Encyclopedia of Environmental Science and Engineering, Volume I and II

(Ben Green) #1

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.


  1. 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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