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Combustion of Fuels — Heating Values and Stoichiometry

Higher and lower heating values of common fuels, combustion stoichiometry, and air-fuel ratios.

combustionfuelsheatingvalues

Overview

The heating value (calorific value) of a fuel quantifies the energy released per unit mass during complete combustion. Two standard measures exist:

  • Higher Heating Value (HHV) — also called gross calorific value, includes the latent heat recovered by condensing water vapor in the combustion products back to liquid.
  • Lower Heating Value (LHV) — also called net calorific value, assumes water remains as vapor in the exhaust; this is the more relevant figure for most real-world combustion equipment.

The difference between HHV and LHV depends on the hydrogen content of the fuel, since hydrogen combustion produces water. Fuels rich in hydrogen (such as natural gas) show the largest gap between HHV and LHV.

Key Formulas

The relationship between higher and lower heating values for a hydrocarbon fuel can be estimated from the mass fraction of hydrogen:

LHV=HHVhfg×9wH100LHV = HHV - h_{fg} \times \frac{9 \, w_H}{100}

where hfgh_{fg} is the latent heat of vaporization of water at 25 °C (approximately 2.442 MJ/kg), wHw_H is the mass percentage of hydrogen in the fuel, and the factor 9 comes from the stoichiometric ratio of water produced per unit mass of hydrogen burned.

Variables

SymbolDescriptionTypical Unit
HHVHigher (gross) heating valueMJ/kg
LHVLower (net) heating valueMJ/kg
hfgh_{fg}Latent heat of vaporization of water at reference temperatureMJ/kg
wHw_HMass fraction of hydrogen in fuel%

Fuel Heating Values

12 rows
Higher and lower heating values of common fuels at 25 °C reference temperature
Fuel
HHV(MJ/kg)
LHV(MJ/kg)
State
Hydrogen141.8120Gas
Methane (natural gas)55.550Gas
Propane50.346.4Gas / Liquid
Butane49.545.7Gas / Liquid
Gasoline46.443.4Liquid
Kerosene46.243Liquid
Diesel45.642.5Liquid
Fuel oil (heavy)42.539.5Liquid
Ethanol29.726.8Liquid
Coal (anthracite)32.531.5Solid
Coal (bituminous)3028Solid
Wood (dry)2018Solid

Source: engineeringtoolbox.com

HHV Comparison

Higher and Lower Heating Values by Fuel

Restored Original Source Tables

The following tables are restored from the original source page to preserve the complete reference data.

Gaseous Fuels - Higher and lower calorific values (heating values)

6 rows
Gaseous Fuels - Higher and lower calorific values (heating values)
Gaseous Fuel
kg/m3(kg/m3)
g/ft3(g/ft3)
kWh/kg(kWh/kg)
MJ/kg(MJ/kg)
Btu/lb(Btu/lb)
MJ/m3(MJ/m3)
Btu/ft3(Btu/ft3)
kWh/kg(kWh/kg)
MJ/kg(MJ/kg)
Btu/lb(Btu/lb)
MJ/m3(MJ/m3)
Btu/ft3(Btu/ft3)
Acetylene1.09731.113.949.92145354.71468
Ammonia22.59690
Hydrogen0.092.5539.4141.76092012.734133.31205159110.8290
Methane0.71620.315.455.52387439.8106913.9502149635.8964
Natural gas (US market)*0.7772214.552.22244640.6109013.147.12026236.6983
Town gas18483

Source: engineeringtoolbox.com

Liquid Fuels - Higher and lower calorific values (heating values)

