LegalizeCommission Delegated Regulation (EU) 2015/2402 of 12 October 2015 reviewing harmonised efficiency reference values for separate production of electricity and heat in application of Directive 2012/27/EU of the European Parliament and of the Council and repealing Commission Implementing Decision 2011/877/EU
Article 1
Establishment of the harmonised efficiency reference values
The harmonised efficiency reference values for separate production of electricity and heat shall be those set out in Annexes I and II respectively.
Article 2
Correction factors for the harmonised efficiency reference values for separate production of electricity
If on the territory of a Member State official meteorological data show differences in the annual ambient temperature of 5 °C or more, that Member State may, subject to notification to the Commission, use several climate zones for the purpose of the first subparagraph using the method set out in Annex III.
Article 3
Application of the harmonised efficiency reference values for the separate production of electricity
Article 4
Application of the harmonised efficiency reference values for the separate production of heat
Article 5
Retrofitting of a cogeneration unit
If the investment cost relating to the retrofitting of a cogeneration unit exceeds 50 % of the investment cost for a new comparable cogeneration unit, the calendar year during which the retrofitted cogeneration unit first produces electricity shall be considered as the year of construction of the retrofitted cogeneration unit for the purpose of Articles 3 and 4.
Article 6
Fuel mix
If the cogeneration unit is operated with more than one kind of fuel, the harmonised efficiency reference values for separate production shall be applied proportionally to the weighted mean of the energy input of the various fuels.
Article 7
Repeal
Decision 2011/877/EU is repealed.
Article 8
Entry into force and application
This Regulation shall enter into force on the first day following that of its publication in the Official Journal of the European Union.
This Regulation shall apply from 1 January 2016.
This Regulation shall be binding in its entirety and directly applicable in all Member States.
ANNEX I
In the following table, the harmonised efficiency (%) reference values for separate production of electricity are based on net calorific value and standard atmospheric ISO conditions (15 °C ambient temperature, 1,013 bar, 60 % relative humidity):
| Category | Energy source | Year of construction | |||
|---|---|---|---|---|---|
| Before 2016 | 2016–2023 | From 2024 | |||
| Solids | S1 | Hard coal including anthracite, bituminous coal, sub-bituminous coal, coke, semi-coke, pet coke | 44,2 | 44,2 | 53,0 |
| S2 | Lignite, lignite briquettes, oil shale | 41,8 | 41,8 | 53,0 | |
| S3 | Peat, peat briquettes | 39,0 | 39,0 | 53,0 | |
| S4 | Dry biomass including wood and other solid biomass including wood pellets and briquettes, dried woodchips, clean and dry waste wood, nut shells and olive and other stones | 33,0 | 37,0 | 37,0 | |
| S5 | Other solid biomass including all wood not included under S4 and black and brown liquor. | 25,0 | 30,0 | 30,0 | |
| S6 | Municipal and industrial waste (non-renewable, of non-biological origin such as plastics, rubber and other synthetic materials) and renewable/bio-degradable waste | 25,0 | 25,0 | 25,0 | |
| Liquids | L7 | Heavy fuel oil, gas/diesel oil, other oil products | 44,2 | 44,2 | 53,0 |
| L8 | Bio-liquids including bio-methanol, bioethanol, bio-butanol, biodiesel, other biofuels and all e-liquids | 44,2 | 44,2 | 44,2 | |
