Default Calorific Values
tabulates IRES default net calorific values, explains fuelwood, charcoal, and bagasse determinations, and supplies the Annex B moisture, charcoal-conversion, and waste-calorific tables
Default Calorific Values
Default calorific values are the energy contents a compiler falls back on when specific, measured values are unavailable. IRES provides its own reference set — Table 4.1 below — for use as a last resort. The default values reproduced here are those used in the 2006 Intergovernmental Panel on Climate Change (IPCC) Guidelines for National Greenhouse Gas Inventories (IPCC 2006); where the 2006 IPCC Guidelines report no value for a product, none is given in the table [IRES, Ch. IV, para. 4.45, PDF p. 61, 2018].
Table 4.1 — Default net calorific values for energy products
All values in GJ per metric ton unless otherwise noted [IRES, Ch. IV, Table 4.1, PDF pp. 61–63, 2018]:
| Section/Division/Group | Class | Title | Default value | Lower value | Upper value |
|---|---|---|---|---|---|
| 0 | Coal | ||||
| 01 | Hard coal | ||||
| 011 | 0110 | Anthracite | 26.7 | 21.6 | 32.2 |
| 012 | Bituminous coal | ||||
| 0121 | Coking coal | 28.2 | 24.0 | 31.0 | |
| 0129 | Other bituminous coal | 25.8 | 19.9 | 30.5 | |
| 02 | Brown coal | ||||
| 021 | 0210 | Sub-bituminous coal | 18.9 | 11.5 | 26.0 |
| 022 | 0220 | Lignite | 11.9 | 5.5 | 21.6 |
| 03 | Coal products | ||||
| 031 | Coal coke | ||||
| 0311 | Coke oven coke | 28.2 | 25.1 | 30.2 | |
| 0312 | Gas coke | 28.2 | 25.1 | 30.2 | |
| 0313 | Coke breeze | ||||
| 0314 | Semi cokes | 28.2 | 25.1 | 30.2 | |
| 032 | 0320 | Patent fuel | 20.7 | 15.1 | 32.0 |
| 033 | 0330 | Brown coal briquettes (BKB) | 20.7 | 15.1 | 32.0 |
| 034 | 0340 | Coal tar | 28.0 | 14.1 | 55.0 |
| 035 | 0350 | Coke oven gas | 38.7 | 19.6 | 77.0 |
| 036 | 0360 | Gas works gas (and other manuf. gases for distribution) | 38.7 | 19.6 | 77.0 |
| 037 | Recovered gases | ||||
| 0371 | Blast furnace gas | 2.47 | 1.20 | 5.00 | |
| 0372 | Basic oxygen steel furnace gas | 7.06 | 3.80 | 15.00 | |
| 0379 | Other recovered gases | ||||
| 039 | 0390 | Other coal products | |||
| 1 | Peat and peat products | ||||
| 11 | Peat | ||||
| 111 | 1110 | Sod peat | 9.76 | 7.80 | 12.5 |
| 112 | 1120 | Milled peat | 9.76 | 7.80 | 12.5 |
| 12 | Peat products | ||||
| 121 | 1210 | Peat briquettes | 9.76 | 7.80 | 12.5 |
| 129 | 1290 | Other peat products | 9.76 | 7.80 | 12.5 |
| 2 | Oil shale/oil sands | ||||
| 20 | Oil shale/oil sands | ||||
| 200 | 2000 | Oil shale/oil sands | 8.9 | 7.1 | 11.1 |
| 3 | Natural gas | ||||
| 30 | Natural gas | ||||
| 300 | 3000 | Natural gas | 48.0(a) | 46.5 | 50.4 |
| 4 | Oil | ||||
| 41 | Conventional crude oil | ||||
| 410 | 4100 | Conventional crude oil | 42.3 | 40.1 | 44.8 |
| 42 | Natural gas liquids (NGL) | ||||
| 420 | 4200 | Natural gas liquids (NGL) | 44.2 | 40.9 | 46.9 |
| 43 | Refinery feedstocks | ||||
| 430 | 4300 | Refinery feedstocks | 43.0 | 36.3 | 46.4 |
| 44 | Additives and oxygenates | ||||
| 440 | 4400 | Additives and oxygenates | |||
| 45 | Other hydrocarbons | ||||
| 450 | 4500 | Other hydrocarbons | |||
