Type: Petrol
a Test methods shall be those specified in EN 228:2004. Member States may adopt the analytical method specified in replacement EN 228:2004 standard if it can be shown to give at least the same accuracy and at least the same level of precision as the analytical method it replaces. | |||
b The values quoted in the specification are ‘true values’. In the establishment of their limit values, the terms of EN ISO 4259:2006 ‘Petroleum products — Determination and application of precision data in relation to methods of test’ have been applied and in fixing a minimum value, a minimum difference of 2R above zero has been taken into account (R = reproducibility). The results of individual measurements shall be interpreted on the basis of the criteria described in EN ISO 4259:2006. | |||
c Member States may decide to continue to permit the placing on the market of unleaded regular grade petrol with a minimum motor octane number (MON) of 81 and a minimum research octane number (RON) of 91. | |||
d The summer period shall begin no later than 1 May and shall not end before 30 September. For Member States with low ambient summer temperatures the summer period shall begin no later than 1 June and shall not end before 31 August. | |||
e In the case of Member States with low ambient summer temperatures and for which a derogation is in effect in accordance with Article 3(4) and (5), the maximum vapour pressure shall be 70 kPa. In the case of Member States for which a derogation is in effect in accordance with Article 3(4) and (5) for petrol containing ethanol, the maximum vapour pressure shall be 60 kPa plus the vapour pressure waiver specified in Annex III. | |||
f Other mono-alcohols and ethers with a final boiling point no higher than that stated in EN 228:2004. | |||
Parametera | Unit | Limitsb | |
---|---|---|---|
Minimum | Maximum | ||
Research octane number | 95c | — | |
Motor octane number | 85 | — | |
Vapour pressure, summer periodd | kPa | — | 60,0e |
Distillation: | |||
| % v/v | 46,0 | — |
| % v/v | 75,0 | — |
Hydrocarbon analysis: | |||
| % v/v | — | 18,0 |
| % v/v | — | 35,0 |
| % v/v | — | 1,0 |
Oxygen content | % m/m | 3,7 | |
Oxygenates | |||
| % v/v | 3,0 | |
| % v/v | 10,0 | |
| % v/v | — | 12,0 |
| % v/v | — | 15,0 |
| % v/v | — | 15,0 |
| % v/v | — | 22,0 |
| % v/v | — | 15,0 |
Sulphur content | mg/kg | — | 10,0 |
Lead content | g/l | — | 0,005 |
Type: Diesel
a Test methods shall be those specified in EN 590:2004. Member States may adopt the analytical method specified in replacement EN 590:2004 standard if it can be shown to give at least the same accuracy and at least the same level of precision as the analytical method it replaces. | |||
b The values quoted in the specification are ‘true values’. In the establishment of their limit values, the terms of EN ISO 4259:2006 ‘Petroleum products — Determination and application of precision data in relation to methods of test’ have been applied and in fixing a minimum value, a minimum difference of 2R above zero has been taken into account (R = reproducibility). The results of individual measurements shall be interpreted on the basis of the criteria described in EN ISO 4259:2006. | |||
c FAME shall comply with EN 14214. | |||
Parametera | Unit | Limitsb | |
---|---|---|---|
Minimum | Maximum | ||
Cetane number | 51,0 | — | |
Density at 15 °C | kg/mc | — | 845,0 |
Distillation: | |||
| °C | — | 360,0 |
Polycyclic aromatic hydrocarbons | % m/m | — | 8,0 |
Sulphur content | mg/kg | — | 10,0 |
FAME content — EN 14078 | % v/v | — | 7,0c |
Bioethanol content (% v/v) | Vapour pressure waiver permitted (kPa) |
---|---|
0 | 0 |
1 | 3,65 |
2 | 5,95 |
3 | 7,20 |
4 | 7,80 |
5 | 8,0 |
6 | 8,0 |
7 | 7,94 |
8 | 7,88 |
9 | 7,82 |
10 | 7,76 |
The permitted vapour pressure waiver for intermediate bioethanol content between the values listed shall be determined by a straight line interpolation between the bioethanol content immediately above and that immediately below the intermediate value.