| L9 | Waste liquids including biodegradable and non-renewable waste (including tallow, fat and spent grain). | 25,0 | 29,0 | 29,0 | |
| Gaseous | G10 | Natural gas, LPG, LNG and biomethane | 52,5 | 53,0 | 53,0 |
| G11A | Traded hydrogen (1) | 44,2 | 44,2 | 53,0 | |
| G11B | Refinery gases, synthesis gas, hydrogen (by-product), e-gases (2) | 44,2 | 44,2 | 44,2 | |
| G12 | Biogas produced from anaerobic digestion, landfill, and sewage treatment | 42,0 | 42,0 | 42,0 | |
| G13 | Coke oven gas, blast furnace gas, mining gas, and other recovered gases (excluding refinery gas) | 35,0 | 35,0 | 35,0 | |
| Other | O14A | Waste heat, including process exhaust gases, product from exothermic chemical reactions (input temperature > 200 °C) | 30,0 | 30,0 | |
| O14B | Waste heat, including process exhaust gases, product from exothermic chemical reactions (input temperature < 200 °C) | 30,0 | 20,0 | ||
| O15 | Nuclear | 33,0 | 33,0 | ||
| O16 | Solar thermal | 30,0 | 30,0 | ||
| O17 | Geothermal | 19,5 | 19,5 | ||
| O18 | Other fuels not mentioned above | 30,0 | 30,0 | ||
| (1) Hydrogen sold from its supplier to a cogeneration unit operator. (2) E-gases are understood as gaseous synthetic fuel originating from renewable hydrogen and carbon dioxide captured either from a concentrated source, such as flue gases from an industrial site, or from the air. |
ANNEX II
In the following table the harmonised efficiency (%) reference values for separate production of heat are based on net calorific value and standard atmospheric ISO conditions (15 °C ambient temperature, 1,013 bar, 60 % relative humidity):
| Category | Energy source | Year of construction | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|
| Before 2016 | 2016–2023 | From 2024 | |||||||||
| Hot water | Steam (1) | Direct use of exhaust gases (2) | Hot water | Steam (1) | Direct use of exhaust gases (2) | Hot water | Steam (1) | Direct use of exhaust gases (2) | |||
| Solids | S1 | Hard coal including anthracite, bituminous coal, sub-bituminous coal, coke, semi-coke, pet coke | 88 | 83 | 80 | 88 | 83 | 80 | 92 | 87 | 84 |
| S2 | Lignite, lignite briquettes, oil shale | 86 | 81 | 78 | 86 | 81 | 78 | 92 | 87 | 84 | |
| S3 | Peat, peat briquettes | 86 | 81 | 78 | 86 | 81 | 78 | 92 | 87 | 84 | |
| S4 | Dry biomass including wood and other solid biomass including wood pellets and briquettes, dried woodchips, clean and dry waste wood, nut shells and olive and other stones | 86 | 81 | 78 | 86 | 81 | 78 | 86 | 81 | 78 | |
| S5 | Other solid biomass including all wood not included under S4 and black and brown liquor. | 80 | 75 | 72 | 80 | 75 | 72 | 80 | 75 | 72 | |
| S6 | Municipal and industrial waste (non-renewable, of non-biological origin such as plastics, rubber and other synthetic materials) and renewable/bio-degradable waste | 80 | 75 | 72 | 80 | 75 | 72 | 80 | 75 | 72 | |
| Liquids | L7 | Heavy fuel oil, gas/diesel oil, other oil products | 89 | 84 | 81 | 85 | 80 | 77 | 92 | 87 | 84 |
| L8 | Bio-liquids including bio-methanol, bioethanol, bio-butanol, biodiesel, other biofuels and all e-liquids | 89 | 84 | 81 | 85 | 80 | 77 | 85 | 80 | 77 | |
| L9 | Waste liquids including biodegradable and non-renewable waste (including tallow, fat and spent grain). | 80 | 75 | 72 | 75 | 70 | 67 | 75 | 70 | 67 | |
| Gaseous | G10 | Natural gas, LPG, LNG and biomethane | 90 | 85 | 82 | 92 | 87 | 84 | 92 | 87 | 84 |
| G11A | Traded hydrogen | 89 | 84 | 81 | 90 | 85 | 82 | 92 | 87 | 84 | |
| G11B | Refinery gases, synthesis gas, hydrogen (by-product), e-gases | 89 | 84 | 81 | 90 | 85 | 82 | 90 | 85 | 82 | |
| G12 | Biogas produced from anaerobic digestion, landfill, and sewage treatment | 70 | 65 | 62 | 80 | 75 | 72 | 80 | 75 | 72 | |
