Heat of combustion explained

The heating value (or energy value or calorific value) of a substance, usually a fuel or food (see food energy), is the amount of heat released during the combustion of a specified amount of it.

The calorific value is the total energy released as heat when a substance undergoes complete combustion with oxygen under standard conditions. The chemical reaction is typically a hydrocarbon or other organic molecule reacting with oxygen to form carbon dioxide and water and release heat. It may be expressed with the quantities:

There are two kinds of enthalpy of combustion, called high(er) and low(er) heat(ing) value, depending on how much the products are allowed to cool and whether compounds like are allowed to condense.The high heat values are conventionally measured with a bomb calorimeter. Low heat values are calculated from high heat value test data. They may also be calculated as the difference between the heat of formation ΔH of the products and reactants (though this approach is somewhat artificial since most heats of formation are typically calculated from measured heats of combustion)..[1]

For a fuel of composition CcHhOoNn, the (higher) heat of combustion is usually to a good approximation (±3%),[2] [3] though it gives poor results for some compounds such as (gaseous) formaldehyde and carbon monoxide, and can be significantly off if, such as for glycerine dinitrate, .[4]

By convention, the (higher) heat of combustion is defined to be the heat released for the complete combustion of a compound in its standard state to form stable products in their standard states: hydrogen is converted to water (in its liquid state), carbon is converted to carbon dioxide gas, and nitrogen is converted to nitrogen gas. That is, the heat of combustion, ΔH°comb, is the heat of reaction of the following process:

(std.) + (c + -) (g) → c (g) + (l) + (g)

Chlorine and sulfur are not quite standardized; they are usually assumed to convert to hydrogen chloride gas and or gas, respectively, or to dilute aqueous hydrochloric and sulfuric acids, respectively, when the combustion is conducted in a bomb calorimeter containing some quantity of water.[5] [6]

Ways of determination

Gross and net

Zwolinski and Wilhoit defined, in 1972, "gross" and "net" values for heats of combustion. In the gross definition the products are the most stable compounds, e.g. (l), (l), (s) and (l). In the net definition the products are the gases produced when the compound is burned in an open flame, e.g. (g), (g), (g) and (g). In both definitions the products for C, F, Cl and N are (g), (g), (g) and (g), respectively.[7]

Dulong's Formula

The heating value of a fuel can be calculated with the results of ultimate analysis of fuel. From analysis, percentages of the combustibles in the fuel (carbon, hydrogen, sulfur) are known. Since the heat of combustion of these elements is known, the heating value can be calculated using Dulong's Formula:

HHV [kJ/g]= 33.87mC + 122.3(mH - mO ÷ 8) + 9.4mS

where mC, mH, mO, mN, and mS are the contents of carbon, hydrogen, oxygen, nitrogen, and sulfur on any (wet, dry or ash free) basis, respectively.[8]

Higher heating value

The higher heating value (HHV; gross energy, upper heating value, gross calorific value GCV, or higher calorific value; HCV) indicates the upper limit of the available thermal energy produced by a complete combustion of fuel. It is measured as a unit of energy per unit mass or volume of substance. The HHV is determined by bringing all the products of combustion back to the original pre-combustion temperature, including condensing any vapor produced. Such measurements often use a standard temperature of 25C. This is the same as the thermodynamic heat of combustion since the enthalpy change for the reaction assumes a common temperature of the compounds before and after combustion, in which case the water produced by combustion is condensed to a liquid. The higher heating value takes into account the latent heat of vaporization of water in the combustion products, and is useful in calculating heating values for fuels where condensation of the reaction products is practical (e.g., in a gas-fired boiler used for space heat). In other words, HHV assumes all the water component is in liquid state at the end of combustion (in product of combustion) and that heat delivered at temperatures below can be put to use.

Lower heating value

The lower heating value (LHV; net calorific value; NCV, or lower calorific value; LCV) is another measure of available thermal energy produced by a combustion of fuel, measured as a unit of energy per unit mass or volume of substance. In contrast to the HHV, the LHV considers energy losses such as the energy used to vaporize water - although its exact definition is not uniformly agreed upon. One definition is simply to subtract the heat of vaporization of the water from the higher heating value. This treats any H2O formed as a vapor that is released as a waste. The energy required to vaporize the water is therefore lost.

