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Nitrogen Balance
Tracking nitrogen species through treatment
Overview
Nitrogen balance tracks all nitrogen species as they transform through wastewater treatment. Understanding N transformations is essential for designing nitrogen removal systems.
Nitrogen Species
Forms of Nitrogen
| Species | Symbol | Description |
|---|---|---|
| Ammonia | NH4-N | Reduced, soluble |
| Nitrite | NO2-N | Oxidized, intermediate |
| Nitrate | NO3-N | Fully oxidized |
| Organic N | Org-N | Bound in organics |
| Particulate N | Part-N | In biomass/solids |
| Dinitrogen | N2 | Gas, denitrification product |
| N2O | N2O | Greenhouse gas |
Aggregate Parameters
| Parameter | Components |
|---|---|
| TKN | NH4-N + Organic-N |
| TN | TKN + NOx-N |
| NOx-N | NO2-N + NO3-N |
| TSN | Total soluble N |
Nitrogen Transformations
Process Flow
Organic N (Influent)
│
├── Ammonification → NH4-N
│ │
│ ┌────────────┴────────────┐
│ │ │
│ Assimilation Nitrification
│ (to biomass) (AOB + NOB)
│ │ │
│ ↓ ↓
│ Particulate N NO3-N
│ (WAS removal) │
│ │
│ Denitrification
│ │
│ ↓
│ N2 (gas)
│ │
└───────────────────────────────────┘Key Reactions
Nitrification (aerobic): $$NH_4^+ + 1.5O_2 \xrightarrow{AOB} NO_2^- + H_2O + 2H^+$$ $$NO_2^- + 0.5O_2 \xrightarrow{NOB} NO_3^-$$
Denitrification (anoxic): $$NO_3^- + organic\ carbon \rightarrow N_2$$
Mass Balance
Overall Balance
$$N_{in} = N_{effluent} + N_{sludge} + N_{gas}$$
Component Tracking
| Stream | NH4 | NO3 | Org-N | Part-N | N2 |
|---|---|---|---|---|---|
| Influent | 35 | 0 | 10 | 5 | 0 |
| Primary eff | 35 | 0 | 8 | 2 | 0 |
| Anoxic eff | 30 | 5 | 5 | 25 | 10 |
| Aerobic eff | 2 | 8 | 3 | 27 | 15 |
| Secondary eff | 1.5 | 6 | 0.5 | 0.5 | - |
| WAS | - | - | - | 20 | - |
ErgoPlanner Configuration
Influent Nitrogen
json
{
"nitrogen": {
"TKN": 45,
"NH4_N": 35,
"organic_N": 10,
"particulate_N_fraction": 0.3
}
}Nitrogen in COD
Biomass contains nitrogen:
- fN,BM = 0.086 g N/g COD (typical)
- Affects sludge N content
Design Considerations
SRT for Nitrification
Minimum SRT depends on temperature:
| Temperature | Min SRT (days) | Safety Factor |
|---|---|---|
| 10°C | 12 | 1.5-2.0 |
| 15°C | 6 | 1.5-2.0 |
| 20°C | 3 | 1.5-2.0 |
$$SRT_{min} = \frac{1}{\mu_{max,A} - b_A}$$
Denitrification Capacity
Carbon requirement: $$COD_{denit} = 2.86 \times NO_3\ removed$$
Internal recycle ratio: $$r = \frac{TN_{target}}{TN_{in} - TN_{target}} - 1$$
Example: MLE Process
Configuration
| Parameter | Value |
|---|---|
| Flow | 20,000 m³/d |
| Influent TKN | 45 mg/L |
| Target TN | <10 mg/L |
| RAS | 100% |
| IRR | 200% |
Results
| Location | NH4-N | NO3-N | TN |
|---|---|---|---|
| Influent | 35 | 0 | 45 |
| Anoxic zone | 25 | 2 | 32 |
| Aerobic zone | 1.5 | 12 | 18 |
| Effluent | 1.0 | 7 | 9 |
N Removal Paths
| Pathway | kg N/d | % of Load |
|---|---|---|
| Denitrification | 600 | 67% |
| WAS | 180 | 20% |
| Effluent | 180 | 20% |
Troubleshooting
| Issue | Cause | Solution |
|---|---|---|
| High NH4 effluent | Low SRT | Increase sludge age |
| High NO3 effluent | Low IRR | Increase recycle |
| Incomplete denit | Low C/N | Add carbon source |
| Rising sludge | Denit in clarifier | Reduce blanket depth |
N2O Emissions
Sources
- AOB pathway (incomplete oxidation)
- Heterotrophic denitrification
- Chemical reactions
Factors Increasing N2O
| Factor | Effect |
|---|---|
| Low DO | Increases AOB pathway |
| High NO2 | Substrate for N2O |
| Low COD/N | Incomplete denit |
| Transients | Upset conditions |
Emission Factors
Typical: 0.1-1% of N load as N2O-N
Best Practices
- Maintain adequate SRT - Safety factor of 1.5-2.0
- Optimize IRR - Balance energy vs N removal
- Provide sufficient carbon - COD/N > 5 for denit
- Control DO - 2 mg/L aerobic, <0.2 anoxic
- Monitor regularly - NH4 and NO3 profiles
Related Topics
References
- Metcalf & Eddy "Wastewater Engineering" 5th Ed
- Henze, M. "Biological Nitrogen Removal"
- WEF MOP 30 "Nutrient Removal"