28 rows
Liquid Fuels - Higher and lower calorific values (heating values)
Liquid Fuel
kg/l(kg/l)
kg/gal(kg/gal)
kWh/kg(kWh/kg)
MJ/kg(MJ/kg)
Btu/lb(Btu/lb)
MJ/l(MJ/l)
Btu/gal(Btu/gal)
kWh/kg(kWh/kg)
MJ/kg(MJ/kg)
Btu/lb(Btu/lb)
MJ/l(MJ/l)
Btu/gal(Btu/gal)
Acetone0.7872.9798.8331.81367125897928.2229.61272623.383580
Butane0.6013.06513.6449.12110929.510587512.5845.31947527.297681
Butanol0.8110.3637.31603630.21083599.5634.41478927.999934
Diesel fuel*0.8463.20212.6745.61960438.613841211.8342.61831536129306
Dimethyl ether (DME)0.6652.5188.8131.71362921.1756558.0328.91242519.268973
Ethane0.5722.16514.4251.92231329.710651313.2847.82055027.398098
Ethanol (100%)0.7892.9878.2529.71276923.4840767.4226.71147921.175583
Diethyl ether (ether)0.7162.7111.94431848730.8110464
Gasoline (petrol)*0.7372.7912.8946.41994834.212269412.0643.41865932114761
Gas oil (heating oil)*0.843.1811.95431849536.112965411.8942.81840136128991
Glycerin1.2634.7815.281981692486098
Heavy fuel oil*0.983.7111.6141.8179714114697410.83391676738.2137129
Kerosene*0.8213.10812.8346.21986237.912666311.94431848735.3126663
Light fuel oil*0.963.63412.22441891742.215155211.2840.61745539139841
LNG*0.4281.62115.3355.22373223.68481013.548.62089420.874670
LPG*0.5372.03313.6949.32119526.59498612.6445.51956124.487664
Marine gas oil*0.8553.23712.7545.91973339.214080411.8942.81840136.6131295
Methanol0.7912.9946.3923988818.2652745.5419.9856815.856562
Methyl ester (biodiesel)0.8883.36111.1740.21728335.712806210.4237.51612233.3119460
MTBE0.7432.81110.56381633728.21012449.7535.11509026.193517
Oils vegetable (biodiesel)*0.923.48311.2540.51741237.313368410.537.81625134.8124772
Paraffin (wax)*0.93.40712.78461977641.414853811.5341.51784237.4134007
Pentane0.632.38513.548.62089430.610985412.645.41949728.6102507
Petroleum naphtha*0.7252.74513.3648.12067934.912514512.4744.91930332.6116819
Propane0.4981.88513.9950.42164725.18996312.8846.41992723.182816
Residual oil*0.9913.75241.815007210.9739.51698239.2140470
Tar*103615477
Turpentine0.8653.27412.22441891738.1136555

Source: engineeringtoolbox.com

Solid Fuels - Higher and lower calorific values (heating values)

12 rows
Solid Fuels - Higher and lower calorific values (heating values)
Solid Fuel*
kg/dm3(kg/dm3)
kWh/kg(kWh/kg)
MJ/kg(MJ/kg)
Btu/lb(Btu/lb)
kWh/kg(kWh/kg)
MJ/kg(MJ/kg)
Btu/lb(Btu/lb)
Anthracite coal9.0632.614015
Bituminous coal8.3930.2129848.062912468
Carbon9.1132.814101
Charcoal8.2229.6127267.8928.412210
Coke7.222611178
Lignite (brown coal)3.89146019
Peat4.72177309
Petroleum coke8.6931.3134578.1929.512683
Semi anthracite8.1929.512683
Sub-Bituminous coal6.7824.410490
Sulfur (s)2.569.239552.559.23939
Wood (dry)0.7014.516.269654.2815.46621

Source: engineeringtoolbox.com

Engineering Notes

Fuel Energy and LHV Estimate

Unit Converter

Fuel Heating Value Unit Converter

  • Reference conditions — All tabulated values are at 25 °C and 1 atm. Heating values shift slightly with pressure and temperature; fuel gas standards (e.g., ISO 6976) specify exact correction procedures.
  • Moisture content — Solid fuels such as wood and coal vary widely in moisture and ash. The values shown assume reasonably dry, representative samples. Always use as-received or as-fired values for real equipment sizing.
  • Hydrogen effect — The HHV-to-LHV gap grows with hydrogen content. For natural gas (~25 % H₂ by mass), the difference is about 10 %. For coal (~4 % H₂), the difference is only 3–4 %.
  • Combustion efficiency — Condensing boilers can recover a portion of the latent heat, bringing effective efficiency closer to the HHV basis. Standard (non-condensing) appliances are rated on an LHV basis in many markets.
  • Unit conversion — 1 Btu/lb ≈ 2.326 kJ/kg. In US practice, heating values are commonly reported in BTU/lb or BTU/ft³; metric data uses MJ/kg or kJ/m³.

References