LHV calculations assume that the water component of a combustion process is in vapor state at the end of combustion, as opposed to the higher heating value (HHV) (a.k.a. gross calorific value or gross CV) which assumes that all of the water in a combustion process is in a liquid state after a combustion process.

Another definition of the LHV is the amount of heat released when the products are cooled to . This means that the latent heat of vaporization of water and other reaction products is not recovered. It is useful in comparing fuels where condensation of the combustion products is impractical, or heat at a temperature below cannot be put to use.

One definition of lower heating value, adopted by the American Petroleum Institute (API), uses a reference temperature of 60F.

Another definition, used by Gas Processors Suppliers Association (GPSA) and originally used by API (data collected for API research project 44), is the enthalpy of all combustion products minus the enthalpy of the fuel at the reference temperature (API research project 44 used 25 °C. GPSA currently uses 60 °F), minus the enthalpy of the stoichiometric oxygen (O2) at the reference temperature, minus the heat of vaporization of the vapor content of the combustion products.

The definition in which the combustion products are all returned to the reference temperature is more easily calculated from the higher heating value than when using other definitions and will in fact give a slightly different answer.

Gross heating value

Gross heating value accounts for water in the exhaust leaving as vapor, as does LHV, but gross heating value also includes liquid water in the fuel prior to combustion. This value is important for fuels like wood or coal, which will usually contain some amount of water prior to burning.

Measuring heating values

The higher heating value is experimentally determined in a bomb calorimeter. The combustion of a stoichiometric mixture of fuel and oxidizer (e.g. two moles of hydrogen and one mole of oxygen) in a steel container at is initiated by an ignition device and the reactions allowed to complete. When hydrogen and oxygen react during combustion, water vapor is produced. The vessel and its contents are then cooled to the original 25 °C and the higher heating value is determined as the heat released between identical initial and final temperatures.

When the lower heating value (LHV) is determined, cooling is stopped at 150 °C and the reaction heat is only partially recovered. The limit of 150 °C is based on acid gas dew-point.

Note: Higher heating value (HHV) is calculated with the product of water being in liquid form while lower heating value (LHV) is calculated with the product of water being in vapor form.

Relation between heating values

The difference between the two heating values depends on the chemical composition of the fuel. In the case of pure carbon or carbon monoxide, the two heating values are almost identical, the difference being the sensible heat content of carbon dioxide between 150 °C and 25 °C (sensible heat exchange causes a change of temperature, while latent heat is added or subtracted for phase transitions at constant temperature. Examples: heat of vaporization or heat of fusion). For hydrogen, the difference is much more significant as it includes the sensible heat of water vapor between 150 °C and 100 °C, the latent heat of condensation at 100 °C, and the sensible heat of the condensed water between 100 °C and 25 °C. All in all, the higher heating value of hydrogen is 18.2% above its lower heating value (142MJ/kg vs. 120MJ/kg). For hydrocarbons, the difference depends on the hydrogen content of the fuel. For gasoline and diesel the higher heating value exceeds the lower heating value by about 10% and 7%, respectively, and for natural gas about 11%.

A common method of relating HHV to LHV is:

HHV=LHV+

H
v\left(
n
H2O,out
nfuel,in

\right)

where Hv is the heat of vaporization of water, n,out is the number of moles of water vaporized and nfuel,in is the number of moles of fuel combusted.[9]

Usage of terms

Engine manufacturers typically rate their engines fuel consumption by the lower heating values since the exhaust is never condensed in the engine, and doing this allows them to publish more attractive numbers than are used in conventional power plant terms. The conventional power industry had used HHV (high heat value) exclusively for decades, even though virtually all of these plants did not condense exhaust either. American consumers should be aware that the corresponding fuel-consumption figure based on the higher heating value will be somewhat higher.

