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Document 32016D1032
Commission Implementing Decision (EU) 2016/1032 of 13 June 2016 establishing best available techniques (BAT) conclusions, under Directive 2010/75/EU of the European Parliament and of the Council, for the non-ferrous metals industries (notified under document C(2016) 3563) (Text with EEA relevance)
Commission Implementing Decision (EU) 2016/1032 of 13 June 2016 establishing best available techniques (BAT) conclusions, under Directive 2010/75/EU of the European Parliament and of the Council, for the non-ferrous metals industries (notified under document C(2016) 3563) (Text with EEA relevance)
Commission Implementing Decision (EU) 2016/1032 of 13 June 2016 establishing best available techniques (BAT) conclusions, under Directive 2010/75/EU of the European Parliament and of the Council, for the non-ferrous metals industries (notified under document C(2016) 3563) (Text with EEA relevance)
C/2016/3563
OJ L 174, 30.6.2016, p. 32–106
(BG, ES, CS, DA, DE, ET, EL, EN, FR, HR, IT, LV, LT, HU, MT, NL, PL, PT, RO, SK, SL, FI, SV)
In force
|
30.6.2016 |
EN |
Official Journal of the European Union |
L 174/32 |
COMMISSION IMPLEMENTING DECISION (EU) 2016/1032
of 13 June 2016
establishing best available techniques (BAT) conclusions, under Directive 2010/75/EU of the European Parliament and of the Council, for the non-ferrous metals industries
(notified under document C(2016) 3563)
(Text with EEA relevance)
THE EUROPEAN COMMISSION,
Having regard to the Treaty on the Functioning of the European Union,
Having regard to Directive 2010/75/EU of the European Parliament and of the Council of 24 November 2010 on industrial emissions (integrated pollution prevention and control) (1), and in particular Article 13(5) thereof,
Whereas:
|
(1) |
Best available techniques (BAT) conclusions are the reference for setting permit conditions for installations covered by Chapter II of Directive 2010/75/EU and competent authorities should set emission limit values which ensure that, under normal operating conditions, emissions do not exceed the emission levels associated with the best available techniques as laid down in the BAT conclusions. |
|
(2) |
The forum composed of representatives of Member States, the industries concerned and non-governmental organisations promoting environmental protection, established by Commission Decision of 16 May 2011 (2), provided the Commission on 4 December 2014 with its opinion on the proposed content of the BAT reference document for the non-ferrous metals industries. That opinion is publicly available. |
|
(3) |
The BAT conclusions set out in the Annex to this Decision are the key element of that BAT reference document. |
|
(4) |
The measures provided for in this Decision are in accordance with the opinion of the Committee established by Article 75(1) of Directive 2010/75/EU, |
HAS ADOPTED THIS DECISION:
Article 1
The best available techniques (BAT) conclusions for the non-ferrous metals industries, as set out in the Annex, are adopted.
Article 2
This Decision is addressed to the Member States.
Done at Brussels, 13 June 2016.
For the Commission
Karmenu VELLA
Member of the Commission
ANNEX
BAT CONCLUSIONS FOR THE NON-FERROUS METALS INDUSTRIES
SCOPE
These BAT conclusions concern certain activities specified in Sections 2.1, 2.5 and 6.8 of Annex I to Directive 2010/75/EU, namely:
— 2.1: Metal ore (including sulphide ore) roasting or sintering;
— 2.5: Processing of non-ferrous metals:
|
(a) |
production of non-ferrous crude metals from ore, concentrates or secondary raw materials by metallurgical, chemical or electrolytic processes; |
|
(b) |
melting, including the alloyage, of non-ferrous metals, including recovered products and operation of non-ferrous metal foundries, with a melting capacity exceeding 4 tonnes per day for lead and cadmium or 20 tonnes per day for all other metals; |
— 6.8: Production of carbon (hard-burnt coal) or electrographite by means of incineration or graphitisation.
In particular, these BAT conclusions cover the following processes and activities:
|
— |
primary and secondary production of non-ferrous metals; |
|
— |
the production of zinc oxide from fumes during the production of other metals; |
|
— |
the production of nickel compounds from liquors during the production of a metal; |
|
— |
the production of silicon-calcium (CaSi) and silicon (Si) in the same furnace as the production of ferro-silicon; |
|
— |
the production of aluminium oxide from bauxite prior to the production of primary aluminium, where this is an integral part of the production of the metal; |
|
— |
the recycling of aluminium salt slag; |
|
— |
the production of carbon and/or graphite electrodes. |
These BAT conclusions do not address the following activities or processes:
|
— |
Iron ore sintering. This is covered in the BAT conclusions for Iron and Steel production. |
|
— |
The production of sulphuric acid based on SO2 gases from non-ferrous metals production. This is covered in the BAT conclusions on Large Volume Inorganic Chemicals-Ammonia, Acids and Fertilisers. |
|
— |
Foundries covered in the BAT conclusions for the Smitheries and Foundries Industry. |
Other reference documents which could be of relevance for the activities covered in these BAT conclusions are the following.
|
Reference document |
Subject |
|
Energy Efficiency (ENE) |
General aspects of energy efficiency |
|
Common Waste Water and Waste Gas Treatment/Management Systems in the Chemical Sector (CWW) |
Waste water treatment techniques to reduce emissions of metals to water |
|
Large Volume Inorganic Chemicals-Ammonia, Acids and Fertilisers (LVIC-AAF) |
Sulphuric acid production |
|
Industrial Cooling Systems (ICS) |
Indirect cooling with water and/or air |
|
Emissions from Storage (EFS) |
Storage and handling of materials |
|
Economics and Cross-media Effects (ECM) |
Economics and cross-media effects of techniques |
|
Monitoring of Emissions to Air and Water from IED installations (ROM) |
Monitoring of emissions to air and water |
|
Waste Treatments Industries (WT) |
Waste handling and treatment |
|
Large Combustion Plants (LCP) |
Combustion plants generating steam and/or electricity |
|
Surface Treatment Using Organic Solvents (STS) |
Non-acid pickling |
|
Surface Treatment of Metals and Plastics (STM) |
Acid pickling |
DEFINITIONS
For the purposes of these BAT conclusions, the following definitions apply:
|
Term used |
Definition |
|
New plant |
A plant first permitted at the site of the installation following the publication of these BAT conclusions or a complete replacement of a plant on the existing foundations of the installation following the publication of these BAT conclusions |
|
Existing plant |
A plant that is not a new plant |
|
Major upgrade |
A major change in the design or technology of a plant and with major adjustments or replacements of the process units and associated equipment |
|
Primary emissions |
Emissions directly vented from the furnaces that are not spread to the areas surrounding the furnaces |
|
Secondary emissions |
Emissions escaping from the furnace lining or during operations such as charging or tapping and which are captured with a hood or enclosure (such as doghouse) |
|
Primary production |
Production of metals using ores and concentrates |
|
Secondary production |
Production of metals using residues and/or scraps, including remelting and alloying processes |
|
Continuous measurement |
Measurement using an ‘automated measuring system’ permanently installed on site for the continuous monitoring of emissions |
|
Periodic measurement |
Determination of a measurand (a particular quantity subject to measurement) at specified time intervals using manual or automated methods |
GENERAL CONSIDERATIONS
Best Available Techniques
The techniques listed and described in these BAT conclusions are neither prescriptive nor exhaustive. Other techniques may be used that ensure at least an equivalent level of environmental protection.
Unless otherwise stated, the BAT conclusions are generally applicable.
Emission levels to air associated with BAT
Emission levels associated with the best available techniques (BAT-AELs) for emissions to air given in these BAT conclusions refer to standard conditions: dry gas at a temperature of 273,15 K, and a pressure of 101,3 kPa.
Averaging periods for emissions to air
For averaging periods for emissions to air, the following definitions apply.
|
Daily average |
Average over a period of 24 hours of valid half-hourly or hourly averages obtained by continuous measurements |
|
Average over the sampling period |
Average value of three consecutive measurements of at least 30 minutes each, unless otherwise stated (1) |
Averaging periods for emissions to water
For averaging periods for emissions to water, the following definition applies.
|
Daily average |
Average over a sampling period of 24 hours taken as a flow-proportional composite sample (or as a time-proportional composite sample provided that sufficient flow stability is demonstrated) (2) |
ACRONYMS
|
Term |
Meaning |
|
BaP |
Benzo[a]pyrene |
|
ESP |
Electrostatic precipitator |
|
I-TEQ |
International toxic equivalency derived by applying international toxic equivalence factors, as defined in Annex VI, part 2 of Directive 2010/75/EU |
|
NOX |
The sum of nitrogen monoxide (NO) and nitrogen dioxide (NO2), expressed as NO2 |
|
PCDD/F |
Polychlorinated dibenzo-p-dioxins and dibenzofurans (17 congeners) |
|
PAH |
Polycyclic aromatic hydrocarbons |
|
TVOC |
Total volatile organic carbon; total volatile organic compounds which are measured by a flame ionisation detector (FID) and expressed as total carbon |
|
VOC |
Volatile organic compounds as defined in Article 3(45) of Directive 2010/75/EU |
1.1. GENERAL BAT CONCLUSIONS
Any relevant process-specific BAT conclusions in Sections 1.2 to 1.9 apply in addition to the general BAT conclusions in this section.
1.1.1. Environmental management systems (EMS)
BAT 1. In order to improve the overall environmental performance, BAT is to implement and adhere to an environmental management system (EMS) that incorporates all of the following features:
|
(a) |
commitment of the management, including senior management; |
|
(b) |
definition of an environmental policy that includes the continuous improvement of the installation by the management; |
|
(c) |
planning and establishing the necessary procedures, objectives and targets, in conjunction with financial planning and investment; |
|
(d) |
implementation of procedures paying particular attention to:
|
|
(e) |
checking performance and taking corrective action, paying particular attention to:
|
|
(f) |
review of the EMS and its continuing suitability, adequacy and effectiveness by senior management; |
|
(g) |
following the development of cleaner technologies; |
|
(h) |
consideration for the environmental impacts from the eventual decommissioning of the installation at the stage of designing a new plant, and throughout its operating life; |
|
(i) |
application of sectoral benchmarking on a regular basis. |
The establishment and implementation of an action plan on diffuse dust emissions (see BAT 6) and the application of a maintenance management system which especially addresses the performance of dust abatement systems (see BAT 4) are also a part of the EMS.
Applicability
The scope (e.g. level of detail) and nature of the EMS (e.g. standardised or non-standardised) will generally be related to the nature, scale and complexity of the installation, and the range of environmental impacts it may have.
1.1.2. Energy management
BAT 2. In order to use energy efficiently, BAT is to use a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Energy efficiency management system (e.g. ISO 50001) |
Generally applicable |
|
b |
Regenerative or recuperative burners |
Generally applicable |
|
c |
Heat recovery (e.g. steam, hot water, hot air) from waste process heat |
Only applicable for pyrometallurgical processes |
|
d |
Regenerative thermal oxidiser |
Only applicable when the abatement of a combustible pollutant is required |
|
e |
Preheat the furnace charge, combustion air or fuel using the heat recovered from hot gases from the melting stage |
Only applicable for roasting or smelting of sulphide ore/concentrate and for other pyrometallurgical processes |
|
f |
Raise the temperature of the leaching liquors using steam or hot water from waste heat recovery |
Only applicable for alumina or hydrometallurgical processes |
|
g |
Use hot gases from the launder as preheated combustion air |
Only applicable for pyrometallurgical processes |
|
h |
Use oxygen-enriched air or pure oxygen in the burners to reduce energy consumption by allowing autogenous smelting or the complete combustion of carbonaceous material |
Only applicable for furnaces that use raw materials containing sulphur or carbon |
|
i |
Dry concentrates and wet raw materials at low temperatures |
Only applicable when drying is performed |
|
j |
Recover the chemical energy content of the carbon monoxide produced in an electric or shaft/blast furnace by using the exhaust gases as a fuel, after the removal of metals, in other production processes or to produce steam/hot water or electricity |
Only applicable to exhaust gases with a CO content > 10 vol-%. Applicability is also influenced by the composition of the exhaust gas and the unavailability of a continuous flow (i.e. batch processes) |
|
k |
Recirculate the flue-gas back through an oxy-fuel burner to recover the energy contained in the total organic carbon present |
Generally applicable |
|
l |
Suitable insulation for high temperature equipment such as steam and hot water pipes |
Generally applicable |
|
m |
Use the heat generated from the production of sulphuric acid from sulphur dioxide to preheat gas directed to the sulphuric acid plant or to generate steam and/or hot water |
Only applicable for non-ferrous metals plants including sulphuric acid or liquid SO2 production |
|
n |
Use high efficiency electric motors equipped with variable-frequency drive, for equipment such as fans |
Generally applicable |
|
o |
Use control systems that automatically activate the air extraction system or adjust the extraction rate depending on actual emissions |
Generally applicable |
1.1.3. Process control
BAT 3. In order to improve overall environmental performance, BAT is to ensure stable process operation by using a process control system together with a combination of the techniques given below.
|
|
Technique |
|
a |
Inspect and select input materials according to the process and the abatement techniques applied |
|
b |
Good mixing of the feed materials to achieve optimum conversion efficiency and reduce emissions and rejects |
|
c |
Feed weighing and metering systems |
|
d |
Processors to control material feed rate, critical process parameters and conditions including the alarm, combustion conditions and gas additions |
|
e |
On-line monitoring of the furnace temperature, furnace pressure and gas flow |
|
f |
Monitor the critical process parameters of the air emission abatement plant such as gas temperature, reagent metering, pressure drop, ESP current and voltage, scrubbing liquid flow and pH and gaseous components (e.g. O2, CO, VOC) |
|
g |
Control dust and mercury in the exhaust gas before transfer to the sulphuric acid plant for plants including sulphuric acid or liquid SO2 production |
|
h |
On-line monitoring of vibrations to detect blockages and possible equipment failure |
|
i |
On-line monitoring of the current, voltage and electrical contact temperatures in electrolytic processes |
|
j |
Temperature monitoring and control at melting and smelting furnaces to prevent the generation of metal and metal oxide fumes through overheating |
|
k |
Processor to control the reagents feeding and the performance of the waste water treatment plant, through on-line monitoring of temperature, turbidity, pH, conductivity and flow |
BAT 4. In order to reduce channelled dust and metal emissions to air, BAT is to apply a maintenance management system which especially addresses the performance of dust abatement systems as part of the environmental management system (see BAT 1).