| G13 | Coke oven gas, blast furnace gas, mining gas, and other recovered gases (excluding refinery gas) | 80 | 75 | 72 | 80 | 75 | 72 | 80 | 75 | 72 | |
| Other | O14A | Waste heat, including process exhaust gases, product from exothermic chemical reactions (input temperature > 200 °C) | — | — | — | 92 | 87 | — | 92 | 87 | — |
| O14B | Waste heat, including process exhaust gases, product from exothermic chemical reactions (input temperature < 200 °C) | — | — | — | 92 | 87 | — | 92 | 87 | — | |
| O15 | Nuclear | — | — | — | 92 | 87 | — | 92 | 87 | — | |
| O16 | Solar thermal | — | — | — | 92 | 87 | — | 92 | 87 | — | |
| O17 | Geothermal | — | — | — | 92 | 87 | — | 92 | 87 | — | |
| O18 | Other fuels not mentioned above | — | — | — | 92 | 87 | — | 92 | 87 | — | |
| (1) Where steam plants do not account for the condensate return in their calculation of CHP heat efficiencies, the steam efficiencies set out in the table should be increased by 5 percentage points. (2) Values for direct heat should be used where the temperature reaches 250 °C or higher. |
ANNEX III
Correction factors relating to the average climatic situation and method for establishing climate zones for the application of the harmonised efficiency reference values for separate production of electricity
(referred to in Article 2(1))
(a) Correction factors relating to the average climatic situation
Ambient temperature correction is based on the difference between the annual average temperature in a Member State and standard atmospheric ISO conditions (15 °C).
The correction will be as follows:
Example:
When the average annual temperature in a Member State is 10 °C, the reference value of a cogeneration unit in that Member State has to be increased by 0,5 %-points.
(b) Ambient temperature correction applies only to gaseous fuels (G10, G11, G12, G13).
(c) The borders of each climate zone will be constituted by isotherms (in full degrees Celsius) of the annual average ambient temperature which differ at least 4 °C. The temperature difference between the average annual ambient temperatures applied in adjacent climate zones will be at least 4 °C. Example: If, for example, for a given Member State the average annual ambient temperature is 12 °C in a certain location and 6 °C in a different location within the Member State, then the Member State has the option to introduce two climate zones, separated by an isotherm of 9 °C: A first climate zone between the isotherms of 9 °C and 13 °C (4 °C difference) with an average annual ambient temperature of 11 °C, and A second climate zone between the isotherms of 5 °C and 9 °C with an average annual ambient temperature of 7 °C.
ANNEX IV
| Connection voltage level | Correction factor (Off-site) | Correction factor (On-site) |
|---|---|---|
| ≥ 345 kV | 1 | 0,976 |
| ≥ 200 – < 345 kV | 0,972 | 0,963 |
| ≥ 100 – < 200 kV | 0,963 | 0,951 |
| ≥ 50 – < 100 kV | 0,952 | 0,936 |
| ≥ 12 – < 50 kV | 0,935 | 0,914 |
| ≥ 0,45 – < 12kV | 0,918 | 0,891 |
| < 0,45 kV | 0,888 | 0,851 |
Example:
A 100 kWel cogeneration unit with a reciprocating engine driven with natural gas generates electricity at 380 V. Of this, 85 % is used for own consumption and 15 % is fed into the grid. The plant was constructed in 2020. The annual ambient temperature is 15 °C (so no climatic correction is necessary).
After the grid loss correction the resulting efficiency reference value for the separate production of electricity in this cogeneration unit would be, on the basis of the weighted mean of the factors in this Annex:
Ref Εη = 53 % × (0,851 × 85 % + 0,888 × 15 %) = 45,4 %
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