The difference between HHV and LHV definitions causes endless confusion when quoters do not bother to state the convention being used.[10] since there is typically a 10% difference between the two methods for a power plant burning natural gas. For simply benchmarking part of a reaction the LHV may be appropriate, but HHV should be used for overall energy efficiency calculations if only to avoid confusion, and in any case, the value or convention should be clearly stated.

Accounting for moisture

Both HHV and LHV can be expressed in terms of AR (all moisture counted), MF and MAF (only water from combustion of hydrogen). AR, MF, and MAF are commonly used for indicating the heating values of coal:

Heat of combustion tables

Fuel! colspan=3
HHVLHV
MJ/kgBTU/lbkJ/molMJ/kg
Hydrogen141.80 61,000 286 119.96
55.50 23,900 890 50.00
51.90 22,400 1,56047.62
Propane50.35 21,700 2,220 46.35
Butane49.50 20,9002,877 45.75
Pentane48.60 21,876 3,509 45.35
46.00 19,900 41.50
46.20 19,862 43.00
Jet kerosene[11] 46.42 - 44.1
44.80 19,300 43.4
Coal (anthracite) 32.50 14,000
Coal (lignite - USA)15.00 6,500
Wood (MAF)21.70 8,700
16.0 6,400 17.0
Peat (dry)15.00 6,500
Peat (damp)6.00 2,500
Higher heating value
of some less common fuels! Fuel !! MJ/kg !! BTU/lb !! kJ/mol
22.7 9,800 726
29.7 12,800 1,367
1-Propanol33.6 14,500 2,020
Acetylene49.9 21,500 1,300
41.8 18,000 3,268
22.5 9,690 382.6
19.4 8,370 622.0
Hexamine30.0 12,900 4,200.0
32.8 14,100 393.5
Lower heating value for some organic compounds
(at 25C)! Fuel! MJ/kg! MJ/L! BTU/lb! kJ/mol
Alkanes
Methane50.0096.921,504802.34
Ethane47.79420,5511,437.2
Propane46.35725.319,9342,044.2
Butane45.75219,6732,659.3
Pentane45.35728.3921,7063,272.6
Hexane44.75229.3019,5043,856.7
Heptane44.56630.4819,1634,465.8
Octane44.42719,1045,074.9
Nonane44.31131.8219,0545,683.3
Decane44.24033.2919,0236,294.5
Undecane44.19432.7019,0036,908.0
Dodecane44.14733.1118,9837,519.6
Isoparaffins
Isobutane45.61319,6142,651.0
Isopentane45.24127.8719,4543,264.1
2-Methylpentane44.68229.1819,2133,850.7
2,3-Dimethylbutane44.65929.5619,2033,848.7
2,3-Dimethylpentane44.49630.9219,1334,458.5
2,2,4-Trimethylpentane44.31030.4919,0535,061.5
Naphthenes
Cyclopentane44.63633.5219,1933,129.0
Methylcyclopentane44.636?33.43?19,193?3,756.6?
Cyclohexane43.45033.8518,6843,656.8
Methylcyclohexane43.38033.4018,6534,259.5
Monoolefins
Ethylene47.195
Propylene45.799
1-Butene45.334
cis-2-Butene45.194
trans-2-Butene45.124
Isobutene45.055
1-Pentene45.031
2-Methyl-1-pentene44.799
1-Hexene44.426
Diolefins
1,3-Butadiene44.613
Isoprene44.078-
Nitrous derived
Nitromethane10.513
Nitropropane20.693
Acetylenes
Acetylene48.241
Methylacetylene46.194
1-Butyne45.590
1-Pentyne45.217
Aromatics
Benzene40.170
Toluene40.589
o-Xylene40.961
m-Xylene40.961
p-Xylene40.798
Ethylbenzene40.938
1,2,4-Trimethylbenzene40.984
n-Propylbenzene41.193
Cumene41.217
Alcohols
Methanol19.93015.788,570638.6
Ethanol26.7022.7712,4121,230.1
1-Propanol30.68024.6513,1921,843.9
Isopropanol30.44723.9313,0921,829.9
n-Butanol33.07526.7914,2222,501.6
Isobutanol32.95926.4314,1722,442.9
tert-Butanol32.58725.4514,0122,415.3
n-Pentanol34.72728.2814,9333,061.2
Isoamyl alcohol31.416?35.64?13,509?2,769.3?
Ethers
Methoxymethane28.70312,3421,322.3
Ethoxyethane33.86724.1614,5632,510.2
Propoxypropane36.35526.7615,6333,568.0
Butoxybutane37.79828.8816,2534,922.4
Aldehydes and ketones
Formaldehyde17.259570.78 [12]
Acetaldehyde24.156
Propionaldehyde28.889
Butyraldehyde31.610
Acetone28.54822.62
Other species
Carbon (graphite)32.808
Hydrogen120.9711.852,017244
Carbon monoxide10.1124,348283.24
Ammonia18.6468,018317.56
Sulfur (solid)9.1633,940293.82
Note

