Division DEFINITIONS
United Kingdom
For the purpose of these BAT conclusions, the following definitions apply:
| Term used | Definition |
|---|---|
| Unit | A segment/subpart of the installation in which a specific processing operation is conducted |
| New unit | A unit first permitted on the site of the installation following the publication of these BAT conclusions or a complete replacement of a unit on the existing foundations of the installation following the publication of these BAT conclusions |
| Existing unit | A unit which is not a new unit |
| Process off-gas | The collected gas generated by a process which must be treated e.g. in an acid gas removal unit and a sulphur recovery unit (SRU) |
| Flue-gas | The exhaust gas exiting a unit after an oxidation step, generally combustion (e.g. regenerator, Claus unit) |
| Tail gas | Common name of the exhaust gas from an SRU (generally Claus process) |
| VOC | Volatile organic compounds as defined in Article 3(45) of Directive 2010/75/EU |
| NMVOC | VOC excluding methane |
| Diffuse VOC emissions | Non-channelled VOC emissions that are not released via specific emission points such as stacks. They can result from ‘area’ sources (e.g. tanks) or ‘point’ sources (e.g. pipe flanges) |
| NOX expressed as NO2 | The sum of nitrogen oxide (NO) and nitrogen dioxide (NO2) expressed as NO2 |
| SOX expressed as SO2 | The sum of sulphur dioxide (SO2) and sulphur trioxide (SO3) expressed as SO2 |
| H2S | Hydrogen sulphide. Carbonyl sulphide and mercaptan are not included |
| Hydrogen chloride expressed as HCl | All gaseous chlorides expressed as HCl |
| Hydrogen fluoride expressed as HF | All gaseous fluorides expressed as HF |
| FCC unit | Fluid catalytic cracking: a conversion process for upgrading heavy hydrocarbons, using heat and a catalyst to break larger hydrocarbon molecules into lighter molecules |
| SRU | Sulphur recovery unit. See definition in Section 1.20.3 |
| Refinery fuel | 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 and refinery oils, pet coke |
| RFG | Refinery fuel gas: off-gases from distillation or conversion units used as a fuel |
| Combustion unit | Unit burning refinery fuels alone or with other fuels for the production of energy at the refinery site, such as boilers (except CO boilers), furnaces, and gas turbines. |
| Continuous measurement | Measurement using an ‘automated measuring system’ (AMS) or a ‘continuous emission monitoring system’ (CEMS) permanently installed on site |
| Periodic measurement | Determination of a measurand at specified time intervals using manual or automated reference methods |
| Indirect monitoring of emissions to air | Estimation of the emissions concentration in the flue-gas of a pollutant obtained through an appropriate combination of measurements of surrogate parameters (such as O2 content, sulphur or nitrogen content in the feed/fuel), calculations and periodic stack measurements. The use of emission ratios based on S content in the fuel is one example of indirect monitoring. Another example of indirect monitoring is the use of PEMS |
| Predictive Emissions monitoring system (PEMS) | System to determine the emissions concentration of a pollutant based on its relationship with a number of characteristic continuously monitored process parameters (e.g. fuel-gas consumption, air/fuel ratio) and fuel or feed quality data (e.g. the sulphur content) of an emission source |
| Volatile liquid hydrocarbon compounds | Petroleum derivatives with a Reid vapour pressure (RVP) of more than 4 kPa, such as naphtha and aromatics |
| Recovery rate | Percentage of NMVOC recovered from the streams conveyed into a vapour recovery unit (VRU) |
- 1.1General BAT conclusions for the refining of mineral oil and gas
- 1.2BAT conclusions for the alkylation process
- 1.3BAT conclusions for base oil production processes
- 1.4BAT conclusions for the bitumen production process
- 1.5BAT conclusions for the fluid catalytic cracking process
- 1.6BAT conclusions for the catalytic reforming process
- 1.7BAT conclusions for the coking processes
- 1.8BAT conclusions for the desalting process
- 1.9BAT conclusions for the combustion units
- 1.10BAT conclusions for the etherification process
- 1.11BAT conclusions for the isomerisation process
- 1.12BAT conclusions for the natural gas refinery
- 1.13BAT conclusions for the distillation process
- 1.14BAT conclusions for the products treatment process
- 1.15BAT conclusions for storage and handling processes
- 1.16BAT conclusions for visbreaking and other thermal processes
- 1.17BAT conclusions for waste gas sulphur treatment
- 1.18BAT conclusions for flares
- 1.19BAT conclusions for integrated emission management