 °C; pH = 6.0  
  >4.8 log10 PFU/ml (12-d) 33 °C; pH = 6.0  
  >4.8 log10 PFU/ml (5-d) 37 °C; pH = 6.0  

Sizun et al. (2000) inspected the survival of HCoV-229E and HCoV-OC43 in suspension and dry conditions where both viruses were stable for at least 6-d in suspension; and HCoV-229E had more resistance to chemical disinfectants than that of HCoV-OC43 as ten times more concentrated disinfectant (i.e., Proviodine) was required for 50% reduction of HCoV-229E but diluted chemical disinfectants had low potency to inactivate virus. Virus persistence was short in dry conditions compared to in suspension and virus had maximum infectivity at neutral pH, whereas inactivation was increased at pH <5.0 and pH >8.0. However, destabilization of lipid bi-layer was the prominent mechanism to inactivate the virus but nucleic acid disruption, protein denaturation and sorption may be other mechanisms in the complete virus removal process.

Darnell et al. (2004) scrutinized the inactivation of SARS-CoV by different mechanisms, i.e., photo-inactivation, thermal inactivation, and chemical inactivation as all inactivation mechanisms had shown noticeable virus removal in favorable conditions. Photons from UVC, UVB, and UVA can be absorbed by DNA and RNA where two neighboring pyrimidines may be covalently bonded to form dimers by photochemical fusion which will give non-paired bases in DNA or RNA; but, UVC can more effectively catalyze this photo-inactivation mechanism than that of UVB (20–100 times slower than UVC) and UVA (weaker than UVB), although UVA can facilitate the formation of ROSs to damage bases and proteins by oxidation. Gamma irradiation (60Co) may not be effective at low dose but high dose can slowly trigger inactivation; where several factors, i.e., irradiation time and dose, wavelength, irradiation distance, pathogen concentration, antibody of pathogen, and pathogen species can affect the removal process. Thermal inactivation can hamper enzymatic activity or denature the proteins for bases, attachment and replication; and high temperature initiated rapid inactivation of virus from solid and aqueous media while aggregation of virus may need longer heat exposure to be inactivated in/on specific media. Chemical–based inactivation by formaldehyde (HCHO) and glutaraldehyde (C5H8O2) can inactivate virus at high temperatures, i.e., 25 °C and 37 °C, when formaldehyde bonds with lysine, a non-protonated amino group of amino acids, form hydroxymethlyamine which reacts with other groups, i.e., amino (−NH2), amide (−CONH2), guanidyl (=C = NH), phenolic (−OH), or imidazole (C3N2) of amino acids to develop inter- or intra-molecular crosslinks. Moreover, DNA/RNA protein crosslink, mutation of specific DNA/RNA or proteins and oxidation of membrane layer to form hydrogen peroxide (H2O2) from unsaturated fatty acids may be possible by UVC and far-UV irradiation. Formaldehyde can also reversibly link with RNA to block genome reading. Besides, spike proteins can suffer conformational change at different pHs (specially at pH 8.0) as this change may affect the infectious nature and attachment with the host cell. Significant inactivation can be achieved at pH 1.0, 12.0, and 14.0 at temperatures of 25 °C and 37 °C whereas no removal may be observed at neutral pH. If these inactivation routes are not observed carefully, SARS-CoV can easily enter inside the human body by ingestion/inhalation or fecal–oral route to cause severe health problems.

Han et al. (2005) perceived the potential of effective inactivation of SARS-CoV by some metal catalysts, i.e., Ag/Al2O3, Cu/Al2O3, and Al2O3 where virus inactivation efficiency of Ag was greater compared to Cu; but Al had little contribution in the removal process. In the presence of air, organic surfaces, i.e., bacteria and virus, cells can be oxidized and decomposed with little or no replication capability of RNA or DNA due to formation of active oxygen atoms since the electron transfer process between the atmospheric oxygen and metals’ surfaces may form those atoms; however, the inactivation process was hampered when a thick layer of microbes acted as a barrier to terminate the electron transfer process between the catalyst and molecular oxygen. Virus cell rupture and incapability of DNA/RNA replication were the obvious outcomes of the process.

Lai et al. (2005) examined the survival and inactivation of SARS-CoV on different surfaces (i.e., paper, cotton gown, disposable gown) and stools (i.e., four samples with different pHs) where virus stability in stool was minimum at 3-h (baby, pH 6–7), 6-h (normal adult, pH 7–8), 1-d (normal adult, pH 8), and 5-d (adult with diarrhea, pH 9) but 24-h on paper and cotton gown and 2-d on disposable gown when virus titer was 106 TCID50/ml; although, >3-log removal can be achieved within 5-min by NaOCl. Moreover, Hulkower et al. (2011) also noticed inactivation of two surrogates, i.e., murine/mouse hepatitis virus (MHV) and transmissible gastroenteritis virus (TGEV) of Coronavirus by 600 mg/l NaOCl where <1-log removal was observed after 1-min contact time.

Wang et al. (2005) studied the inactivation efficiency of two disinfectants, i.e., NaOCl and chlorine dioxide (ClO2) for SARS-CoV, E. coli, and f2 bacteriophage removal from dechlorinated tap water, hospital and domestic wastewater when SARS-CoV could survive in those wastewaters for 2-d at 20 °C and RNA was detectable in those systems even after 7-d; but SARS-CoV had persisted for 14-d at 4 °C. Although SARS-CoV could survive about 3-d and 17-d at 20 °C in stool and urine, respectively, because of salt in urine to support osmotic pressure; SARS-CoV could stay alive in stool and urine no more than 17-d at 4 °C. SARS-CoV was completely inactivated by chlorine with a concentration of 10 mg/l and high concentration, i.e., 40 mg/l was required to achieve the same level of inactivation by ClO2; however, E. coli and f2 phage could not be inactivated completely by 10 mg/l of both disinfectants so SARS-CoV was easier to inactivate compared to the other two microbes. SARS-CoV concentration was several times lower than that of E. coli and f2 phage in the aliquot, and the aforementioned conclusion is very difficult to achieve. A number of inactivation mechanisms, e.g., reaction with amino acids: i.e., cysteine, tryptophan, and tyrosine; capsid protein alteration; protein and RNA synthesis hampering; reaction with fatty acids; and conformational change of outer layer membrane lipid and proteins to interrupt permeability (Olivieri et al. 1985) were identified. SARS-CoV inactivation was also dependent on temperature, pH, wastewater composition, RH, disinfectant type, and contact time.

Kariwa et al. (2006) explored SARS-CoV inactivation by heat (56 °C), photo (UV) and chemical agents (i.e., povidone-iodine (PVP-I), 100% acetone, 100% methanol, 3.5% paraformaldehyde, 2.5% glutaraldehyde) when significant inactivation was noticed after treatment with the above-stated inactivation agents - although antigenicity of SARS-CoV was perceived after reactivation of methanol and acetone-treated virus. However, nucleocapsid protein was also discovered after heat inactivation, indicating degradation of lipid bi-layer by thermal treatment.

Casanova et al. (2009) analyzed the survival of two surrogates, i.e., MHV and TGEV of Coronavirus in reagent-grade water, lake water, and pasteurized settled wastewater (PSWW) at temperatures of 4 and 25 °C. Declining infectivity for TGEV and MHV was about 0.6-log/week and 0.8-log/week, respectively, at 25 °C in reagent-grade water while the infectivity rate declined by about 1.5-log/week and 2-log/week, respectively, at 25 °C in PSWW, but no significant infectivity decreased at 4 °C in reagent-grade water; hence, infectivity declined more rapidly at 25 °C in all three types of water. Survival rate of virus in reagent-grade water was higher than that in PSWW and other factors, i.e., virus type, temperature, incubation time, aliquot composition, organic nutrient, pH, other microbes’ concentration, presence of proteolytic enzymes and high molecular weight chemicals may affect the removal rate and mechanisms. Although pH had no or minimal impact on virus infectivity, Coronavirus can survive for a long time in water and wastewater, and regular inspection should be practiced in plumbing and exhaust systems in residential, industrial, and office buildings.

Gundy et al. (2009) attempted to comprehend the survival of human Coronaviruses (HCoV) and polioviruses (PV) in tap water and wastewater collected from primary (filtered) and activated sludge secondary (unfiltered) effluent at 4 °C and 23 °C. A number of factors such as temperature, organic matter, solid concentration, presence of other microbes, surface science of pathogens and aerobic microorganisms can affect virus survival in water and increasing temperature of water can decrease virus survival due to denaturation of proteins and activity of extracellular enzymes. Moreover, the presence of other solvents and detergents can also help in inactivation of viruses. The survival of HCoV and PV was, therefore, the same in tap water, but in wastewater, PV can survive six times longer in both filtered and unfiltered samples. Survival of HCoV was higher in unfiltered water than that of filtered water. Again, the presence of organic matter and solids has a significant impact on virus protection but settled solids can increase virus removal from aqueous phase.