| 46 | Oil products | ||||
| 461 | 4610 | Refinery gas | 49.5 | 47.5 | 50.6 |
| 462 | 4620 | Ethane | 46.4 | 44.9 | 48.8 |
| 463 | 4630 | Liquefied petroleum gases (LPG) | 47.3 | 44.8 | 52.2 |
| 464 | 4640 | Naphtha | 44.5 | 41.8 | 46.5 |
| 465 | Gasolines | ||||
| 4651 | Aviation gasoline | 44.3 | 42.5 | 44.8 | |
| 4652 | Motor gasoline | 44.3 | 42.5 | 44.8 | |
| 4653 | Gasoline-type jet fuel | 44.3 | 42.5 | 44.8 | |
| 466 | Kerosenes | ||||
| 4661 | Kerosene-type jet fuel | 44.1 | 42.0 | 45.0 | |
| 4669 | Other kerosene | 43.8 | 42.4 | 45.2 | |
| 467 | Gas oil/diesel oil and Heavy gas oil | ||||
| 4671 | Gas oil/diesel oil | 43.0 | 41.4 | 43.3 | |
| 4672 | Heavy gas oil | ||||
| 468 | 4680 | Fuel oil | 40.4 | 39.8 | 41.7 |
| 469 | Other oil products | ||||
| 4691 | White spirit and special boiling point industrial spirits | 40.2 | 33.7 | 48.2 | |
| 4692 | Lubricants | 40.2 | 33.5 | 42.3 | |
| 4693 | Paraffin waxes | 40.2 | 33.7 | 48.2 | |
| 4694 | Petroleum coke | 32.5 | 29.7 | 41.9 | |
| 4695 | Bitumen | 40.2 | 33.5 | 41.2 | |
| 4699 | Other oil products n.e.c. | 40.2 | 33.7 | 48.2 | |
| 5 | Biofuels | ||||
| 51 | Solid biofuels | ||||
| 511 | Fuelwood, wood residues and by-products | 15.6 | 7.9 | 31.0 | |
| 5111 | Wood pellets | 17.3(b) | |||
| 5119 | Other Fuelwood, wood residues and by-products | 13.9(b) | |||
| 512 | 5120 | Bagasse | |||
| 513 | 5130 | Animal waste | |||
| 514 | 5140 | Black liquor | 11.8 | 5.9 | 23.0 |
| 515 | 5150 | Other vegetal material and residues | |||
| 516 | 5160 | Charcoal | 29.5 | 14.9 | 58.0 |
| 52 | Liquid biofuels | ||||
| 521 | 5210 | Biogasoline | 26.8(c) | 13.6 | 54.0 |
| 522 | 5220 | Biodiesels | 36.8(c) | 13.6 | 54.0 |
| 523 | 5230 | Bio jet kerosene | |||
| 529 | 5290 | Other liquid biofuels | 27.4 | 13.8 | 54.0 |
| 53 | Biogases | ||||
| 531 | Biogases from anaerobic fermentation | ||||
| 5311 | Landfill gas | 50.4 | 25.4 | 100.0 | |
| 5312 | Sewage sludge gas | 50.4 | 25.4 | 100.0 | |
| 5319 | Other biogases from anaerobic fermentation | 50.4 | 25.4 | 100.0 | |
| 532 | 5320 | Biogases from thermal processes | |||
| 6 | Waste | ||||
| 61 | Industrial waste | ||||
| 610 | 6100 | Industrial waste | |||
| 62 | Municipal waste | ||||
| 620 | 6200 | Municipal waste | 11.6 / 10.0(d) | 6.8 / 7.0(d) | 18.0 / 18.0(d) |
| 7 | Electricity | ||||
| 70 | Electricity | ||||
| 700 | 7000 | Electricity | |||
| 8 | Heat | ||||
| 80 | Heat | ||||
| 800 | 8000 | Heat | |||
| 9 | Nuclear fuels and other fuels n.e.c. | ||||
| 91 | Uranium and plutonium | ||||
| 910 | Uranium and plutonium | ||||
| 9101 | Uranium ores | ||||
| 9109 | Other uranium and plutonium | ||||
| 92 | Other nuclear fuels | ||||
| 920 | 9200 | Other nuclear fuels | |||
| 99 | Other fuels n.e.c. | ||||
| 990 | 9900 | Other fuels n.e.c. |
Notes to Table 4.1 [IRES, Ch. IV, Table 4.1 notes, PDF p. 63, 2018]:
- (a) The table’s values are per mass, but natural gas calorific values are often expressed per volume instead. For example, United Nations (1988) gives an NCV of 39.02 GJ/thousand m³ under standard conditions for natural gas — a figure not derived from the value shown here.
