1. Blending Principles
Air-gas blending combines air with fuel gas to achieve specific mixture properties for combustion control, flammability management, or dilution purposes.
Fundamental Concepts
- Volumetric blending: Gas volumes add linearly at constant T and P
- Partial pressures: Each component contributes pressure proportional to its mole fraction (Dalton's Law)
- Mass conservation: Total mass = sum of component masses
Design objective
Match burner WI
Blend air to bring rich fuel back inside the burner's ±5% Wobbe band.
Control handles
Air & fuel valves
Pair ratio control with outlet analyzer feedback (WI or O₂ trim) for drift-free operation.
Field check
Velocity > flame speed
Keep mixer velocity above flame speed to avoid flashback when blending near LEL.
2. Mixture Properties
Mixture properties are calculated using mole-weighted averages assuming ideal gas behavior.
| Property | Calculation | Units |
|---|---|---|
| Molecular Weight | MWmix = Σ(yi × MWi) | lb/lbmol |
| Specific Gravity | SGmix = MWmix / 28.97 | dimensionless |
| Density | ρ = (P × MW) / (R × T) | lb/ft³ |
| Heating Value | HHVmix = Σ(yi × HHVi) | BTU/scf |
| Wobbe Index | WI = HHV / √SG | BTU/scf |
Ideal gas check
Z ≈ 1
Acceptable for low/medium pressure pipeline gas; add EOS correction for HP blends.
Analyzer drift
±1–2%
Validate WI or O₂ analyzers with bottle gas before tight combustion tuning.
Blend stability
Static mixer
Short pipe section with static mixer minimizes stratification before analyzer.
3. Combustion Requirements
Complete combustion requires correct air-fuel ratio. Too little air = CO formation and soot; too much air = efficiency loss.
Stoichiometric Air Requirement
For methane (primary component of natural gas):
| Component | Stoich. Air (scf/scf) | HHV (BTU/scf) |
|---|---|---|
| Methane (CH₄) | 9.52 | 1,012 |
| Ethane (C₂H₆) | 16.68 | 1,773 |
| Propane (C₃H₈) | 23.82 | 2,516 |
| Hydrogen (H₂) | 2.39 | 325 |
Excess Air
- 0% excess: Stoichiometric (theoretical minimum)
- 10–20% excess: Typical industrial burners
- 30–50% excess: Conservative design for variable fuel composition
Set stoichiometric base. Calibrate fuel composition, set initial air based on stoich + desired excess.
Use analyzer feedback. Tie O₂ or WI analyzer to air-valve trim; bias for stable flame over peak efficiency.
Check emissions + stack temp. Confirm CO/NOx and stack losses at low/high loads; lock in alarm limits.
4. Applications
Common Uses
- Burner control: Adjusting air-fuel ratio for efficient combustion
- Flare systems: Ensuring proper combustion at varying flow rates
- Inerting: Diluting flammable gas below LEL for safe tank entry
- Fuel gas conditioning: Adjusting heating value or Wobbe Index
- Pilot gas: Creating stable ignition source mixtures
Wobbe Index Adjustment
When fuel gas composition varies, air blending adjusts the Wobbe Index to maintain consistent burner performance:
5. Safety Considerations
Flammability Limits
Natural gas flammability in air:
- LEL (Lower Explosive Limit): ~5% gas in air
- UEL (Upper Explosive Limit): ~15% gas in air
Too lean
<5% gasSafe for entry/inerting; verify with gas detector.
Flammable
5–15% gasAvoid operation unless system is engineered for ignition control.
Too rich
>15% gasAbove UEL but still treat as hazardous; watch for air ingress.
⚠ Safe operation: Keep mixture below 50% LEL (2.5% gas) OR above UEL with controlled ignition. Never operate in flammable range without proper controls.
Operational Hazards & Mitigation
| Hazard | Mitigation |
|---|---|
| Flashback | Flame arrestors, maintain flow velocity > flame speed |
| Incomplete combustion | CO monitoring, maintain excess air, burner maintenance |
| Mixture variation | Continuous composition monitoring, automatic ratio control |
| Static ignition | Grounding/bonding, humidity control, flow velocity limits |
References
- NFPA 86 – Standard for Ovens and Furnaces
- API 537 – Flare Details for Refinery and Petrochemical Service
- GPSA, Section 22 (Combustion)
- API 2000 – Venting Atmospheric and Low-Pressure Storage Tanks
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