1.1.4. Diffuse emissions
1.1.4.1. General approach for the prevention of diffuse emissions
BAT 5. In order to prevent or, where this is not practicable, to reduce diffuse emissions to air and water, BAT is to collect diffuse emissions as much as possible nearest to the source and treat them.
BAT 6. In order to prevent or, where this is not practicable, to reduce diffuse dust emissions to air, BAT is to set up and implement an action plan on diffuse dust emissions, as part of the environmental management system (see BAT 1), that incorporates both of the following measures:
|
a. |
identify the most relevant diffuse dust emission sources (using e.g. EN 15445); |
|
b. |
define and implement appropriate actions and techniques to prevent or reduce diffuse emissions over a given time frame. |
1.1.4.2. Diffuse emissions from the storage, handling and transport of raw materials
BAT 7. In order to prevent diffuse emissions from the storage of raw materials, BAT is to use a combination of the techniques given below.
|
|
Technique |
||||
|
a |
Enclosed buildings or silos/bins for storing dust-forming materials such as concentrates, fluxes and fine materials |
||||
|
b |
Covered storage of non-dust-forming materials such as concentrates, fluxes, solid fuels, bulk materials and coke and secondary materials that contain water-soluble organic compounds |
||||
|
c |
Sealed packaging of dust-forming materials or secondary materials that contain water-soluble organic compounds |
||||
|
d |
Covered bays for storing material which has been pelletised or agglomerated |
||||
|
e |
Use water sprays and fog sprays with or without additives such as latex for dust-forming materials |
||||
|
f |
Dust/gas extraction devices placed at the transfer and tipping points for dust-forming materials |
||||
|
g |
Certified pressure vessels for storing chlorine gas or mixtures that contain chlorine |
||||
|
h |
Tank construction materials that are resistant to the contained materials |
||||
|
i |
Reliable leak detection systems and display of tank’s level, with an alarm to prevent overfills |
||||
|
j |
Store reactive materials in double-walled tanks or tanks placed in chemical-resistant bunds of the same capacity and use a storage area that is impermeable and resistant to the material stored |
||||
|
k |
Design storage areas so that
|
||||
|
l |
Use inert gas blanketing for the storage of materials that react with air |
||||
|
m |
Collect and treat emissions from storage with an abatement system designed to treat the compounds stored. Collect and treat before discharge any water that washes dust away. |
||||
|
n |
Regular cleaning of the storage area and, when needed, moistening with water |
||||
|
o |
Place the longitudinal axis of the heap parallel to the prevailing wind direction in the case of outdoor storage |
||||
|
p |
Protective planting, windbreak fences or upwind mounts to lower the wind velocity in the case of outdoor storage |
||||
|
q |
One heap instead of several where feasible in the case of outdoor storage |
||||
|
r |
Use oil and solid interceptors for the drainage of open outdoor storage areas. Use of concreted areas that have kerbs or other containment devices for the storage of material that can release oil, such as swarf |
Applicability
BAT 7. e is not applicable to processes that require dry materials or ores/concentrates that naturally contain sufficient humidity to prevent dust formation. The applicability may be limited in regions with water shortages or with very low temperatures
BAT 8. In order to prevent diffuse emissions from the handling and transport of raw materials, BAT is to use a combination of the techniques given below.
|
|
Technique |
|
a |
Enclosed conveyors or pneumatic systems to transfer and handle dust-forming concentrates and fluxes and fine-grained material |
|
b |
Covered conveyors to handle non-dust-forming solid materials |
|
c |
Extraction of dust from delivery points, silo vents, pneumatic transfer systems and conveyor transfer points, and connection to a filtration system (for dust-forming materials) |
|
d |
Closed bags or drums to handle materials with dispersible or water-soluble components |
|
e |
Suitable containers to handle pelletised materials |
|
f |
Sprinkling to moisten the materials at handling points |
|
g |
Minimise transport distances |
|
h |
Reduce the drop height of conveyor belts, mechanical shovels or grabs |
|
i |
Adjust the speed of open belt conveyors (< 3,5 m/s) |
|
j |
Minimise the speed of descent or free fall height of the materials |
|
k |
Place transfer conveyors and pipelines in safe, open areas above ground so that leaks can be detected quickly and damage from vehicles and other equipment can be prevented. If buried pipelines are used for non-hazardous materials, document and mark their course and adopt safe excavation systems |
|
l |
Automatic resealing of delivery connections for handling liquid and liquefied gas |
|
m |
Back-vent displaced gases to the delivery vehicle to reduce emissions of VOC |
|
n |
Wash wheels and chassis of vehicles used to deliver or handle dusty materials |
|
o |
Use planned campaigns for road sweeping |
|
p |
Segregate incompatible materials (e.g. oxidising agents and organic materials) |
|
q |
Minimise material transfers between processes |
Applicability
BAT 8.n. may not be applicable when ice could be formed.
1.1.4.3. Diffuse emissions from metal production
BAT 9. In order to prevent or, where this is not practicable, to reduce diffuse emissions from metal production, BAT is to optimise the efficiency of off-gas collection and treatment by using a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Thermal or mechanical pretreatment of secondary raw material to minimise organic contamination of the furnace feed |
Generally applicable |
|
b |
Use a closed furnace with a properly designed dedusting system or seal the furnace and other process units with an adequate vent system |
The applicability may be restricted by safety constraints (e.g. type/design of the furnace, risk of explosion) |
|
c |
Use a secondary hood for furnace operations such as charging and tapping |
The applicability may be restricted by safety constraints (e.g. type/design of the furnace, risk of explosion) |
|
d |
Dust or fume collection where dusty material transfers take place (e.g. furnace charging and tapping points, covered launders) |
Generally applicable |
|
e |
Optimise the design and operation of hooding and ductwork to capture fumes arising from the feed port and from hot metal, matte or slag tapping and transfers in covered launders |
For existing plants, the applicability may be limited by space and plant configuration restrictions |
|
f |
Furnace/reactor enclosures such as ‘house-in-house’ or ‘doghouse’ for tapping and charging operations |
For existing plants, the applicability may be limited by space and plant configuration restrictions |
|
g |
Optimise the off-gas flow from the furnace through computerised fluid dynamics studies and tracers |
Generally applicable |
|
h |
Charging systems for semi-closed furnaces to add raw materials in small amounts |
Generally applicable |
|
i |
Treat the collected emissions in an adequate abatement system |
Generally applicable |
1.1.5. Monitoring of emissions to air
BAT 10. BAT is to monitor the stack emissions to air with at least the frequency given below and in accordance with EN standards. If EN standards are not available, BAT is to use ISO, national or other international standards that ensure the provision of data of an equivalent scientific quality.
|
Parameter |
Monitoring associated with |
Minimum monitoring frequency |
Standard(s) |
||
|
Dust (4) |
Copper: BAT 38, BAT 39, BAT 40, BAT 43, BAT 44, BAT 45 Aluminium: BAT 56, BAT 58, BAT 59, BAT 60, BAT 61, BAT 67, BAT 81, BAT 88 Lead, Tin: BAT 94, BAT 96, BAT 97 Zinc, Cadmium: BAT 119, BAT 122 Precious metals: BAT 140 Ferro-alloys: BAT 155, BAT 156, BAT 157, BAT 158 Nickel, Cobalt: BAT 171 Other non-ferrous metals: emissions from production stages such as raw material pretreatment, charging, smelting, melting and tapping |
Continuous (3) |
EN 13284-2 |
||
|
Copper: BAT 37, BAT 38, BAT 40, BAT 41, BAT 42, BAT 43, BAT 44, BAT 45 Aluminium: BAT 56, BAT 58, BAT 59, BAT 60, BAT 61, BAT 66, BAT 67, BAT 68, BAT 80, BAT 81, BAT 82, BAT 88 Lead, Tin: BAT 94, BAT 95, BAT 96, BAT 97 Zinc, Cadmium: BAT 113, BAT 119, BAT 121, BAT 122, BAT 128, BAT 132 Precious metals: BAT 140 Ferro-alloys: BAT 154, BAT 155, BAT 156, BAT 157, BAT 158 Nickel, Cobalt: BAT 171 Carbon/graphite: BAT 178, BAT 179, BAT 180, BAT 181 Other non-ferrous metals: emissions from production stages such as raw material pretreatment, charging, smelting, melting and tapping |
Once per year (3) |
EN 13284-1 |
|||
|
Antimony and its compounds, expressed as Sb |
Lead, Tin: BAT 96, BAT 97 |
Once per year |
EN 14385 |
||
|
Arsenic and its compounds, expressed as As |
Copper: BAT 37, BAT 38, BAT 39, BAT 40, BAT 42, BAT 43, BAT 44, BAT 45 Lead, Tin: BAT 96, BAT 97 Zinc: BAT 122 |
Once per year |
EN 14385 |
||
|
Cadmium and its compounds, expressed as Cd |
Copper: BAT 37, BAT 38, BAT 39, BAT 40, BAT 41, BAT 42, BAT 43, BAT 44, BAT 45 Lead, Tin: BAT 94, BAT 95, BAT 96, BAT 97 Zinc, Cadmium: BAT 122, BAT 132 Ferro-alloys: BAT 156 |
Once per year |
EN 14385 |
||
|
Chromium (VI) |
Ferro-alloys: BAT 156 |
Once per year |
No EN standard available |
||
|
Copper and its compounds, expressed as Cu |
Copper: BAT 37, BAT 38, BAT 39, BAT 40, BAT 42, BAT 43, BAT 44, BAT 45 Lead, Tin: BAT 96, BAT 97 |
Once per year |
EN 14385 |
||
|
Nickel and its compounds, expressed as Ni |
Nickel, Cobalt: BAT 172, BAT 173 |
Once per year |
EN 14385 |
||
|
Lead and its compounds, expressed as Pb |
Copper: BAT 37, BAT 38, BAT 39, BAT 40, BAT 41, BAT 42, BAT 43, BAT 44, BAT 45 Lead, Tin: BAT 94, BAT 95, BAT 96, BAT 97 Ferro-alloys: BAT 156 |
Once per year |
EN 14385 |
||
|
Thallium and its compounds, expressed as Tl |
Ferro-alloys: BAT 156 |
Once per year |
EN 14385 |
||
|
Zinc and its compounds, expressed as Zn |
Zinc, Cadmium: BAT 113, BAT 114, BAT 119, BAT 121, BAT 122, BAT 128, BAT 132 |
Once per year |
EN 14385 |
||
|
Other metals, if relevant (5) |
Copper: BAT 37, BAT 38, BAT 39, BAT 40, BAT 41, BAT 42, BAT 43, BAT 44, BAT 45 Lead, Tin: BAT 94, BAT 95, BAT 96, BAT 97 Zinc, Cadmium: BAT 113, BAT 119, BAT 121, BAT 122, BAT 128, BAT 132 Precious metals: BAT 140 Ferro-alloys: BAT 154, BAT 155, BAT 156, BAT 157, BAT 158 Nickel, Cobalt: BAT 171 Other non-ferrous metals |
Once per year |
EN 14385 |
||
|
Mercury and its compounds, expressed as Hg |
Copper, Aluminium, Lead, Tin, Zinc, Cadmium, Ferro-alloys, Nickel, Cobalt, Other non-ferrous metals: BAT 11 |
Continuous or once per year (3) |
EN 14884 EN 13211 |
||
|
SO2 |
Copper: BAT 49 Aluminium: BAT 60, BAT 69 Lead, Tin: BAT 100 Precious metals: BAT 142, BAT 143 Nickel, Cobalt: BAT 174 |
EN 14791 |
|||
|
Zinc, Cadmium: BAT 120 |
Continuous |
||||
|
Carbon/graphite: BAT 182 |
Once per year |
||||
|
NOX, expressed as NO2 |
Copper, Aluminium, Lead, Tin, FeSi, Si (pyrometallurgical processes): BAT 13 Precious metals: BAT 141 Other non-ferrous metals (9) |
Continuous or once per year (3) |
EN 14792 |
||
|
Carbon/graphite |
Once per year |
||||
|
TVOC |
Copper: BAT 46 Aluminium: BAT 83 Lead, Tin: BAT 98 Zinc, Cadmium: BAT 123 Other non-ferrous metals (10) |
Continuous or once per year (3) |
EN 12619 |
||
|
Ferro-alloys: BAT 160 Carbon/graphite: BAT 183 |
Once per year |
||||
|
Formaldehyde |
Carbon/graphite: BAT 183 |
Once per year |
No EN standard available |
||
|
Phenol |
Carbon/graphite: BAT 183 |
Once per year |
No EN standard available |
||
|
PCDD/F |
Copper: BAT 48 Aluminium: BAT 83 Lead, Tin: BAT 99 Zinc, Cadmium: BAT 123 Precious metals: BAT 146 Ferro-alloys: BAT 159 |
Once per year |
EN 1948 parts 1, 2 and 3 |
||
|
H2SO4 |
Copper: BAT 50 Zinc, Cadmium: BAT 114 |
Once per year |
No EN standard available |
||
|
NH3 |
Aluminium: BAT 89 Precious metals: BAT 145 Nickel, Cobalt: BAT 175 |
Once per year |
No EN standard available |
||
|
Benzo-[a]-pyrene |
Aluminium: BAT 59, BAT 60, BAT 61 Ferro-alloys: BAT 160 Carbon/graphite: BAT 178, BAT 179, BAT 180, BAT 181 |
Once per year |
ISO 11338-1 ISO 11338-2 |
||
|
Gaseous fluorides, expressed as HF |
Aluminium: BAT 60, BAT 61, BAT 67 |
Continuous (3) |
ISO 15713 |
||
|
Aluminium: BAT 60, BAT 67, BAT 84 Zinc, Cadmium: BAT 124 |
Once per year (3) |
||||
|
Total fluorides |
Aluminium: BAT 60, BAT 67 |
Once per year |
No EN standard available |
||
|
Gaseous chlorides, expressed as HCl |
Aluminium: BAT 84 |
Continuous or once per year (3) |
EN 1911 |
||
|
Zinc, Cadmium: BAT 124 Precious metals: BAT 144 |
Once per year |
||||
|
Cl2 |
Aluminium: BAT 84 Precious metals: BAT 144 Nickel, Cobalt: BAT 172 |
Once per year |
No EN standard available |
||
|
H2S |
Aluminium: BAT 89 |
Once per year |
No EN standard available |
||
|
PH3 |
Aluminium: BAT 89 |
Once per year |
No EN standard available |
||
|
Sum of AsH3 and SbH3 |
Zinc, Cadmium: BAT 114 |
Once per year |
No EN standard available |
||
|
|||||
1.1.6. Mercury emissions
BAT 11. In order to reduce mercury emissions to air (other than those that are routed to the sulphuric acid plant) from a pyrometallurgical process, BAT is to use one or both of the techniques given below.