- (b) Source: Austrian Energy Agency.
- (c) Source: IEA.
- (d) Values refer to the biomass/non-biomass fraction, respectively.
The SIEC codes and titles above match Table 3.1’s classification; see Coal, Biofuels and Waste for the underlying product definitions.
Fuelwood
Fuelwood — the principal cooking/heating energy source in rural areas of many developing countries — is poorly captured in statistics, largely because it is often produced by households for their own use or traded informally [IRES, Ch. IV, para. 4.46, PDF p. 64, 2018]. Wood species and moisture/ash content vary widely and strongly affect calorific value, so countries are encouraged to identify typical fuelwood mixes and average water content, and to establish country-specific volume-to-mass conversion factors [IRES, Ch. IV, para. 4.47, PDF p. 64, 2018].
Fuelwood can be measured by volume (stacked — the stere/stacked cubic metre, or the cord of 128 stacked cubic feet — or solid volume, via water displacement) or by weight. Volume measurement is relatively insensitive to moisture content; weight is highly sensitive to it, since more water per unit weight means less actual fuelwood, so moisture content must be accurately specified whenever fuelwood is weighed [IRES, Ch. IV, para. 4.48, PDF p. 64, 2018].
Moisture content (mc) is measured on two possible bases:
Dry basis: mc% = [(wet weight − dry weight) / dry weight] × 100
Wet basis: mc% = [(wet weight − dry weight) / wet weight] × 100
[IRES, Ch. IV, para. 4.49, PDF p. 64, 2018]
The two bases diverge sharply for very wet biomass (100% mc dry basis = 50% mc wet basis) but converge for air-dry biomass (15% mc dry basis ≈ 13% mc wet basis); it is important to state which basis is used, and most (not all) fuelwood moisture is reported on a dry basis [IRES, Ch. IV, para. 4.50, PDF p. 64, 2018].
Ash content is a second determinant of fuelwood’s energy value: generally around 1 per cent for fuelwood, but up to 4 per cent for some species, since the substances forming ash carry no energy value — wood with 4% ash content has roughly 3% less energy content than wood with 1% ash content [IRES, Ch. IV, para. 4.51, PDF p. 64, 2018].
Default calorific values for fuelwood (mass to energy) vary with the moisture content of green, air-dried and oven-dried wood, as shown in Table 4.2 [IRES, Ch. IV, para. 4.52, PDF p. 64, 2018]. When fuelwood is collected in volume units, Table 4.3 gives the conversion factors to mass units [IRES, Ch. IV, para. 4.53, PDF p. 65, 2018].
