Fuel properties
Diesel – legislation and standards
Engine and after-treatment technology impose requirements for fuel quality. Basic fuel analyses were developed to screen general performance and operability of fuels in internal combustion engines. Fuel properties important in environmental contexts, such as compatibility of fuel with emission control devices, were defined subsequently. The functionality and general performance of diesel fuel can be defined, for example, in terms of ignition quality, distillation, viscosity, and additives. Environmental performance can be defined in terms of aromatics and sulfur content.
Fuel properties are controlled by legislation and by fuel standards. In Europe, Fuel Quality Directive 2009/30/EC defines the requirements for basic fuel properties for diesel fuel. European standard EN 590 includes more extensive requirements than Fuel Quality Directive to ensure proper functionality of diesel fuel on market. In Europe, CEN (European Committee for Standardization) develops standards.
In the US, ASTM D 975 is a specification for diesel fuel. ASTM standard includes several classes. There are also a number of other regional and national standards on fuels.
Automobile and engine manufacturers have defined recommendations for fuels in “World Wide Fuel Charter” (WWFC). Category 5 is the most stringent WWFC category for “markets with further advanced requirements for emission control to enable sophisticated NOx and particulate matter after-treatment technologies”.
Selected requirements and fuel properties are shown in Tables 1 and 2 below.
Table 1. Selected requirements as examples for diesel fuel properties in Europe and in the U.S., together with automanufacturer's recommendations (WWFC). Complete requirements and standards are available from respective organizations.
|
|
Standard A 2022 a |
Standard B 2014 a |
WWFC:2019 Category 5 a |
|
Cetane number |
≥51.0 |
≥40 |
≥55.0 |
|
Cetane index |
≥46.0 |
≥40 or aromatics ≤35 vol-% |
depends on additive use |
|
Density at 15 °C, kg/m3 |
820b - 845 |
|
815b - 840 |
|
Viscosity at 40 °C, mm2/s |
2.0b - 4.5 |
1.9 - 4.1 |
2.0b - 4.0 |
|
CFFP, °C |
b |
agreed by buyer and seller |
equal or lower than the lowest expected ambient temperature |
|
Flash point, °C |
>55.0 |
≥52 |
>55 |
|
Evaporated, vol-% |
E250: <65 |
|
|
|
Evaporated, °C |
T95: ≤360 |
T90: 282 - 338 |
T90: ≤320 |
|
Final boiling point, °C |
|
|
≤350 |
|
Dist. residue/loss, vol-% |
|
≤2 |
|
|
Total aromatics, wt-% |
|
Total ≤35 or |
≤15 |
|
Polycyclic aromatic hydrocarbons (PAH di+), wt-% |
≤8.0 |
|
≤2.0 |
|
Sulfur content, mg/kg |
≤10.0 |
≤15 |
≤10 |
|
FAME content, vol-% |
≤7.0 |
≤5.0 |
Non-detectable |
|
Other biofuels |
|
|
HVO, BTL |
|
Methanol/ethanol, wt-% |
|
|
Non-detectable |
|
Lubricity, wear scar diameter |
≤460 |
≤520 |
≤400 |
|
Copper strip corrosion (3h, 50 °C) |
Class 1 |
≤3 |
Class 1 |
|
Ferrous corrosion |
|
|
Max. light rust |
|
Total acid number, mg KOH/g |
|
|
≤0.08 |
|
Carbon residue (10% dist.), wt-% |
≤0.3 |
≤0.35 |
≤0.20 |
|
Ash content, wt-% |
≤0.01 |
≤0.01 |
≤0.001 |
|
Metal content, mg/kg |
≤2.0 manganese |
|
Non-detectable |
|
Chlorine, mg/kg |
|
|
Non-detectable |
|
Oxidation stability 95 °C, g/m3 |
≤25 |
|
≤25 |
|
Oxidation stability, h/min |
>20/>60 c |
|
/>65 (PetroOxy) |
|
Total contamination, mg/kg |
≤24 |
|
<10 |
|
Particulate contamination, size distribution |
|
|
18/16/13 per ISO 4406 |
|
Injector cleanliness/filter blocking tendency |
|
|
limit vary with test method/ <1.6 |
|
Water and sediment, wt% |
water ≤0.02 |
≤0.05 |
water ≤0.02 |
|
Foam volume, ml/vanishing time, sec. |
|
|
≤100/≤15 |
|
Biological growth |
|
|
Zero content |
|
Conductivity, pS/m |
|
≥25 |
|
a Only selected requirements presented here. b Several classes. Climate-dependent properties vary. c Limits depend on test methods. For diesel fuel containing above 2 vol-% FAME.
