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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 ​

MetricUnitCalculation
Energy consumptionkWh/MLTotal electrical demand
Energy productionkWh/MLCHP generation
Net energykWh/MLProduction - consumption
Self-sufficiency%Production / consumption × 100
Carbon creditkg CO2eExported × 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 ​

TechnologyElectrical ηThermal ηTotal ηSize Range
IC engine35-42%40-50%80-90%50 kW - 5 MW
Gas turbine25-32%50-55%80-85%500 kW - 50 MW
Microturbine25-30%50-55%80-85%30-250 kW
Fuel cell (MCFC)45-55%25-35%75-85%250 kW - 3 MW
Stirling engine25-30%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 FactorRelative η
100%100%
75%97%
50%88%
25%71%

Typical IC Engine Specifications ​

ParameterValue
Electrical efficiency38-42%
Thermal efficiency43-47%
Maintenance interval2,000 hours
Major overhaul60,000 hours
Oil consumption0.3 g/kWh
Availability90-95%

Biogas Fuel Requirements ​

ParameterIC EngineMicroturbineFuel Cell
CH4 minimum40%35%40%
H2S maximum500 ppm200 ppm1 ppm
Siloxanes max10 mg/m³0.1 mg/m³0.01 mg/m³
Moisture<80% RH<60% RH<5% RH
Pressure50-200 mbar200-500 mbar5-50 mbar

Thermal Recovery ​

Heat Sources ​

SourceTemperatureRecovery Potential
Engine jacket85-95°C25-30% of fuel
Exhaust gas400-500°C15-20% of fuel
Oil cooler70-80°C3-5% of fuel
Charge air40-60°C2-3% of fuel

Heat Utilization ​

ApplicationTemperature RequiredPriority
Digester heating35-55°CHigh
Building heating40-70°CMedium
Sludge drying80-120°CMedium
Hot water60-80°CLow
Absorption chiller85-100°CLow

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/d

CHP outputs:

E_electrical = 6,163 × 0.40 = 2,465 kWh/d
E_thermal = 6,163 × 0.45 = 2,773 kWh/d

Thermal balance:

Available: 2,773 kWh/d
Required for digester: 800 kWh/d
Surplus heat: 1,973 kWh/d

Energy Self-Sufficiency ​

Calculation ​

$$Self\text{-}Sufficiency = \frac{E_{generated}}{E_{consumed}} \times 100%$$

Benchmark by Plant Type ​

Plant ConfigurationTypical Self-Sufficiency
Conventional AS (no AD)0%
AS + Primary sludge digestion30-50%
AS + Full sludge digestion50-70%
BNR + Digestion40-60%
A-stage + B-stage + Digestion70-100%
Co-digestion80-150%
Advanced recovery100-200%

Energy-Positive Examples ​

FeatureImpact 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 ​

FactorValue
Feed-in tariff£50-100/MWh
ROCs/REGO£5-20/MWh
Avoided importGrid price
Network charges-£5-15/MWh

Grid Connection Options ​

TypeCapacityVoltage
LV connection<100 kW400V
HV connection100 kW - 1 MW11 kV
Grid connection>1 MW33 kV

Alternative Energy Uses ​

Biomethane Upgrade ​

Convert biogas to grid-quality biomethane:

ParameterRaw BiogasBiomethane
CH455-70%>97%
CO230-45%❤️%
H2S100-10,000 ppm<4 ppm
Energy density6 kWh/m³10 kWh/m³

Upgrade technologies:

  • Water scrubbing (95-98%)
  • Chemical scrubbing (99%)
  • PSA (97-99%)
  • Membrane separation (95-99%)
  • Cryogenic (99%+)

Vehicle Fuel ​

ApplicationFuel QualityInfrastructure
Municipal fleetBiomethaneFueling station
Collection vehiclesCNG/biomethaneSlow fill overnight
Public transportBiomethaneFast fill

Thermal-Only Use ​

Where CHP not viable:

OptionEfficiencyApplication
Boiler85-95%Direct heat
Absorption chillerCOP 0.7Cooling
ORC10-15% electricalLow-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 ​

MetricUnitTarget
Specific energy consumptionkWh/m³<0.4
Self-sufficiency%>70%
CHP availability%>90%
Heat utilization%>80%
Carbon intensitykg CO2e/m³<0.3

Monitoring Dashboard ​

ParameterFrequencyPurpose
Biogas flowContinuousYield tracking
CH4 contentDailyEnergy content
CHP outputContinuousPerformance
Heat demandContinuousBalance
Grid import/export15-minCost/credit

Optimization Strategies ​

Maximize Generation ​

StrategyBenefit
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 ​

StrategySavings
ABAC aeration control20-30% aeration
VFD on all motors15-25% pumping
LED lighting50-80% lighting
Heat recovery10-20% heating
Process optimization10-15% overall

Troubleshooting ​

IssueCauseSolution
Low CHP outputLow biogas qualityCheck H2S, moisture
Poor heat utilizationMismatched supply/demandHeat storage, scheduling
High importLow biogas yieldReview AD performance
Export curtailmentGrid constraintsStorage, load shifting
DeratingHigh ambient tempCooling, capacity planning

References ​

  1. UKWIR (2019). Energy Optimization in Water Utilities
  2. WEF (2017). Energy Production and Efficiency Research Foundation
  3. IEA Bioenergy (2020). Biogas Country Report Summary
  4. US EPA (2021). Combined Heat and Power Partnership
  5. CIBSE (2012). CHP for Buildings