Division DEFINITIONS
United Kingdom
For the purposes of these BAT conclusions, the following definitions apply:
| Commission Implementing Decision 2012/249/EU of 7 May 2012 concerning the determination of start-up and shut-down periods for the purposes of Directive 2010/75/EU of the European Parliament and of the Council on industrial emissions (OJ L 123, 9.5.2012, p. 44). | |
| Term used | Definition |
|---|---|
| General terms | |
| Boiler | Any combustion plant with the exception of engines, gas turbines, and process furnaces or heaters |
| Combined-cycle gas turbine (CCGT) | A CCGT is a combustion plant where two thermodynamic cycles are used (i.e. Brayton and Rankine cycles). In a CCGT, heat from the flue-gas of a gas turbine (operating according to the Brayton cycle to produce electricity) is converted to useful energy in a heat recovery steam generator (HRSG), where it is used to generate steam, which then expands in a steam turbine (operating according to the Rankine cycle to produce additional electricity). For the purpose of these BAT conclusions, a CCGT includes configurations both with and without supplementary firing of the HRSG |
| Combustion plant | Any technical apparatus in which fuels are oxidised in order to use the heat thus generated. For the purposes of these BAT conclusions, a combination formed of:
is considered as a single combustion plant. For calculating the total rated thermal input of such a combination, the capacities of all individual combustion plants concerned, which have a rated thermal input of at least 15 MW, shall be added together |
| Combustion unit | Individual combustion plant |
| Continuous measurement | Measurement using an automated measuring system permanently installed on site |
| Direct discharge | Discharge (to a receiving water body) at the point where the emission leaves the installation without further downstream treatment |
| Flue-gas desulphurisation (FGD) system | System composed of one or a combination of abatement technique(s) whose purpose is to reduce the level of SOX emitted by a combustion plant |
| Flue-gas desulphurisation (FGD) system — existing | A flue-gas desulphurisation (FGD) system that is not a new FGD system |
| Flue-gas desulphurisation (FGD) system — new | Either a flue-gas desulphurisation (FGD) system in a new plant or a FGD system that includes at least one abatement technique introduced or completely replaced in an existing plant following the publication of these BAT conclusions |
| Gas oil | Any petroleum-derived liquid fuel falling within CN code 2710 19 25, 2710 19 29, 2710 19 47, 2710 19 48, 2710 20 17 or 2710 20 19. Or any petroleum-derived liquid fuel of which less than 65 vol-% (including losses) distils at 250 °C and of which at least 85 vol-% (including losses) distils at 350 °C by the ASTM D86 method |
| Heavy fuel oil (HFO) | Any petroleum-derived liquid fuel falling within CN code 2710 19 51 to 2710 19 68, 2710 20 31, 2710 20 35, 2710 20 39. Or any petroleum-derived liquid fuel, other than gas oil, which, by reason of its distillation limits, falls within the category of heavy oils intended for use as fuel and of which less than 65 vol-% (including losses) distils at 250 °C by the ASTM D86 method. If the distillation cannot be determined by the ASTM D86 method, the petroleum product is also categorised as a heavy fuel oil |
| Net electrical efficiency (combustion unit and IGCC) | Ratio between the net electrical output (electricity produced on the high-voltage side of the main transformer minus the imported energy — e.g. for auxiliary systems' consumption) and the fuel/feedstock energy input (as the fuel/feedstock lower heating value) at the combustion unit boundary over a given period of time |
| Net mechanical energy efficiency | Ratio between the mechanical power at load coupling and the thermal power supplied by the fuel |
| Net total fuel utilisation (combustion unit and IGCC) | Ratio between the net produced energy (electricity, hot water, steam, mechanical energy produced minus the imported electrical and/or thermal energy (e.g. for auxiliary systems' consumption)) and the fuel energy input (as the fuel lower heating value) at the combustion unit boundary over a given period of time |
| Net total fuel utilisation (gasification unit) | Ratio between the net produced energy (electricity, hot water, steam, mechanical energy produced, and syngas (as the syngas lower heating value) minus the imported electrical and/or thermal energy (e.g. for auxiliary systems' consumption)) and the fuel/feedstock energy input (as the fuel/feedstock lower heating value) at the gasification unit boundary over a given period of time |
| Operated hours | The time, expressed in hours, during which a combustion plant, in whole or in part, is operated and is discharging emissions to air, excluding start-up and shutdown periods |
| Periodic measurement | Determination of a measurand (a particular quantity subject to measurement) at specified time intervals |
| Plant — existing | A combustion plant that is not a new plant |
| Plant — new | A combustion plant first permitted at the installation following the publication of these BAT conclusions or a complete replacement of a combustion plant on the existing foundations following the publication of these BAT conclusions |