Table 4.2 — Influence of moisture content on net calorific values of standard fuelwood (wood with 1% ash content)
[IRES, Ch. IV, Table 4.2, PDF p. 65, 2018]
| Wood state | Dry basis | Wet basis | Kilocalories per kilogram | Btus per pound | Megajoules per kilogram |
|---|---|---|---|---|---|
| Green wood | 160 | 62 | 1 360 | 2 450 | 5.7 |
| Green wood | 140 | 59 | 1 530 | 2 750 | 6.4 |
| Green wood | 120 | 55 | 1 720 | 3 100 | 7.2 |
| Green wood | 100 | 50 | 1 960 | 3 530 | 8.2 |
| Green wood | 80 | 45 | 2 220 | 4 000 | 9.3 |
| Green wood | 70 | 41 | 2 390 | 4 300 | 10.0 |
| Green wood | 60 | 38 | 2 580 | 4 640 | 10.8 |
| Air-dried wood | 50(a) | 33(a) | 2 790 | 5 030 | 11.7 |
| Air-dried wood | 40 | 29 | 3 030 | 5 460 | 12.7 |
| Air-dried wood | 30 | 23 | 3 300 | 5 930 | 13.8 |
| Air-dried wood | 25(b) | 20(b) | 3 460 | 6 230 | 14.5 |
| Air-dried wood | 20 | 17 | 3 630 | 6 530 | 15.2 |
| Oven-dried wood | 15 | 13 | 3 820 | 6 880 | 16.0 |
| Oven-dried wood | 10 | 9 | 4 010 | 7 220 | 16.8 |
| Oven-dried wood | 5 | 5 | 4 230 | 7 610 | 17.7 |
| Oven-dried wood | 0 | 0 | 4 470 | 8 040 | 18.7 |
Notes: (a) average of as-received fuelwood on cordwood basis (4-foot lengths); (b) average of logged fuelwood. Source: United Nations (1987) [IRES, Ch. IV, Table 4.2 notes, PDF p. 65, 2018].
Table 4.3 — Conversion table for fuelwood (wood with 25% moisture content)
[IRES, Ch. IV, Table 4.3, footnote 37, PDF p. 65, 2018]
| Fuelwood | Metric tons per solid cubic metre | Metric tons per cord | Stacked cubic metres (stere) per metric ton |
|---|---|---|---|
| General | 0.707 | 1.71 | 2.12 |
| Coniferous | 0.570 | 1.38 | 2.63 |
| Non-Coniferous | 0.742 | 1.79 | 2.02 |
Cubic metre measured under bark at 25% moisture content (dry basis); weight includes bark. “General” is weighted 20% coniferous / 80% non-coniferous. Source: Forest Products Conversion Factors for the UNECE Region, UNECE/FAO, 2010, updated 2015 [IRES, Ch. IV, Table 4.3, footnote 37, PDF p. 65, 2018].
Annex B, Table 5 — Influence of moisture on solid volume and weight of standard fuelwood:
Percentage moisture content of fuelwood:
| 100 | 80 | 60 | 40 | 20 | 15 | 12 | 10 | 0 | |
|---|---|---|---|---|---|---|---|---|---|
| Solid volume in m³ per ton | 0.80 | 0.89 | 1.00 | 1.14 | 1.33 | 1.39 | 1.43 | 1.45 | 1.60 |
| Weight in tons per m³ | 1.25 | 1.12 | 1.00 | 0.88 | 0.75 | 0.72 | 0.70 | 0.69 | 0.63 |
Source: United Nations (1987) [IRES, Annex B, Table 5, PDF p. 163, 2018].
Charcoal
The amount of biomass (usually fuelwood) needed to yield a given quantity of charcoal depends mainly on three factors: parent wood density, moisture content, and the means of production [IRES, Ch. IV, para. 4.54, PDF p. 65, 2018].
Wood density is the principal yield determinant — charcoal weight can vary by a factor of 2 for equal volumes of input. Drier wood yields more charcoal. The means of production also matters: charcoal is produced in earth-covered pits, oil drums, brick or steel kilns, and retorts, with less sophisticated methods generally losing more powdered charcoal (fines), leaving more incomplete carbonization, and combusting more of the charcoal product itself, all of which lower yields [IRES, Ch. IV, para. 4.55, PDF p. 65, 2018]. Powdered charcoal is always produced during manufacture and transport; when briquetted, the briquettes can weigh 50–100% more per given volume of un-powdered charcoal, owing to greater density [IRES, Ch. IV, para. 4.56, PDF pp. 65–66, 2018].
