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 biologicalsystem 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
2NH O NO H O 4H
NO O42Nitrosomonas
2222Nitrobacte
⎯→⎯⎯⎯⎯
rr
⎯→⎯⎯⎯ 2 NO 3
The third stage accomplished denitrification–conversion of
nitrites and nitrates to atmospheric nitrogen under anaerobic
conditions:322NO CH OH 3NO CO H O2NO CH OH N CO H O 2OH33 222
23 222 →→PHOSPHORUS AND BOD REMOVAL NITRIFICATION DENITRIFICATIONCoagulating Chemical Application (Optional Points)Air Air MethanolRaw
WastewaterSettling Settling Settling Reaction Settling
Ta n kAeration
Ta n kWaste Sludge
Waste Sludge Waste Sludge Waste SludgeReturn
SludgeReturn
SludgeReturn
SludgeAeration Effluent
TankFIGURE 22 Typical three-stage treatment process for nutrient removal.TABLE 4
Operating parameters of conventional anaerobic digestersParameters Unmixed Mixed
Bv – Loading Rate, 0.02–0.05 0.1–0.3
1b VSS/day/cubic ft
kg VSS/day/cubic metre0.32–0.80 1.6–3.2t ̄ – Detention time, days 30–90 10–15
E – Volatile Solids
Reduction percent50–70 50Mixing Absent Present
pH 6.8–7.4 6.8–7.4
Temperature, °C 30–35 30–35C002_001_r03.indd 156C002_001_r03.indd 156 11/18/2005 10:15:55 AM11/18/2005 10:15:55 AM