Research Article
Study of Carbonaceous and Nitrogenous Pollutant Removal Efficiencies in a Hybrid Membrane Bioreactor
Table 2
Operational conditions of the HMBR.
| Height of packing bed (cm) | Number of period | Number of days in the period | Accumulated time from day to day | Concentration of COD at the inlet Kg/m3 | Concentration of Kg N/m3 | Air flowrate L/h | Average COD loading rate kgCOD/(m3⋅d) | Average loading rate kgN/(m3⋅d) |
| Phase I 27 cm | 1 | 16 | 1–16 | 250–1000 | 16–65 | 120 | | | 2 | 10 | 17–26 | 2000 | 135 | 2,87 | 0,19 | 3 | 7 | 27–33 | 60 | 4 | 8 | 34–41 | 2500 | 165 | 3,59 | 0,24 | 5 | 8 | 42–49 | 120 | 6 | 10 | 50–59 | 3000 | 202 | 4,30 | 0,29 | 7 | 7 | 60–66 | 60 | 8 | 7 | 67–73 | 5000 | 335 | 7,17 | 0,48 | 9 | 6 | 74–79 | 120 | Phase II 54 cm | 10 | 10 | 80–89 | 3000 | 202 | 180 | 4,30 | 0,29 | 11 | 14 | 90–103 | 60 | 12 | 7 | 104–110 | 5700 | 380 | 8,18 | 0,55 | 13 | 8 | 111–118 | 120 | 14 | 11 | 119–129 | 180 | 15 | 5 | 130–134 | 4000 | 270 | 5,74 | 0,39 | 16 | 5 | 135–139 | 60 | 17 | 9 | 140–148 | 120 | 18 | 5 | 149–153 | 60 | Phase III 0 cm | 19 | 6 | 154–159 | 4000 | 270 | 5,74 | 0,39 | 20 | 7 | 160–166 | 120 |
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