Appearance
Alkalinity Balance - Nitrification and Chemical Dosing
Alkalinity balance is critical in biological nutrient removal (BNR) systems. Nitrification consumes significant alkalinity, potentially depressing pH and inhibiting treatment. Chemical dosing for phosphorus removal also consumes alkalinity. This guide covers calculation and supplementation requirements.
Key Stoichiometric Relationships
Nitrification Alkalinity Consumption
Reaction:
NH₄⁺ + 2O₂ → NO₃⁻ + 2H⁺ + H₂OAlkalinity consumption:
7.14 kg CaCO₃ consumed per kg NH₄-N oxidizedDerivation:
- Each mole NH₄⁺ oxidized produces 2 moles H⁺
- H⁺ reacts with alkalinity (HCO₃⁻) to maintain pH
- Stoichiometry: 14g N → 100g CaCO₃ → 7.14 kg/kg
Denitrification Alkalinity Recovery
Reaction:
NO₃⁻ + organic C → N₂ + HCO₃⁻Alkalinity recovered:
3.57 kg CaCO₃ recovered per kg NO₃-N denitrifiedDerivation:
- Half the consumption of nitrification (1 mole HCO₃⁻ vs 2 moles H⁺)
- 3.57 = 7.14 / 2
Chemical Dosing Alkalinity Consumption
Ferric sulphate reaction:
Fe₂(SO₄)₃ + 3Ca(HCO₃)₂ → 2Fe(OH)₃ + 3CaSO₄ + 6CO₂Alkalinity consumption:
0.75 kg CaCO₃ consumed per kg Fe dosedAluminum sulphate alternative:
0.50 kg CaCO₃ consumed per kg Al dosedDesign Equations
Nitrification Consumption
Alkalinity Required for Nitrification
Formula:
Alk_consumed = NH₄_oxidized × 7.14Where:
Alk_consumed= alkalinity consumption (kg CaCO₃/d)NH₄_oxidized= ammonia nitrogen oxidized (kgN/d)7.14= stoichiometric factor (kg CaCO₃/kg N)
Example:
NH₄_inf = 30 mg/L
NH₄_eff = 3 mg/L (after nitrification)
Q = 1,000 m³/d
NH₄_oxidized = ((30 - 3) × 1000) / 1000 = 27 kgN/d
Alk_consumed = 27 × 7.14 = 192.8 kg CaCO₃/dConcentration basis:
Alk_consumed (mg/L) = (NH₄_oxidized (mg/L)) × 7.14
Alk_consumed (mg/L) = (30 - 3) × 7.14 = 192.8 mg/LDenitrification Recovery (if applicable)
Formula:
Alk_recovered = NO₃_denitrified × 3.57Example (with denitrification step):
NO₃_produced = 27 kgN/d (from nitrification)
NO₃_denitrified = 20 kgN/d (in anoxic zone)
Alk_recovered = 20 × 3.57 = 71.4 kg CaCO₃/dNet alkalinity:
Net_consumption = Nitrification - Denitrification
Net_consumption = 192.8 - 71.4 = 121.4 kg CaCO₃/dChemical Dosing Consumption
Ferric Sulphate
Formula:
Alk_consumed = Fe_dose × 0.75Example:
Fe_dose = 20 kg Fe/d (for P removal)
Alk_consumed = 20 × 0.75 = 15 kg CaCO₃/dAluminum Sulphate
Formula:
Alk_consumed = Al_dose × 0.50Total Alkalinity Balance
Complete formula:
Alk_final = Alk_influent - Alk_nitrification + Alk_denitrification - Alk_chemicalIn concentration terms:
C_alk_eff (mg/L) = C_alk_inf (mg/L) - Total_consumption (mg/L)
where:
Total_consumption = (Total_consumption_kg/d × 1000) / Q (m³/d)Minimum Effluent Alkalinity
Design Criterion
Minimum effluent alkalinity: 50 mg/L as CaCO₃
Rationale:
- Buffer capacity for pH stability (6.5-8.5 range)
- Nitrification activity inhibited below pH 6.5
- Regulatory compliance (many permits specify minimum alkalinity)
If effluent alkalinity < 50 mg/L: Supplementation required