|
|
Technique |
|
a |
Use raw materials with a low mercury content, including by cooperating with providers in order to remove mercury from secondary materials. |
|
b |
Use adsorbents (e.g. activated carbon, selenium) in combination with dust filtration (11) |
BAT-associated emission levels: See Table 1.
Table 1
BAT-associated emission levels for mercury emissions to air (other than those that are routed to the sulphuric acid plant) from a pyrometallurgical process using raw materials containing mercury
|
Parameter |
|
|
Mercury and its compounds, expressed as Hg |
0,01-0,05 |
The associated monitoring is in BAT 10.
1.1.7. Sulphur dioxide emissions
BAT 12. In order to reduce emissions of SO2 from off-gases with a high SO2 content and to avoid the generation of waste from the flue-gas cleaning system, BAT is to recover sulphur by producing sulphuric acid or liquid SO2.
Applicability
Only applicable to plants producing copper, lead, primary zinc, silver, nickel and/or molybdenum.
1.1.8. NOX emissions
BAT 13. In order to prevent NOX emissions to air from a pyrometallurgical process, BAT is to use one of the techniques given below.
|
|
Technique (14) |
|
a |
Low-NOX burners |
|
b |
Oxy-fuel burners |
|
c |
Flue-gas recirculation (back through the burner to reduce the temperature of the flame) in the case of oxy-fuel burners |
The associated monitoring is in BAT 10.
1.1.9. Emissions to water, including their monitoring
BAT 14. In order to prevent or reduce the generation of waste water, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Measure the amount of fresh water used and the amount of waste water discharged |
Generally applicable |
|
b |
Reuse waste water from cleaning operations (including anode and cathode rinse water) and spills in the same process |
Generally applicable |
|
c |
Reuse weak acid streams generated in a wet ESP and wet scrubbers |
Applicability may be restricted depending on the metal and solid content of the waste water |
|
d |
Reuse waste water from slag granulation |
Applicability may be restricted depending on the metal and solid content of the waste water |
|
e |
Reuse surface run-off water |
Generally applicable |
|
f |
Use a closed circuit cooling system |
Applicability may be restricted when a low temperature is required for process reasons |
|
g |
Reuse treated water from the waste water treatment plant |
Applicability may be restricted by the salt content |
BAT 15. In order to prevent the contamination of water and to reduce emissions to water, BAT is to segregate uncontaminated waste water streams from waste water streams requiring treatment.
Applicability
The segregation of uncontaminated rainwater may not be applicable in the case of existing waste water collection systems.
BAT 16. BAT is to use ISO 5667 for water sampling and to monitor the emissions to water at the point where the emission leaves the installation at least once per month (15) and in accordance with EN standards. If EN standards are not available, BAT is to use ISO, national or other international standards that ensure the provision of data of an equivalent scientific quality.
|
Parameter |
Applicable for the production of (16) |
Standard(s) |
|
Mercury (Hg) |
Copper, Lead, Tin, Zinc, Cadmium, Precious metals, Ferro-alloys, Nickel, Cobalt, and other non-ferrous metals |
EN ISO 17852, EN ISO 12846 |
|
Iron (Fe) |
Copper, Lead, Tin, Zinc, Cadmium, Precious metals, Ferro-alloys, Nickel, Cobalt, and other non-ferrous metals |
EN ISO 11885 EN ISO 15586 EN ISO 17294-2 |
|
Arsenic (As) |
Copper, Lead, Tin, Zinc, Cadmium, Precious metals, Ferro-alloys, Nickel, and Cobalt |
|
|
Cadmium (Cd) |
||
|
Copper (Cu) |
||
|
Nickel (Ni) |
||
|
Lead (Pb) |
||
|
Zinc (Zn) |
||
|
Silver (Ag) |
Precious metals |
|
|
Aluminium (Al) |
Aluminium |
|
|
Cobalt (Co) |
Nickel, and Cobalt |
|
|
Chromium total (Cr) |
Ferro-alloys |
|
|
Chromium(VI) (Cr(VI)) |
Ferro-alloys |
EN ISO 10304-3 EN ISO 23913 |
|
Antimony (Sb) |
Copper, Lead, and Tin |
EN ISO 11885 EN ISO 15586 EN ISO 17294-2 |
|
Tin (Sn) |
Copper, Lead, and Tin |
|
|
Other metals, if relevant (17) |
Aluminium, Ferro-alloys, and other non-ferrous metals |
|
|
Sulphate (SO4 2-) |
Copper, Lead, Tin, Zinc, Cadmium, Precious metals, Nickel, Cobalt, and other non-ferrous metals |
EN ISO 10304-1 |
|
Fluoride (F-) |
Primary aluminium |
|
|
Total suspended solids (TSS) |
Aluminium |
EN 872 |
BAT 17. In order to reduce emissions to water, BAT is to treat the leakages from the storage of liquids and the waste water from non-ferrous metals production, including from the washing stage in the Waelz kiln process, and to remove metals and sulphates by using a combination of the techniques given below.
|
|
Technique (18) |
Applicability |
|
a |
Chemical precipitation |
Generally applicable |
|
b |
Sedimentation |
Generally applicable |
|
c |
Filtration |
Generally applicable |
|
d |
Flotation |
Generally applicable |
|
e |
Ultrafiltration |
Only applicable to specific streams in non-ferrous metals production |
|
f |
Activated carbon filtration |
Generally applicable |
|
g |
Reverse osmosis |
Only applicable to specific streams in non-ferrous metals production |
BAT-associated emission levels
The BAT-associated emission levels (BAT-AELs) for direct emissions to a receiving water body from the production of copper, lead, tin, zinc, cadmium, precious metals, nickel, cobalt and ferro-alloys are given in Table 2.
These BAT-AELs apply at the point where the emission leaves the installation.
Table 2
BAT-associated emission levels for direct emissions to a receiving water body from the production of copper, lead, tin, zinc (including the waste water from the washing stage in the Waelz kiln process), cadmium, precious metals, nickel, cobalt and ferro-alloys
|
BAT-AEL (mg/l) (daily average) |
||||||||
|
Parameter |
Production of |
|||||||
|
Copper |
Lead and/or Tin |
Zinc and/or Cadmium |
Precious metals |
Nickel and/or Cobalt |
Ferro-alloys |
|||
|
Silver (Ag) |
NR |
≤ 0,6 |
NR |
|||||
|
Arsenic (As) |
≤ 0,1 (19) |
≤ 0,1 |
≤ 0,1 |
≤ 0,1 |
≤ 0,3 |
≤ 0,1 |
||
|
Cadmium (Cd) |
0,02–0,1 |
≤ 0,1 |
≤ 0,1 |
≤ 0,05 |
≤ 0,1 |
≤ 0,05 |
||
|
Cobalt (Co) |
NR |
≤ 0,1 |
NR |
0,1-0,5 |
NR |
|||
|
Chromium total (Cr) |
NR |
≤ 0,2 |
||||||
|
Chromium (VI) (Cr(VI)) |
NR |
≤ 0,05 |
||||||
|
Copper (Cu) |
0,05-0,5 |
≤ 0,2 |
≤ 0,1 |
≤ 0,3 |
≤ 0,5 |
≤ 0,5 |
||
|
Mercury (Hg) |
0,005–0,02 |
≤ 0,05 |
≤ 0,05 |
≤ 0,05 |
≤ 0,05 |
≤ 0,05 |
||
|
Nickel (Ni) |
≤ 0,5 |
≤ 0,5 |
≤ 0,1 |
≤ 0,5 |
≤ 2 |
≤ 2 |
||
|
Lead (Pb) |
≤ 0,5 |
≤ 0,5 |
≤ 0,2 |
≤ 0,5 |
≤ 0,5 |
≤ 0,2 |
||
|
Zinc (Zn) |
≤ 1 |
≤ 1 |
≤ 1 |
≤ 0,4 |
≤ 1 |
≤ 1 |
||
|
||||||||
The associated monitoring is in BAT 16.
1.1.10. Noise
BAT 18. In order to reduce noise emissions, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Use embankments to screen the source of noise |
|
b |
Enclose noisy plants or components in sound-absorbing structures |
|
c |
Use anti-vibration supports and interconnections for equipment |
|
d |
Orientation of noise-emitting machinery |
|
e |
Change the frequency of the sound |
1.1.11. Odour
BAT 19. In order to reduce odour emissions, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Appropriate storage and handling of odorous materials |
Generally applicable |
|
b |
Minimise the use of odorous materials |
Generally applicable |
|
c |
Careful design, operation and maintenance of any equipment that could generate odour emissions |
Generally applicable |
|
d |
Afterburner or filtration techniques, including biofilters |
Applicable only in limited cases (e.g. in the impregnation stage during speciality production in the carbon and graphite sector) |
1.2. BAT CONCLUSIONS FOR COPPER PRODUCTION
1.2.1. Secondary materials
BAT 20. In order to increase the secondary materials’ recovery yield from scrap, BAT is to separate non-metallic constituents and metals other than copper by using one or a combination of the techniques given below.
|
|
Technique |
|
a |
Manual separation of large visible constituents |
|
b |
Magnetic separation of ferrous metals |
|
c |
Optical or eddy current separation of aluminium |
|
d |
Relative density separation of different metallic and non-metallic constituents (using a fluid with a different density or air) |
1.2.2. Energy
BAT 21. In order to use energy efficiently in primary copper production, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Optimise the use of the energy contained in the concentrate using a flash smelting furnace |
Only applicable for new plants and for major upgrades of existing plants |
|
b |
Use the hot process gases from the melting stages to heat up the furnace charge |
Only applicable to shaft furnaces |
|
c |
Cover the concentrates during transport and storage |
Generally applicable |
|
d |
Use the excess heat produced during the primary smelting or converting stages to melt secondary materials containing copper |
Generally applicable |
|
e |
Use the heat in the gases from anode furnaces in a cascade for other processes such as drying |
Generally applicable |
BAT 22. In order to use energy efficiently in secondary copper production, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Reduce the water content of the feed material |
Applicability is limited when the moisture content of the materials is used as a technique to reduce diffuse emissions |
|
b |
Produce steam by recovering excess heat from the smelting furnace to heat up the electrolyte in refineries and/or to produce electricity in a co-generation installation |
Applicable if an economically viable demand of steam exists |
|
c |
Melt scraps using the excess heat that is produced during the smelting or converting process |
Generally applicable |
|
d |
Holding furnace between processing stages |
Only applicable for batch-wise operated smelters where a buffer capacity of molten material is required |
|
e |
Preheat the furnace charge using the hot process gases from the melting stages |
Only applicable to shaft furnaces |
BAT 23. In order to use energy efficiently in electrorefining and electrowinning operations, BAT is to use a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Apply insulation and covers to electrolysis tanks |
Generally applicable |
|
b |
Addition of surfactants to the electrowinning cells |
Generally applicable |
|
c |
Improved cell design for lower energy consumption by optimisation of the following parameters: space between anode and cathode, anode geometry, current density, electrolyte composition and temperature |
Only applicable for new plants and for major upgrades of existing plants |
|
d |
Use of stainless steel cathode blanks |
Only applicable for new plants and for major upgrades of existing plants |
|
e |
Automatic cathode/anode changes to achieve an accurate placement of the electrodes into the cell |
Only applicable for new plants and for major upgrades of existing plants |
|
f |
Short circuit detection and quality control to ensure that electrodes are straight and flat and that the anode is exact in weight |
Generally applicable |
1.2.3. Air emissions
BAT 24. In order to reduce secondary emissions to air from furnaces and auxiliary devices in primary copper production and to optimise the performance of the abatement system, BAT is to collect, mix and treat secondary emissions in a centralised off-gas cleaning system.