a Not including animal oil produced from animal by-products classified as category 3 material in accordance with Regulation (EC) No 1774/2002 of the European Parliament and of the Council of 3 October 2002 laying down health rules concerning animal by-products not intended for human consumptionb. | ||
Biofuel production pathway | Typical greenhouse gas emission saving | Default greenhouse gas emission saving |
---|---|---|
Sugar beet ethanol | 61 % | 52 % |
Wheat ethanol (process fuel not specified) | 32 % | 16 % |
Wheat ethanol (lignite as process fuel in CHP plant) | 32 % | 16 % |
Wheat ethanol (natural gas as process fuel in conventional boiler) | 45 % | 34 % |
Wheat ethanol (natural gas as process fuel in CHP plant) | 53 % | 47 % |
Wheat ethanol (straw as process fuel in CHP plant) | 69 % | 69 % |
Corn (maize) ethanol, Community produced (natural gas as process fuel in CHP plant) | 56 % | 49 % |
Sugar cane ethanol | 71 % | 71 % |
The part from renewable sources of ethyl-Tertio-butyl-ether (ETBE) | Equal to that of the ethanol production Pathway used | |
The part from renewable sources of tertiary-amyl-ethyl-ether (TAEE) | Equal to that of the ethanol production pathway used | |
Rape seed biodiesel | 45 % | 38 % |
Sunflower biodiesel | 58 % | 51 % |
Soybean biodiesel | 40 % | 31 % |
Palm oil biodiesel (process not specified) | 36 % | 19 % |
Palm oil biodiesel (process with methane capture at oil mill) | 62 % | 56 % |
Waste vegetable or animala oil biodiesel | 88 % | 83 % |
Hydrotreated vegetable oil from rape seed | 51 % | 47 % |
Hydrotreated vegetable oil from sunflower | 65 % | 62 % |
Hydrotreated vegetable oil from palm oil (process not specified) | 40 % | 26 % |
Hydrotreated vegetable oil from palm oil (process with methane capture at oil mill) | 68 % | 65 % |
Pure vegetable oil from rape seed | 58 % | 57 % |
Biogas from municipal organic waste as compressed natural gas | 80 % | 73 % |
Biogas from wet manure as compressed natural gas | 84 % | 81 % |
Biogas from dry manure as compressed natural gas | 86 % | 82 % |
Biofuel production pathway | Typical greenhouse gas emission saving | Default greenhouse gas emission saving |
---|---|---|
Wheat straw ethanol | 87 % | 85 % |
Waste wood ethanol | 80 % | 74 % |
Farmed wood ethanol | 76 % | 70 % |
Waste wood Fischer-Tropsch diesel | 95 % | 95 % |
Farmed wood Fischer-Tropsch diesel | 93 % | 93 % |
Waste wood dimethylether (DME) | 95 % | 95 % |
Farmed wood DME | 92 % | 92 % |
Waste wood methanol | 94 % | 94 % |
Farmed wood methanol | 91 % | 91 % |
The part from renewable sources of methyl-tertio-butyl-ether (MTBE) | Equal to that of the methanol production pathway used |
E = eec + el + ep + etd + eu – esca – eccs – eccr – eee
where
=
total emissions from the use of the fuel;
=
emissions from the extraction or cultivation of raw materials;
=
annualised emissions from carbon stock changes caused by land use change;
=
emissions from processing;
=
emissions from transport and distribution;
=
emissions from the fuel in use;
=
emission savings from soil carbon accumulation via improved agricultural management;
=
emission savings from carbon capture and geological storage;
=
emission savings from carbon capture and replacement; and
=
emission savings from excess electricity from cogeneration.
Emissions from the manufacture of machinery and equipment shall not be taken into account.
SAVING = (EF – EB )/EF
where
=
total emissions from the biofuel; and
=
total emissions from the fossil fuel comparator.