Kumar et al. (2015) examined the inactivation of MARS-CoV by gamma irradiation (60Co) and chemical disinfectants where high irradiation dose, i.e., 2–4 Mrad can enhance the removal rate; and TRIzol or 1:1 methanol:acetone, two chemical disinfectants, can excellently remove envelope viruses without any reactivation possibility of virus cell and RNA. Cell penetration by rays and disinfectants was an important factor which depended on cell types and disinfectant concentrations or ray density; however, formation of aldehyde crosslink was not dependent on cell penetration rate. Protein denaturation and membrane estrangement were the two possible mechanisms for inactivation by TRIzol with a minimum contact time of 10-min.

Kim & Jang (2018) explored photolysis and photo-catalysis oxidation (PCO) of MS2 phage, as SARS-CoV-2 surrogate, by utilizing UVC (254 nm), VUV, or FUV (<222 nm) with TiO2 catalyst or Pd nanoparticle-deposited TiO2 (Pd-TiO2) sheet catalyst where numerous factors, i.e., RH, irradiation time and rate, distance travelled by photons, type of catalysts, composition of catalysts, amount of catalysts, specific energy given, reactor types, catalyst surface area to reactor volume ratio (S/V, m2/m3), and catalyst placement can stimulate the inactivation process. Significant MS2 inactivation was observed by FUV irradiation with or without catalyst as high photon energy can easily interrupt most of the chemical bonds of proteins, enzymes, and nucleic acids to promote the virus removal process; and dissociation of oxygen and water forms ozone to further accelerate the inactivation process, although inactivation by ozone (3,537 ppb) was comparatively higher than that of UV. Low ozone dose (150 ppb) had six times less inactivation potential compared to VUV photolysis because reactive oxygen generation was less. The inactivation prospect between UV and VUV was considerably different, but catalyst-reinforced VUV + UV irradiation noticeably increased ozone formation and degradation process including other chain reactions to promote inactivation. When a catalyst was used, Pd had almost no inactivation ability so catalyst-induced inactivation was mainly supported by TiO2 and VUV; but high S/V ratio influenced high inactivation rate. High RH, furthermore, increases inactivation rate as reactive oxygens and other toxins can be easily generated and transported into cells where any smooth transportation of those elements can be hampered at dry conditions. Besides, too-high RH, hydrophobicity and surface charge can also impede the inactivation process. Moreover, Bogdan et al. (2015) revealed the inactivation potential of different microorganisms by photocatalytic oxidation in the order of viruses > prions > Gram-negative bacteria > Gram-positive bacteria > yeasts > molds where the reverse order was observed for resistance to photocatalytic inactivation. Photocatalytic inactivation can easily and quickly damage both enveloped and non-enveloped virus cells with the inactivation order of non-enveloped virus > enveloped virus; nevertheless, the same postulate was not reinforced by all research groups. Generally, envelope, a plasma membrane, is formed by virus-derived glycoproteins and host cell-derived phospholipid bi-layers where factors, i.e., number of layers, their thickness and structural form of shielding the nucleic materials, can influence the overall cell damaging mechanisms, as impairment of capsid proteins and nucleic acid can quickly inactivate virus cells. Although these nanostructured metals have noticeable virucidal property, actual inactivation mechanisms should be investigated more meticulously to gain the precise knowledge about damaging microbes’ cells.

Ye et al. (2018) had comprehended the inactivation potential of Φ6, a surrogate of Coronavirus, by FC and UV254 by noticing the reactions of genomes, proteins, and lipids. The inactivation of virus was quick by FC but virion had 15–30 times more resistance than that of other viruses, e.g., influenza A, MS2, or adenovirus under UV254; although aggregation, adsorption on particles, and oxidant accumulation on virus surface were detected. Genome damage in the presence of FC may not trigger inactivation as some genome repair mechanisms may slow down the annihilation process; however, significant reactivity of genomes was observed in the disinfection process by FC and UV. Susceptibility of Φ6 was dependent on three distinct protein layers, i.e., membrane proteins (five types), nucleocapsid proteins (two types), and polymerase complex proteins (four types); vulnerability was increased when membrane protein reactions started with FC as nucleocapsid proteins and polymerase complex proteins can be easily penetrated by FC molecules but membrane proteins are not easily penetrable. These protein reactions inactivate virus by structural changes, membrane penetration, hindering solvent accessibility, interruption of binding capability with host cell or UV-sensitive amino acids, e.g., Trp (W), Tyr (Y), and Phe (F) sequences. Again, membrane lipid formed by different types of phospholipids, e.g., phosphatidylethanolamine (PE), phosphatidylglycerol (PG), or cardiolipin (CL) had no impact on the inactivation process.

Ahmed et al. (2020) applied the thermal inactivation process for SARS-CoV-2 and MHV RNA in three types of samples, i.e., untreated wastewater, autoclaved wastewater (controlled or no biological activity), and dechlorinated tap water (free from enzymatic activity). First order decay rate constant was high at a temperature of 37 °C compared to that of 4 °C in autoclaved wastewater and untreated wastewater/tap water for SARS-CoV-2 and MHV; however, SARS-CoV-2 decay rate was slow in tap water compared to untreated wastewater. Temperature effect was not dependent on matrix. RNases release was higher in autoclaved wastewater because of cell lysis at high temperature (121 °C) and pressure (15 psi); and those active enzymes assisted in RNA degradation, whereas this process was not perceptible in untreated wastewater.

Biasin et al. (2021) remarked on SARS-CoV-2 inactivation and replication inhibition by UVC irradiation because UVC photons can be absorbed by nucleic acid bases and capsid proteins to produce photo-products to damage the virus cell where electron transfer can alter the oxidizing properties of the cell. Although inactivation rate was affected by virus concentration and UVC dose, partial inactivation may promote inhibition of infection, and recovery from that harsh condition may depend on the antibody of the virus. Eickmann et al. (2020) also confirmed the inactivation of SARS-CoV, Crimean–Congo hemorrhagic fever virus (CCHFV) and Nipah virus (NiV) by short-wave UV light and visible light (with methylene blue) as both types of rays could impair the nucleic acid transcription and virus replication by forming ROSs, yet formation of ROSs and inactivation rate were increased with increasing intensity of photons. The same research group in 2018 had shown significant inactivation of MARS-CoV and ZEBOV in the same mechanisms by utilizing those two rays (Eickmann et al. 2018).

Bivins et al. (2020) witnessed the persistence of SARS-CoV-2 in water and wastewater at different temperatures, i.e., 20 °C, 50 °C, and 70 °C. Targeted virus had a faster decay rate than that for MHV and TGEV in pasteurized wastewater (WW), but targeted virus had high persistence in unpasteurized WW. Although persistence of the SARS-CoV-2 RNA signal was higher than the SARS-CoV-2 in WW, infectiousness of virus may not be confirmed by RNA signal.

Buonanno et al. (2020) introduced a far-UVC or vacuum UV (VUV) irradiation system to inactivate two airborne HCoVs (229E and OC43) as surrogates of SARS-CoV-2. 229E had better resistance to far-UVC compared to OC43 where spike glycoprotein and other proteins were impaired due to far-UVC irradiation. A myriad number of factors, i.e., structural difference, genome size, nucleic acid arrangement, irradiation rate, contact time, RH, temperature, and wavelength may influence the inactivation process; however, similar inactivation rate by UV was suggested for all types of Coronaviruses. In the context of bio-physically based principle, far-UVC had the capability to penetrate micro-/nano-sized biological materials, e.g., bacteria or viruses; but this ray cannot penetrate human skin stratum corneum (i.e., outermost layer of skin) or ocular tear layer while UVC at 254 nm can pierce both micro- and mega-level bio-materials. The actual health hazard of far-UVC, nonetheless, should be tested by further research since far-UVC can generate ROSs and hydroxyl radicals may damage chemical bonds (Hadi et al. 2020).

Chan et al. (2020) followed different factors to understand the infectivity of SARS-CoV-2 and SARS-CoV, where both viruses had shown the same level of stability in a comparable environment. SARS-CoV-2 was less stable on a surface than in a solution, but high temperature and high RH were factors for viability. Moreover, extreme pH can completely reduce the viability by <1-d and neutral or near neutral pH (i.e., 5–9) had ≤1.5-log reduction within the 1st day, although chemical disinfectants can quickly inactivate the viruses within 5-min from 0.92-log removal to 3.75-log removal.

Chen et al. (2020) depicted thermal and chemical inactivation (by TRIzol reagent, a mixture of acid phenol and guanidinium thiocyanate) of SARS-CoV-2's open reading frame (ORF-1ab) and nucleo-capsid protein (N) gene where complete inactivation of genes was achieved at a temperature of 100 °C by boiling and 121 °C by autoclave; lowest inactivation was shown by TRIzol reagent. Moreover, synergic impacts of pressure and temperature were the major contributors in the inactivation process at high temperature and chemical reagent destroyed the lipid bi-layer without affecting the integrity and stability of the protein bases of the genes.