Description
Secondary emissions from various sources are collected, mixed, and treated in a single centralised off-gas cleaning system, designed to effectively treat the pollutants present in each of the flows. Care is taken not to mix streams which are not chemically compatible and to avoid undesirable chemical reactions among the different collected flows.
Applicability
The applicability may be limited for existing plants by their design and layout.
1.2.3.1. Diffuse emissions
BAT 25. In order to prevent or reduce diffuse emissions from pretreatment (such as blending, drying, mixing, homogenisation, screening and pelletisation) of primary and secondary materials, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Use enclosed conveyers or pneumatic transfer systems for dusty materials |
Generally applicable |
|
b |
Carry out activities with dusty materials such as mixing in an enclosed building |
For existing plants, application may be difficult due to the space requirements |
|
c |
Use dust suppression systems such as water cannons or water sprinklers |
Not applicable for mixing operations carried out indoors. Not applicable for processes that require dry materials. The application is also limited in regions with water shortages or with very low temperatures |
|
d |
Use enclosed equipment for operations with dusty material (such as drying, mixing, milling, air separation and pelletisation) with an air extraction system connected to an abatement system |
Generally applicable |
|
e |
Use an extraction system for dusty and gaseous emissions, such as a hood in combination with a dust and gas abatement system |
Generally applicable |
BAT 26. In order to prevent or reduce diffuse emissions from charging, smelting and tapping operations in primary and secondary copper smelters and from holding and melting furnaces, BAT is to use a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Briquetting and pelletisation of raw materials |
Applicable only when the process and the furnace can use pelletised raw materials |
|
b |
Enclosed charging system such as single jet burner, door sealing (20), closed conveyers or feeders equipped with an air extraction system in combination with a dust and gas abatement system |
The jet burner is applicable only for flash furnaces |
|
c |
Operate the furnace and gas route under negative pressure and at a sufficient gas extraction rate to prevent pressurisation |
Generally applicable |
|
d |
Capture hood/enclosures at charging and tapping points in combination with an off-gas abatement system (e.g. housing/tunnel for ladle operation during tapping, and which is closed with a movable door/barrier equipped with a ventilation and abatement system) |
Generally applicable |
|
e |
Encapsulate the furnace in vented housing |
Generally applicable |
|
f |
Maintain furnace sealing |
Generally applicable |
|
g |
Hold the temperature in the furnace at the lowest required level |
Generally applicable |
|
h |
Boosted suction systems (20) |
Generally applicable |
|
i |
Enclosed building in combination with other techniques to collect the diffuse emissions |
Generally applicable |
|
j |
Double bell charging system for shaft/blast furnaces |
Generally applicable |
|
k |
Select and feed the raw materials according to the type of furnace and abatement techniques used |
Generally applicable |
|
l |
Use of lids on throats of rotary anode furnace |
Generally applicable |
BAT 27. In order to reduce diffuse emissions from Peirce-Smith converter (PS) furnace in primary and secondary copper production, BAT is to use a combination of the techniques given below.
|
|
Technique |
|
a |
Operate the furnace and gas route under negative pressure and at a sufficient gas extraction rate to prevent pressurisation |
|
b |
Oxygen enrichment |
|
c |
Primary hood over the converter opening to collect and transfer the primary emissions to an abatement system |
|
d |
Addition of materials (e.g. scrap and flux) through the hood |
|
e |
System of secondary hoods in addition to the main one to capture emissions during charging and tapping operations |
|
f |
Furnace located in enclosed building |
|
g |
Apply motor-driven secondary hoods, to move them according to the process stage, to increase the efficiency of the collection of secondary emissions |
|
h |
Boosted suction systems (21) and automatic control to prevent blowing when the converter is ‘rolled out’ or ‘rolled in’ |
BAT 28. In order to reduce diffuse emissions from a Hoboken converter furnace in primary copper production, BAT is to use a combination of the techniques given below.
|
|
Technique |
|
a |
Operate furnace and gas route under negative pressure during charging, skimming and tapping operations |
|
b |
Oxygen enrichment |
|
c |
Mouth with closed lids during operation |
|
d |
Boosted suction systems (22) |
BAT 29. In order to reduce diffuse emissions from the matte conversion process, BAT is to use a flash converting furnace.
Applicability
Applicable only to new plants or major upgrades of existing plants.
BAT 30. In order to reduce diffuse emissions from a top-blown rotary converter (TBRC) furnace in secondary copper production, BAT is to use a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Operate the furnace and gas route under negative pressure and at a sufficient gas extraction rate to prevent pressurisation |
Generally applicable |
|
b |
Oxygen enrichment |
Generally applicable |
|
c |
Furnace located in enclosed building in combination with techniques to collect and transfer diffuse emissions from charging and tapping to an abatement system |
Generally applicable |
|
d |
Primary hood over the converter opening to collect and transfer the primary emissions to an abatement system |
Generally applicable |
|
e |
Hoods or crane integrated hood to collect and transfer the emissions from charging and tapping operations to an abatement system |
For existing plants, a crane integrated hood is only applicable to major upgrades of the furnace hall |
|
f |
Addition of materials (e.g. scrap and flux) through the hood |
Generally applicable |
|
g |
Boosted suction system (23) |
Generally applicable |
BAT 31. In order to reduce diffuse emissions from copper recovery with a slag concentrator, BAT is to use the techniques given below.
|
|
Technique |
|
a |
Dust suppression techniques such as a water spray for handling, storage and crushing of slag |
|
b |
Grinding and flotation performed with water |
|
c |
Delivery of the slag to the final storage area via hydro transport in a closed pipeline |
|
d |
Maintain a water layer in the pond or use a dust suppressant such as lime milk in dry areas |
BAT 32. In order to reduce diffuse emissions from copper-rich slag furnace treatment, BAT is to use a combination of the techniques given below.
|
|
Technique |
|
a |
Dust suppression techniques such as a water spray for handling, storage and crushing of the final slag |
|
b |
Operation of the furnace under negative pressure |
|
c |
Enclosed furnace |
|
d |
Housing, enclosure and hood to collect and transfer the emissions to an abatement system |
|
e |
Covered launder |
BAT 33. In order to reduce diffuse emissions from anode casting in primary and secondary copper production, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Use an enclosed tundish |
|
b |
Use a closed intermediate ladle |
|
c |
Use a hood, equipped with an air extraction system, over the casting ladle and over the casting wheel |
BAT 34. In order to reduce diffuse emissions from electrolysis cells, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Addition of surfactants to the electrowinning cells |
Generally applicable |
|
b |
Use covers or a hood to collect and transfer the emissions to an abatement system |
Only applicable for electrowinning cells or refining cells for low-purity anodes. Not applicable when the cell needs to remain uncovered to maintain the cell temperature at workable levels (approximately 65 °C) |
|
c |
Closed and fixed pipelines for transferring the electrolyte solutions |
Generally applicable |
|
d |
Gas extraction from the washing chambers of the cathode stripping machine and anode scrap washing machine |
Generally applicable |
BAT 35. In order to reduce diffuse emissions from the casting of copper alloys, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Use enclosures or hoods to collect and transfer the emissions to an abatement system |
|
b |
Use covering for the melts in holding and casting furnaces |
|
c |
Boosted suction system (24) |
BAT 36. In order to reduce diffuse emissions from non-acid and acid pickling, BAT is to use one of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Encapsulate the pickling line with a solution of isopropanol operating in a closed circuit |
Only applicable for pickling of copper wire rod in continuous operations |
|
b |
Encapsulate the pickling line to collect and transfer the emissions to an abatement system |
Only applicable for acid pickling in continuous operations |
1.2.3.2. Channelled dust emissions
Descriptions of the techniques mentioned in this section are given in Section 1.10.
The BAT-associated emission levels are all given in Table 3.
BAT 37. In order to reduce dust and metal emissions to air from the reception, storage, handling, transport, metering, mixing, blending, crushing, drying, cutting and screening of raw materials, and the pyrolytic treatment of copper turnings in primary and secondary copper production, BAT is to use a bag filter.
BAT 38. In order to reduce dust and metal emissions to air from concentrate drying in primary copper production, BAT is to use a bag filter.
Applicability
In the event of a high organic carbon content in the concentrates (e.g. around 10 wt-%), bag filters may not be applicable (due to blinding of the bags) and other techniques (e.g. ESP) may be used.
BAT 39. In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from the primary copper smelter and converter, BAT is to use a bag filter and/or a wet scrubber.
BAT 40. In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid plant) from the secondary copper smelter and converter and from the processing of secondary copper intermediates, BAT is to use a bag filter.
BAT 41. In order to reduce dust and metal emissions to air from the secondary copper holding furnace, BAT is to use a bag filter.
BAT 42. In order to reduce dust and metal emissions to air from copper-rich slag furnace processing, BAT is to use a bag filter or a scrubber in combination with an ESP.
BAT 43. In order to reduce dust and metal emissions to air from the anode furnace in primary and secondary copper production, BAT is to use a bag filter or a scrubber in combination with an ESP.
BAT 44. In order to reduce dust and metal emissions to air from anode casting in primary and secondary copper production, BAT is to use a bag filter or, in the case of off-gases with a water content close to the dew point, a wet scrubber or a demister.
BAT 45. In order to reduce dust and metal emissions to air from a copper melting furnace, BAT is to select and feed the raw materials according to the furnace type and the abatement system used and to use a bag filter.
Table 3
BAT-associated emission levels for dust emissions to air from copper production
|
Parameter |
BAT |
Process |
BAT-AEL (mg/Nm3) |
|
Dust |
BAT 37 |
Reception, storage, handling, transport, metering, mixing, blending, crushing, drying, cutting and screening of raw materials, and the pyrolytic treatment of copper turnings in primary and secondary copper production |
|
|
BAT 38 |
Concentrate drying in primary copper production |
||
|
BAT 39 |
Primary copper smelter and converter (emissions other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) |
||
|
BAT 40 |
Secondary copper smelter and converter and processing of secondary copper intermediates (emissions other than those that are routed to the sulphuric acid plant) |
||
|
BAT 41 |
Secondary copper holding furnace |
≤ 5 (25) |
|
|
BAT 42 |
Copper-rich slag furnace processing |
||
|
BAT 43 |
Anode furnace (in primary and secondary copper production) |
||
|
BAT 44 |
Anode casting (in primary and secondary copper production) |
||
|
BAT 45 |
Copper melting furnace |
The associated monitoring is in BAT 10.
1.2.3.3. Organic compound emissions
BAT 46. In order to reduce organic compound emissions to air from the pyrolytic treatment of copper turnings, and the drying, smelting and melting of secondary raw materials, BAT is to use one of the techniques given below.
|
|
Technique (33) |
Applicability |
|
a |
Afterburner or post-combustion chamber or regenerative thermal oxidiser |
The applicability is restricted by the energy content of the off-gases that need to be treated, as off-gases with a lower energy content require a higher fuel use |
|
b |
Injection of adsorbent in combination with a bag filter |
Generally applicable |
|
c |
Design of furnace and the abatement techniques according to the raw materials available |
Only applicable to new furnaces or major upgrades of existing furnaces |
|
d |
Select and feed the raw materials according to the furnace and the abatement techniques used |
Generally applicable |
|
e |
Thermal destruction of TVOC at high temperatures in the furnace (> 1 000 °C) |
Generally applicable |
BAT-associated emission levels: See Table 4.
Table 4
BAT-associated emission levels for emissions to air of TVOC from the pyrolytic treatment of copper turnings, and the drying, smelting and melting of secondary raw materials
|
Parameter |
|
|
TVOC |
3-30 |
The associated monitoring is in BAT 10.
BAT 47. In order to reduce organic compound emissions to air from solvent extraction in hydrometallurgical copper production, BAT is to use both of the techniques given below and to determine the VOC emissions annually, e.g. through mass balance.
|
|
Technique |
|
a |
Process reagent (solvent) with lower steam pressure |
|
b |
Closed equipment such as closed mixing tanks, closed settlers and closed storage tanks |
BAT 48. In order to reduce PCDD/F emissions to air from the pyrolytic treatment of copper turnings, smelting, melting, fire refining and converting operations in secondary copper production, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Select and feed the raw materials according to the furnace and the abatement techniques used |
|
b |
Optimise combustion conditions to reduce the emissions of organic compounds |
|
c |
Use charging systems, for a semi-closed furnace, to give small additions of raw material |
|
d |
Thermal destruction of PCDD/F in the furnace at high temperatures (> 850 °C) |
|
e |
Use oxygen injection in the upper zone of the furnace |
|
f |
Internal burner system |
|
g |
Post-combustion chamber or afterburner or regenerative thermal oxidiser (36) |
|
h |
Avoid exhaust systems with a high dust build-up for temperatures > 250 °C |
|
i |
Rapid quenching (36) |
|
j |
Injection of adsorption agent in combination with an efficient dust collection system (36) |
BAT-associated emission levels: See Table 5.
