Commission Implementing Regulation (EU) 2018/2066Show full title

1. DEFINITION OF TIERS FOR ACTIVITY DATA U.K.

The uncertainty thresholds in Table 1 shall apply to tiers relevant to activity data requirements in accordance with point (a) of Article 28(1) and the first subparagraph of Article 29(2), and Annex IV, of this Regulation. The uncertainty thresholds shall be interpreted as maximum permissible uncertainties for the determination of source streams over a reporting period.

Where Table 1 does not include activities listed in Annex I to Directive 2003/87/EC and the mass balance is not applied, the operator shall use the tiers listed in Table 1 under ‘Combustion of fuels and fuels used as process input’ for those activities.

Table 1

Tiers for activity data (maximum permissible uncertainty for each tier)

a For monitoring emissions from catalytic cracker regeneration (other catalyst regeneration and flexi-cokers) in mineral oil refineries, the required uncertainty is related to the total uncertainty of all emissions from that source.
b Amount [t] of CKD or bypass dust (where relevant) leaving the kiln system over a reporting period estimated using industry best practice guidelines.
Activity/source stream type	Parameter to which the uncertainty is applied	Tier 1	Tier 2	Tier 3	Tier 4
Combustion of fuels and fuels used as process input
Commercial standard fuels	Amount of fuel [t] or [Nm3]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Other gaseous and liquid fuels	Amount of fuel [t] or [Nm3]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Solid fuels	Amount of fuel [t]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Flaring	Amount of flare gas [Nm3]	± 17,5 %	± 12,5 %	± 7,5 %
Scrubbing: carbonate (Method A)	Amount carbonate consumed [t]	± 7,5 %
Scrubbing: gypsum (Method B)	Amount gypsum produced [t]	± 7,5 %
Scrubbing: urea	Amount urea consumed	± 7,5 %
Refining of mineral oil
Catalytic cracker regenerationa	Uncertainty requirements apply separately for each emission source	± 10 %	± 7,5 %	± 5 %	± 2,5 %
Production of coke
Mass balance methodology	Each input and output material [t]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Metal ore roasting and sintering
Carbonate input and process residues	Carbonate input material and process residues [t]	± 5 %	± 2,5 %
Mass balance methodology	Each input and output material [t]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Production of iron and steel
Fuel as process input	Each mass flow into and from the installation [t]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Mass balance methodology	Each input and output material [t]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Production of cement clinker
Kiln input based (Method A)	Each relevant kiln input [t]	± 7,5 %	± 5 %	± 2,5 %
Clinker output (Method B)	Clinker produced [t]	± 5 %	± 2,5 %
CKD	CKD or bypass dust [t]	n.a.b	± 7,5 %
Non-carbonate carbon	Each raw material [t]	± 15 %	± 7,5 %
Production of lime and calcination of dolomite and magnesite
Carbonates and other process materials (Method A)	Each relevant kiln input [t]	± 7,5 %	± 5 %	± 2,5 %
Alkali earth oxide (Method B)	Lime produced [t]	± 5 %	± 2,5 %
Kiln dust (Method B)	Kiln dust [t]	n.a.b	± 7,5 %
Manufacture of glass and mineral wool
Carbonates and other process materials (input)	Each carbonate raw material or additives associated with CO2 emissions [t]	± 2,5 %	± 1,5 %
Manufacture of ceramic products
Carbon inputs (Method A)	Each carbonate raw material or additive associated with CO2 emissions [t]	± 7,5 %	± 5 %	± 2,5 %
Alkali oxide (Method B)	Gross production including rejected products and cullet from the kilns and shipment [t]	± 7,5 %	± 5 %	± 2,5 %
Scrubbing	Dry CaCO3 consumed [t]	± 7,5 %
Production of pulp and paper
Make up chemicals	Amount of CaCO3 and Na2CO3 [t]	± 2,5 %	± 1,5 %
Production of carbon black
Mass balance methodology	Each input and output material [t]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Production of ammonia
Fuel as process input	Amount fuel used as process input [t] or [Nm3]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Production of hydrogen and synthesis gas
Fuel as process input	Amount fuel used as process input for hydrogen production [t] or [Nm3]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Mass balance methodology	Each input and output material [t]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Production of bulk organic chemicals
Mass balance methodology	Each input and output material [t]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Production or processing of ferrous and non-ferrous metals, including secondary aluminium
Process emissions	Each input material or process residue used as input material in the process [t]	± 5 %	± 2,5 %
Mass balance methodology	Each input and output material [t]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
Primary aluminium production
Mass balance methodology	Each input and output material [t]	± 7,5 %	± 5 %	± 2,5 %	± 1,5 %
PFC emissions (slope method)	primary aluminium production in [t], anode effect minutes in [number anode effects/cell day] and [anode effect minutes/ occurrence]	± 2,5 %	± 1,5 %
PFC emissions (overvoltage method)	primary aluminium production in [t], anode effect overvoltage [mV] and current efficiency [-]	± 2,5 %	± 1,5 %