Inflection Point Engineering Fired Heaters Design Guide

Efficiency

Chapter from the Fired Heaters Design Guide.

HEATER EFFICIENCY CALCULATION

Efficiency Calculation Methods

DIRECT METHOD (Input-Output):
η = Q_absorbed / Q_fired × 100%
• Q_absorbed = process duty (BTU/hr) from heat balance
• Q_fired = fuel flow × NHV (or LHV)
• Simple but requires accurate fuel flow measurement

INDIRECT METHOD (Heat Loss — preferred for field evaluation):
η = 100% - ΣLosses
Losses include:
• Stack loss (largest): sensible heat in flue gas above ambient
• Radiation & convection loss from casing (1-3% typical)
• Unaccounted losses (0.5-1%)

Stack Loss Calculation:
Q_stack = m_flue × Cp × (T_stack - T_ambient)
• m_flue from combustion stoichiometry (fuel composition + excess air)
• Cp of flue gas ≈ 0.25-0.27 BTU/lb·°F
• T_stack from stack thermocouple

Efficiency Improvement Opportunities

Opportunity Typical Savings Implementation Risk/Limitation Payback
Reduce excess air 1-2% per 5% excess air reduction Burner tuning, O2 trim control CO formation if too low Immediate (operational)
Add convection surface (APH) 5-10% efficiency gain Air preheater installation Acid dew point corrosion, cost 1-3 years
Install economizer 3-5% efficiency gain Water/oil preheating coil Flue gas ΔP, acid dew point 1-3 years
Repair/replace insulation 0.5-2% per heater Refractory and casing repair Access during turnaround <1 year
Optimize draft 0.5-1% Stack damper adjustment Flame instability if too low Immediate
Combustion air preheat 1% per 40°F air preheat Recover stack heat to combustion air Burner design must accommodate 2-4 years

Source: Fired_Heaters_Design_Guide_v1.xlsx · sheet “Efficiency”