Table 3.
Nitrogen removal in laboratory-, pilot- and full-scale nitritation-denitritation systems.
| Influent NH4+ conc. (mg-N/L) | C/N ratio | Operational temperature (°C) | HRT (days) | NH4+ conversion rates (%) | NRR (kg-N/m3-day) | NRE (%) | Remarks | References | |
|---|---|---|---|---|---|---|---|---|---|
| 1 | 4,559 ± 201 | - | 36 ± 1 | - | 60 | - | - | 250 l system | Ganigué et al. (2010) |
| 2 | >1,000 | 2.4 | 30–40 | >90 | - | 65-95a | Full-scale system | Mulder et al. (2001) | |
| 3 | 1,135 | 2.2 | 30–32 | 2.3 | 80b | 1.0 | 67 | 5.65 l CSTR | Fux et al. (2006) |
| 4 | 1,216 | 1.94 | 1.0–1.6 | 95c | 3.0–3.6 | 93 | 6 l SBR with continuous sludge addition | ||
| 5 | 400–700 | - | 35 | - | 1-3d | - | 95-98 | 7 l CSTR operated with sequencing of operations | Claros et al. (2012) |
| 6 | 1750-1900b | - | - | 1.86-2.71/2.71 | 79–98 | 0.63 | 95 | Two-stage SBRs (10 l/6 l) | Zhang et al. (2019) |
| 7 | 200 ± 18e | 3 | 20–22 | 0.71–3.33 | - | - | 100 | 5 l SBR | Bernat et al. (2016) |
From Figure 6 in the source file.
Estimated in Figure 2 in the source file.
Estimated from Figure 3 in the source file.
Figure 3a in the source file;
NO2−.