Hasan et al. (2020) observed antimicrobial efficiency of nanostructured aluminum (Al) sheets with rough (etched) and smooth (unetched) surfaces for SARS-CoV-2, where substantial virus inactivation on a rough surface was noticed within a very short time compared to on a smooth surface; factors, i.e., virus envelope and capsid composition, virus species, nanoscale topography, mechanical and physicochemical characteristics of nanostructured materials can affect the inactivation process. Furthermore, etched Al had noteworthy polarization resistance than that of unetched Al to increase corrosion resistance, but charge benefit cannot be enjoyed for virus separation from gaseous or liquid media.

Heilingloh et al. (2020) evaluated the photo-inactivation of SARS-CoV-2 by UV irradiation and UVC had higher inactivation capacity than that of UVA in high virus titer. Inagaki et al. (2020) investigated the photo-inactivation of SARS-CoV-2 by deep UV light-emitting diode (DUV-LED) with wavelength of 280 nm, and UV irradiation generally hampers the transcription, translation, and replication of DNA and RNA by forming pyrimidine dimers in DNA and RNA. Moreover, target species, irradiation rate, light source, and environmental conditions may influence the removal rate but cytopathic effects were not detected among the cells. Generally, UVC irradiation on DNA or RNA forms different types of chemical structures, i.e., cyclobutane type dimers, namely, cyclobutane pyrimidine dimers (CPD), inter-strand (i.e., between different DNAs) photoproducts, intra-strand (i.e., within the same DNA) photoproducts, and spore photoproducts, i.e., 5,6-dihydro-5-(α-thyminyl)-thymine formation due to photo-reaction of two thymine moieties. Pyrimidine (cytosine and thymine for DNA; cytosine and uracil for RNA) dimerization is possible between adjacent bases due to photo-reaction but photoproducts’ formation may be observed between non-adjacent pyrimidines; and types of photoproducts in a double-strand DNA depend on the chemical structure of the bases as several complex isomers may be observed. Anyway, spore photoproduct can act as a DNA repair enzyme to restore the original structure of the base moieties and structural consistency of DNA/RNA (Douki et al. 2003). However, six covalent-linked dimers, i.e., thymine = thymine, cytosine = cytosine, cytosine = thymine, uracil = uracil, thymine = cytosine, and uracil = thymine can be possible because of UV irradiation on DNA/RNA (Hadi et al. 2020). Moreover, CPD formation by UVC is generally 100 times higher than that of UVB and 1,000 times greater compared to UVA when factors, e.g., wavelength, dose, and photon adsorption capability of DNA/RNA can affect the formation process, although cells have slow and incomplete CPD repair mechanisms (Perdiz et al. 2000). Increasing CPD and photoproducts’ formation may decrease cell survival rate and microbes’ sensitivity to this phenomenon should be carefully examined. Again, formation and repair capability of the defect of DNA or RNA are dependent on UV exposure pattern, photo-reactions induced by that exposure and subsequent antibody formation by virus to present a specific treatment process.

Hessling et al. (2020) monitored the effect of SARS-CoV-2 inactivation by considering different factors, i.e., temperature, RH, pH, and composition of aliquot where high protein concentration and low humidity can adversely affect virus inactivation but elevated temperature can quickly inactivate virus within pH 6–8.

Gerchman et al. (2020) investigated wavelength, i.e., 267, 279, 286, and 297 nm effect of UV-LED for surrogate HCoV inactivation and concluded that longer wavelength needs a higher irradiation dose to kill virus. Four types of proteins in different locations, i.e., spike (S), envelope (E), membrane (M), and nucleocapsid (N) responsible for viral functions, assembly and pathogenesis can be damaged by UV irradiation. In this context, Mayer et al. (2015) hypothesized several factors, i.e., pyrimidine content, dimerization potential, capsid diameter, genome length, surface charge, conformational alteration, pH, sorption surface, amino acids and their functional groups, ROS concentration, structure of capsid protein, types of oxidants and photo-catalyst for effective inactivation of different types of viruses; although capsid protein structure is the most important factor in the damaging mechanism.

Jiang et al. (2020) researched the immediate impact of heat of sub-second duration to inactivate MHV, a surrogate of major types of Coronaviruses, by a flow-through extreme heating (oil bath) and subsequent quick cooling by ice bath process where the virion particles were relatively stable at room temperature; removal rate increased with increasing temperature (>65 °C) for a very short duration. The advantages of using this kind of process are to save huge amounts of energy and to inactivate the pathogens very quickly, but infrastructure development will be a major issue.

Leung et al. (2020) radiated gamma rays to inactivate SARS-CoV-2 where ionizing radiation can inactivate virus by damaging or crosslinking DNA, RNA, and other cellular macromolecules by forming reactive hydroxyl radicals, free electrons, and unstable ions, and high radiation dose can severely destroy the DNA or RNA integrity. However, the suggested dose of <0.5 Mrad may not inactivate all pathogens in a wastewater sample so a high dose should be recommended.

Kampf (2020) discussed the inactivation of Coronaviruses by disinfecting agents on inanimate surfaces as virus particles can survive on inanimate surfaces for 9-d and application of 0.1% NaOCl, 0.5% H2O2, and 71% C2H5OH can effectively inactivate the viruses within 1-min. Moreover, iso-propanol (CH3CHOHCH3), formaldehyde (HCHO), glutaraldehyde (C5H8O2), and povidone iodine (C6H9I2NO) have potential inactivation capability from different surfaces, although elevated temperatures and physical-mechanical properties of those surfaces can affect efficiency. Kampf et al. (2020) reported the persistence of Coronaviruses on inanimate surfaces, e.g., steel (8–120 h), aluminum (2–8 h), metal (120 h), wood (96 h), paper (3–120 h), glass (96–120 h), plastic (8–216 h), PVC (120 h), silicon rubber (120 h), latex (8 h), ceramic (120 h), teflon (120 h), and disposable gowns (8 h) where 0.3– > 5.5 log10 inactivation can be achieved by different biocidal agents mentioned elsewhere in this paper within 15-s to 3-d. Riddell et al. (2020) learned about the viability of SARS-CoV-2 on different common surfaces, e.g., stainless steel, polymer note, paper note, glass, cotton, and vinyl at different temperatures, i.e., 20 °C, 30 °C and 40 °C, and virus reduction was increased with increasing temperature.

Patterson et al. (2020) also inspected photo-, chemical and thermal inactivation of SARS-CoV-2 to collect downstream biological assays for other purposes, and similar inactivation mechanisms by all three processes have been discussed elsewhere in this report. Moreover, detergent discharged in wastewater may disrupt the lipid layer of envelope but ingredients of a detergent may not disturb the protein structure of the virus. Exposure rate rather than illumination time was important for UVC inactivation, although UVA had no efficiency due to limitation in cell penetration.

Coronavirus inactivation by solar radiation (notably UVC, 254 nm) was investigated by Sagripanti & Lytle (2020) by considering certain factors, i.e., temperature, humidity, sunlight intensity, location, seasons, irradiation duration and rate. UV sensitivity of SARS-CoV-2 was three times higher than that of influenza A as the genome size of influenza A was 2.2 times shorter than that of Coronavirus, which had higher inactivation rate with increasing irradiation time and duration. Virus infectivity, however, can be hampered during summer with high solar intensity while, during winter, inactivation rate may be increased with time as solar intensity is generally low at that time. Furthermore, Middle Eastern and African countries observed less severe infection compared to fatality rates in Europe. Moreover, an infected person indoors should be more contagious due to the presence of favorable factors, although a person will be exposed to fewer virus titers outdoors under high solar intensity.

Tizaoui (2020) fathomed out the virucidal efficacy of a powerful oxidant named ozone by evaluating SARS-CoV-2 virus inactivation mechanisms where ozone can react with proteins, amino acids, and lipids (polyunsaturated fatty acids) to form ROSs or reactive radicals (RCOO); and form lipid or protein oxidation products, i.e., hydrogen peroxide (H2O2), ozonides, and lipid peroxides; and change in virus integrity by damaging structural protein capsid and lipid envelope. Binding efficacy of spike S-protein and angiotensin converting enzyme 2 (ACE2) is 10 to 20 times higher for SARS-CoV-2 and ozone oxidation to S-protein can hamper this infection process. Moreover, the virus reproduction system can be impeded by damaging genome capsid and RNA. Amino acids, i.e., tryptophan, cysteine, and methionine have high reactivity with ozone, although those reactions are dependent on degree of ionization which is a function of pH; and ozone inactivation rate increases with increasing pH. Besides, fatty acids’ reactivity with ozone follows a sequence, i.e., arachidonic acid (AA) > linoleic acid (LA) > oleic acid (OA) > palmitic acid (PA). Again, the effectiveness of ozone water to inactivate SARS-CoV-2 was examined by Hu et al. (2021), and ozone (18–36 mg/l) can completely inactivate all viruses (4.0 × 103–4.0 × 104 PFU/ml) within 1-min; but ozone concentration <18 mg/l may need longer contact time to fully kill all viruses. Viable cells from 1.0 × 102 to 7.0 × 102 PFU/ml were, however, detected in aqueous samples treated by ozone concentration <9 mg/l. Although ozone gas has an adverse effect on healthy tissue, gaseous phase inactivation can also be possible by ozone gas.