Table 5
BAT-associated emission levels for PCDD/F emissions to air from the pyrolytic treatment of copper turnings, smelting, melting, fire refining and converting operations in secondary copper production
|
Parameter |
BAT-AEL (ng I-TEQ/Nm3) (37) |
|
PCDD/F |
≤ 0,1 |
The associated monitoring is in BAT 10.
1.2.3.4. Sulphur dioxide emissions
Descriptions of the techniques mentioned in this section are given in Section 1.10.
BAT 49. In order to reduce SO2 emissions (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from primary and secondary copper production, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
||||
|
a |
Dry or semi-dry scrubber |
Generally applicable |
||||
|
b |
Wet scrubber |
Applicability may be limited in the following cases:
|
||||
|
c |
Polyether-based absorption/desorption system |
Not applicable in the case of secondary copper production. Not applicable in the absence of a sulphuric acid or liquid SO2 plant |
BAT-associated emission levels: See Table 6.
Table 6
BAT-associated emission levels for SO2 emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant or power plant) from primary and secondary copper production
|
Parameter |
Process |
BAT-AEL (mg/Nm3) (38) |
|
SO2 |
Primary copper production |
50-500 (39) |
|
Secondary copper production |
50-300 |
The associated monitoring is in BAT 10.
1.2.3.5. Acid emissions
BAT 50. In order to reduce acid gas emissions to air from exhaust gases from the electrowinning cells, the electrorefining cells, the washing chamber of the cathode stripping machine and the anode scrap washing machine, BAT is to use a wet scrubber or a demister.
1.2.4. Soil and groundwater
BAT 51. In order to prevent soil and groundwater contamination from copper recovery in the slag concentrator, BAT is to use a drainage system in cooling areas and a correct design of the final slag storage area to collect overflow water and avoid fluid leakage.
BAT 52. In order to prevent soil and groundwater contamination from the electrolysis in primary and secondary copper production, BAT is to use a combination of the techniques given below.
|
|
Technique |
|
a |
Use of a sealed drainage system |
|
b |
Use of impermeable and acid-resistant floors |
|
c |
Use of double-walled tanks or placement in resistant bunds with impermeable floors |
1.2.5. Waste water generation
BAT 53. In order to prevent the generation of waste water from primary and secondary copper production, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Use the steam condensate for heating the electrolysis cells, to wash the copper cathodes or send it back to steam boiler |
|
b |
Reuse the water collected from the cooling area, flotation process and hydro transportation of final slag in the slag concentration process |
|
c |
Recycle the pickling solutions and the rinse water |
|
d |
Treat the residues (crude) from the solvent extraction step in hydrometallurgical copper production to recover the organic solution content |
|
e |
Centrifuge the slurry from cleaning and settlers from the solvent extraction step in hydrometallurgical copper production |
|
f |
Reuse the electrolysis bleed after the metal removal stage in the electrowinning and/or the leaching process |
1.2.6. Waste
BAT 54. In order to reduce the quantities of waste sent for disposal from primary and secondary copper production, BAT is to organise operations so as to facilitate process residues reuse or, failing that, process residues recycling, including by using one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Recover metals from the dust and slime coming from the dust abatement system |
Generally applicable |
|
b |
Reuse or sell the calcium compounds (e.g. gypsum) generated by the abatement of SO2 |
Applicability may be restricted depending on the metal content and on the availability of a market |
|
c |
Regenerate or recycle the spent catalysts |
Generally applicable |
|
d |
Recover metal from the waste water treatment slime |
Applicability may be restricted depending on the metal content and on the availability of a market/process |
|
e |
Use weak acid in the leaching process or for gypsum production |
Generally applicable |
|
f |
Recover the copper content from the rich slag in the slag furnace or slag flotation plant |
|
|
g |
Use the final slag from furnaces as an abrasive or (road) construction material or for another viable application |
Applicability may be restricted depending on the metal content and on the availability of a market |
|
h |
Use the furnace lining for recovery of metals or reuse as refractory material |
|
|
i |
Use the slag from the slag flotation as an abrasive or construction material or for another viable application |
|
|
j |
Use the skimming from the melting furnaces to recover the metal content |
Generally applicable |
|
k |
Use the spent electrolyte bleed to recover copper and nickel. Reuse the remaining acid to make up the new electrolyte or to produce gypsum |
|
|
l |
Use the spent anode as a cooling material in pyrometallurgical copper refining or remelting |
|
|
m |
Use anode slime to recover precious metals |
|
|
n |
Use the gypsum from the waste water treatment plant in the pyrometallurgical process or for sale |
Applicability may be restricted depending on the quality of the generated gypsum |
|
o |
Recover metals from sludge |
Generally applicable |
|
p |
Reuse the depleted electrolyte from the hydrometallurgical copper process as a leaching agent |
Applicability may be restricted depending on the metal content and on the availability of a market/process |
|
q |
Recycle copper scales from rolling in a copper smelter |
Generally applicable |
|
r |
Recover metals from the spent acid pickling solution and reuse the cleaned acid solution |
1.3. BAT CONCLUSIONS FOR ALUMINIUM PRODUCTION INCLUDING ALUMINA AND ANODE PRODUCTION
1.3.1. Alumina production
1.3.1.1. Energy
BAT 55. In order to use energy efficiently during the production of alumina from bauxite, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Description |
Applicability |
|
a |
Plate heat exchangers |
Plate heat exchangers allow a higher heat recovery from the liquor flowing to the precipitation area in comparison with other techniques such as flash cooling plants |
Applicable if the energy from the cooling fluid can be reused in the process and if the condensate balance and the liquor conditions allow it |
|
b |
Circulating fluidised bed calciners |
Circulating fluidised bed calciners have a much higher energy efficiency than rotary kilns, since the heat recovery from the alumina and the flue-gas is greater |
Only applicable to smelter-grade aluminas. Not applicable to speciality/non-smelter-grade aluminas, as these require a higher level of calcination that can currently only be achieved with a rotary kiln |
|
c |
Single stream digestion design |
The slurry is heated up in one circuit without using live steam and therefore without dilution of the slurry (in contrast to the double-stream digestion design) |
Only applicable to new plants |
|
d |
Selection of the bauxite |
Bauxite with a higher moisture content carries more water into the process, which increases the energy need for evaporation. In addition, bauxites with a high monohydrate content (boehmite and/or diaspore) require a higher pressure and temperature in the digestion process, leading to higher energy consumption |
Applicable within the constraints related to the specific design of the plant, since some plants are specifically designed for a certain quality of bauxite, which limits the use of alternative bauxite sources |
1.3.1.2. Air emissions
BAT 56. In order to reduce dust and metal emissions from alumina calcination, BAT is to use a bag filter or an ESP.
1.3.1.3. Waste
BAT 57. In order to reduce the quantities of waste sent for disposal and to improve the disposal of bauxite residues from alumina production, BAT is to use one or both of the techniques given below.
|
|
Technique |
|
a |
Reduce the volume of bauxite residues by compacting in order to minimise the moisture content, e.g. using vacuum or high-pressure filters to form a semi-dry cake |
|
b |
Reduce/minimise the alkalinity remaining in the bauxite residues in order to allow disposal of the residues in a landfill |
1.3.2. Anode production
1.3.2.1. Air emissions
1.3.2.1.1.
BAT 58. In order to reduce dust emissions to air from a paste plant (removing coke dust from operations such as coke storage and grinding), BAT is to use a bag filter.
BAT-associated emission levels: See Table 7.
BAT 59. In order to reduce dust and PAH emissions to air from a paste plant (hot pitch storage, paste mixing, cooling and forming), BAT is to use one or a combination of the techniques given below.
|
|
Technique (40) |
|
a |
Dry scrubber using coke as the adsorbent agent, with or without precooling, followed by a bag filter |
|
b |
Regenerative thermal oxidiser |
|
c |
Catalytic thermal oxidiser |
BAT-associated emission levels: See Table 7.
Table 7
BAT-associated emission levels for dust and BaP (as an indicator of PAH) emissions to air from a paste plant
|
Parameter |
Process |
BAT-AEL (mg/Nm3) |
||||
|
Dust |
|
2-5 (41) |
||||
|
BaP |
Hot pitch storage, paste mixing, cooling and forming |
0,001-0,01 (42) |
The associated monitoring is in BAT 10.
1.3.2.1.2.
BAT 60. In order to reduce dust, sulphur dioxide, PAH and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter, BAT is to use one or a combination of the techniques given below.
|
|
Technique (43) |
Applicability |
||||
|
a |
Use of raw materials and fuels containing a low amount of sulphur |
Generally applicable for reducing SO2 emissions |
||||
|
b |
Dry scrubber using alumina as the adsorbent agent followed by a bag filter |
Generally applicable for reducing dust, PAH and fluoride emissions |
||||
|
c |
Wet scrubber |
Applicability for reducing dust, SO2, PAH and fluoride emissions may be limited in the following cases:
|
||||
|
d |
Regenerative thermal oxidiser in combination with a dust abatement system |
Generally applicable for reducing dust and PAH emissions. |
BAT-associated emission levels: See Table 8.
Table 8
BAT-associated emission levels for dust, BaP (as an indicator of PAH) and fluoride emissions to air from a baking plant in an anode production plant integrated with a primary aluminium smelter
|
Parameter |
BAT-AEL (mg/Nm3) |
|
Dust |
2-5 (44) |
|
BaP |
0,001-0,01 (45) |
|
HF |
0,3-0,5 (44) |
|
Total fluorides |
≤ 0,8 (45) |
The associated monitoring is in BAT 10.
BAT 61. In order to reduce dust, PAH and fluoride emissions to air from a baking plant in a stand-alone anode production plant, BAT is to use a pre-filtration unit and a regenerative thermal oxidiser followed by a dry scrubber (e.g. lime bed).
BAT-associated emission levels: See Table 9.
Table 9
BAT-associated emission levels for dust, BaP (as an indicator of PAH) and fluoride emissions to air from a baking plant in a stand-alone anode production plant
|
Parameter |
BAT-AEL (mg/Nm3) |
|
Dust |
2-5 (46) |
|
BaP |
0,001-0,01 (47) |
|
HF |
≤ 3 (46) |
The associated monitoring is in BAT 10.
1.3.2.2. Waste water generation
BAT 62. In order to prevent the generation of waste water from anode baking, BAT is to use a closed water cycle.
Applicability
Generally applicable to new plants and major upgrades. The applicability may be limited due to water quality and/or product quality requirements.
1.3.2.3. Waste
BAT 63. In order to reduce the quantities of waste sent for disposal, BAT is to recycle carbon dust from the coke filter as a scrubbing medium.
Applicability
There may be restrictions on applicability depending on the ash content of the carbon dust.
1.3.3. Primary aluminium production
1.3.3.1. Air emissions
BAT 64. In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using the Søderberg technology, BAT is to use a combination of the techniques given below.
|
|
Technique |
|
a |
Use of paste with a pitch content between 25 % and 28 % (dry paste) |
|
b |
Upgrade the manifold design to allow closed point feeding operations and improved off-gas collection efficiency |
|
c |
Alumina point feeding |
|
d |
Increased anode height combined with the treatment in BAT 67 |
|
e |
Anode top hooding when high current density anodes are used, connected to the treatment in BAT 67 |
BAT 64(c): Point feeding of alumina avoids the regular crust-breaking (such as during manual side feed or bar broken feed), and thus reduces the associated fluoride and dust emissions.
BAT 64(d): An increased anode height helps to achieve lower temperatures in the anode top, resulting in lower emissions to air.
BAT-associated emission levels: See Table 12.
BAT 65. In order to prevent or collect diffuse emissions from electrolytic cells in primary aluminium production using prebaked anodes, BAT is to use a combination of the techniques given below.
|
|
Technique |
|
a |
Automatic multiple point feeding of alumina |
|
b |
Complete hood coverage of the cell and adequate off-gas extraction rates (to lead the off-gas to the treatment in BAT 67) taking into account fluoride generation from bath and carbon anode consumption |
|
c |
Boosted suction system connected to the abatement techniques listed in BAT 67 |
|
d |
Minimisation of the time for changing anodes and other activities that require cell hoods to be removed |
|
e |
Efficient process control system avoiding process deviations that might otherwise lead to increased cell evolution and emissions |
|
f |
Use of a programmed system for cell operations and maintenance |
|
g |
Use of established efficient cleaning methods in the rodding plant to recover fluorides and carbon |
|
h |
Storage of removed anodes in a compartment near the cell, connected to the treatment in BAT 67, or storage of the butts in confined boxes |
Applicability
BAT 65.c and h are not applicable to existing plants
BAT-associated emission levels: See Table 12.
1.3.3.1.1.
BAT 66. In order to reduce dust emissions from the storage, handling and transport of raw materials, BAT is to use a bag filter.
BAT-associated emission levels: See Table 10.
Table 10
BAT-associated emission levels for dust from the storage, handling and transport of raw materials
|
Parameter |
BAT-AEL (mg/Nm3) (48) |
|
Dust |
≤ 5-10 |
The associated monitoring is in BAT 10.