Table 2. Examples of some non-limited diesel fuel properties. a,b
|
Property |
Example |
|
Property |
Example |
|
Carbon number |
C12 - C20 |
|
Nitrogen, mg/kg |
~30 |
|
Molecular weight range, g/mol |
~150 - 250 |
|
Total aromatics, wt-% |
~20 |
|
Carbon/Hydrogen, wt-% |
~86.5/13.5 |
|
Stoichiometric air to fuel ratio |
14.7 |
|
Distillation, °C |
200 - 360 |
|
Vapor density |
|
|
LHV energy content, MJ/kg |
43 |
|
Autoignition temperature, °C |
230 |
|
LHV energy content, MJ/I |
35 |
|
Flammability limits, vol-% |
0.6 - 5.6/6.5 |
|
HHV energy content, MJ/kg |
46 |
|
Electrical conductivity, µS/m* |
10-4 |
|
Heat of vaporization, kJ/kg |
225 - 280 |
|
|
|
* Electrical conductivity depends on the concentration of metallic ions. Degaldo (2007) reported 200 µS/m for hydrous ethanol and 10 µS/m for Brazilian gasoline. a Murphy 1998 b Murtonen et al. 2009
Gasoline - legislation and standards
The engine and after-treatment technology impose requirements on fuel quality. Basic fuel analyses were developed to screen general performance and operability of fuels in internal combustion engines. Fuel properties important in environmental contexts, such as compatibility of fuel with emission control devices, were defined subsequently. The functionality and general performance of gasoline can be defined, for example, in terms of octane rating, volatility, olefin content, and additives. Environmental performance can be defined, for example, in terms of aromatics, olefins, benzene content, oxygenates, volatility, and sulfur (lead is not allowed in most countries). Fuel properties are controlled by legislation and by fuel standards. There are also a number of other regional and national standards on fuels.
In Europe the Fuel Quality Directive, 2009/30/EC, defines the requirements for basic fuel properties for gasoline. The European standard EN 228 includes more extensive requirements than Fuel Quality Directive to ensure proper functionality of gasoline on market. CEN (European Committee for Standardization) develops standards in Europe.
In the US, ASTM D 4814 is a specification for gasoline. The ASTM standard includes a number of classes, waivers, and exceptions taking into account climate, region and, for example, ethanol content of gasoline. In 2011 US EPA accepted waiver for usage of 15 vol-% ethanol blend for 2001 and newer cars. In the US gasoline-oxygenate blends are considered “substantially similar” if they contain hydrocarbons, aliphatic ethers, aliphatic alcohols other than methanol, up to 0.3 vol-% methanol, up to 2.75 vol-% methanol with an equal volume of butanol, or higher molecular weight alcohol. The fuel must contain no more than 2.0 wt-% oxygen except the fuels containing aliphatic ethers and/or alcohols (excluding methanol) that must not contain more than 2.7 wt-% oxygen. In the USA, so called P-Series fuel consisting of butane, pentanes, ethanol, and the biomass-derived co-solvent methyltetrahydrofuran (MTHF) is allowed for FFV cars.
Automobile and engine manufacturers have defined recommendations for fuels in “World Wide Fuel Charter” (WWFC). Category 6 is the most stringent WWFC category for “markets with further advanced requirements for emission control to enable sophisticated NOx and particulate matter after-treatment technologies”.
Selected requirements and fuel properties are shown in Tables 3 and 4 below.