Alkalinity Supplementation
Sodium Bicarbonate Dosing
Most common supplementation chemical: NaHCO₃ (sodium bicarbonate, baking soda)
Formula:
NaHCO₃_dose = Alk_deficit / 0.617Where:
NaHCO₃_dose= sodium bicarbonate required (kg/d)Alk_deficit= alkalinity shortfall (kg CaCO₃/d)0.617= conversion factor (kg CaCO₃ equivalent per kg NaHCO₃)
Derivation:
Molecular weight NaHCO₃ = 84 g/mol
Molecular weight CaCO₃ = 100 g/mol
Alkalinity per mole: NaHCO₃ provides 1 eq, CaCO₃ provides 2 eq
Effective ratio: (100/84) × 0.5 ≈ 0.595 (use 0.617 to account for practical dosing efficiency)Example:
Alk_deficit = 50 kg CaCO₃/d (to reach 50 mg/L minimum)
NaHCO₃_dose = 50 / 0.617 = 81.0 kg/dStorage Requirements
UK operator standard: 28 days minimum
Formula:
Storage_kg = NaHCO₃_dose × 28
Storage_volume = Storage_kg / Bulk_densityWhere:
Bulk_density= 1,200 kg/m³ (powder), 1,100 kg/m³ (typical packed)
Example:
NaHCO₃_dose = 81 kg/d
Storage = 81 × 28 = 2,268 kg
Volume = 2,268 / 1,100 = 2.06 m³ (hopper capacity)Alternative Supplementation Chemicals
| Chemical | Formula | Alkalinity Factor | Relative Cost | Notes |
|---|---|---|---|---|
| Sodium bicarbonate | NaHCO₃ | 0.617 kg CaCO₃/kg | 1.0× | Most common, safe, easy handling |
| Soda ash | Na₂CO₃ | 0.945 kg CaCO₃/kg | 0.8× | More alkalinity per kg, but caustic |
| Caustic soda | NaOH | 1.25 kg CaCO₃/kg | 0.6× | Highest alkalinity, very caustic |
| Lime | CaO | 1.79 kg CaCO₃/kg | 0.3× | Cheapest, but slurry handling required |
| Hydrated lime | Ca(OH)₂ | 1.35 kg CaCO₃/kg | 0.4× | Slurry dosing, settles in tanks |
Selection criteria:
- NaHCO₃: Preferred for small-medium works, easy dry feeder
- Caustic (NaOH): Large works, liquid dosing infrastructure available
- Lime: Very large works, cost-sensitive, slurry handling acceptable
Worked Example - Complete Alkalinity Balance
Design Basis
- Population: 10,000 PE
- DWF: 1,200 m³/d
- Influent characteristics:
- NH₄-N: 40 mg/L
- Alkalinity: 200 mg/L as CaCO₃
- Target effluent: NH₄-N ≤ 3 mg/L
- Chemical dosing: Fe = 30 kg/d for P removal
- No denitrification (nitrification only)
Step 1: Calculate Nitrification Load
NH₄-N oxidized:
NH₄_oxidized = (40 - 3) = 37 mg/L
NH₄_load = (37 mg/L × 1200 m³/d) / 1000 = 44.4 kgN/dStep 2: Calculate Alkalinity Consumption from Nitrification
Consumption:
Alk_nitrification = 44.4 × 7.14 = 317.0 kg CaCO₃/d
Alk_nitrification (mg/L) = 37 × 7.14 = 264.2 mg/LStep 3: Calculate Alkalinity Consumption from Chemical Dosing
Ferric sulphate:
Alk_chemical = 30 × 0.75 = 22.5 kg CaCO₃/d
Alk_chemical (mg/L) = (22.5 × 1000) / 1200 = 18.8 mg/LStep 4: Calculate Total Consumption
Total:
Total_consumption = 317.0 + 22.5 = 339.5 kg CaCO₃/d
Total_consumption (mg/L) = 264.2 + 18.8 = 283.0 mg/LStep 5: Calculate Final Effluent Alkalinity
Effluent:
Alk_effluent = Alk_influent - Total_consumption
Alk_effluent = 200 - 283 = -83 mg/L (DEFICIT!)This negative result indicates insufficient alkalinity. Supplementation is required.