Vatter et al. (2020) observed the photo-inactivation of Coronavirus surrogate bacteriophage Φ6, an enveloped dsRNA, under visible light in the presence of endogenous photosensitizers, i.e., porphyrins, flavins, or NADH (nicotinamide adenine dinucleotide (NAD) + hydrogen (H)) which can absorb visible light and, subsequently, produce ROSs to destroy virus cells. ROSs generally attack envelope, proteins, and nucleic acids of pathogens and inactivation rate can be increased with increasing photosensitizer concentration when concentration of photosensitizer and irradiation rate are negatively co-related. The visible violet or blue light had less antimicrobial effect than UV light. Some photosensitizers, i.e., riboflavin (vitamin B2) with UV-B and amotosalen with UV-A can enhance pathogen inactivation capability at long wavelengths (Keil et al. 2016; Hindawi et al. 2018; Hadi et al. 2020), although the health hazards of those chemicals should be evaluated by long-term research as further contamination of water and wastewater will not be acceptable for end-users. However, some surrogates are used as models of Ebola virus and Coronavirus to understand the inactivation potential and mechanisms, actual inactivation of the emerging viruses depending on titer concentration, sample types and composition, disinfectant types and concentrations, cell structure of targeted pathogens, different internal (i.e., in vivo) and external (i.e., in vitro) influencing parameters, and physicochemical factors of the surrounding environment.

Hindawi et al. (2018) introduced amotosalen, a photoactive mutagen, to enhance the photolysis effectiveness of UVA where amotosalen/UVA generally expedited the formation of crosslinks in nucleic acids to impede transcription and replication and no breakdown of strands was detected, though. Moreover, no CPE, i.e., agglutination or syncytia was observed in inactivated samples after 7-d. However, this type of process was successfully used to inactivate pathogens from blood, serum, and platelets without distorting the main components. Keil et al. (2020) enhanced the photo-inactivation efficiency of SARS-CoV-2 by damaging nucleic acid in an irreversible way by employing UVB with riboflavin. Furthermore, Dunford et al. (1997) proved ROS generation by TiO2 photo-catalysis process irradiated by UVA; subsequently, UVA can be effectively applied as a virucidal agent and trigger photogenotoxic activity of TiO2.

Zhang et al. (2020) explored the deactivation efficiency of SARS-CoV-2 by NaOCl in septic tank wastewater sourced from a hospital and a high dose of NaOCl (6,700 g/m3 > 800 g/m3) was more effective in inactivation of virus RNA because viral RNA was not completely inactivated at 800 g/m3 NaOCl dose; although, DBPs, i.e., trichloromethane (332 μg/L), tribromomethane (1.9 μg/L), bromodichloromethane (5.1 μg/L), dibromochloromethane (0.6 μg/L) formation were noticeably elevated at high concentration of NaOCl. Viral RNA was in high concentration at the top (10.0 × 103 copies/L) of the water level compared to the bottom (5.1 × 103 copies/L) of a septic tank when slow release of virus particles from stool was spotted as septic tank effluent had more virus concentration than that of influent into the septic tank. Effective solid–liquid separation process was suggested to cause DBPs’ formation to dwindle in the treatment process as disinfectant dose can be reduced due to the partitioning process. WHO recommended disinfection guidelines, i.e., FC >0.5 mg/L with minimum 30-min contact time at pH <8.0, may not, however, be effective to safeguard public health.

Bardi & Oliaee (2021) investigated the impacts of temperature and OL for inactivating SARS-CoV-2 in the anaerobic co-digestion (AcoD) process where virus genes were significantly decreased with increasing OL as four stages, i.e., hydrolysis, acidogenesis, acetogenesis, and methanogenesis of anaerobic digestion with formation of various intermediate metabolites, e.g., ammonia (NH3)/ammonium , alcohols (–OH), formate (HCOO), hydrogen, and volatile fatty acids (VFAs) can hamper virus persistence because protein denaturation and lipid fragmentation may rupture the virus envelope. High OL can decrease pH and increase accumulation of the metabolites where low pH can damage hemagglutinin-glycoprotein based spikes; and synergistic impacts of temperature and metabolites can hinder in-vivo biological functions. The presence of alcohols precipitates the protein and nucleic acids of virus, further accelerating the pathogen inactivation process, and temperature has a more dominant role in the removal process than OL.

Chan et al. (2011) attempted to understand the effects of temperature (i.e., 38 °C, 33 °C, 28 °C) and RH (i.e., >95%, 80–89%) on viability of SARS-CoV-2 where virus inactivation rate was fairly similar in suspension and dry condition within a 25-d period; and high temperature (i.e., 38 °C) with high RH had a high mortality rate but high RH with low temperature (i.e., 28 °C and 33 °C) had little impact on virus infectivity. SARS-CoV-2 can persist longer in the environment than can HCoV-229E/OC43, where fomites and environmental conditions may significantly influence the virus inactivation process. Occurrence rate of SARS on a low temperature day was 18.18-fold higher than that on a high temperature day, and tropical countries all over the world had relatively low-to-moderate infection cases of SARS due to this reason. Moreover, a well-ventilated open room can reduce virus viability and reduce nosocomial transmission; but, some factors, i.e., wind velocity, daily sunlight, air pressure, smooth surface, mobile or immobile fomites, virus morphology, outdoor and indoor air quality can affect the transmission, dispersion, and survivability of virus.

Guo et al. (2021) developed an alternative disinfection process to prevent and inactivate SARS-CoV-2 infectivity and S protein in the model of pseudovirus by using plasma-activated water (PAW) with contact time of 5-min and 10-min. Binding efficiency between receptor-binding domain (RBD) of globular S1 of S-protein and human cellular receptor cells, i.e., hACE2-COS-7 and hACE2-HEK-293T, was significantly decreased by damaging RBD protein after treatment by PAW-5 and PAW-10 since these bindings have been responsible for SARS-CoV-2 infection. Although PAW-5-treated virus had little cell distortion and PAW-10-treated virus suffered noticeable aggregation and complex formation, untreated viruses had clear spherical morphology with diameter 20–40 nm. Moreover, myriad reactive species, e.g., H2O2, nitrite , peroxynitrite (ONOO), singlet oxygen , and other electrons produced from RBD can effectively inactivate S-protein; and bonding between these S-proteins may further cause aggregation. Decreasing molecular weight of the RBD after treatment of PAW-10 was also realized. Freshly formed reactive species had high inactivation or damaging potential compared to old reactive species because concentrations of species were decreased when the pH of the media was changed from acidic to basic due to formation of species that were confirmed by different probe testing. These species, as well, preferably reacted with amino acids, i.e., tyrosine and tryptophan to form 3-nitrotyrosine, 6-nitrotryptophan, and dityrosine with minor changes in molecular weight by oxidation or nitration modification to accelerate RBD inactivation. The same inactivation mechanisms can also be observed in other sections of S-protein in this destructive process. It is claimed that PAW does not contaminate the system by generating harmful elements; nonetheless, more research should be conducted to ensure this.

Hokajärvi et al. (2021) scrutinized the viability of two SARS-CoV-2 RNA biomarkers, i.e., E-Sarbeco (envelope gene) and N2 (nucleocapsid gene) assays in wastewater where linear decay was perceived at a temperature of 4 °C but no decay was noticed at −20 °C and −75 °C. N2 gene had slightly more decay rate compared to E-Sarbeco gene in the wastewater indicating the different sensitivity of envelope and nucleocapsid protein against thermal source. Survival of both enveloped and non-enveloped viruses may be the same at cold temperature, although inactivation rate may be rapid with increasing temperature; and sampling location, organic matter concentration, particulate matter and other microbes’ concentration may also affect the pathogen removal process. Enveloped virus had a high tendency to attach with particulate matter compared to non-enveloped virus.

Khaiboullina et al. (2021) recognized photocatalytic efficiency of a layer of TiO2 nanoparticles (TNPs) activated by UVC to inactivate HCoV-NL63, a surrogate of SARS-CoV-2 with similar virion structure, when the inactivation rate of virus and RNA was increased with increasing TiO2 concentration, irradiation rate and contact time. Degradation was not only detected in spike proteins but also in other parts of the virus and genomic regions of RNA. When UVC alone can effectively inactivate virus, inactivation time was reduced with increasing virus removal efficiency by adding TNPs in the system; and no virus reactivation was noticed after treatment by TNPs. Virus and its RNA were quickly degraded in dry condition compared to in wet conditions with or without adding any TNPs, confirming rapid inactivation efficiency in dry condition because a dry environment can hamper moisture and other nutrient transport processes. TNPs activated by UVC had enhanced inactivation capacity of the system with increasing RH. UVC-activated TNPs can excite electron (e) from valance band (VB) to conduction band (CB) and excited e can facilitate the generation of ROSs, i.e., OH and can not only oxidize the virus and RNA but also assist in H2O2 generation to further accelerate the inactivation process (Figure 2), although band gap is one of the important factors for the efficiency of the process to hamper recombination of the electron-hole (eh+). Formed OH can permeate through the cell envelope, disintegrate the nucleic acid structures by damaging the phosphodiester linkage, a promoter to form pyrimidine dimer, or full oxidation of purine and pyrimidine to form inorganics, i.e., CO2, H2O, and NH3; nonetheless, microbes can develop their own detoxification mechanisms against ROSs (Bogdan et al. 2015) and antioxidant development by emerging viruses should be well studied by detailed research.

