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Energy Recovery
Biogas utilization, CHP systems, thermal recovery, and energy self-sufficiency for wastewater treatment
Overview
Energy recovery from biogas represents the primary pathway to achieving energy-positive wastewater treatment. ErgoPlanner models complete energy balances including CHP electrical and thermal efficiency, parasitic loads, and grid export potential.
Energy Balance Framework
Plant Energy Flow
INPUTS OUTPUTS
────── ───────
┌─────────────────┐
│ BIOGAS │
│ Energy Content │──────────────┐
└─────────────────┘ │
▼
┌─────────────────┐ ┌──────────────────┐
│ GRID │ │ CHP │
│ Electricity │──────│ Generator │
└─────────────────┘ └────────┬─────────┘
│ │
│ ┌────┴────┐
▼ ▼ ▼
┌─────────────────┐ ┌──────────┐ ┌──────────┐
│ TREATMENT │ │ ELECTRIC │ │ THERMAL │
│ PROCESS │◄──│ OUTPUT │ │ OUTPUT │
└─────────────────┘ └──────────┘ └──────────┘Energy Metrics
| Metric | Unit | Calculation |
|---|---|---|
| Energy consumption | kWh/ML | Total electrical demand |
| Energy production | kWh/ML | CHP generation |
| Net energy | kWh/ML | Production - consumption |
| Self-sufficiency | % | Production / consumption × 100 |
| Carbon credit | kg CO2e | Exported × grid factor |
CHP Systems
Combined Heat and Power
CHP converts biogas to both electricity and useful heat:
$$E_{total} = Q_{biogas} \times %CH_4 \times LHV_{CH4}$$
$$E_{electrical} = E_{total} \times \eta_{electrical}$$
$$E_{thermal} = E_{total} \times \eta_{thermal}$$
Where:
- LHV_CH4 = 35.8 MJ/Nm³ = 9.94 kWh/Nm³
- eta_electrical = Electrical efficiency (30-42%)
- eta_thermal = Thermal efficiency (40-50%)
CHP Technology Comparison
| Technology | Electrical η | Thermal η | Total η | Size Range |
|---|---|---|---|---|
| IC engine | 35-42% | 40-50% | 80-90% | 50 kW - 5 MW |
| Gas turbine | 25-32% | 50-55% | 80-85% | 500 kW - 50 MW |
| Microturbine | 25-30% | 50-55% | 80-85% | 30-250 kW |
| Fuel cell (MCFC) | 45-55% | 25-35% | 75-85% | 250 kW - 3 MW |
| Stirling engine | 25-30% | 50-55% | 80% | 1-100 kW |
IC Engine Performance
Electrical Efficiency Curve
$$\eta_e(load) = \eta_{max} \times \left(1 - k \times (1 - load)^2\right)$$
Where k ≈ 0.15
| Load Factor | Relative η |
|---|---|
| 100% | 100% |
| 75% | 97% |
| 50% | 88% |
| 25% | 71% |
Typical IC Engine Specifications
| Parameter | Value |
|---|---|
| Electrical efficiency | 38-42% |
| Thermal efficiency | 43-47% |
| Maintenance interval | 2,000 hours |
| Major overhaul | 60,000 hours |
| Oil consumption | 0.3 g/kWh |
| Availability | 90-95% |
Biogas Fuel Requirements
| Parameter | IC Engine | Microturbine | Fuel Cell |
|---|---|---|---|
| CH4 minimum | 40% | 35% | 40% |
| H2S maximum | 500 ppm | 200 ppm | 1 ppm |
| Siloxanes max | 10 mg/m³ | 0.1 mg/m³ | 0.01 mg/m³ |
| Moisture | <80% RH | <60% RH | <5% RH |
| Pressure | 50-200 mbar | 200-500 mbar | 5-50 mbar |
Thermal Recovery
Heat Sources
| Source | Temperature | Recovery Potential |
|---|---|---|
| Engine jacket | 85-95°C | 25-30% of fuel |
| Exhaust gas | 400-500°C | 15-20% of fuel |
| Oil cooler | 70-80°C | 3-5% of fuel |
| Charge air | 40-60°C | 2-3% of fuel |
Heat Utilization
| Application | Temperature Required | Priority |
|---|---|---|
| Digester heating | 35-55°C | High |
| Building heating | 40-70°C | Medium |
| Sludge drying | 80-120°C | Medium |
| Hot water | 60-80°C | Low |
| Absorption chiller | 85-100°C | Low |
Digester Heating Demand
$$Q_{heating} = Q_{feed} \times \rho \times C_p \times (T_{dig} - T_{feed}) + Q_{losses}$$
Where:
- Q_feed = Feed flow (m³/d)
- rho = Density ≈ 1020 kg/m³
- Cp = Specific heat ≈ 4.18 kJ/kg·K
- T_dig = Digester temperature (35 or 55°C)
- Q_losses = Heat losses through walls
Typical demand: 40-60 kWh/m³ sludge (mesophilic)
Heat Balance Example
Given:
- Biogas production: 1,000 Nm³/d @ 62% CH4
- CHP: 500 kWe, η_e = 40%, η_th = 45%
- Digester heating: 800 kWh/d
Calculation:
Energy input:
E_input = 1000 × 0.62 × 9.94 = 6,163 kWh/dCHP outputs:
E_electrical = 6,163 × 0.40 = 2,465 kWh/d
E_thermal = 6,163 × 0.45 = 2,773 kWh/dThermal balance:
Available: 2,773 kWh/d
Required for digester: 800 kWh/d
Surplus heat: 1,973 kWh/dEnergy Self-Sufficiency
Calculation
$$Self\text{-}Sufficiency = \frac{E_{generated}}{E_{consumed}} \times 100%$$
Benchmark by Plant Type
