156 BIOLOGICAL TREATMENT OF WASTEWATER
Depending on pH, ammonia can be toxic to anaerobic
bacteria and free ammonia is more toxic. If concentration
of free ammonia exceeds 150 mg/L, severe toxicity will
result, whereas the concentration of ammonium ions must be
greater than 3000 mg/L to have the same effect. At a concen-
tration of 1600 mg/L as N, ammonia can upset the process.^20
The volatile acids cause little inhibition in anaerobic reac-
tors at neutral pH.^21 Operating parameters of conventional
anaerobic digesters are shown in Table 4.
- NUTRIENT REMOVAL
Biological nitrification and denitrification is one of the
common methods for nitrogen removal from wastewaters.
In warmer climates, nitrification may occur to a consider-
able degree in conventional aerobic biological treatment
processes, followed by serious adverse effects of denitrifica-
tion in settling tanks and/or the receiving bodies of water. In
northern cold climates, below 18°C, a three-stage biological
system as shown in Figure 22 is considered necessary for
nutrient removal.^46 In the first stage, carbonaceous BOD is
reduced to a level below 50 mg/L. In the second stage, the
ammonia, present in effluent from the first stage, is oxidized
to nitrites and nitrates by nitrosomonas and nitrobacters,
respectively, as shown below:
23 2 2
2
NH O NO H O 4H
NO O
42
Nitrosomonas
22
22
Nitrobacte
⎯→⎯⎯⎯⎯
rr
⎯→⎯⎯⎯ 2 NO 3
The third stage accomplished denitrification–conversion of
nitrites and nitrates to atmospheric nitrogen under anaerobic
conditions:
32
2
NO CH OH 3NO CO H O
2NO CH OH N CO H O 2OH
33 222
23 222
→
→
PHOSPHORUS AND BOD REMOVAL NITRIFICATION DENITRIFICATION
Coagulating Chemical Application (Optional Points)
Air Air Methanol
Raw
Wastewater
Settling Settling Settling Reaction Settling
Ta n k
Aeration
Ta n k
Waste Sludge
Waste Sludge Waste Sludge Waste Sludge
Return
Sludge
Return
Sludge
Return
Sludge
Aeration Effluent
Tank
FIGURE 22 Typical three-stage treatment process for nutrient removal.
TABLE 4
Operating parameters of conventional anaerobic digesters
Parameters Unmixed Mixed
Bv – Loading Rate, 0.02–0.05 0.1–0.3
1b VSS/day/cubic ft
kg VSS/day/cubic metre
0.32–0.80 1.6–3.2
t ̄ – Detention time, days 30–90 10–15
E – Volatile Solids
Reduction percent
50–70 50
Mixing Absent Present
pH 6.8–7.4 6.8–7.4
Temperature, °C 30–35 30–35
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