Figure 2

ROSs and disinfectant generation by photocatalytic nanocomposite.

Figure 2

ROSs and disinfectant generation by photocatalytic nanocomposite.

Close modal

Moreover, H2O2 reactions are pH dependent as OH formation increases with increasing pH of the solution, although the relationship is not a linear one. Application of TNPs may reduce UV irradiation rate and time so practical application is highly likely during an outbreak. Iron (Fe), zinc (Zn), and magnesium (Mg) have convincing roles in virus cell replication and propagation; nucleic acid synthesis, transcription, replication, and repair; protein synthesis and repair; controlling enzymatic (e.g., RNA polymerase, various proteases, kinase, reductase, ATPase, cytochromes) and non-enzymatic activities (Liu et al. 2020) inside living cells; while nano-sized Fe, Zn, Au, Ag, and Ti can penetrate the envelope layer through nutrient transfer process of a pathogen cell to damage the transcription, replication, and restoration process outside a living cell.

Kitagawa et al. (2021) investigated the SARS-CoV-2 inactivation efficiency by FUVC-222 nm with intermittent irradiation and continuous irradiation where both types of irradiation inactivated the same percentage of viruses if the total photon penetration was the same and inactivation rate was increased with increasing fluence rate. Photo-reactivation, however, is a cell or DNA repair mechanism caused by an enzyme known as photolyase and light energy; but this repair mechanism was absent in this FUVC-supported process due to lack of enzyme or cellular activities responsible for this photo-reactivation.

Kumar et al. (2021) evaluated SARS-CoV-2 removal efficacy by targeting three types of gene sequences, i.e., ORF1ab, N and S proteins, in upflow anaerobic sludge blanket (UASB), clarifier, polishing pond, and aeration tank of a wastewater treatment plant (WWTP); where about >1.3-log removal of SARS-CoV-2 RNA was noticed in the UASB process and significant concentrations of ORF1ab, N and S proteins were detected in raw wastewater, UASB inlet and outlet, and aeration tank - although removal efficiency of virus from aeration tank, polishing pond, and clarifiers was not specifically determined. No virus or its protein/gene was identified in the final effluent indicating some removal of virus in aeration tank, clarifier, and polishing pond. The fate of the biological particles was not traced in every point of the system. Virus reduction in different stages, i.e., activated sludge (AS) process, anaerobic/anoxic/oxic (A2O) process, coagulation-flocculation and sand filtration has been witnessed by researchers and plant operators.

Ogilvie et al. (2021) looked into the effectiveness of QACs (i.e., benzalkonium chloride or dimethyl benzyl ammonium chloride or alkyl dimethyl ethylbenzyl ammonium chlorides) to inactivate SARS-CoV-2 in water with organic (i.e., 5% bovine serum albumin (BSA) or 0.5% bovine mucin (BM)) and inorganic (i.e., hard water) loading to understand the disinfection efficacy in different scenarios. Inactivation rate was decreased in the presence of organic or inorganic loadings compared to without those loadings because disinfectant may react with organic or inorganic matters or virus may be shielded by organic particles; and increasing contact time would simultaneously increase inactivation rate and reaction time with organic or inorganic compounds in the system.

Tu et al. (2021) comprehended SARS-CoV-2 inactivation by electrochemical oxidation when porous nickel (Ni) was used as cathode and anode NiOOH was formed in-situ in Na2CO3 aqueous solution; porous structure of electrode had increased the diffusion of virus particles and active sites for the oxidation process as virus inactivation was increased with increasing voltage. No thermal inactivation was observed as temperature was below 37 °C and continuous inactivation was possible for about 1,000-h with voltage of 4 V or 5 V by the system. RBD of spike glycoprotein (GP) was significantly reduced due to the presence of ROSs because several aromatic amino acids, i.e., tyrosine, phenylalanine, and tryptophan that had high reactivity with ROSs, were identified during the electrochemical cleavage of the cell; and longer contact time had influenced the degradation of protein to form small peptide and amino acid particles. However, several factors, i.e., abundant lattice oxygen (Olat) sites to support oxygen and oxygen species generation reactions, formation of α-carbon radicals and decomposition of peptide bonding, accelerate the virus inactivation process.

Xiling et al. (2021) investigated the inactivation efficiency of SARS-CoV-2 by thermal and chemical agents where increasing disinfectant concentrations had removed a high percentage of viruses and >30% ethanol solution can inactivate about >4-log virus titer within 0.5-min when OL was a vital factor in the stability of the virus. SARS-CoV-2 had similar heat and ethanol resistance compared to other Coronaviruses, however, genome disintegration and protein degradation were detected after the chlorine-based disinfection process. Although di-N-decyldimethylammonium bromide/chloride (DNB/DNC), two types of QAC, had attained about ≥4.92-log removal after 1-min with 170 mg/l, their mutagenic and reproductive toxicity (>0.3 mg/l) on human and mammals may make them inappropriate to apply in water and RRF.

While chemical inactivation can damage the virus cell within a very short time, additional cost may be incurred for the treatment of DBPs formed due to chemical treatment and a long inactivation time being necessary for natural thermal inactivation; photo-inactivation can not only inactivate the pathogen cells but also decontaminate other organic and inorganic pollutants from water. However, O3 and UV irradiation can significantly reduce DBP formation and exceptionally increase pathogen inactivation and organic degradation in the aqueous phase; complete inactivation is very important to restrict any possibility of DNA/RNA mutations where these kinds of spontaneous mutations can alter resistance mechanisms of viruses and other pathogens. Again, denature, renature, and degradation of protein structures, e.g., glycoproteins and nucleocapsids, may also stimulate the RNA/DNA mutations where infectivity may severely change due to any insertion or deletion in DNA/RNA sequence. Furthermore, the structure of Coronavirus may affect the inactivation process where diffusion (of ions or photons) and surface tension phenomena impede proper contact between the pathogen and inactivation agents. On the other hand, organic loading can also decrease the efficiency of amine group (-NH2) compounds in the inactivation process by forming RNH2, RR'NH, and RR'R”N when organic compounds may also react with other oxidizing agents to form stable or recalcitrant pollutants in aqueous phase. Then again, carboxylic functional group (-COOH) derived from biological (i.e., lipid, protein, amino or fatty acid degradation) and other sources may form ammonium salt if upstream treatment processes are not effective and stoichiometric calculations are not done accurately during chloramine-based disinfection. Thus, organic loading has significant interference in the disinfection process done by oxidizing agents.

Zika virus

Some inactivation mechanisms of ZIKV, a species of the Flaviviridae family, are shown in Table 4. Austin et al. (2019) had demonstrated ZIKV inactivation by UV-irradiation and 1, 5 iodonaphthyl azide (INA), a hydrophobic photo-active agent. Complete inactivation of ZIKV was perceived in the presence of combined UV and INA since INA was effectively bound with virus cells when illuminated by UV radiation. Damaging of virus envelope protein and distortion of virus RNA were the two suggested virion inactivation mechanisms by INA.