:
1
:
296
:
23
el = (CSR – CSA ) × 3,664 × 1/20 × 1/P – eB (1),
where
=
annualised greenhouse gas emissions from carbon stock change due to land use change (measured as mass of CO2-equivalent per unit biofuel energy);
=
the carbon stock per unit area associated with the reference land use (measured as mass of carbon per unit area, including both soil and vegetation). The reference land use shall be the land use in January 2008 or 20 years before the raw material was obtained, whichever was the later;
=
the carbon stock per unit area associated with the actual land use (measured as mass of carbon per unit area, including both soil and vegetation). In cases where the carbon stock accumulates over more than one year, the value attributed to CSA shall be the estimated stock per unit area after 20 years or when the crop reaches maturity, whichever is the earlier;
=
the productivity of the crop (measured as biofuel energy per unit area per year); and
=
bonus of 29 gCO2eq/MJ biofuel if biomass is obtained from restored degraded land under the conditions provided for in point 8.
was not in use for agriculture or any other activity in January 2008; and
falls into one of the following categories:
severely degraded land, including such land that was formerly in agricultural use;
heavily contaminated land.
The bonus of 29 gCO2eq/MJ shall apply for a period of up to 10 years from the date of conversion of the land to agricultural use, provided that a steady increase in carbon stocks as well as a sizable reduction in erosion phenomena for land falling under (i) are ensured and that soil contamination for land falling under (ii) is reduced.
‘severely degraded land’ means land that, for a significant period of time, has either been significantly salinated or presented significantly low organic matter content and been severely eroded;
‘heavily contaminated land’ means land that is unfit for the cultivation of food and feed due to soil contamination.
Such land shall include land that has been the subject of a Commission decision in accordance with the fourth subparagraph of Article 7c(3).
In accounting for the consumption of electricity not produced within the fuel production plant, the greenhouse gas emission intensity of the production and distribution of that electricity shall be assumed to be equal to the average emission intensity of the production and distribution of electricity in a defined region. As an exception to this rule producers may use an average value for an individual electricity production plant for electricity produced by that plant, if that plant is not connected to the electricity grid.
All co-products, including electricity that does not fall under the scope of point 16, shall be taken into account for the purposes of that calculation, except for agricultural crop residues, including straw, bagasse, husks, cobs and nut shells. Co-products that have a negative energy content shall be considered to have an energy content of zero for the purpose of the calculation.
Wastes, agricultural crop residues, including straw, bagasse, husks, cobs and nut shells, and residues from processing, including crude glycerine (glycerine that is not refined), shall be considered to have zero life-cycle greenhouse gas emissions up to the process of collection of those materials.
In the case of fuels produced in refineries, the unit of analysis for the purposes of the calculation referred to in point 17 shall be the refinery.
a Not including animal oil produced from animal by-products classified as category 3 material in accordance with Regulation (EC) No 1774/2002. | ||
