OpenLegislation

Division 57

United Kingdom

Original text. Later amendments are not shown.

BAT is to reduce NOX emissions from the melting furnace by using one or a combination of the following techniques:

A description of the techniques is given in Section 1.10.2.

Techniquef1 Applicability
(i) Combustion modifications

(a)

Reduction of air/fuel ratio

Applicable to air/fuel conventional furnaces.

Full benefits are achieved at normal or complete furnace rebuild, when combined with optimum furnace design and geometry

(b)

Reduced combustion air temperature

Applicable 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)

(c)

Staged combustion:

  • Air staging

  • Fuel staging

Fuel staging is applicable to most conventional air/fuel furnaces.

Air staging has very limited applicability due to the technical complexity

(d)

Flue-gas recirculation

The applicability of this technique is limited to the use of special burners with automatic recirculation of the waste gas

(e)

Low-NOX burners

The technique is generally applicable.

The 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.

Full benefits are achieved at normal or complete furnace rebuild, when combined with optimum furnace design and geometry

(f)

Fuel choice

The 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

(ii)

Electric melting

Not applicable for large volume glass productions (> 300 tonnes/day).

Not applicable for productions requiring large pull variations.

The implementation requires a complete furnace rebuild

(iii)

Oxy-fuel melting

The maximum environmental benefits are achieved for applications at the time of a complete furnace rebuild

Table 47

BAT-AELs for NOX emissions from the melting furnace in the mineral wool sector

The conversion factors of 2 × 10–3 for glass wool and 2,5 × 10–3 for stone wool have been used (see Table 2).

The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).

ParameterProductMelting techniqueBAT-AEL
mg/Nm3 kg/tonne melted glassf2
NOX expressed as NO2 Glass woolFuel/air and electric furnaces< 200 – 500< 0,4 – 1,0
Oxy-fuel meltingf3 Not applicable< 0,5
Stone woolAll types of furnaces< 400 – 500< 1,0 – 1,25

Annotations

Footnotes

f1

A description of the techniques is given in Section 1.10.2.

f2

The conversion factors of 2 × 10–3 for glass wool and 2,5 × 10–3 for stone wool have been used (see Table 2).

f3

The achievable levels depend on the quality of the natural gas and oxygen available (nitrogen content).