Three variables determine charcoal’s energy value: moisture content, ash content, and degree of carbonization. Average charcoal moisture content is 5%. Average ash content is 4% for wood charcoal, but near 20% for charcoal from woody crop residues (e.g. coffee shrubs). Assuming complete carbonization, wood charcoal (4% ash, 5% moisture) averages ~30.8 MJ/kg; crop-residue charcoal (20% ash, 5% moisture) averages ~25.7 MJ/kg [IRES, Ch. IV, paras. 4.57–4.58, PDF p. 66, 2018].
Annex B, Table 6 — Fuelwood to charcoal conversion table.
Influence of parent wood density on charcoal production (weight in kg of charcoal produced per cubic metre of fuelwood):
| Coniferous wood | Average tropical hardwoods | Preferred tropical hardwoods | Mangrove (rhizophora) |
|---|---|---|---|
| 115 | 170 | 180 | 285 |
Influence of wood moisture content on charcoal production (quantity of wood required to produce 1 ton of charcoal):
| Moisture content (dry basis) | 100 | 80 | 60 | 40 | 20 | 15 | 10 |
|---|---|---|---|---|---|---|---|
| Volume of wood required (cubic metres) | 17.6 | 16.2 | 13.8 | 10.5 | 8.1 | 6.6 | 5.8 |
| Weight of wood required (tons) | 12.6 | 11.6 | 9.9 | 7.5 | 5.8 | 4.7 | 4.1 |
Source: United Nations (1987) [IRES, Annex B, Table 6, PDF p. 163, 2018].
Annex B, Table 7 — Fuelwood requirement for charcoal production by kiln type (cubic metres of fuelwood per ton of charcoal, by percentage moisture content of fuelwood):
| Kiln Type | 15 | 20 | 40 | 60 | 80 | 100 |
|---|---|---|---|---|---|---|
| Earth kiln | 10 | 13 | 16 | 21 | 24 | 27 |
| Portable steel kiln | 6 | 7 | 9 | 13 | 15 | 16 |
| Brick kiln | 6 | 6 | 7 | 10 | 11 | 12 |
| Retort | 4.5 | 4.5 | 5 | 7 | 8 | 9 |
Data are based on the assumption of standard hardwood as input into the process. Source: United Nations (1987) [IRES, Annex B, Table 7, PDF p. 164, 2018].
Vegetal and animal wastes
Agricultural wastes and food-processing by-products are used as fuel, substituting for woody biomass in fuelwood-deficient areas [IRES, Ch. IV, para. 4.59, PDF p. 66, 2018].
Moisture and ash content are the two key determinants of non-woody plant biomass’s energy value: wood’s ash content is generally ~1%, but crop residues range from 3% to over 20%, and — as with fuelwood — ash carries no energy value, so 20%-ash biomass has roughly 19% less energy than otherwise-similar 1%-ash biomass. Such data are rarely collected directly and are usually derived from crop/waste or end-product/waste ratios. Given the wide cross-country variability in ash and moisture content, it is recommended that animal and vegetal wastes be reported to international organizations in an energy unit (preferably TJ) rather than their natural units — national authorities are generally best placed to assess these wastes’ energy content, alternatively estimable from the measured heat or electricity output of the transformation devices that use them, applying standard efficiency factors [IRES, Ch. IV, para. 4.60, PDF p. 66, 2018].
Bagasse: two worked estimation methods
Bagasse — the fibrous cane residue from sugar production — is important enough, and compositionally consistent enough, that international organizations report it separately from ordinary vegetal waste, in its natural (weight) unit, rather than folding it into the general recommendation above. Its availability can be estimated from either the sugar cane input to sugar mills or the output of centrifugal cane sugar [IRES, Ch. IV, para. 4.61, PDF p. 66, 2018].