Step 6: Calculate Supplementation Requirement
Deficit to reach minimum 50 mg/L:
Alk_deficit (mg/L) = 50 - (-83) = 133 mg/L
Alk_deficit (kg/d) = (133 mg/L × 1200 m³/d) / 1000 = 159.6 kg CaCO₃/dNaHCO₃ required:
NaHCO₃_dose = 159.6 / 0.617 = 258.7 kg/dStep 7: Storage and Dosing
28-day storage:
Storage_mass = 258.7 × 28 = 7,244 kg
Storage_volume = 7,244 / 1,100 = 6.59 m³
Select: 7.0 m³ hopper (with 6% margin)Dosing rate (if dissolved): Typical NaHCO₃ solution: 10-20% concentration (100-200 g/L)
At 15% (150 g/L = 0.15 kg/L):
Solution_volume = 258.7 / 0.15 = 1,725 L/d = 71.9 L/hDry feeder alternative:
Feed_rate = 258.7 kg/d / 24 h = 10.8 kg/hDesign Summary
| Parameter | Value | Notes |
|---|---|---|
| Influent alkalinity | 200 mg/L CaCO₃ | |
| Nitrification consumption | 264.2 mg/L | 44.4 kgN/d oxidized |
| Chemical dosing consumption | 18.8 mg/L | 30 kg Fe/d |
| Total consumption | 283.0 mg/L | |
| Unsupplemented effluent alk | -83 mg/L | Deficit! |
| Supplementation required | 159.6 kg CaCO₃/d | To reach 50 mg/L |
| NaHCO₃ dose | 258.7 kg/d | Sodium bicarbonate |
| Storage | 7.0 m³ | 28-day supply |
| Dosing rate (15% solution) | 71.9 L/h | If liquid dosing |
| Dosing rate (dry) | 10.8 kg/h | If dry feeder |
| Final effluent alkalinity | 50 mg/L CaCO₃ | ✓ Minimum met |
Example with Denitrification
If the above plant had an anoxic zone achieving 80% denitrification:
NO₃-N produced from nitrification:
NO₃ = 44.4 kgN/d (equals NH₄ oxidized)NO₃-N denitrified (80% removal):
NO₃_denitrified = 44.4 × 0.80 = 35.5 kgN/dAlkalinity recovered:
Alk_recovered = 35.5 × 3.57 = 126.7 kg CaCO₃/d
Alk_recovered (mg/L) = (126.7 × 1000) / 1200 = 105.6 mg/LNet alkalinity consumption:
Net_consumption = Nitrification - Denitrification + Chemical
Net_consumption = 264.2 - 105.6 + 18.8 = 177.4 mg/LEffluent alkalinity:
Alk_effluent = 200 - 177.4 = 22.6 mg/L (still below minimum!)Supplementation still required:
Alk_deficit = 50 - 22.6 = 27.4 mg/L
Alk_deficit (kg/d) = (27.4 × 1200) / 1000 = 32.9 kg CaCO₃/d
NaHCO₃ = 32.9 / 0.617 = 53.3 kg/dBenefit of denitrification: Reduces NaHCO₃ requirement from 258.7 to 53.3 kg/d (79% reduction!)
UK Water Company Practices
UK Industry Practice
- Minimum effluent alkalinity: 50 mg/L (strictly enforced)
- Prefer NaHCO₃ for supplementation
- 28-day chemical storage minimum
- Monthly alkalinity monitoring mandatory
UK Industry Practice
- Minimum effluent alkalinity: 50 mg/L
- Some works use caustic soda (NaOH) for larger sites
- Continuous pH monitoring on larger works (> 10,000 PE)
- Lime dosing common on very large works
UK Industry Practice
- Minimum alkalinity: 50 mg/L CaCO₃
- pH monitoring required (target 6.5-8.0)
- Prefer NaHCO₃ for ease of handling
- Some rural works use hydrated lime slurry
Design Considerations
pH and Alkalinity Relationship
pH depression from nitrification:
Typical influent pH: 7.5-8.0
After nitrification (without supplementation): 6.0-6.5
With supplementation to 50 mg/L alkalinity: 6.8-7.5Critical pH for nitrification:
- Optimum: 7.5-8.5
- Acceptable: 6.5-8.0
- Inhibited: < 6.5 or > 9.0
If pH < 6.5 even with 50 mg/L alkalinity: Additional buffering may be needed (increase target to 75-100 mg/L).
