Total Nitrogen Exceeding the Standard and Its Impact on Sewage Treatment Systems
The impact of excessive total nitrogen on The Sewage Treatment system is mainly reflected in process efficiency, microbial activity, and effluent stability, as detailed in the following analysis and recommendations:
1. Decreased Process Efficiency
- Impeded Denitrification
Excessive total nitrogen often accompanies reduced denitrification efficiency. High dissolved oxygen (DO) levels in the anoxic zone (>0.5 mg/L) disrupt the anoxic environment, inhibiting denitrifying bacteria activity and preventing effective conversion of nitrate nitrogen to nitrogen gas. Additionally, insufficient carbon-to-nitrogen ratio (C/N<4) restricts the denitrification process, preventing complete nitrogen removal.
- Restricted Nitrification
Accumulation of ammonia nitrogen may suppress nitrifying bacteria activity, especially when influent ammonia nitrogen concentration fluctuates or pH deviates from the suitable range (6.5-8.0), significantly reducing nitrification rates. Low temperatures (<15℃) also decrease both nitrification and denitrification efficiency.
2. Imbalanced Microbial System
- Inhibition of Bacterial Communities
High concentrations of free ammonia (FA>60 mg/L) directly inhibit the activity of nitrifying bacteria (AOB and NOB), leading to system collapse. Additionally, insufficient carbon sources may cause heterotrophic bacteria to proliferate excessively, reducing space for denitrifying bacteria.
- Abnormal Sludge Activity
Short sludge age (SRT) or excessive sludge wasting prevents nitrifying bacteria from completing their reproductive cycles. High sludge loading (>0.15 kgBOD/kgMLSS·d) may cause non-filamentous bulking, reducing sludge settleability.
3. Uncontrolled Operating Parameters
- Malfunctioning Recirculation Ratios
Insufficient internal recirculation ratio (<300%) prevents adequate return of nitrate nitrogen to the anoxic zone, affecting denitrification efficiency. Excessive external recirculation ratio (>50%) may introduce dissolved oxygen into the anoxic zone, disrupting denitrification conditions.
- DO and pH Fluctuations
Insufficient dissolved oxygen (DO<2 mg/L) in the aeration tank limits nitrification, while excessive DO disrupts anoxic zone denitrification. Deviations in pH from the optimal range (7.2-8.0 for nitrification, 6.5-8.0 for denitrification) inhibit key enzyme activity.
4. Effluent Quality and Ecological Risks
- Worsened Eutrophication
Excessive total nitrogen in effluent (>1.0 mg/L) directly causes water eutrophication, leading to algal blooms, dissolved oxygen depletion, and ecological chain collapse.
- Accumulation of Toxic Substances
Excessive nitrate and nitrite may accumulate through the food chain, posing health risks (e.g., carcinogenic risks).
Recommendations
1. Process Optimization
- Supplement carbon sources (e.g., sodium acetate) to adjust C/N to 4-6.
- Control internal recirculation ratio (300-500%) and external recirculation ratio (30-50%).
- Install pre-denitrification tanks or MBR processes to extend sludge age.
2. Parameter Regulation
- Maintain anoxic zone DO<0.5 mg/L and aerobic zone DO=2-4 mg/L.
- Add alkalinity (e.g., sodium carbonate) to stabilize pH at 7.0-8.0.
3. Emergency Measures
- Add denitrifying bacterial agents to accelerate system recovery.
- Use chemical methods (e.g., breakpoint chlorination) for rapid nitrogen reduction in the short term.
Excessive total nitrogen requires dynamic adjustment of processes based on real-time monitoring data (e.g., ORP, MLSS). Specific standards can be referenced in the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918—2002).