Method (a) — Central American studies. Fuel bagasse yield is approximately 280 kg per metric ton of sugar cane processed. Assuming 50% moisture content at time of use, 1 metric ton of bagasse yields 7.72 GJ. For 1 metric ton of processed sugar cane, this gives:
2.16 GJ = 0.516 Gcal = 0.074 tce = 0.051 toe
[IRES, Ch. IV, para. 4.62, PDF p. 66, 2018]
Method (b) — Economic Commission for Latin America and the Caribbean (ECLAC). Based on observations, ECLAC proposed 3.26 kg bagasse yield per kilogram of centrifugal sugar produced. For 1 metric ton of sugar produced, this gives:
25.2 GJ = 6 Gcal = 0.86 tce = 0.59 toe
[IRES, Ch. IV, para. 4.63, PDF p. 67, 2018]
The two methods are not interchangeable estimates of the same quantity — method (a) is per ton of sugar cane processed, method (b) per ton of sugar produced — and IRES presents both without recommending one over the other.
Animal waste (dung) is another significant agricultural by-product: it can be dried and burned directly for space heating, cooking or crop drying; fed into biogas digestors (yielding gas for cooking/heating/lighting plus a fertilizer residue); used as biodiesel feedstock; or spread with minimal treatment as fertilizer [IRES, Ch. IV, para. 4.64, PDF p. 67, 2018].
Annex B, Table 8 — Energy values of selected animal and vegetal wastes:
| Wastes | Average moisture content: dry basis (percentage) | Approximate ash content (percentage) | Net calorific value (MJ/kg) |
|---|---|---|---|
| Animal dung | 15 | 23–27 | 13.6 |
| Groundnut shells | 3–10 | 4–14 | 16.7 |
| Coffee husks | 13 | 8–10 | 15.5–16.3 |
| Bagasse | 40–50 | 10–12 | 8.4–10.5 |
| Cotton husks | 5–10 | 3 | 16.7 |
| Coconut husks | 5–10 | 6 | 16.7 |
| Rice hulls | 9–11 | 15–20 | 13.8–15.1 |
| Olives (pressed) | 15–18 | 3 | 16.75 |
| Oil-palm fibres | 55 | 10 | 7.5–8.4 |
| Oil-palm husks | 55 | 5 | 7.5–8.4 |
| Bagasse | 30 | 10–12 | 12.6 |
| Bagasse | 50 | 10–12 | 8.4 |
| Bark | 15 | 1 | 11.3 |
| Coffee husk, cherries | 30 | 8–10 | 13.4 |
| Coffee husk, cherries | 60 | 8–10 | 6.7 |
| Corncobs | 15 | 1–2 | 19.3 |
| Nut hulls | 15 | 1–5 | 18.0 |
| Rice straw & husk | 15 | 15–20 | 13.4 |
| Wheat straw & husk | 15 | 8–9 | 19.1 |
| Municipal garbage | .. | .. | 19.7 |
| Paper | 5 | 1 | 17.6 |
| Sawdust | 50 | 1 | 11.7 |
Note: two dots (..) indicate that data are not available. Source: United Nations (1987) [IRES, Annex B, Table 8, PDF p. 164, 2018]. Bagasse appears three times in the source table at different moisture contents (40–50%, 30%, 50%) — reproduced as three separate rows, not merged, since each row is a distinct moisture-content observation.
Related
- IRES Annexes and References — Annex B, Tables 5–8, the source of the fuelwood-moisture, charcoal-conversion and animal/vegetal-waste tables above
- Calorific Values — the general default-vs-specific distinction and the weighted-average calculation method this table backs
- Measurement Units — the mass, volume and energy units Table 4.1 and the biomass tables are expressed in
- Coal — coal, peat and coal-product classes whose default NCVs appear in Table 4.1
- Biofuels — fuelwood, charcoal, bagasse and biogas classes whose default NCVs and biomass-specific determination methods are detailed above
- Waste — industrial/municipal waste default NCVs in Table 4.1
Source material
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