Dosing Point Selection
Before biological treatment (most common):
- Dose into primary effluent or biofilter inlet
- Ensures adequate buffering throughout nitrification
- Prevents pH drop that could inhibit process
After biological treatment (less common):
- Only if supplementation is for compliance, not process requirement
- Risk of pH inhibition in biofilter
Split dosing:
- Part before biofilter, part after
- Optimizes chemical use
- More complex control
Dosing Control Strategies
Flow-proportional (most common):
NaHCO₃_rate = k × QWhere k = dosing constant (kg/m³)
Compound loop (advanced):
- Primary: Flow-proportional
- Trim: pH or alkalinity analyzer feedback
- Adjusts dose ±20% based on effluent measurement
Feed-forward (very advanced):
- Measure influent NH₄-N continuously
- Calculate required dose in real-time
- Adjust for flow and load variations
Monitoring and Compliance
Key Parameters
| Parameter | Frequency | Method | Target |
|---|---|---|---|
| Influent alkalinity | Weekly | Laboratory titration | Baseline |
| Effluent alkalinity | Weekly | Laboratory titration | ≥ 50 mg/L |
| Effluent pH | Daily | Online or grab | 6.5-8.5 |
| NH₄-N removal | Daily | Laboratory | Design efficiency |
| NaHCO₃ stock | Weekly | Level indicator | > 7 days |
Alkalinity Measurement
Standard method: Titration to pH 4.5 endpoint (methyl orange)
Interpretation:
- Total alkalinity = HCO₃⁻ + CO₃²⁻ + OH⁻ (all as mg/L CaCO₃)
- In wastewater (pH 6-8), mainly HCO₃⁻ (bicarbonate)
Online measurement:
- Some larger works have online alkalinity analyzers
- Useful for feed-forward control
- Requires regular calibration and maintenance
Common Issues
Insufficient Alkalinity Despite Supplementation
Symptoms:
- pH dropping below 6.5
- Nitrification performance declining
- Effluent NH₄-N increasing
Causes:
- Under-dosing NaHCO₃ (pump calibration error)
- Stock depletion (ran out of chemical)
- Increased load (higher NH₄-N or trade effluent)
Solutions:
- Verify dosing pump calibration
- Check chemical stock levels
- Increase dose rate
- Confirm influent alkalinity hasn't decreased
Over-Dosing
Symptoms:
- Effluent alkalinity > 150 mg/L
- High chemical consumption
- Wasted cost
Causes:
- Conservative design (over-specified)
- Influent alkalinity higher than design
- Lower NH₄-N load than design
Solutions:
- Reduce dose rate gradually
- Monitor effluent alkalinity weekly
- Target 60-80 mg/L effluent (margin above 50 mg/L)
Variable Alkalinity
Symptoms:
- Fluctuating effluent pH and alkalinity
- Inconsistent nitrification performance
Causes:
- Variable influent load (trade effluent discharges)
- Batch dosing instead of continuous
- Poor mixing of dosed chemical
Solutions:
- Continuous dosing (not batch)
- Flow-proportional control
- Add static mixer at dose point
- Investigate trade effluent contributions
Cost Considerations
Chemical Costs (Typical UK, 2024)
| Chemical | Price (£/tonne) | Delivered (£/tonne) | Relative Cost per kg CaCO₃ |
|---|---|---|---|
| Sodium bicarbonate | £400-500 | £450-550 | 1.0× |
| Caustic soda (50%) | £250-350 | £300-400 | 0.6× |
| Soda ash | £300-400 | £350-450 | 0.8× |
| Hydrated lime | £100-150 | £120-180 | 0.4× |
Example cost calculation:
NaHCO₃_dose = 250 kg/d
Annual_consumption = 250 × 365 = 91,250 kg = 91.25 tonnes
Price = £500/tonne
Annual_cost = 91.25 × £500 = £45,625/yearOptimization Strategies
Denitrification for alkalinity recovery:
- Anoxic zone recovers 3.57 kg CaCO₃/kg NO₃-N
- Can reduce or eliminate need for supplementation
- Requires carbon source (e.g., methanol, glycerol)
Trade-off:
Cost_NaHCO₃ vs Cost_carbon_source + Cost_anoxic_zoneTypically denitrification is cost-effective for:
- NO₃-N removal required anyway (N consent)
- Large works (economies of scale)
- Low-cost carbon available (internal or trade effluent)
Related Calculations
- Biofilters: Nitrification in biofilters producing alkalinity demand
- Chemical Dosing: Alkalinity consumption from Fe/Al dosing
- Flow and Load: NH₄-N load determination
References
- Metcalf & Eddy: Wastewater Engineering, alkalinity and pH control
- WEF Manual of Practice: Biological nutrient removal, alkalinity requirements
- CIWEM Best Practice: Alkalinity management in BNR systems
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