Fired Heater Efficiency

API-560 Heat Loss Method, Measurement & Best Practices

Master the science of thermal efficiency optimization in industrial fired heaters

Table of Contents

What, Why, and How of Fired Heater Efficiency

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What is Efficiency?

Fired heater efficiency measures how effectively fuel energy is converted to useful process heat. Three key metrics: fuel efficiency (commercial), thermal efficiency (holistic), and combustion efficiency (burner performance).

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Why It Matters

Fired heaters are the largest energy consumers in refineries. A 1% efficiency improvement on a large heater can save millions annually while reducing emissions and enhancing safety.

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How to Optimize

Through precise measurement using API-560 standards, minimizing stack losses, reducing excess air, and implementing advanced control systems for real-time optimization.

API-560 in 5 Steps

1 Collect operational data: temperatures, oxygen levels, fuel composition, and humidity under steady-state conditions
2 Complete combustion worksheet using fuel composition to calculate stoichiometric parameters and heat release
3 Calculate excess air from oxygen measurements and determine all sensible heat credits from preheated inputs
4 Quantify heat losses: stack loss (largest), radiation loss, and incomplete combustion losses
5 Apply final efficiency formulas: thermal efficiency and fuel efficiency calculations based on energy balance

Key Energy Losses

Stack Loss (60-85%)

Heat carried away by hot flue gases. Controlled by reducing stack temperature and minimizing excess air.

Setting Loss (1.5-2.5%)

Heat lost through external surfaces via radiation and convection. Indicates refractory condition.

Incomplete Combustion (~0%)

Energy lost due to unburned fuel (CO, hydrocarbons). Should be negligible in well-operated heaters.

Annex G Workflow

Interactive Efficiency Tools

Excess Air vs. Efficiency

Estimated Efficiency: 87.5%
Stack Loss: 12.5%

Stack Temperature Impact

Temperature Loss: 8.2%
Optimal range: 200-320°C

Efficiency Test Checklist

Instrumentation and Measurement

Required Input Parameters

Parameter Symbol Units Measurement Method
Ambient Air Temperature Ta °C / °F Calibrated thermometer, shielded from radiation
Relative Humidity RH % Sling psychrometer or electronic sensor
Flue Gas Exit Temperature Te °C / °F Multi-point traverse or thermocouple grid
Flue Gas Oxygen O₂ vol % Zirconia oxide or electrochemical analyzer
Fuel Composition - vol % / mass % Gas chromatograph analysis
Lower Heating Value LHV kJ/kg Calculated from composition or calorimetry

✅ Best Practices

  • • Place probes downstream of final heat transfer surface
  • • Sample in central third of duct cross-section
  • • Use EPA Method 1 for large duct traverses
  • • Co-locate O₂ and temperature sensors
  • • Calibrate instruments before each test
  • • Seal all test ports during measurement

❌ Common Errors

  • • Sampling upstream of air leaks (tramp air)
  • • Single-point measurement in stratified flow
  • • Uncalibrated or drifting instruments
  • • Non-representative fuel samples
  • • Ignoring humidity in air calculations
  • • Operating during transient conditions

Complex Heater Configurations

Multi-Cell with Common Convection

Cell A Cell B Common Convection Stack

Multiple radiant cells sharing a common convection section. Overall efficiency calculated from single stack measurement, but cell-specific monitoring required for control.

Key Challenge: Individual cell performance masked in overall measurement

Independent Heaters, Common Stack

Heater 1 Heater 2 Common Stack O₂ O₂

Independent heaters with separate process services sharing a common stack. Each heater requires individual flue gas measurement for meaningful performance monitoring.

Key Requirement: Individual O₂ and temperature measurement before gas streams combine

⚠️ Measurement Strategy

For complex configurations, the "black box" API-560 approach is insufficient for diagnostics and control. Use process simulators (Aspen HYSYS) or CFD (OpenFOAM) for detailed analysis of internal behavior and optimization opportunities.

Example Calculations & Sensitivity Analysis

API-560 Combustion Worksheet (Sample)

Component Vol % Mol. Wt. Mass Fraction LHV (kJ/kg) LHV Contrib. Stoich. Air
CH₄ 92.5 16.04 0.8534 50,016 42,689 14.65
C₂H₆ 5.0 30.07 0.0863 47,490 4,098 1.38
N₂ 1.5 28.01 0.0241 0 0 0
CO₂ 1.0 44.01 0.0362 0 0 0
Total 100.0 - 1.000 - 46,787 16.03

Sensitivity Analysis: Stack Temperature vs. Efficiency

This chart shows how efficiency decreases with increasing stack temperature. A 50°C increase from 300°C to 350°C typically reduces efficiency by 2-3 percentage points.

Tools & Downloads

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Excel Template

API-560 Annex G calculation spreadsheet with built-in formulas and validation.

Download
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Python Model

Open-source Python model for automated efficiency calculations and sensitivity analysis.

GitHub Repo
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Web Calculator

Interactive web-based calculator for efficiency estimates and excess air calculations.

Open Calculator

Software Comparison Matrix

Tool Cost Expertise Accuracy Best For
Excel Spreadsheet Low Medium High API-560 calculations, custom reporting
HeaterSIM High High Very High Detailed design, thermal modeling
Aspen HYSYS Very High High High Plant-wide simulation, integration
Python/MATLAB Low High High Automation, sensitivity analysis
Online Calculators Free Low Low Quick estimates, education

Frequently Asked Questions

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