| Plant Configuration | Typical Self-Sufficiency |
|---|---|
| Conventional AS (no AD) | 0% |
| AS + Primary sludge digestion | 30-50% |
| AS + Full sludge digestion | 50-70% |
| BNR + Digestion | 40-60% |
| A-stage + B-stage + Digestion | 70-100% |
| Co-digestion | 80-150% |
| Advanced recovery | 100-200% |
Energy-Positive Examples
| Feature | Impact on Balance |
|---|---|
| Co-digestion (FOG, food waste) | +30-100% biogas |
| Thermal hydrolysis | +15-25% biogas |
| A-stage carbon capture | +20-40% net |
| Membrane aeration | -30% consumption |
| Anammox (sidestream) | -20% aeration |
Grid Export
Carbon Credit Calculation
$$Credit_{CO2} = E_{export} \times EF_{grid}$$
Where:
- E_export = Exported electricity (kWh)
- EF_grid = Grid carbon intensity (kg CO2/kWh)
Export Economics
| Factor | Value |
|---|---|
| Feed-in tariff | £50-100/MWh |
| ROCs/REGO | £5-20/MWh |
| Avoided import | Grid price |
| Network charges | -£5-15/MWh |
Grid Connection Options
| Type | Capacity | Voltage |
|---|---|---|
| LV connection | <100 kW | 400V |
| HV connection | 100 kW - 1 MW | 11 kV |
| Grid connection | >1 MW | 33 kV |
Alternative Energy Uses
Biomethane Upgrade
Convert biogas to grid-quality biomethane:
| Parameter | Raw Biogas | Biomethane |
|---|---|---|
| CH4 | 55-70% | >97% |
| CO2 | 30-45% | ❤️% |
| H2S | 100-10,000 ppm | <4 ppm |
| Energy density | 6 kWh/m³ | 10 kWh/m³ |
Upgrade technologies:
- Water scrubbing (95-98%)
- Chemical scrubbing (99%)
- PSA (97-99%)
- Membrane separation (95-99%)
- Cryogenic (99%+)
Vehicle Fuel
| Application | Fuel Quality | Infrastructure |
|---|---|---|
| Municipal fleet | Biomethane | Fueling station |
| Collection vehicles | CNG/biomethane | Slow fill overnight |
| Public transport | Biomethane | Fast fill |
Thermal-Only Use
Where CHP not viable:
| Option | Efficiency | Application |
|---|---|---|
| Boiler | 85-95% | Direct heat |
| Absorption chiller | COP 0.7 | Cooling |
| ORC | 10-15% electrical | Low-grade heat |
Configuration
Example Configuration
json
{
"energyRecovery": {
"chp": {
"technology": "ic_engine",
"capacity": 500,
"electricalEfficiency": 0.40,
"thermalEfficiency": 0.45,
"availability": 0.92,
"minimumLoad": 0.50
},
"thermal": {
"digesterHeating": true,
"buildingHeating": true,
"heatExport": false,
"absorptionChiller": false
},
"grid": {
"exportEnabled": true,
"importTariff": 150,
"exportTariff": 80,
"gridCarbonFactor": 0.21
},
"alternativeUse": {
"biomethaneUpgrade": false,
"vehicleFuel": false,
"boilerBackup": true
}
}
}Performance Indicators
Key Metrics
| Metric | Unit | Target |
|---|---|---|
| Specific energy consumption | kWh/m³ | <0.4 |
| Self-sufficiency | % | >70% |
| CHP availability | % | >90% |
| Heat utilization | % | >80% |
| Carbon intensity | kg CO2e/m³ | <0.3 |
Monitoring Dashboard
| Parameter | Frequency | Purpose |
|---|---|---|
| Biogas flow | Continuous | Yield tracking |
| CH4 content | Daily | Energy content |
| CHP output | Continuous | Performance |
| Heat demand | Continuous | Balance |
| Grid import/export | 15-min | Cost/credit |
Optimization Strategies
Maximize Generation
| Strategy | Benefit |
|---|---|
| Co-digestion | +30-100% biogas |
| THP pretreatment | +15-25% yield |
| Two-stage digestion | +10-15% VS destruction |
| Temperature optimization | +5-10% kinetics |
| Mixing optimization | +5% gas release |
Minimize Consumption
| Strategy | Savings |
|---|---|
| ABAC aeration control | 20-30% aeration |
| VFD on all motors | 15-25% pumping |
| LED lighting | 50-80% lighting |
| Heat recovery | 10-20% heating |
| Process optimization | 10-15% overall |
Troubleshooting
| Issue | Cause | Solution |
|---|---|---|
| Low CHP output | Low biogas quality | Check H2S, moisture |
| Poor heat utilization | Mismatched supply/demand | Heat storage, scheduling |
| High import | Low biogas yield | Review AD performance |
| Export curtailment | Grid constraints | Storage, load shifting |
| Derating | High ambient temp | Cooling, capacity planning |
Related Topics
References
- UKWIR (2019). Energy Optimization in Water Utilities
- WEF (2017). Energy Production and Efficiency Research Foundation
- IEA Bioenergy (2020). Biogas Country Report Summary
- US EPA (2021). Combined Heat and Power Partnership
- CIBSE (2012). CHP for Buildings