BAT 67. In order to reduce dust, metal and fluoride emissions to air from electrolytic cells, BAT is to use one of the techniques given below.
|
|
Technique (49) |
Applicability |
||||
|
a |
Dry scrubber using alumina as the adsorbent agent followed by a bag filter |
Generally applicable |
||||
|
b |
Dry scrubber using alumina as the adsorbent agent followed by a bag filter and a wet scrubber |
Applicability may be limited in the following cases:
|
BAT-associated emission levels: See Table 11 and Table 12.
Table 11
BAT-associated emission levels for dust and fluoride emissions to air from electrolytic cells
|
Parameter |
BAT-AEL (mg/Nm3) |
|
Dust |
2-5 (50) |
|
HF |
≤ 1,0 (50) |
|
Total fluorides |
≤ 1,5 (51) |
The associated monitoring is in BAT 10.
1.3.3.1.2.
BAT-associated emission levels for the total emissions of dust and fluoride to air from the electrolysis house (collected from the electrolytic cells and roof vents): See Table 12.
Table 12
BAT-associated emission levels for the total emissions of dust and fluoride to air from the electrolysis house (collected from the electrolytic cells and roof vents)
|
Parameter |
BAT |
BAT-AELs for new plants (kg/t Al) (52) |
|
|
Dust |
Combination of BAT 64, BAT 65 and BAT 67 |
≤ 1,2 |
≤ 0,6 |
|
Total fluorides |
≤ 0,6 |
≤ 0,35 |
The associated monitoring is in BAT 10.
BAT 68. In order to prevent or reduce dust and metal emissions to air from melting and molten metal treatment and casting in primary aluminium production, BAT is to use one or both of the techniques given below.
|
|
Technique |
|
a |
Use of liquid metal from electrolysis and uncontaminated aluminium material, i.e. solid material free of substances such as paint, plastic or oil (e.g. the top and the bottom part of the billets that are cut for quality reasons) |
|
b |
Bag filter (54) |
BAT-associated emission levels: See Table 13.
Table 13
BAT-associated emission levels for dust emissions to air from melting and molten metal treatment and casting in primary aluminium production
|
Parameter |
|
|
Dust |
2-25 |
The associated monitoring is in BAT 10.
1.3.3.1.3.
BAT 69. In order to reduce emissions to air from electrolytic cells, BAT is to use one or both of the techniques given below.
|
|
Technique |
Applicability |
||||
|
a |
Use of low-sulphur anodes |
Generally applicable |
||||
|
b |
Wet scrubber (57) |
Applicability may be limited in the following cases:
|
BAT 69(a): Anodes containing less than 1,5 % sulphur as a yearly average can be produced by an appropriate combination of the raw materials used. A minimum sulphur content of 0,9 % as a yearly average is required for the viability of the electrolysis process.
BAT-associated emission levels: See Table 14.
Table 14
BAT-associated emission levels for SO2 emissions to air from electrolytic cells
|
Parameter |
|
|
SO2 |
≤ 2,5-15 |
The associated monitoring is in BAT 10.
1.3.3.1.4.
BAT 70. In order to reduce perfluorocarbon emissions to air from primary aluminium production, BAT is to use all of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Automatic multiple point feeding of alumina |
Generally applicable |
|
b |
Computer control of the electrolysis process based on active cell databases and monitoring of cell operating parameters |
Generally applicable |
|
c |
Automatic anode effect suppression |
Not applicable to Søderberg cells because the anode design (one piece only) does not allow the bath flow associated with this technique |
BAT 70(c): The anode effect takes place when the alumina content of the electrolyte falls below 1-2 %. During anode effects, instead of decomposing alumina, the cryolite bath is decomposed into metal and fluoride ions, the latter forming gaseous perfluorocarbons, which react with the carbon anode.
1.3.3.1.5.
BAT 71. In order to reduce CO and PAH emissions to air from primary aluminium production using the Søderberg technology, BAT is to combust the CO and the PAH in the cell exhaust gas.
1.3.3.2. Waste water generation
BAT 72. In order to prevent the generation of waste water, BAT is to reuse or recycle cooling water and treated waste water, including rainwater, within the process.
Applicability
Generally applicable to new plants and major upgrades. The applicability may be limited due to water quality and/or product quality requirements. The amount of cooling water, treated waste water and rainwater that is reused or recycled cannot be higher than the amount of water needed for the process.
1.3.3.3. Waste
BAT 73. In order to reduce the disposal of spent pot lining, BAT is to organise operations on site so as to facilitate its external recycling, such as in cement manufacturing in the salt slag recovery process, as a carburiser in the steel or ferro-alloy industry or as a secondary raw material (e.g. rock wool), depending on the end consumer’s requirements.
1.3.4. Secondary aluminium production
1.3.4.1. Secondary materials
BAT 74. In order to increase the raw materials’ yield, BAT is to separate non-metallic constituents and metals other than aluminium by using one or a combination of the techniques given below depending on the constituents of the treated materials.
|
|
Technique |
|
a |
Magnetic separation of ferrous metals |
|
b |
Eddy current separation (using moving electromagnetic fields) of aluminium from the other constituents |
|
c |
Relative density separation (using a fluid with a different density) of different metals and non-metallic constituents |
1.3.4.2. Energy
BAT 75. In order to use energy efficiently, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Preheating of the furnace charge with the exhaust gas |
Only applicable for non-rotating furnaces |
|
b |
Recirculation of the gases with unburnt hydrocarbons back into the burner system |
Only applicable for reverberatory furnaces and dryers |
|
c |
Supply the liquid metal for direct moulding |
Applicability is limited by the time needed for the transportation (maximum 4-5 hours) |
1.3.4.3. Air emissions
BAT 76. In order to prevent or reduce emissions to air, BAT is to remove oil and organic compounds from the swarf before the smelting stage using centrifugation and/or drying (60).
Applicability
Centrifugation is only applicable to highly oil-contaminated swarf, when it is applied before the drying. The removal of oil and organic compounds may not be needed if the furnace and the abatement system are designed to handle the organic material.
1.3.4.3.1.
BAT 77. In order to prevent or reduce diffuse emissions from the pretreatment of scraps, BAT is to use one or both of the techniques given below.
|
|
Technique |
|
a |
Closed or pneumatic conveyor, with an air extraction system |
|
b |
Enclosures or hoods for the charging and for the discharge points, with an air extraction system |
BAT 78. In order to prevent or reduce diffuse emissions from the charging and discharging/tapping of melting furnaces, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Placing a hood on top of the furnace door and at the taphole with off-gas extraction connected to a filtration system |
Generally applicable |
|
b |
Fume collection enclosure that covers both the charging and tapping zones |
Only applicable for stationary drum furnaces |
|
c |
Sealed furnace door (61) |
Generally applicable |
|
d |
Sealed charging carriage |
Only applicable for non-rotating furnaces |
|
e |
Boosted suction system that can be modified according to the process needed (61) |
Generally applicable |
BAT 78(a) and (b): Consist of applying a covering with extraction to collect and handle the off-gases from the process.
BAT 78(d): The skip seals against the open furnace door during the discharge of scrap and maintains furnace sealing during this stage.
BAT 79. In order to reduce emissions from skimmings/dross treatment, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Cooling of skimmings/dross, as soon as they are skimmed from the furnace, in sealed containers under inert gas |
|
b |
Prevention of wetting of the skimmings/dross |
|
c |
Compaction of skimmings/dross with an air extraction and dust abatement system |
1.3.4.3.2.
BAT 80. In order to reduce dust and metal emissions from the swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport in secondary aluminium production, BAT is to use a bag filter.
BAT-associated emission levels: See Table 15.
Table 15
BAT-associated emission levels for dust emissions to air from the swarf drying and the removal of oil and organic compounds from the swarf, from the crushing, milling and dry separation of non-metallic constituents and metals other than aluminium, and from the storage, handling and transport in secondary aluminium production
|
Parameter |
BAT-AEL (mg/Nm3) (62) |
|
Dust |
≤ 5 |
The associated monitoring is in BAT 10.
BAT 81. In order to reduce dust and metal emissions to air from furnace processes such as charging, melting, tapping and molten metal treatment in secondary aluminium production, BAT is to use a bag filter.
BAT-associated emission levels: See Table 16.
Table 16
BAT-associated emission levels for dust emissions to air from furnace processes such as charging, melting, tapping and molten metal treatment in secondary aluminium production
|
Parameter |
BAT-AEL (mg/Nm3) (63) |
|
Dust |
2-5 |
The associated monitoring is in BAT 10.
BAT 82. In order to reduce dust and metal emissions to air from remelting in secondary aluminium production, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Use of uncontaminated aluminium material i.e. solid material free of substances such as paint, plastic or oil (e.g. billets) |
|
b |
Optimise combustion conditions to reduce the emissions of dust |
|
c |
Bag filter |
BAT-associated emission levels: See Table 17.
Table 17
BAT-associated emission levels for dust from remelting in secondary aluminium production
|
Parameter |
|
|
Dust |
2-5 |
The associated monitoring is in BAT 10.
1.3.4.3.3.
BAT 83. In order to reduce emissions to air of organic compounds and PCDD/F from the thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace, BAT is to use a bag filter in combination with at least one of the techniques given below.
|
|
Technique (66) |
|
a |
Select and feed the raw materials according to the furnace and the abatement techniques used |
|
b |
Internal burner system for melting furnaces |
|
c |
Afterburner |
|
d |
Rapid quenching |
|
e |
Activated carbon injection |
BAT-associated emission levels: See Table 18.
Table 18
BAT-associated emission levels for emissions to air of TVOC and PCDD/F from the thermal treatment of contaminated secondary raw materials (e.g. swarf) and from the melting furnace
|
Parameter |
Unit |
BAT-AEL |
|
TVOC |
mg/Nm3 |
≤ 10-30 (67) |
|
PCDD/F |
ng I-TEQ/Nm3 |
≤ 0,1 (68) |
The associated monitoring is in BAT 10.
1.3.4.3.4.
BAT 84. In order to reduce emissions to air of HCl, Cl2 and HF from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment, BAT is to use one or a combination of the techniques given below.
|
Technique |
|
|
a |
Select and feed the raw materials according to the furnace and the abatement techniques used (69) |
|
b |
Ca(OH)2 or sodium bicarbonate injection in combination with a bag filter (69) |
|
c |
Control of the refining process, adapting the quantity of refining gas used to remove the contaminants present into the molten metals |
|
d |
Use of dilute chlorine with inert gas in the refining process |
BAT 84(d): Using chlorine diluted with inert gas instead of only pure chlorine, to reduce the emission of chlorine. Refining can also be performed using only the inert gas.
BAT-associated emission levels: See Table 19.
Table 19
BAT-associated emission levels for HCl, Cl2 and HF emissions to air from the thermal treatment of contaminated secondary raw materials (e.g. swarf), the melting furnace, and remelting and molten metal treatment
|
Parameter |
BAT-AEL (mg/Nm3) |
|
HCl |
≤ 5-10 (70) |
|
Cl2 |
|
|
HF |
≤ 1 (73) |
The associated monitoring is in BAT 10.
1.3.4.4. Waste
BAT 85. In order to reduce the quantities of waste sent for disposal from secondary aluminium production, BAT is to organise operations on site so as to facilitate process residues reuse or, failing that, process residues recycling, including by using one or a combination of the techniques given below.
|
|
Technique |
|
a |
Reuse collected dust in the process in the case of a melting furnace using salt cover or in the salt slag recovery process |
|
b |
Full recycling of the salt slag |
|
c |
Apply skimmings/dross treatment to recover aluminium in the case of furnaces that do not use salt cover |
BAT 86. In order to reduce the quantities of salt slag produced from secondary aluminium production, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Increase the quality of raw material used through the separation of the non-metallic constituents and metals other than aluminium for scraps where aluminium is mixed with other constituents |
Generally applicable |
|
b |
Remove oil and organic constituents from contaminated swarf before melting |
Generally applicable |
|
c |
Metal pumping or stirring |
Not applicable for rotary furnaces |
|
d |
Tilting rotary furnace |
There may be restrictions on the use of this furnace due to the size of the feed materials |
1.3.5. Salt slag recycling process
1.3.5.1. Diffuse emissions
BAT 87. In order to prevent or reduce diffuse emissions from the salt slag recycling process, BAT is to use one or both of the techniques given below.
|
|
Technique |
|
a |
Enclose equipment with gas extraction connected to a filtration system |
|
b |
Hood with gas extraction connected to a filtration system |
1.3.5.2. Channelled dust emissions
BAT 88. In order to reduce dust and metal emissions to air from crushing and dry milling associated with the salt slag recovery process, BAT is to use a bag filter.
BAT-associated emission levels: See Table 20.
Table 20
BAT-associated emission levels for dust emissions to air from crushing and dry milling associated with the salt slag recovery process
|
Parameter |
BAT-AEL (mg/Nm3) (74) |
|
Dust |
2-5 |
The associated monitoring is in BAT 10.
1.3.5.3. Gaseous compounds
BAT 89. In order to reduce gaseous emissions to air from wet milling and leaching from the salt slag recovery process, BAT is to use one or a combination of the techniques given below.
|
|
Technique (75) |
|
a |
Activated carbon injection |
|
b |
Afterburner |
|
c |
Wet scrubber with H2SO4 solution |
BAT-associated emission levels: See Table 21.
