India |
Secondary + tertiary treatment |
– Sequencing batch reactor (SBR) + Cl2 (site: 3 and 4) |
All negative |
Arora et al. (2020) |
|
|
– Moving bed biofilm reactor (MBBR) + UV (site: 5) |
All negative |
|
|
|
– Sequencing batch reactor (SBR) + without tertiary (site: 6) |
All negative |
|
Iran – Tehran |
Secondary + tertiary treatment |
– Extended aeration activated sludge (EAAS) system + Cl2 disinfection (Modules: 1–4) |
Positive samples: 2/4 = 50.0% |
Nasseri et al. (2021) |
|
|
– Oxidation ditch method + UV disinfection (Modules: 5–6) |
All negative |
|
– Anzali |
|
– Extended aeration activated sludge (EAAS) system + Cl2 disinfection |
All negative |
|
– Qom |
|
– Conventional activated sludge (CAS) system with diffuser aeration + Cl2 disinfection |
All negative |
|
Japan |
Secondary treatment |
– Activated sludge (AS) system |
Positive sample: 1/5 = 20.0% |
Haramoto et al. (2020) |
Italy (Padua, Veneto, NE Italy) |
Secondary + tertiary treatment |
– Activated sludge (AS) system + peracetic acid and terminal UV lamps |
Positive sample: 2/2 = 100% |
Baldovin et al. (2021) |
Spain |
Secondary treatment |
– Activated sludge (AS) system |
Positive sample: 2/18 = 11.1% |
Randazzo et al. (2020b) |
|
Tertiary treatment |
– Coagulation, flocculation, and filtration, UV and NaClO disinfection |
Positive sample: 0/13 = 0% |
|
Spain (North–Western) |
Primary treatment |
– Primary settler |
Positive sample: 1/2 = 50% |
Balboa et al. (2021) |
|
Secondary treatment |
– SBR and microfiltration |
Positive sample: 0/5 = 0% |
|
USA |
Secondary treatment |
– Activated sludge (AS) system |
Positive sample: 0/4 = 0% |
Sherchan et al. (2020) |
|
Tertiary treatment (Final effluent) |
– Cl2 disinfection |
Positive sample: 0/4 = 0% |
|
UAE |
Secondary treatment |
– Activated sludge process (ASP)/clarification |
Positive sample |
Hasan et al. (2021) |
|
Tertiary treatment |
– Sand filtration, disinfection, and chlorination |
None of the 11 WWTPs' treated effluents tested positive |
|
Israel |
Secondary treatment |
– Activated sludge process |
– ~1 log10 RNA removal by the primary and secondary treatment |
Abu Ali et al. (2021) |
|
Tertiary treatment |
– Sand filtration and disinfection through chlorination |
– > 100 copies/L of SARS-CoV-2 RNA remained the secondary effluent |
|
Saudi Arabia |
Secondary treatment |
– Activated sludge (AS) system |
N1: 0.3 log10 reduction (50%) |
Hong et al. (2021) |
|
Tertiary treatment |
– Chlorination |
N3: 0.5 log10 reduction (70%) |
|
|
(Hospital WWTP) |
|
|
|