{
  "url": "https://openlegislation.uk/eu-decision-2012-134/annex/division-5/division-1.2/division-1.2.2/division-17",
  "json_url": "https://openlegislation.uk/eu-decision-2012-134/annex/division-5/division-1.2/division-1.2.2/division-17.json",
  "legislation": "eudn/2012/134",
  "legislation_title": "Commission Implementing Decision of 28 February 2012 establishing the best available techniques (BAT) conclusions under Directive 2010/75/EU of the European Parliament and of the Council on industrial emissions for the manufacture of glass (notified under document C(2012) 865) (Text with EEA relevance) (2012/134/EU)",
  "legislation_url": "https://openlegislation.uk/eu-decision-2012-134",
  "path": "annex/division/5/division/1.2/division/1.2.2/division/17",
  "kind": "division",
  "number": "17",
  "heading": null,
  "text": "BAT is to reduce NOX emissions from the melting furnace by using one or a combination of the following techniques:\nI.. primary techniques, such as:\nA description of the techniques is given in Section 1.10.2.\nTechnique\nApplicability\n(i) Combustion modifications\n(a)\nReduction of air/fuel ratio\nApplicable to air/fuel conventional furnaces.\nFull benefits are achieved at normal or complete furnace rebuild, when combined with optimum furnace design and geometry\n(b)\nReduced combustion air temperature\nApplicable only under installation-specific circumstances due to a lower furnace efficiency and higher fuel demand (i.e. use of recuperative furnaces in place of regenerative furnaces)\n(c)\nStaged combustion:\nAir staging\nFuel staging\nFuel staging is applicable to most conventional air/fuel furnaces.\nAir staging has very limited applicability due to its technical complexity\n(d)\nFlue-gas recirculation\nThe applicability of this technique is limited to the use of special burners with automatic recirculation of the waste gas\n(e)\nLow-NOX burners\nThe technique is generally applicable.\nThe achieved environmental benefits are generally lower for applications to cross-fired, gas-fired furnaces due to technical constraints and a lower degree of flexibility of the furnace.\nFull benefits are achieved at normal or complete furnace rebuild, when combined with optimum furnace design and geometry\n(f)\nFuel choice\nThe applicability is limited by the constraints associated with the availability of different types of fuel, which may be impacted by the energy policy of the Member State\n(ii)\nSpecial furnace design\nThe applicability is limited to batch formulations that contain high levels of external cullet (> 70 %).\nThe application requires a complete rebuild of the melting furnace.\nThe shape of the furnace (long and narrow) may pose space restrictions\n(iii)\nElectric melting\nNot applicable for large volume glass productions (> 300 tonnes/day).\nNot applicable for productions requiring large pull variations.\nThe implementation requires a complete furnace rebuild\n(iv)\nOxy-fuel melting\nThe maximum environmental benefits are achieved for applications at the time of a complete furnace rebuild\nII.. secondary techniques, such as:\nA description of the techniques is given in Section 1.10.2.\nTechnique\nApplicability\n(i)\nSelective catalytic reduction (SCR)\nThe application may require an upgrade of the dust abatement system in order to guarantee a dust concentration of below 10 – 15 mg/Nm3 and a desulphurisation system for the removal of SOX emissions.\nDue to the optimum operating temperature window, the applicability is limited to the use of electrostatic precipitators. In general, the technique is not used with a bag filter system because the low operating temperature, in the range of 180 – 200 °C, would require reheating of the waste gases.\nThe implementation of the technique may require significant space availability\n(ii)\nSelective non-catalytic reduction(SNCR)\nThe technique is applicable to recuperative furnaces.\nVery limited applicability to conventional regenerative furnaces, where the correct temperature window is difficult to access or does not allow a good mixing of the flue-gases with the reagent.\nIt may be applicable to new regenerative furnaces equipped with split regenerators; however, the temperature window is difficult to maintain due to the reversal of fire between the chambers that causes a cyclical temperature change\nTable 7\nBAT-AELs for NOX emissions from the melting furnace in the container glass sector\nThe conversion factor reported in Table 2 for general cases (1,5 × 10–3) has been applied, with the exception of electric melting (specific cases: 3 × 10–3).\nThe lower value refers to the use of special furnace designs, where applicable.\nThese values should be reconsidered in the occasion of a normal or complete rebuild of the melting furnace.\nThe achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).\nParameter\nBAT\nBAT-AEL\nmg/Nm3\nkg/tonne melted glass\nNOX expressed as NO2\nCombustion modifications, special furnace designs\n500 – 800\n0,75 – 1,2\nElectric melting\n< 100\n< 0,3\nOxy-fuel melting\nNot applicable\n< 0,5 – 0,8\nSecondary techniques\n< 500\n< 0,75",
  "extent": "E+W+S+N.I.",
  "status": null,
  "version": "current",
  "annotations": [
    {
      "type": "footnote",
      "label": "f1",
      "text": "A description of the techniques is given in Section 1.10.2."
    },
    {
      "type": "footnote",
      "label": "f2",
      "text": "A description of the techniques is given in Section 1.10.2."
    },
    {
      "type": "footnote",
      "label": "f3",
      "text": "The conversion factor reported in Table 2 for general cases (1,5 × 10–3) has been applied, with the exception of electric melting (specific cases: 3 × 10–3)."
    },
    {
      "type": "footnote",
      "label": "f4",
      "text": "The lower value refers to the use of special furnace designs, where applicable."
    },
    {
      "type": "footnote",
      "label": "f5",
      "text": "These values should be reconsidered in the occasion of a normal or complete rebuild of the melting furnace."
    },
    {
      "type": "footnote",
      "label": "f6",
      "text": "The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content)."
    }
  ],
  "outstanding_effects": [],
  "provenance": {
    "source": "legislation.gov.uk",
    "source_url": "https://www.legislation.gov.uk/eudn/2012/134/annex/division/5/division/1.2/division/1.2.2/division/17",
    "retrieved_at": "2026-11-01T15:15:31.348652+00:00"
  },
  "licence": "Open Government Licence v3.0",
  "licence_url": "https://www.nationalarchives.gov.uk/doc/open-government-licence/version/3/",
  "attribution": "Contains public sector information licensed under the Open Government Licence v3.0. Source: legislation.gov.uk, The National Archives."
}