Table 21
BAT-associated emission levels for gaseous emissions to air from wet milling and leaching from the salt slag recovery process
|
Parameter |
BAT-AEL (mg/Nm3) (76) |
|
NH3 |
≤ 10 |
|
PH3 |
≤ 0,5 |
|
H2S |
≤ 2 |
The associated monitoring is in BAT 10.
1.4. BAT CONCLUSIONS FOR LEAD AND/OR TIN PRODUCTION
1.4.1. Air emissions
1.4.1.1. Diffuse emissions
BAT 90. In order to prevent or reduce diffuse emissions from preparation (such as metering, mixing, blending, crushing, cutting, screening) of primary and secondary materials (excluding batteries), BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Enclosed conveyer or pneumatic transfer system for dusty material |
Generally applicable |
|
b |
Enclosed equipment. When dusty materials are used the emissions are collected and sent to an abatement system |
Only applicable for feed blends prepared with a dosing bin or loss-in-weight system |
|
c |
Mixing of raw materials carried out in an enclosed building |
Only applicable for dusty materials. For existing plants, application may be difficult due to the space required |
|
d |
Dust suppression systems such as water sprays |
Only applicable for mixing carried out outdoors |
|
e |
Pelletisation of raw materials |
Applicable only when the process and the furnace can use pelletised raw materials |
BAT 91. In order to prevent or reduce diffuse emissions from material pretreatment (such as drying, dismantling, sintering, briquetting, pelletising and battery crushing, screening and classifying) in primary lead and secondary lead and/or tin production, BAT is to use one or both of the techniques given below.
|
|
Technique |
|
a |
Enclosed conveyer or pneumatic transfer system for dusty material |
|
b |
Enclosed equipment. When dusty materials are used the emissions are collected and sent to an abatement system |
BAT 92. In order to prevent or reduce diffuse emissions from charging, smelting and tapping operations in lead and/or tin production, and from pre-decoppering operations in primary lead production, BAT is to use an appropriate combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Encapsulated charging system with an air extraction system |
Generally applicable |
|
b |
Sealed or enclosed furnaces with door sealing (77) for processes with a discontinuous feed and output |
Generally applicable |
|
c |
Operate furnace and gas routes under negative pressure and at a sufficient gas extraction rate to prevent pressurisation |
Generally applicable |
|
d |
Capture hood/enclosures at charging and tapping points |
Generally applicable |
|
e |
Enclosed building |
Generally applicable |
|
f |
Complete hood coverage with an air extraction system |
In existing plants or major upgrades of existing plants, application may be difficult due to the space requirements |
|
g |
Maintain furnace sealing |
Generally applicable |
|
h |
Maintain the temperature in the furnace at the lowest required level |
Generally applicable |
|
i |
Apply a hood at the tapping point, ladles and drossing area with an air extraction system |
Generally applicable |
|
j |
Pretreatment of dusty raw material, such as pelletisation |
Applicable only when the process and the furnace can use pelletised raw materials |
|
k |
Apply a doghouse for ladles during tapping |
Generally applicable |
|
l |
An air extraction system for charging and tapping area connected to a filtration system |
Generally applicable |
BAT 93. In order to prevent or reduce diffuse emissions from remelting, refining and casting in primary and secondary lead and/or tin production, BAT is to use a combination of the techniques given below.
|
|
Technique |
|
a |
Hood on the crucible furnace or kettle with an air extraction system |
|
b |
Lids to close the kettle during the refining reactions and addition of chemicals |
|
c |
Hood with air extraction system at launders and tapping points |
|
d |
Temperature control of the melt |
|
e |
Closed mechanical skimmers for removal of dusty dross/residues |
1.4.1.2. Channelled dust emissions
BAT 94. In order to reduce dust and metal emissions to air from raw material preparation (such as reception, handling, storage, metering, mixing, blending, drying, crushing, cutting and screening) in primary and secondary lead/or and tin production, BAT is to use a bag filter.
BAT-associated emission levels: See Table 22.
Table 22
BAT-associated emission levels for dust emissions to air from raw material preparation in primary and secondary lead and/or tin production
|
Parameter |
BAT-AEL (mg/Nm3) (78) |
|
Dust |
≤ 5 |
The associated monitoring is in BAT 10.
BAT 95. In order to reduce dust and metal emissions to air from battery preparation (crushing, screening and classifying), BAT is to use a bag filter or a wet scrubber.
BAT-associated emission levels: See Table 23.
Table 23
BAT-associated emission levels for dust emissions to air from battery preparation (crushing, screening and classifying)
|
Parameter |
BAT-AEL (mg/Nm3) (79) |
|
Dust |
≤ 5 |
The associated monitoring is in BAT 10.
BAT 96. In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use a bag filter.
BAT-associated emission levels: See Table 24.
Table 24
BAT-associated emission levels for dust and lead emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production
|
Parameter |
BAT-AEL (mg/Nm3) |
|
Dust |
|
|
Pb |
≤ 1 (82) |
The associated monitoring is in BAT 10.
BAT 97. In order to reduce dust and metal emissions to air from remelting, refining and casting in primary and secondary lead and/or tin production, BAT is to use the techniques given below.
|
|
Technique |
|
a |
For pyrometallurgical processes: maintain the temperature of the melt bath at the lowest possible level according to the process stage in combination with a bag filter |
|
b |
For hydrometallurgical processes: use a wet scrubber |
BAT-associated emission levels: See Table 25.
Table 25
BAT-associated emission levels for dust and lead emissions to air from remelting, refining and casting in primary and secondary lead and/or tin production
|
Parameter |
BAT-AEL (mg/Nm3) |
|
Dust |
|
|
Pb |
≤ 1 (85) |
The associated monitoring is in BAT 10.
1.4.1.3. Organic compound emissions
BAT 98. In order to reduce emissions of organic compounds to air from the raw material drying and smelting process in secondary lead and/or tin production, BAT is to use one or a combination of the techniques given below.
|
|
Technique (86) |
Applicability |
|
a |
Select and feed the raw materials according to the furnace and the abatement techniques used |
Generally applicable |
|
b |
Optimise combustion conditions to reduce the emissions of organic compounds |
Generally applicable |
|
c |
Afterburner or regenerative thermal oxidiser |
The applicability is restricted by the energy content of the off-gases that need to be treated, as off-gases with a lower energy content lead to a higher use of fuels |
BAT-associated emission levels: See Table 26.
Table 26
BAT-associated emission levels for TVOC emissions to air from the raw material drying and smelting process in secondary lead and/or tin production
|
Parameter |
BAT-AEL (mg/Nm3) (87) |
|
TVOC |
10-40 |
The associated monitoring is in BAT 10.
BAT 99. In order to reduce PCDD/F emissions to air from the smelting of secondary lead and/or tin raw materials, BAT is to use one or a combination of the techniques given below.
|
Technique |
|
|
a |
Select and feed the raw materials according to the furnace and the abatement techniques used (88) |
|
b |
Use charging systems, for a semi-closed furnace, to give small additions of raw material (88) |
|
c |
Internal burner system (88) for melting furnaces |
|
d |
Afterburner or regenerative thermal oxidiser (88) |
|
e |
Avoid exhaust systems with a high dust build-up at temperatures > 250 °C (88) |
|
f |
Rapid quenching (88) |
|
g |
Injection of adsorption agent in combination with efficient dust collection system (88) |
|
h |
Use of efficient dust collection system |
|
i |
Use of oxygen injection in the upper zone of the furnace |
|
j |
Optimise combustion conditions to reduce the emissions of organic compounds (88) |
BAT-associated emission levels: See Table 27.
Table 27
BAT-associated emission levels for PCDD/F emissions to air from the smelting of secondary lead and/or tin raw materials
|
Parameter |
BAT-AEL (ng I-TEQ/Nm3) (89) |
|
PCDD/F |
≤ 0,1 |
The associated monitoring is in BAT 10.
1.4.1.4. Sulphur dioxide emissions
BAT 100. In order to prevent or reduce SO2 emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
||||
|
a |
Alkaline leaching of raw materials that contain sulphur in the form of sulphate |
Generally applicable |
||||
|
b |
Dry or semi-dry scrubber (90) |
Generally applicable |
||||
|
c |
Wet scrubber (90) |
Applicability may be limited in the following cases:
|
||||
|
d |
Fixation of sulphur in the smelt phase |
Only applicable for secondary lead production |
BAT 100(a): An alkali salt solution is used to remove sulphates from secondary materials prior to smelting.
BAT 100(d): The fixation of sulphur in the smelt phase is achieved by adding iron and soda (Na2CO3) in the smelters which react with the sulphur contained in the raw materials to form Na2S-FeS slag.
BAT-associated emission levels: See Table 28.
Table 28
BAT-associated emission levels for SO2 emissions to air (other than those that are routed to the sulphuric acid or liquid SO2 plant) from charging, smelting and tapping in primary and secondary lead and/or tin production
|
Parameter |
|
|
SO2 |
50-350 |
The associated monitoring is in BAT 10.
1.4.2. Soil and groundwater protection
BAT 101. In order to prevent the contamination of soil and groundwater from battery storage, crushing, screening and classifying operations, BAT is to use an acid-resistant floor surface and a system for the collection of acid spillages.
1.4.3. Waste water generation and treatment
BAT 102. In order to prevent the generation of waste water from the alkaline leaching process, BAT is to reuse the water from the sodium sulphate crystallisation of the alkali salt solution.
BAT 103. In order to reduce emissions to water from battery preparation when the acid mist is sent to the waste water treatment plant, BAT is to operate an adequately designed waste water treatment plant to abate the pollutants contained in this stream.
1.4.4. Waste
BAT 104. In order to reduce the quantities of waste sent for disposal from primary lead production, BAT is to organise operations on site so as to facilitate process residues reuse or, failing that, process residues recycling, including by using one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Reuse of the dust from the dust removal system in the lead production process |
Generally applicable |
|
b |
Se and Te recovery from wet or dry gas cleaning dust/sludge |
The applicability can be limited by the quantity of mercury present |
|
c |
Ag, Au, Bi, Sb and Cu recovery from the refining dross |
Generally applicable |
|
d |
Recovery of metals from the waste water treatment sludge |
Direct smelting of the waste water treatment plant sludge might be limited by the presence of elements such as As, Tl and Cd |
|
e |
Addition of flux materials that make the slag more suitable for external use |
Generally applicable |
BAT 105. In order to allow the recovery of the polypropylene and polyethylene content of the lead battery, BAT is to separate it from the batteries prior to smelting.
Applicability
This may not be applicable for shaft furnaces due to the gas permeability provided by undismantled (whole) batteries, which is required by the furnace operations.
BAT 106. In order to reuse or recover the sulphuric acid collected from the battery recovery process, BAT is to organise operations on site so as to facilitate its internal or external reuse or recycling, including one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Reuse as a pickling agent |
Generally applicable depending on the local conditions such as presence of the pickling process and compatibility of the impurities present in the acid with the process |
|
b |
Reuse as raw material in a chemical plant |
Applicability may be restricted depending on the local availability of a chemical plant |
|
c |
Regeneration of the acid by cracking |
Only applicable when a sulphuric acid or liquid sulphur dioxide plant is present |
|
d |
Production of gypsum |
Only applicable if the impurities present in the recovery acid do not affect the gypsum quality or if gypsum of a lower quality can be used for other purposes such as a flux agent |
|
e |
Production of sodium sulphate |
Only applicable for the alkaline leaching process |
BAT 107. In order to reduce the quantities of waste sent for disposal from secondary lead and/or tin production, BAT is to organise operations on site so as to facilitate process residues reuse or, failing that, process residues recycling, including by using one or a combination of the techniques given below.
|
|
Technique |
|
a |
Reuse the residues in the smelting process to recover lead and other metals |
|
b |
Treat the residues and the wastes in dedicated plants for material recovery |
|
c |
Treat the residues and the wastes so that they can be used for other applications |
1.5. BAT CONCLUSIONS FOR ZINC AND/OR CADMIUM PRODUCTION
1.5.1. Primary zinc production
1.5.1.1. Hydrometallurgical zinc production
1.5.1.1.1.
BAT 108. In order to use energy efficiently, BAT is to recover heat from the off-gases produced in the roaster using one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Use a waste heat boiler and turbines to produce electricity |
Applicability may be restricted depending on energy prices and the energy policy of the Member State |
|
b |
Use a waste heat boiler and turbines to produce mechanical energy to be used within the process |
Generally applicable |
|
c |
Use a waste heat boiler to produce heat to be used within the process and/or for office heating |
Generally applicable |
1.5.1.1.2.
1.5.1.1.2.1. Diffuse emissions
BAT 109. In order to reduce diffuse dust emissions to air from the roaster feed preparation and the feeding itself, BAT is to use one or both of the techniques given below.
|
|
Technique |
|
a |
Wet feeding |
|
b |
Completely enclosed process equipment connected to an abatement system |
BAT 110. In order to reduce diffuse dust emissions to air from calcine processing, BAT is to use one or both of the techniques given below.
|
|
Technique |
|
a |
Perform operations under negative pressure |
|
b |
Completely enclosed process equipment connected to an abatement system |
BAT 111. In order to reduce diffuse emissions to air from leaching, solid-liquid separation and purification, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Cover tanks with a lid |
Generally applicable |
|
b |
Cover process liquid inlet and outlet launders |
Generally applicable |
|
c |
Connect tanks to a central mechanical draught abatement system or to a single tank abatement system |
Generally applicable |
|
d |
Cover vacuum filters with hoods and connect them to an abatement system |
Only applicable to the filtering of hot liquids in the leaching and solid-liquid separation stages |
BAT 112. In order to reduce diffuse emissions to air from electrowinning, BAT is to use additives, especially foaming agents, in the electrowinning cells.
