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 Β±5% Wobbe band.
Control handles
Air & fuel valves
Pair ratio control with outlet analyzer feedback (WI or Oβ 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 = Ξ£(yi Γ MWi) | lb/lbmol |
| Specific Gravity | SGmix = MWmix / 28.97 | dimensionless |
| Density | Ο = (P Γ MW) / (R Γ T) | lb/ftΒ³ |
| Heating Value | HHVmix = Ξ£(yi Γ HHVi) | BTU/scf |
| Wobbe Index | WI = HHV / βSG | BTU/scf |
Ideal gas check
Z β 1
Acceptable for low/medium pressure pipeline gas; add EOS correction for HP blends.
Analyzer drift
Β±1β2%
Validate WI or Oβ 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 (CHβ) | 9.52 | 1,012 |
| Ethane (CβHβ) | 16.68 | 1,773 |
| Propane (CβHβ) | 23.82 | 2,516 |
| Hydrogen (Hβ) | 2.39 | 325 |
Excess Air
- 0% excess: Stoichiometric (theoretical minimum)
- 10β20% excess: Typical industrial burners
- 30β50% 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 Oβ 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
5β15% gasAvoid operation unless system is engineered for ignition control.
Too rich
>15% gasAbove UEL but still treat as hazardous; watch for air ingress.
β 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 β Standard for Ovens and Furnaces
- API 537 β Flare Details for Refinery and Petrochemical Service
- GPSA, Section 22 (Combustion)
- API 2000 β Venting Atmospheric and Low-Pressure Storage Tanks
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