Higher heating values of natural gases from various sources

The International Energy Agency reports the following typical higher heating values per Standard cubic metre of gas:[13]

The lower heating value of natural gas is normally about 90% of its higher heating value. This table is in Standard cubic metres (1atm, 15°C), to convert to values per Normal cubic metre (1atm, 0°C), multiply above table by 1.0549.

See also

Further reading

External links

Notes and References

  1. Web site: Effect of structural conduction and heat loss on combustion in micro-channels . Taylor & Francis Online.
  2. Schmidt-Rohr . Klaus . Why Combustions Are Always Exothermic, Yielding About 418 kJ per Mole of O 2 . Journal of Chemical Education . 8 December 2015 . 92 . 12 . 2094–2099 . 10.1021/acs.jchemed.5b00333 . 2015JChEd..92.2094S . free .
  3. Dlugogorski, B. Z.; Mawhinney, J. R.; Duc, V. H. (1994). "The Measurement of Heat Release Rates by Oxygen Consumption Calorimetry in Fires Under Suppression". Fire Safety Science 1007: 877.
  4. It gives 545 kJ/mole, whereas the value calculated from heats of formation is around 1561 kJ/mole. For glycerine trinitrate (nitroglycerine) it gives 0, though nitroglycerine does not actually combust.
  5. Kharasch . M.S. . Heats of combustion of organic compounds . Bureau of Standards Journal of Research . February 1929 . 2 . 2 . 359 . 10.6028/jres.002.007 . free .
  6. Web site: Theoretical Analysis of Waste Heat Recovery from an Internal Combustion Engine in a Hybrid Vehicle . Jstor.
  7. Book: Zwolinski . Bruno J . Wilhoit . Randolf C. . Heats of formation and Heats of Combustion . 316–342 . https://web.mit.edu/8.13/8.13c/references-fall/aip/aip-handbook-section4l.pdf . Dwight E. . Gray . Bruce H. . Billings . American Institute of Physics Handbook . 1972 . McGraw-Hill . 978-0-07-001485-5 . 2021-08-06 . 2021-08-06 . https://web.archive.org/web/20210806144519/https://web.mit.edu/8.13/8.13c/references-fall/aip/aip-handbook-section4l.pdf . dead .
  8. Hosokai . Sou . Matsuoka . Koichi . Kuramoto . Koji . Suzuki . Yoshizo . Modification of Dulong's formula to estimate heating value of gas, liquid and solid fuels . Fuel Processing Technology . 1 November 2016 . 152 . 399–405 . 10.1016/j.fuproc.2016.06.040 .
  9. Air Quality Engineering, CE 218A, W. Nazaroff and R. Harley, University of California Berkeley, 2007
  10. Web site: The difference between LCV and HCV (or Lower and Higher Heating Value, or Net and Gross) is clearly understood by all energy engineers. There is no 'right' or 'wrong' definition. - Claverton Group. www.claverton-energy.com.
  11. Web site: CDP Technical Note: Conversion of fuel data to MWh.
  12. Web site: Methanal. webbook.nist.gov.
  13. Web site: Key World Energy Statistics (2016). iea.org.