Table 2.
Reactor | HRT | Influent conc. mg/L | Removal efficiency (%) | NLR kg-N/m3/d | NRR kg-N/m3/d | Reference | ||
---|---|---|---|---|---|---|---|---|
NH4–N | NO2–N | NH4–N | NO2–N | |||||
UASB reactor | 0.2 h | 300 | 360 | 90 | N.A. | 89.1 | 74.3–76.7 | [28] |
EGSB reactor | 6–0.3 h | 494 | 522 | 94.68 | 99.84 | 77.84 | 57.14 | [29] |
EGSB reactor | 1.5 h | 661.9 | 767.2 | 71.7 | 94.1 | 22.87 | 18.65 | [30] |
AGSB reactor | 1.1 h | 400 | 500 | N.A. | N.A. | N.A. | 15.40 | [26] |
UASB reactor | N.A. | 320–340 | 350–380 | 96.1 | 95.2 | 7.2 | 6.2 | [27] |
Upflow filter system | 1.99 h | 305 | 304 | 74.2 | 92.4 | 7.34 | 6.11 | [71] |
UASB reactor | 0.12 h | 16.87 ± 2.09 | 20.57 ± 2.31 | 92.81 | 94.35 | N.A. | 5.72 | [72] |
ALR reactor | 5.4 h | 546 | N.A. | 94.4 | N.A. | 2.37 | 2.29 | [73] |
UASB reactor | 0.28 h | 16.87 ± 2.09 | 20.57 ± 2.31 | 78.45 | 92.31 | N.A. | 2.28 | [72] |
UBF reactor | 1.54 h | 976.0 | 1280 | 88.84 | 98.1 | 34.5 | N.A. | [74] |
SBR reactor | 0.18 d | 500 | 580 | 97 | 97 | 0.156 | N.A. | [75] |
SBR reactor | 3 d | 268 | 345 | 83.6 | 100 | N.A. | N.A. | [76] |
SBR reactor | 1.5 h | N.A. | N.A. | 80.9 | 88 | N.A. | N.A. | [77] |
N.A.: not available.