Biofuel production pathway | Typical greenhouse gas emissions(gCO2eq/MJ) | Default greenhouse gas emissions(gCO2eq/MJ) |
---|---|---|
Sugar beet ethanol | 12 | 12 |
Wheat ethanol | 23 | 23 |
Corn (maize) ethanol, Community produced | 20 | 20 |
Sugar cane ethanol | 14 | 14 |
The part from renewable sources of ETBE | Equal to that of the ethanol production pathway used | |
The part from renewable sources of TAEE | Equal to that of the ethanol production pathway used | |
Rape seed biodiesel | 29 | 29 |
Sunflower biodiesel | 18 | 18 |
Soybean biodiesel | 19 | 19 |
Palm oil biodiesel | 14 | 14 |
Waste vegetable or animala oil biodiesel | 0 | 0 |
Hydrotreated vegetable oil from rape seed | 30 | 30 |
Hydrotreated vegetable oil from sunflower | 18 | 18 |
Hydrotreated vegetable oil from palm oil | 15 | 15 |
Pure vegetable oil from rape seed | 30 | 30 |
Biogas from municipal organic waste as compressed natural gas | 0 | 0 |
Biogas from wet manure as compressed natural gas | 0 | 0 |
Biogas from dry manure as compressed natural gas | 0 | 0 |
Biofuel production pathway | Typical greenhouse gas emissions(gCO2eq/MJ) | Default greenhouse gas emissions(gCO2eq/MJ) |
---|---|---|
Sugar beet ethanol | 19 | 26 |
Wheat ethanol (process fuel not specified) | 32 | 45 |
Wheat ethanol (lignite as process fuel in CHP plant) | 32 | 45 |
Wheat ethanol (natural gas as process fuel in conventional boiler) | 21 | 30 |
Wheat ethanol (natural gas as process fuel in CHP plant) | 14 | 19 |
Wheat ethanol (straw as process fuel in CHP plant) | 1 | 1 |
Corn (maize) ethanol, Community produced (natural gas as process fuel in CHP plant) | 15 | 21 |
Sugar cane ethanol | 1 | 1 |
The part from renewable sources of ETBE | Equal to that of the ethanol production pathway used | |
The part from renewable sources of TAEE | Equal to that of the ethanol production pathway used | |
Rape seed biodiesel | 16 | 22 |
Sunflower biodiesel | 16 | 22 |
Soybean biodiesel | 18 | 26 |
Palm oil biodiesel (process not specified) | 35 | 49 |
Palm oil biodiesel (process with methane capture at oil mill) | 13 | 18 |
Waste vegetable or animal oil biodiesel | 9 | 13 |
Hydrotreated vegetable oil from rape seed | 10 | 13 |
Hydrotreated vegetable oil from sunflower | 10 | 13 |
Hydrotreated vegetable oil from palm oil (process not specified) | 30 | 42 |
Hydrotreated vegetable oil from palm oil (process with methane capture at oil mill) | 7 | 9 |
Pure vegetable oil from rape seed | 4 | 5 |
Biogas from municipal organic waste as compressed natural gas | 14 | 20 |
Biogas from wet manure as compressed natural gas | 8 | 11 |
Biogas from dry manure as compressed natural gas | 8 | 11 |
Biofuel production pathway | Typical greenhouse gas emissions(gCO2eq/MJ) | Default greenhouse gas emissions(gCO2eq/MJ) |
---|---|---|
Sugar beet ethanol | 2 | 2 |
Wheat ethanol | 2 | 2 |
Corn (maize) ethanol, Community produced | 2 | 2 |
Sugar cane ethanol | 9 | 9 |
The part from renewable sources of ETBE | Equal to that of the ethanol production pathway used | |
The part from renewable sources of TAEE | Equal to that of the ethanol production pathway used | |
Rape seed biodiesel | 1 | 1 |
Sunflower biodiesel | 1 | 1 |
Soybean biodiesel | 13 | 13 |
Palm oil biodiesel | 5 | 5 |
Waste vegetable or animal oil biodiesel | 1 | 1 |
Hydrotreated vegetable oil from rape seed | 1 | 1 |
Hydrotreated vegetable oil from sunflower | 1 | 1 |
Hydrotreated vegetable oil from palm oil | 5 | 5 |
Pure vegetable oil from rape seed | 1 | 1 |
Biogas from municipal organic waste as compressed natural gas | 3 | 3 |
Biogas from wet manure as compressed natural gas | 5 | 5 |
Biogas from dry manure as compressed natural gas | 4 | 4 |