Table 4

Zika virus inactivation mechanisms with process efficacy

Pathogen genusDisinfectants or inactivation process (Concentration)% removal/log-removal or TCID50 (Contact time/intensity)Other propertiesReferences
ZIKV UV (100 W) 0.5-log TCID50/ml (20-min) Initial virus titer = 5.4-log TCID50/ml Austin et al. (2019)  
 INA (100 μM) 1.45-log TCID50/ml (20-min)   
 UV+ INA (50 μM) 5.4-log TCID50/ml (20-min)   
 UV+ INA (100 μM) 5.4-log TCID50/ml (20-min)   
ZIKV Thermal inactivation 1-log (6-d) Wastewater; Initial concentration = 105 copy number/μL; 35 °C Muirhead (2019)  
  2-log (13-d)   
  3-log (20-d)   
  1-log (14-d) 25 °C  
  2-log (28-d)   
  3-log (41-d)   
  1-log (123-d) 4 °C  
  2-log (209-d)   
  3-log (295-d)   
ZIKV-PRVABC59 Thermal inactivation 4.4 log10 TCID50/ml (120-min) Initial virus titer = 7.375 log10 TCID50/ml; LOL; 60 °C Wilde et al. (2016)  
  0.9 log10 TCID50/ml (120-min) HOL; 60 °C  
 Chemical inactivation, IsoPropyl alcohol, (70% v/v) 5.2 log10 TCID50/ml (120-s) LOL  
  5.6 log10 TCID50/ml (120-s) HOL  
 Quaternary ammonium/alcohol 3.6 log10 TCID50/ml (120-s) LOL  
  3.4 log10 TCID50/ml (120-s) HOL  
 NaOCl (500 mg/l) 4.2 log10 TCID50/ml (120-s) LOL  
 NaOCl (2,000 mg/l) 4.2 log10 TCID50/ml (120-s) LOL  
 NaOCl (500 mg/l) 0.0 log10 TCID50/ml (120-s) HOL;  
 NaOCl (2,000 mg/l) 1.8 log10 TCID50/ml (120-s) HOL  
 NaOCl (5,260 mg/l) 2.3 log10 TCID50/ml (120-s) HOL  
 NaOCl (10,000 mg/l) 3.05 log10 TCID50/ml (120-s) HOL  
 Peracetic acid (1,000 mg/l) 4.9 log10 TCID50/ml (120-s) LOL  
  1.3 log10 TCID50/ml (120-s) HOL  
 Acidic condition 0.3 log10 TCID50/ml (120-s) pH = 4.0; LOL  
  0.5 log10 TCID50/ml (120-s) pH = 4.0; HOL  
 Basic condition 0.9 log10 TCID50/ml (120-s) pH = 10.0; LOL  
  0.8 log10 TCID50/ml (120-s) pH = 10.0; HOL  
Pathogen genusDisinfectants or inactivation process (Concentration)% removal/log-removal or TCID50 (Contact time/intensity)Other propertiesReferences
ZIKV UV (100 W) 0.5-log TCID50/ml (20-min) Initial virus titer = 5.4-log TCID50/ml Austin et al. (2019)  
 INA (100 μM) 1.45-log TCID50/ml (20-min)   
 UV+ INA (50 μM) 5.4-log TCID50/ml (20-min)   
 UV+ INA (100 μM) 5.4-log TCID50/ml (20-min)   
ZIKV Thermal inactivation 1-log (6-d) Wastewater; Initial concentration = 105 copy number/μL; 35 °C Muirhead (2019)  
  2-log (13-d)   
  3-log (20-d)   
  1-log (14-d) 25 °C  
  2-log (28-d)   
  3-log (41-d)   
  1-log (123-d) 4 °C  
  2-log (209-d)   
  3-log (295-d)   
ZIKV-PRVABC59 Thermal inactivation 4.4 log10 TCID50/ml (120-min) Initial virus titer = 7.375 log10 TCID50/ml; LOL; 60 °C Wilde et al. (2016)  
  0.9 log10 TCID50/ml (120-min) HOL; 60 °C  
 Chemical inactivation, IsoPropyl alcohol, (70% v/v) 5.2 log10 TCID50/ml (120-s) LOL  
  5.6 log10 TCID50/ml (120-s) HOL  
 Quaternary ammonium/alcohol 3.6 log10 TCID50/ml (120-s) LOL  
  3.4 log10 TCID50/ml (120-s) HOL  
 NaOCl (500 mg/l) 4.2 log10 TCID50/ml (120-s) LOL  
 NaOCl (2,000 mg/l) 4.2 log10 TCID50/ml (120-s) LOL  
 NaOCl (500 mg/l) 0.0 log10 TCID50/ml (120-s) HOL;  
 NaOCl (2,000 mg/l) 1.8 log10 TCID50/ml (120-s) HOL  
 NaOCl (5,260 mg/l) 2.3 log10 TCID50/ml (120-s) HOL  
 NaOCl (10,000 mg/l) 3.05 log10 TCID50/ml (120-s) HOL  
 Peracetic acid (1,000 mg/l) 4.9 log10 TCID50/ml (120-s) LOL  
  1.3 log10 TCID50/ml (120-s) HOL  
 Acidic condition 0.3 log10 TCID50/ml (120-s) pH = 4.0; LOL  
  0.5 log10 TCID50/ml (120-s) pH = 4.0; HOL  
 Basic condition 0.9 log10 TCID50/ml (120-s) pH = 10.0; LOL  
  0.8 log10 TCID50/ml (120-s) pH = 10.0; HOL  

Muirhead (2019) examined the thermal degradation of ZIKV RNA in municipal wastewater at three different temperatures, i.e., 4 °C, 25 °C, and 35 °C, by assuming a high inactivation rate of ZIKV outside a host. Survivability of ZIKV and integrality of RNA was ten times higher at 4 °C than that at 25 °C. Moreover, ZIKV lingered in urine compared to serum, although persistence of ZIKV RNA gradually decreased in urine because high hydrolysis activity in urine can degrade RNA if no inhibitor for the hydrolysis process was present in the system. However, the findings of the research contradicted the initial assumption of the project.

Wilde et al. (2016) investigated ZIKV inactivation by thermal and chemical means, i.e., NaOCl, isopropyl alcohol, per-acetic acid and quaternary ammonium/alcohol process at different pHs with two types of organic loadings, i.e., low and high (LOL and HOL), where inactivation potential of isopropyl alcohol and quaternary ammonium was not dependent on OL but OL highly influenced disinfection properties of NaOCl and per-acetic acid. Inactivation efficiency was independent of contact time and inactivation was fast in a sample with LOL compared to a sample with HOL, as OL may affect virus viability by improving protein binding, shielding virus particles, or maintaining and distributing a different arrangement for virus on surfaces. Moreover, extreme acidic or basic pH may not be effective in ZIKV inactivation but ZIKV had less resistance to all applied removal processes than that of two other Flaviviridae members, i.e., bovine viral diarrhea virus (BVDV-NADL) and West Nile virus (WNV-B956).

Thermal inactivation had shown auspicious prospects in inactivating emerging pathogens, although application of a cheap and low-carbon energy source will be an enormous task when the world is desperately searching for renewable energy sources. While solarization can inactivate the virus cell with a long time duration, converged solar rays can inactivate the virus within a very short time as heat generation will be very high by this process.

Lassa virus

Table 5 shows removal of Lassa virus, a member of the Arenaviridae family, in different scenarios to understand the effectiveness of different processes. Elliott et al. (1982) reported Lassa virus inactivation by gamma irradiation (60Co) where more energy was required to inactivate Lassa virus compared to Ebola virus and Marburg virus; but UV irradiation (1,200–2,000 W/cm2) can inactivate Lassa virus within 20-min.

Table 5

Persistence of Lassa virus in different environments

Pathogen genusDisinfectants or inactivation process (Concentration)% removal/log-removal or TCID50 (Contact time/intensity)Other propertiesReferences
Lassa virus-Josiah Thermal inactivation 5-log10 PFU/ml (37-min) Initial virus titer = 106 PFU/ml; 60 °C Mitchell & McCormick (1984)  
Lassa virus Photo-inactivation (gamma irradiation, 60Co) 100% (116 × 104 rads) Initial virus titer = 6.0 log10 TCID50/ml; 4 °C Elliott et al. (1982)  
  100% (199 × 104 rads) −60 °C  
Pathogen genusDisinfectants or inactivation process (Concentration)% removal/log-removal or TCID50 (Contact time/intensity)Other propertiesReferences
Lassa virus-Josiah Thermal inactivation 5-log10 PFU/ml (37-min) Initial virus titer = 106 PFU/ml; 60 °C Mitchell & McCormick (1984)  
Lassa virus Photo-inactivation (gamma irradiation, 60Co) 100% (116 × 104 rads) Initial virus titer = 6.0 log10 TCID50/ml; 4 °C Elliott et al. (1982)  
  100% (199 × 104 rads) −60 °C  

In addition, Mitchell & McCormick (1984) studied Lassa virus thermal inactivation at 60 °C temperature and found such temperature can inactivate proteins and denature nucleic acids that are necessary for infectiousness. Many factors, i.e., presence of salts and organic compounds, pH and density of suspension, and presence of other microbes may influence the morbidity and mortality rate of virus and related virus may not be inactivated at the same rate.

Photolysis of Lassa virus is promising by not only UV irradiation (i.e., UVA, UVB, UVC, FUV) but also photo-assisted Fenton-reaction where UVA can catalyze the formation of OH and other ROSs in the presence of nano-sized semiconductor materials where health effect, because of UVC and gamma particle irradiation, can be abated; but adsorption of those rays on nano structure is an important issue to generate ROSs. A high energy level of photon sources can easily promote the electron transfer process and oxidize the cell components; while low energy level of photon sources needs some sensitizers or photocatalytic agents (i.e., semiconductor materials with organic or inorganic compounds) to support the ROSs’ generation and oxidation of cells. Therefore, the energy level of photon sources can affect the extent of damage to cells since increasing the wavelength by three times can decrease the energy level by three times; and for this reason, UV has high inactivation capability compared to visible light. Wavelength effect on inactivation, however, should be cautiously scrutinized to kill the virus so that highly resistant pathogens can be quickly inactivated in practical scenarios. Furthermore, the nano-structured particles can damage the cell envelopes by penetration depending on envelope thickness and composition where penetrated particles can hamper the internal cell functions and nucleic acids. Cell abrasion on rough particles may also rupture the external cell of pathogens; nonetheless, virus replication depends on virus DNA/RNA.