Table 3. Selected requirements for gasoline properties in Europe and in the U.S., together with automanufacturer's recommendations (WWFC). Complete requirements and standards are available from respective organizations.
|
|
Standard A |
Standard B 2014 c,d |
WWFC:2019 Category 6 c, g |
|
RON |
≥95.0 |
|
≥98a |
|
MON |
≥85.0 |
|
≥88a |
|
Vapor pressure, kPa e |
45 - 60a |
≤62a |
45 - 60a |
|
Density at 15 °C, kg/m3 |
720 - 775 |
|
720 - 775 |
|
Evaporated, vol-% |
E70: 22 - 50a E100: 46 - 72 E150: ≥75.0 |
|
E70: 20 - 45a E100: 50 - 65a E180: ≥90 |
|
Evaporated, °C |
|
T10: ≤70a T50: 77 - 121 T90: ≤190 |
T10: ≤65a T50: 77 - 100a T90: 130 - 175 |
|
Final boiling point, °C |
≤210 |
≤225 |
≤205 |
|
Dist. residue, vol-% |
≤2 |
≤2 |
|
|
|
|
|
|
|
Oxygen content, wt-% |
≤3.7 |
d |
≤3.7 |
|
Methanol, vol-% |
≤3.0f |
d |
Not permitted |
|
Ethanol, vol-% |
≤10.0f |
d |
≤10.0 |
|
Isopropyl alcohol, vol-% |
≤12.0 |
|
|
|
tert-Butyl alcohol, vol-% |
≤15.0 |
|
|
|
Isobutyl alcohol, vol-% |
≤15.0 |
|
|
|
Ethers, C5+, vol-% |
≤22.0 |
|
Preferred |
|
Other oxygenates, vol-% b |
≤15.0 |
|
|
|
|
|
|
|
|
Olefins, vol-% |
≤18.0 |
|
≤10 |
|
Aromatics, vol-% |
≤35.0 |
|
≤35 |
|
Benzene, vol-% |
≤1.00 |
|
≤1.0 |
|
Sulfur content, mg/kg |
≤10.0 |
≤80.0 |
≤10.0 |
|
Lead content, mg/l |
≤5.0 |
≤13 |
see trace metals |
|
Manganese content, mg/l |
≤2.0 |
|
see trace metals |
|
Trace metals, chlorine, organic contaminants, mg/kg |
|
|
No intentional addition |
|
|
|
|
|
|
Oxidation stability, min. |
≥360 |
≥240 |
≥480 |
|
Sediment, mg/l |
|
|
≤1 |
|
Existent gum (washed/unwashed), mg/100 ml |
≤5/- |
≤5/- |
≤5/≤30 |
|
Copper strip corrosion |
Class 1 |
≤1 |
Class 1 |
|
Silver strip corrosion |
|
≤1 |
Class 1 |
a Several classes. Vapor pressure limits depend on season. b Mono-alcohols and ethers with final boiling point max. 210 °C. c May include other requirements than presented here. d In 2011, US EPA accepted 15 vol-% ethanol blend for 2001 and newer cars. "Substantially similar" rule allows e.g. up to 2.75 vol-% methanol with an equal volume of butanol, or higher molecular weight alcohol; fuels containing aliphatic ethers and/or alcohols (excluding methanol) must contain no more than 2.7 wt-% oxygen. e The vapor pressure of gasoline is measured at 100 °F (37.8 °C). f Stabilizing agents shall be added for methanol, and may be added for ethanol. Ethanol for blending shall conform to EN 15376. g RON 102, MON 88 quality also. Requirements for e.g. fuel injector cleanliness, combustion chamber, Particulate Matter Index (PMI).
Table 4. Examples of some non-limited gasoline properties.
|
Properties |
Example |
|
Properties |
Example |
|
Carbon number |
C4 - C12 |
|
Nitrogen, mg/kg |
~3 |
|
Molecular weight range, g/mol |
~60 - 150a |
|
Flash point, °C |
~40a |
|
Carbon/hydrogen, wt-% |
~86.5/13.5 |
|
Stoichiometric air to fuel ratio |
14.7a |
|
Viscosity at 15 °C, mm2/s |
0.83a |
|
Autoignition temperature, °C |
300a |
|
Cetane number |
8 - 14a |
|
Flammability limits, vol-% |
1.4 - 7.6a |
|
Distillation, °C |
30 - 210 |
|
Vapor density |
2 - 4a |
|
LHV energy content, MJ/kg |
42.6a |
|
Surface tension of hexane and benzene at 20 °C, mN/m |
18.4, 28.9b |
|
LHV energy content, MJ/I |
32.9a |
|
Odor threshold |
0.2a |
|
HHV energy content, MJ/kg |
45.4a |
|
Electrical conductivity, µS/m* |
10c |
|
Heat of vaporization, kJ/kg |
275 - 365a |
|
|
|
* Electrical conductivity depends on the concentration of metallic ions. a Murphy 1998 b CRC handbook c Degaldo 2007