| Post-combustion plant | System designed to purify the flue-gases by combustion which is not operated as an independent combustion plant, such as a thermal oxidiser (i.e. tail gas incinerator), used for the removal of the pollutant(s) (e.g. VOC) content from the flue-gas with or without the recovery of the heat generated therein. Staged combustion techniques, where each combustion stage is confined within a separate chamber, which may have distinct combustion process characteristics (e.g. fuel to air ratio, temperature profile), are considered integrated in the combustion process and are not considered post-combustion plants. Similarly, when gases generated in a process heater/furnace or in another combustion process are subsequently oxidised in a distinct combustion plant to recover their energetic value (with or without the use of auxiliary fuel) to produce electricity, steam, hot water/oil or mechanical energy, the latter plant is not considered a post-combustion plant |
| Predictive emissions monitoring system (PEMS) | System used to determine the emissions concentration of a pollutant from an emission source on a continuous basis, based on its relationship with a number of characteristic continuously monitored process parameters (e.g. the fuel gas consumption, the air to fuel ratio) and fuel or feed quality data (e.g. the sulphur content) |
| Process fuels from the chemical industry | Gaseous and/or liquid by-products generated by the (petro-)chemical industry and used as non-commercial fuels in combustion plants |
| Process furnaces or heaters | Process furnaces or heaters are:
As a consequence of the application of good energy recovery practices, process heaters/furnaces may have an associated steam/electricity generation system. This is considered to be an integral design feature of the process heater/furnace that cannot be considered in isolation |
| Refinery fuels | Solid, liquid or gaseous combustible material from the distillation and conversion steps of the refining of crude oil. Examples are refinery fuel gas (RFG), syngas, refinery oils, and pet coke |
| Residues | Substances or objects generated by the activities covered by the scope of this document, as waste or by-products |
| Start-up and shut-down period | The time period of plant operation as determined pursuant to the provisions of Commission Implementing Decision 2012/249/EUf1 |
| Unit — existing | A combustion unit that is not a new unit |
| Unit- new | A combustion unit first permitted at the combustion plant following the publication of these BAT conclusions or a complete replacement of a combustion unit on the existing foundations of the combustion plant following the publication of these BAT conclusions |
| Valid (hourly average) | An hourly average is considered valid when there is no maintenance or malfunction of the automated measuring system |
| Term used | Definition |
|---|---|
| Pollutants/parameters | |
| As | The sum of arsenic and its compounds, expressed as As |
| C3 | Hydrocarbons having a carbon number equal to three |
| C4+ | Hydrocarbons having a carbon number of four or greater |
| Cd | The sum of cadmium and its compounds, expressed as Cd |
| Cd+Tl | The sum of cadmium, thallium and their compounds, expressed as Cd+Tl |
| CH4 | Methane |
| CO | Carbon monoxide |
| COD | Chemical oxygen demand. Amount of oxygen needed for the total oxidation of the organic matter to carbon dioxide |
| COS | Carbonyl sulphide |
| Cr | The sum of chromium and its compounds, expressed as Cr |
| Cu | The sum of copper and its compounds, expressed as Cu |
| Dust | Total particulate matter (in air) |
| Fluoride | Dissolved fluoride, expressed as F– |
| H2S | Hydrogen sulphide |
| HCl | All inorganic gaseous chlorine compounds, expressed as HCl |
| HCN | Hydrogen cyanide |
| HF | All inorganic gaseous fluorine compounds, expressed as HF |
| Hg | The sum of mercury and its compounds, expressed as Hg |
| N2O | Dinitrogen monoxide (nitrous oxide) |
| NH3 | Ammonia |
| Ni | The sum of nickel and its compounds, expressed as Ni |
| NOX | The sum of nitrogen monoxide (NO) and nitrogen dioxide (NO2), expressed as NO2 |
| Pb | The sum of lead and its compounds, expressed as Pb |
| PCDD/F | Polychlorinated dibenzo-p-dioxins and -furans |
| RCG | Raw concentration in the flue-gas. Concentration of SO2 in the raw flue-gas as a yearly average (under the standard conditions given under General considerations) at the inlet of the SOX abatement system, expressed at a reference oxygen content of 6 vol-% O2 |
| Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V | The sum of antimony, arsenic, lead, chromium, cobalt, copper, manganese, nickel, vanadium and their compounds, expressed as Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V |
| SO2 | Sulphur dioxide |
| SO3 | Sulphur trioxide |
| SOX | The sum of sulphur dioxide (SO2) and sulphur trioxide (SO3), expressed as SO2 |
| Sulphate | Dissolved sulphate, expressed as SO4 2– |
| Sulphide, easily released | The sum of dissolved sulphide and of those undissolved sulphides that are easily released upon acidification, expressed as S2– |
| Sulphite | Dissolved sulphite, expressed as SO3 2– |
| TOC | Total organic carbon, expressed as C (in water) |
| TSS | Total suspended solids. Mass concentration of all suspended solids (in water), measured via filtration through glass fibre filters and gravimetry |
| TVOC | Total volatile organic carbon, expressed as C (in air) |
| Zn | The sum of zinc and its compounds, expressed as Zn |
Annotations
Footnotes
- f1
-
Commission Implementing Decision 2012/249/EU of 7 May 2012 concerning the determination of start-up and shut-down periods for the purposes of Directive 2010/75/EU of the European Parliament and of the Council on industrial emissions (OJ L 123, 9.5.2012, p. 44).