Division 59
United Kingdom
BAT is to reduce SOX emissions from the melting furnace by using one or a combination of the following techniques:
| A description of the techniques is given in Sections 1.10.3 and 1.10.6. | |
| Techniquef1 | Applicability |
|---|---|
| (i) Minimisation of the sulphur content in the batch formulation and optimisation of the sulphur balance | In glass wool production, the technique is generally applicable within the constraints of the availability of low-sulphur raw materials, in particular external cullet. High levels of external cullet in the batch formulation limit the possibility of optimising the sulphur balance due to a variable sulphur content. In the stone wool production, the optimisation of the sulphur balance may require a trade-off approach between the removal of SOX emissions from the flue-gases and the management of the solid waste, deriving from the treatment of the flue-gases (filter dust) and/or from the fiberising process, which may be recycled into the batch formulation (cement briquettes) or may need to be disposed of |
| (ii) Use of low sulphur content fuels | The applicability may be limited by the constraints associated with the availability of low sulphur fuels, which may be impacted by the energy policy of the Member State |
| (iii) Dry or semi-dry scrubbing, in combination with a filtration system | Electrostatic precipitators are not applicable to cupola furnaces for stone wool production (see BAT 56) |
| (iv) Use of wet scrubbing | The technique is generally applicable within technical constraints; i.e. need for a specific waste water treatment plant |
Table 49
BAT-AELs for SOX 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 lower levels of the ranges are associated with the use of electric melting. The higher levels are associated with high levels of cullet recycling. | |||
| The BAT-AEL is associated with conditions where the reduction of SOX emissions has a high priority over a lower production of solid waste. | |||
| When reduction of waste has a high priority over SOX emissions, higher emission values may be expected. The achievable levels should be based on a sulphur balance. | |||
| Parameter | Product/conditions | BAT-AEL | |
|---|---|---|---|
| mg/Nm3 | kg/tonne melted glassf2 | ||
| SOX expressed as SO2 | Glass wool | ||
| Gas-fired and electric furnacesf3 | < 50 – 150 | < 0,1 – 0,3 | |
| Stone wool | |||
| Gas-fired and electric furnaces | < 350 | < 0,9 | |
| Cupola furnaces, no briquettes or slag recyclingf4 | < 400 | < 1,0 | |
| Cupola furnaces, with cement briquettes or slag recyclingf5 | < 1 400 | < 3,5 | |
Annotations
Footnotes
- f1
-
A description of the techniques is given in Sections 1.10.3 and 1.10.6.
- 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 lower levels of the ranges are associated with the use of electric melting. The higher levels are associated with high levels of cullet recycling.
- f4
-
The BAT-AEL is associated with conditions where the reduction of SOX emissions has a high priority over a lower production of solid waste.
- f5
-
When reduction of waste has a high priority over SOX emissions, higher emission values may be expected. The achievable levels should be based on a sulphur balance.