Therefore, these four emerging viruses can be effectively inactivated by different disinfectants in aqueous phase, although comparing the vulnerability to inactivation of these viruses with other well-known human waterborne viruses, e.g., adenovirus, reovirus, rotavirus, norovirus, etc., is a challenge as several factors may affect the inactivation process while wastewater must simultaneously contain several pathogens. Consequently, it is impossible to inactivate all these pathogens one by one in the treatment plant. The inactivation rate of these four emerging viruses by different disinfectants, however, should be compared with indicator microorganisms (e.g., coliform bacteria, E. coli, enterococci group, MS2 coliphage, enteric viruses, etc.) currently practiced for disinfection. Thus, susceptibility to inactivation of these well-known human waterborne viruses can be compared with these four emerging viruses by C.t or l.t values for different disinfectants as shown in Table 6. The well-known human waterborne viruses are more vulnerable to available disinfectants compared to the four emerging viruses; and for this reason, these four emerging viruses can develop into the situation of an epidemic or a pandemic if early alertness fails.

Table 6

C.t or l.t values for inactivating well-known human waterborne viruses and four emerging viruses

PathogensDisinfectant typesC.t (mg.min/l) or l.t (s.mW/cm2) value% inactivatedReferences
E. coli Combined chlorine 100–115 99% Jacangelo et al. (1997)  
FC 1.0–2.5 99% 
ClO2 1.0–2.5 99% 
Ozone 0.01–0.025 99% 
UV 10–25 99% 
Adenovirus Combined chlorine 30–110 99% Jacangelo et al. (1997)  
FC 0.01–0.5 99% 
ClO2 0.06–0.1 99% 
Ozone 0.1–0.2 99% 
UV 80–100 99% 
Reovirus FC 1.35–2.1 99.99% Liu (1973)  
UV 70–80 99% Jacangelo et al. (1997)  
Rotavirus FC 0.98 (pH = 7.0) 99% Kong et al. (2021)  
UV 20–70 99% Jacangelo et al. (1997)  
ClO2 0.22 (pH = 6.5) –20 (pH = 7.2) ≥99.9% Harakeh & Butler (1984), Chen & Vaughn (1990) and Ge et al. (2021)  
Ozone 0.005–2.5 (pH = 7.2) ≥99.99% Harakeh & Butler (1984) and Kong et al. (2021)  
Norovirus Combined chlorine 26 (pH = 7.0) 99% Cromeans et al. (2010)  
FC <0.02 (pH = 7.0) 99% 
Ozone 0.72 (pH = 7.0) –1.4 99%–99.99% Lim et al. (2010) and Kong et al. (2021)  
Coronavirus 
 SARS-CoV-2 FC 500–1,250 >99.9% Xiling et al. (2021)  
Ozone 1.2–36 ≥99.99% Kong et al. (2021) and Hu et al. (2021)  
FUVC 30–50 ≥99.99% Kitagawa et al. (2021) and Kong et al. (2021)  
 SARS-CoV FC 0.6–218.2 100% Wang et al. (2005)  
NaOCl 20–1,200 100% 
ClO2 200–1,200 100% 
UVC 3,614.4 >99.99% Darnell et al. (2004)  
 MARS-CoV UVC 200 >99.9% Eickmann et al. (2018) a 
Visible light 1.2 × 105 >99.9% 
 Ebola virus NaOCl 3.33–50,000 >99.99% Bibby et al. (2017) and Cook et al. (2016)  
UVC 200 >99.99% Eickmann et al. (2018) a 
Visible light 1.2 × 105 >99.99% 
 Zika virus NaOCl 10,520 >99% Wilde et al. (2016)  
 Lassa virus Gamma irradiation 1.44 × 109–2.4 × 109 100% Elliott et al. (1982)  
PathogensDisinfectant typesC.t (mg.min/l) or l.t (s.mW/cm2) value% inactivatedReferences
E. coli Combined chlorine 100–115 99% Jacangelo et al. (1997)  
FC 1.0–2.5 99% 
ClO2 1.0–2.5 99% 
Ozone 0.01–0.025 99% 
UV 10–25 99% 
Adenovirus Combined chlorine 30–110 99% Jacangelo et al. (1997)  
FC 0.01–0.5 99% 
ClO2 0.06–0.1 99% 
Ozone 0.1–0.2 99% 
UV 80–100 99% 
Reovirus FC 1.35–2.1 99.99% Liu (1973)  
UV 70–80 99% Jacangelo et al. (1997)  
Rotavirus FC 0.98 (pH = 7.0) 99% Kong et al. (2021)  
UV 20–70 99% Jacangelo et al. (1997)  
ClO2 0.22 (pH = 6.5) –20 (pH = 7.2) ≥99.9% Harakeh & Butler (1984), Chen & Vaughn (1990) and Ge et al. (2021)  
Ozone 0.005–2.5 (pH = 7.2) ≥99.99% Harakeh & Butler (1984) and Kong et al. (2021)  
Norovirus Combined chlorine 26 (pH = 7.0) 99% Cromeans et al. (2010)  
FC <0.02 (pH = 7.0) 99% 
Ozone 0.72 (pH = 7.0) –1.4 99%–99.99% Lim et al. (2010) and Kong et al. (2021)  
Coronavirus 
 SARS-CoV-2 FC 500–1,250 >99.9% Xiling et al. (2021)  
Ozone 1.2–36 ≥99.99% Kong et al. (2021) and Hu et al. (2021)  
FUVC 30–50 ≥99.99% Kitagawa et al. (2021) and Kong et al. (2021)  
 SARS-CoV FC 0.6–218.2 100% Wang et al. (2005)  
NaOCl 20–1,200 100% 
ClO2 200–1,200 100% 
UVC 3,614.4 >99.99% Darnell et al. (2004)  
 MARS-CoV UVC 200 >99.9% Eickmann et al. (2018) a 
Visible light 1.2 × 105 >99.9% 
 Ebola virus NaOCl 3.33–50,000 >99.99% Bibby et al. (2017) and Cook et al. (2016)  
UVC 200 >99.99% Eickmann et al. (2018) a 
Visible light 1.2 × 105 >99.99% 
 Zika virus NaOCl 10,520 >99% Wilde et al. (2016)  
 Lassa virus Gamma irradiation 1.44 × 109–2.4 × 109 100% Elliott et al. (1982)  

Note: E. coli as indicator microorganism.

aSample type is mentioned elsewhere in this report; 1 s.mW/cm2 = 1 mJ/cm2.

A number of thermal-, photo-, and chemical-inactivation processes are deciphered in the above discussion to remove four types of emerging contagious pathogens from aqueous phase and inactivation mechanisms by thermal- and photo-based systems as shown in Figure 3. When all the mentioned inactivation processes have demonstrated significant removal of virions from different media, any possibility of cell recovery should be meticulously observed as two steps of inactivation were noticed for all viruses. Furthermore, pathogens’ inactivation may be quickly possible by using some experimentally determined Ct values, but increasing the value of C can increase total chemical cost for treatment of specific pathogens; while decreasing the C value may increase treatment time (t) as well as hydraulic retention time (HRT) of the system since increasing the HRT is a challenge for specific reactor. Natural attenuation in winter may be hampered, however all inactivation processes may be affected by temperature fluctuation. Moreover, the virus separation process by membrane filtrations, i.e., ultrafiltration, nanofiltration, or reverse osmosis, is also shown in Figure 4 as pore size of these filters is <2–50 nm which is small enough to restrain a virus of >40 nm in diameter. Additionally, negatively charged virus and amino acids in proteins with different functional groups can form organic–inorganic composites with multi-valent cations (i.e., Ca2+, Al3+, Ti4+) (Figure 5) to precipitate at reactor bottom by following the principles of coagulation–flocculation. Precipitated biological sludge can be inactivated at the bottom by UV irradiation or heat where there is no need to illuminate or heat the whole water volume to save energy. Some unit operations and processes, e.g., sedimentation or clarification, filtration, coagulation–flocculation, precipitation, sorption, aerobic and anaerobic digestion, AOP and sludge processing can separate pathogens from aqueous phase, and partially or fully inactivate those pathogens, but operation and process reliability can downgrade the full inactivation objective. However, only pathogen separation or recovery is not a sustainable and hygienic way to reduce environmental impacts on a country's social and economic infrastructure as different types of pathogens have been discovered frequently without any clear knowledge about their attitude, life-cycle, propagation, enumeration, and infectivity in the environment. For example, Naegleria fowleri is a recently documented free-living amoeba available in any warm water such as ponds or lakes, responsible for causing a rapid and deadly brain infection known as primary amoebic meningoencephalitis (PAM) which may cause symptoms of morbidity within days with a fatality rate of 95% (Chaubey & Borah 2019). SARS-CoV-2, similarly, has been recently recognized and is a widely dispersed pathogen that is responsible for respiratory illness in both symptomatic and asymptomatic forms and precise treatment of these illnesses is still under rigorous research and observation.

Figure 3

Various impacts on virus/pathogens due to photo- and thermal-inactivation (active anion tails of soap or detergent may also rupture the lipid bi-layer to facilitate the process of fracture).

Figure 3

Various impacts on virus/pathogens due to photo- and thermal-inactivation (active anion tails of soap or detergent may also rupture the lipid bi-layer to facilitate the process of fracture).