Biofuel production pathway | Typical greenhouse gas emissions(gCO2eq/MJ) | Default greenhouse gas emissions(gCO2eq/MJ) |
---|---|---|
Sugar beet ethanol | 33 | 40 |
Wheat ethanol (process fuel not specified) | 57 | 70 |
Wheat ethanol (lignite as process fuel in CHP plant) | 57 | 70 |
Wheat ethanol (natural gas as process fuel in conventional boiler) | 46 | 55 |
Wheat ethanol (natural gas as process fuel in CHP plant) | 39 | 44 |
Wheat ethanol (straw as process fuel in CHP plant) | 26 | 26 |
Corn (maize) ethanol, Community produced (natural gas as process fuel in CHP plant) | 37 | 43 |
Sugar cane ethanol | 24 | 24 |
The part from renewable sources of ETBE | Equal to that of the ethanol production pathway used | |
The part from renewable sources of TAEE | Equal to that of the ethanol production pathway used | |
Rape seed biodiesel | 46 | 52 |
Sunflower biodiesel | 35 | 41 |
Soybean biodiesel | 50 | 58 |
Palm oil biodiesel (process not specified) | 54 | 68 |
Palm oil biodiesel (process with methane capture at oil mill) | 32 | 37 |
Waste vegetable or animal oil biodiesel | 10 | 14 |
Hydrotreated vegetable oil from rape seed | 41 | 44 |
Hydrotreated vegetable oil from sunflower | 29 | 32 |
Hydrotreated vegetable oil from palm oil (process not specified) | 50 | 62 |
Hydrotreated vegetable oil from palm oil (process with methane capture at oil mill) | 27 | 29 |
Pure vegetable oil from rape seed | 35 | 36 |
Biogas from municipal organic waste as compressed natural gas | 17 | 23 |
Biogas from wet manure as compressed natural gas | 13 | 16 |
Biogas from dry manure as compressed natural gas | 12 | 15 |
Biofuel production pathway | Typical greenhouse gas missions(gCO2eq/MJ) | Default greenhouse gas emissions(gCO2eq/MJ) |
---|---|---|
Wheat straw ethanol | 3 | 3 |
Waste wood ethanol | 1 | 1 |
Farmed wood ethanol | 6 | 6 |
Waste wood Fischer-Tropsch diesel | 1 | 1 |
Farmed wood Fischer-Tropsch diesel | 4 | 4 |
Waste wood DME | 1 | 1 |
Farmed wood DME | 5 | 5 |
Waste wood methanol | 1 | 1 |
Farmed wood methanol | 5 | 5 |
The part from renewable sources of MTBE | Equal to that of the methanol production pathway used |
Biofuel production pathway | Typical greenhouse gas emissions(gCO2eq/MJ) | Default greenhouse gas emissions(gCO2eq/MJ) |
---|---|---|
Wheat straw ethanol | 5 | 7 |
Wood ethanol | 12 | 17 |
Wood Fischer-Tropsch diesel | 0 | 0 |
Wood DME | 0 | 0 |
Wood methanol | 0 | 0 |
The part from renewable sources of MTBE | Equal to that of the methanol production pathway used |
Biofuel production pathway | Typical greenhouse gas emissions(gCO2eq/MJ) | Default greenhouse gas emissions(gCO2eq/MJ) |
---|---|---|
Wheat straw ethanol | 2 | 2 |
Waste wood ethanol | 4 | 4 |
Farmed wood ethanol | 2 | 2 |
Waste wood Fischer-Tropsch diesel | 3 | 3 |
Farmed wood Fischer-Tropsch diesel | 2 | 2 |
Waste wood DME | 4 | 4 |
Farmed wood DME | 2 | 2 |
Waste wood methanol | 4 | 4 |
Farmed wood methanol | 2 | 2 |
The part from renewable sources of MTBE | Equal to that of the methanol production pathway used |
Biofuel production pathway | Typical greenhouse gas emissions(gCO2eq/MJ) | Default greenhouse gas emissions(gCO2eq/MJ) |
---|---|---|
Wheat straw ethanol | 11 | 13 |
Waste wood ethanol | 17 | 22 |
Farmed wood ethanol | 20 | 25 |
Waste wood Fischer-Tropsch diesel | 4 | 4 |
Farmed wood Fischer-Tropsch diesel | 6 | 6 |
Waste wood DME | 5 | 5 |
Farmed wood DME | 7 | 7 |
Waste wood methanol | 5 | 5 |
Farmed wood methanol | 7 | 7 |
The part from renewable sources of MTBE | Equal to that of the methanol production pathway used” |
The quotient obtained by dividing the molecular weight of CO2 (44,010 g/mol) by the molecular weight of carbon (12,011 g/mol) is equal to 3,664.