Close modal
Figure 4

Virus separation from biologically contaminated water/wastewater by ultra- or nano-filter.

Figure 4

Virus separation from biologically contaminated water/wastewater by ultra- or nano-filter.

Close modal
Figure 5

Bonding of negatively charged virus, protein, and amino acids with multivalent cations in aqueous phase. This bio-chemical sludge will precipitate at the bottom of a reactor and facilitate degradation or inactivation.

Figure 5

Bonding of negatively charged virus, protein, and amino acids with multivalent cations in aqueous phase. This bio-chemical sludge will precipitate at the bottom of a reactor and facilitate degradation or inactivation.

Close modal

Hence, strategic management of the water and wastewater industry to tackle sudden and continuous deadly biological load should be formulated by adapting WBE to generate early warnings to the public where these warnings will facilitate the forecasting system for an epidemic or pandemic. Basic strategic concepts, i.e., monitoring, designing, implementation and performance evaluation for a water and wastewater treatment plant are briefly discussed in Figure 6 to follow the initial trend or resurgence of outbreaks. Some desalination plants have been practicing chlorine spiking at the beginning of the treatment to remove harmful algae and this practice can simultaneously remove these pathogens, although high concentrations of DBPs may be expected at the end due to initial high concentration of NOMs, e.g., fulvic acids, humic acids, and humins in natural water. However, secondary and tertiary treatment can effectively decontaminate the water whereas aerosolized forms of virus can be significantly reduced by that initial disinfection effort. Moreover, treatment plant operators as front-line combatants against these deadly pathogens should follow rigorous safety rules as aerosolized virus or suspended virus from untreated water and wastewater can probably reach the nosocomial or gastrointestinal routes to cause illness.

Figure 6

Strategic management of water and wastewater treatment plants to effectively manage deadly waterborne outbreaks.

Figure 6

Strategic management of water and wastewater treatment plants to effectively manage deadly waterborne outbreaks.

Close modal

Some conventional disinfectants, i.e., chlorine, iodine, bromine, chloramines, ClO2, O3, H2O2, solarization, UV, gamma irradiation, and heat treatment can effectively inactivate pathogens in water, wastewater and sludge management processes, although some alcohol and aldehyde-based disinfectants mentioned in this review are reported without any practical application for water and wastewater treatment but those disinfectants have a use in other parts of treatment plants. Novel nanotechnology-based disinfectants, i.e., TiO2, ZnO, zero valent iron nanoparticles (ZVINPs), chitosan, MgO, carbon-nanotubes with single- and multi-wall (SWCNT and MWCNT), nano silver and gold (nAg and nAu), fullerene (nC60), Al2O3 (Hossain et al. 2014), and AOPs (O3 + H2O2, O3 + UV, H2O2 + UV, TiO2 + UV, TiO2 + H2O2 + UV) with Fenton reactions and photo-Fenton reactions have demonstrated their antimicrobial effectiveness in laboratory experiments and a few state-of-the-art treatment processes where reduction of DBPs’ formation is a priority. Likewise, other ROS generating elements, i.e., mixed metal oxides (e.g., FeTiO3, CaTiO3) and metal sulfides (e.g., ZnS, MnS) (Hoffmann et al. 1995), are potential candidates for pathogen inactivation at different temperature ranges (<0 to >500 °C) where leachate from those elements should be carefully tested for possible further contamination in aqueous phase. Furthermore, photocatalytic nanocomposites should be synthesized by cost-effective and novel environmentally friendly elements so that those composites can be activated by both visible and UV wavelength with synergistic impacts to remove various chemical and biological contaminants. Besides, ROSs, e.g., singlet oxygen (1O2), hydroperoxyl radical , superoxide , dihydrogen trioxide , hydroxyl radical (OH) generation, by activating some nanostructured composites, may also expedite the pathogen removal process from aqueous and gaseous phase where the life-span of these ROSs will be generally very short so the possibility of adverse health effects may be insignificant. Pathogen inactivation by highly concentrated laser beams may also be a better removal technique although the cost-effectiveness and resource availability of the treatment should be carefully investigated. Above and beyond, interaction between different factors may be comprehensively studied with the help of tools such as design of experiment (DoE) where marginal effect of nominal factors can be considered in the inactivation process. Moreover, effective de-chlorination, de-ozonation or other decontamination processes can further elevate potable water quality. Nanostructured disinfectants, however, have momentous prospects in the water and wastewater industry, where those particles or structures are immobilized on membrane or other surfaces (Figure 7) without any leaching into aqueous phase as separation and recovery of nanostructured elements is a challenging task to safeguard public health from another contamination. Nevertheless, understanding of inactivation mechanisms is imperative because reduced disinfectant concentration or irradiation rate can be applied if the specific inactivation process is known, where high chemical dosing can intensify DBPs’ generation or high irradiation rate may affect benign cells and power consumption. Optimization of different parameters in the pathogen inactivation process can be well-tuned if the sensitivity of proteins, lipids, and nucleic acids to different inactivation agents is deciphered.

Figure 7

Nano-particle-assisted AOP to inactivate pathogens in plug-flow reactor. Permeable membrane sheets are rotatable with respect to direction of photon sources.

Figure 7

Nano-particle-assisted AOP to inactivate pathogens in plug-flow reactor. Permeable membrane sheets are rotatable with respect to direction of photon sources.

Close modal

Although climate change impacts have been rigorously scrutinized in the water and wastewater industry, elevated temperature can effectively inactivate pathogens and reduce active disinfectant concentrations to be used as primary and secondary disinfectants. However, the stability of disinfectants, e.g., chlorine, ozone, and other alcohol-based disinfectants in aqueous phase or on solid surfaces, may be decreased at high temperature so changing climate has both advantages and disadvantages on the pathogen inactivation process. Moreover, warm weather will cause proliferation of the transmission and dispersion of ZIKV by two major ZIKV vectors by increasing their breeding ground where mosquitos can quickly complete their life-cycle in a warm contaminated environment. Other vectors or virus reservoirs may also behave differently in a warm climate because transmission, life-cycle, mutation, and infectivity of virus may be altered due to temperature change. Volatilization of disinfectants may, furthermore, deteriorate air quality in warm weather but warm weather can accelerate the disinfection kinetics or reactions. Elevated temperature, besides, can accelerate the formation of by-products in the disinfection process and volatility of many DBPs, e.g., chloroform, may also simultaneously increase to raise volatile organic carbon (VOC) concentration in air. Moreover, thermal- and photo-inactivation are energy-intensive processes where millions of gallons of water per day must be treated to supply potable water in every corner of the world; however, renewable energy applications in the water and wastewater sector may shrink the carbon footprint and other greenhouse gas emissions from resource recovery and utilization facilities.

Gene editing or gene restructuring may be a potential technique to reduce virus infectivity or vectors’ selectivity for pathogens, but researchers must be extremely watchful about gene mutation that can elevate the aggressiveness of the virus. Gene editing, however, can effectively transmute virus behavior towards specific infection, although a huge amount of resources must be employed by the researchers by concentrating on broad legalistic approaches. Besides, internal and external defense mechanisms governed by virions’ genes, function of radical scavengers and superoxide dismutase (SOD) or superoxide reductase (SOR) in the recovery process should be comprehensively studied to upgrade the inactivation route. All these four re-emerging viruses, however, can be used as biological weapons or bioterrorism agents, therefore, strict regulations should be adapted in the laboratories and RRFs. Environmental biotechnology will enhance the benefit of recovered pathogens when recovery efficiency can maximize the impact and further biological contamination can be reduced by following effective biosafety rules. Furthermore, identification of cytotoxic, mutagens and teratogens can downgrade the probability of rapid mutation of pathogens since prompt mutation can hamper the inactivation and vaccination practice but virus dispersion and infectivity may be multi-fold if discharge and abundance of those mutagenic agents cannot be significantly reduced. In this context, application of geographic information system (GIS), artificial intelligence (AI), and satellite techniques can help in monitoring, tracking, natural attenuation and performance evaluation of specific contaminants in the aqueous and gaseous phases.

Biological and chemical sludge from aerobic and anaerobic treatment processes must be effectively treated by UV or gamma irradiation where partially inactivated pathogens in sludge can be recovered and aerosolized in the agricultural field and can cause a catastrophe in the surrounding area. Moreover, there is a possibility of infection by these viruses at every stage in water and RRFs so judicious and practical bio-safety protocols are necessary.

Although researchers have been working very hard to develop vaccines for controlling contagious diseases caused by these four viruses, the aggressive infectious nature of these pathogens may still infect millions of people. Effective thermal-, photo-, and chemical inactivation can entirely remove these pathogens from water and RRFs; but quick and accurate detection of these pathogens is vital to thwart any deadly outbreaks in the community through gaseous and aqueous media. However, source identification and minimization should be cautiously implemented so that biological contamination and the subsequent decontamination burden can be reduced. Therefore, possible inactivation mechanisms have been rigorously depicted for each process so that more effective disinfection units and cost-effective disinfectants can be developed. According to the author's knowledge, this kind of review report is extremely rare in the current scientific community.

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

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