1.5.1.1.2.2. Channelled emissions
BAT 113. In order to reduce dust and metal emissions to air from the handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing, BAT is to use a bag filter.
BAT-associated emission levels: See Table 29.
Table 29
BAT-associated emission levels for dust emissions to air from the handling and storage of raw materials, dry roaster feed preparation, dry roaster feeding and calcine processing
|
Parameter |
BAT-AEL (mg/Nm3) (93) |
|
Dust |
≤ 5 |
The associated monitoring is in BAT 10.
BAT 114. In order to reduce zinc and sulphuric acid emissions to air from leaching, purification and electrolysis, and to reduce arsane and stibane emissions from purification, BAT is to use one or a combination of the techniques given below.
|
|
Technique (94) |
|
a |
Wet scrubber |
|
b |
Demister |
|
c |
Centrifugal system |
BAT-associated emission levels: See Table 30.
Table 30
BAT-associated emission levels for zinc and sulphuric acid emissions to air from leaching, purification and electrolysis and for arsane and stibane emissions from purification
|
Parameter |
BAT-AEL (mg/Nm3) (95) |
|
Zn |
≤ 1 |
|
H2SO4 |
< 10 |
|
Sum of AsH3 and SbH3 |
≤ 0,5 |
The associated monitoring is in BAT 10.
1.5.1.1.3.
BAT 115. In order to prevent soil and groundwater contamination, BAT is to use a watertight bunded area for tanks used during leaching or purification and a secondary containment system of the cell houses.
1.5.1.1.4.
BAT 116. In order to reduce fresh water consumption and prevent the generation of waste water, BAT is to use a combination of the techniques given below.
|
|
Technique |
|
a |
Return of the bleed from the boiler and the water from the closed cooling circuits of the roaster to the wet gas cleaning or the leaching stage |
|
b |
Return of the waste water from the cleaning operations/spills of the roaster, the electrolysis and the casting to the leaching stage |
|
c |
Return of the waste water from the cleaning operations/spills of the leaching and purification, the filter cake washing and the wet gas scrubbing to the leaching and/or purification stages |
1.5.1.1.5.
BAT 117. In order to reduce the quantities of waste sent for disposal, BAT is to organise operations on site so as to facilitate process residues reuse or, failing that, process residues recycling, including by using one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Reuse of the dust collected in the concentrate storage and handling within the process (together with the concentrate feed) |
Generally applicable |
|
b |
Reuse of the dust collected in the roasting process via the calcine silo |
Generally applicable |
|
c |
Recycling of residues containing lead and silver as raw material in an external plant |
Applicable depending on the metal content and on the availability of a market/process |
|
d |
Recycling of residues containing Cu, Co, Ni, Cd, Mn as raw material in an external plant to obtain a saleable product |
Applicable depending on the metal content and on the availability of a market/process |
BAT 118. In order to make the leaching waste suitable for final disposal, BAT is to use one of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Pyrometallurgical treatment in a Waelz kiln |
Only applicable to neutral leaching wastes that do not contain too many zinc ferrites and/or do not contain high concentrations of precious metals |
|
b |
Jarofix process |
Only applicable to jarosite iron residues. Limited applicability due to an existing patent |
|
c |
Sulphidation process |
Only applicable to jarosite iron residues and direct leach residues |
|
d |
Compacting iron residues |
Only applicable to goethite residues and gypsum-rich sludge from the waste water treatment plant |
BAT 118(b): The Jarofix process consists of mixing jarosite precipitates with Portland cement, lime and water.
BAT 118(c): The sulphidation process consists of the addition of NaOH and Na2S to the residues in an elutriating tank and in sulphidation reactors.
BAT 118(d): Compacting iron residues consists of reducing the moisture content by means of filters and the addition of lime or other agents.
1.5.1.2. Pyrometallurgical zinc production
1.5.1.2.1.
1.5.1.2.1.1. Channelled dust emissions
BAT 119. In order to reduce dust and metal emissions to air (other than those that are routed to the sulphuric acid plant) from pyrometallurgical zinc production, BAT is to use a bag filter.
Applicability
In the event of a high organic carbon content in the concentrates (e.g. around 10 wt-%), bag filters might not be applicable due to the blinding of the bags and other techniques (e.g. wet scrubber) might be used.
BAT-associated emission levels: See Table 31.
Table 31
BAT-associated emission levels for dust emissions to air (other than those that are routed to the sulphuric acid plant) from pyrometallurgical zinc production
|
Parameter |
|
|
Dust |
2-5 |
The associated monitoring is in BAT 10.
BAT 120. In order to reduce SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from pyrometallurgical zinc production, BAT is to use a wet desulphurisation technique.
BAT-associated emission levels: See Table 32.
Table 32
BAT-associated emission levels for SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from pyrometallurgical zinc production
|
Parameter |
BAT-AEL (mg/Nm3) (98) |
|
SO2 |
≤ 500 |
The associated monitoring is in BAT 10.
1.5.2. Secondary zinc production
1.5.2.1. Air emissions
1.5.2.1.1.
BAT 121. In order to reduce dust and metal emissions to air from pelletising and slag processing, BAT is to use a bag filter.
BAT-associated emission levels: See Table 33.
Table 33
BAT-associated emission levels for dust emissions to air from pelletising and slag processing
|
Parameter |
BAT-AEL (mg/Nm3) (99) |
|
Dust |
≤ 5 |
The associated monitoring is in BAT 10.
BAT 122. In order to reduce dust and metal emissions to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use a bag filter.
Applicability
A bag filter may not be applicable for a clinker operation (where chlorides need to be abated instead of metal oxides).
BAT-associated emission levels: See Table 34.
Table 34
BAT-associated emission levels for dust emissions to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln
|
Parameter |
|
|
Dust |
2-5 |
The associated monitoring is in BAT 10.
1.5.2.1.2.
BAT 123. In order to reduce emissions of organic compounds to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one or a combination of the techniques given below.
|
|
Technique (103) |
Applicability |
|
a |
Injection of adsorbent (activated carbon or lignite coke) followed by a bag filter and/or ESP |
Generally applicable |
|
b |
Thermal oxidiser |
Generally applicable |
|
c |
Regenerative thermal oxidiser |
May not be applicable due to safety reasons |
BAT-associated emission levels: See Table 35.
Table 35
BAT-associated emission levels for emissions to air of TVOC and PCDD/F from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln
|
Parameter |
Unit |
BAT-AEL |
|
TVOC |
mg/Nm3 |
2-20 (104) |
|
PCDD/F |
ng I-TEQ/Nm3 |
≤ 0,1 (105) |
The associated monitoring is in BAT 10.
1.5.2.1.3.
BAT 124. In order to reduce emissions of HCl and HF to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln, BAT is to use one of the techniques given below.
|
|
Technique (106) |
Process |
||||
|
a |
Injection of adsorbent followed by a bag filter |
|
||||
|
b |
Wet scrubber |
|
BAT-associated emission levels: See Table 36.
Table 36
BAT-associated emission levels for emissions of HCl and HF to air from the melting of metallic and mixed metallic/oxidic streams, and from the slag fuming furnace and the Waelz kiln
|
Parameter |
BAT-AEL (mg/Nm3) (107) |
|
HCl |
≤ 1,5 |
|
HF |
≤ 0,3 |
The associated monitoring is in BAT 10.
1.5.2.2. Waste water generation and treatment
BAT 125. In order to reduce the consumption of fresh water in the Waelz kiln process, BAT is to use multiple-stage countercurrent washing.
Water coming from a previous washing stage is filtered and reused in the following washing stage. Two or three stages can be used, allowing up to three times less water consumption in comparison with single-stage countercurrent washing.
BAT 126. In order to prevent or reduce halide emissions to water from the washing stage in the Waelz kiln process, BAT is to use crystallisation.
1.5.3. Melting, alloying and casting of zinc ingots and zinc powder production
1.5.3.1. Air emissions
1.5.3.1.1.
BAT 127. In order to reduce diffuse dust emissions to air from the melting, alloying and casting of zinc ingots, BAT is to use equipment under negative pressure.
1.5.3.1.2.
BAT 128. In order to reduce dust and metal emissions to air from the melting, alloying and casting of zinc ingots and zinc powder production, BAT is to use a bag filter.
BAT-associated emission levels: See Table 37.
Table 37
BAT-associated emission levels for dust emissions to air from the melting, alloying and casting of zinc ingots and zinc powder production
|
Parameter |
BAT-AEL (mg/Nm3) (108) |
|
Dust |
≤ 5 |
The associated monitoring is in BAT 10.
1.5.3.2. Waste water
BAT 129. In order to prevent the generation of waste water from the melting and casting of zinc ingots, BAT is to reuse the cooling water.
1.5.3.3. Waste
BAT 130. In order to reduce the quantities of waste sent for disposal from the melting of zinc ingots, BAT is to organise operations on site so as to facilitate process residues reuse or, failing that, process residues recycling, including by using one or both of the techniques given below.
|
|
Technique |
|
a |
Use of the oxidised fraction of the zinc dross and the zinc-bearing dust from the melting furnaces in the roasting furnace or in the hydrometallurgical zinc production process |
|
b |
Use of the metallic fraction of the zinc dross and the metallic dross from cathode casting in the melting furnace or recovery as zinc dust or zinc oxide in a zinc refining plant |
1.5.4. Cadmium production
1.5.4.1. Air emissions
1.5.4.1.1.
BAT 131. In order to reduce diffuse emissions to air, BAT is to use one or both of the techniques given below.
|
|
Technique |
|
a |
Central extraction system connected to an abatement system for leaching and solid-liquid separation in hydrometallurgical production; for briquetting/pelletising and fuming in pyrometallurgical production; and for melting, alloying and casting processes |
|
b |
Cover cells for the electrolysis stage in hydrometallurgical production |
1.5.4.1.2.
BAT 132. In order to reduce dust and metal emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots, BAT is to use one or a combination of the techniques given below.
|
|
Technique (109) |
Applicability |
||||
|
a |
Bag filter |
Generally applicable |
||||
|
b |
ESP |
Generally applicable |
||||
|
c |
Wet scrubber |
Applicability may be limited in the following cases:
|
BAT-associated emission levels: See Table 38.
Table 38
BAT-associated emission levels for dust and cadmium emissions to air from pyrometallurgical cadmium production and the melting, alloying and casting of cadmium ingots
|
Parameter |
BAT-AEL (mg/Nm3) (110) |
|
Dust |
2-3 |
|
Cd |
≤ 0,1 |
The associated monitoring is in BAT 10.
1.5.4.2. Waste
BAT 133. In order to reduce the quantities of waste sent for disposal from hydrometallurgical cadmium production, BAT is to organise operations on site so as to facilitate process residues reuse or, failing that, process residues recycling, including by using one of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Extract the cadmium from the zinc process as a cadmium-rich cementate in the purification section, further concentrate and refine it (by electrolysis or a pyrometallurgical process) and finally transform it into marketable cadmium metal or cadmium compounds |
Only applicable if an economically viable demand exists |
|
b |
Extract the cadmium from the zinc process as a cadmium-rich cementate in the purification section, and then apply a set of hydrometallurgical operations in order to obtain a cadmium-rich precipitate (e.g. cement (Cd metal), Cd(OH)2) that is landfilled, while all other process flows are recycled in the cadmium plant or in the zinc plant flow |
Only applicable if suitable landfill is available |
1.6. BAT CONCLUSIONS FOR PRECIOUS METALS PRODUCTION
1.6.1. Air emissions
1.6.1.1. Diffuse emissions
BAT 134. In order to reduce diffuse emissions to air from a pretreatment operation (such as crushing, sieving and mixing), BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Enclose pretreatment areas and transfer systems for dusty materials |
|
b |
Connect pretreatment and handling operations to dust collectors or extractors via hoods and a ductwork system for dusty materials |
|
c |
Electrically interlock pretreatment and handling equipment with their dust collector or extractor, in order to ensure that no equipment may be operated unless the dust collector and filtering system are in operation |
BAT 135. In order to reduce diffuse emissions to air from smelting and melting (both Doré and non-Doré operations), BAT is to use all of the techniques given below.
|
|
Technique |
|
a |
Enclose buildings and/or smelting furnace areas |
|
b |
Perform operations under negative pressure |
|
c |
Connect furnace operations to dust collectors or extractors via hoods and a ductwork system |
|
d |
Electrically interlock furnace equipment with their dust collector or extractor, in order to ensure that no equipment may be operated unless the dust collector and filtering system are in operation |
BAT 136. In order to reduce diffuse emissions to air from leaching and gold electrolysis, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Closed tanks/vessels and closed pipes for transfer of solutions |
|
b |
Hoods and extraction systems for electrolytic cells |
|
c |
Water curtain for gold production, to prevent chlorine gas emissions during the leaching of anode slimes with hydrochloric acid or other solvents |
BAT 137. In order to reduce diffuse emissions from a hydrometallurgical operation, BAT is to use all of the techniques given below.
|
|
Technique |
|
a |
Containment measures, such as sealed or enclosed reaction vessels, storage tanks, solvent extraction equipment and filters, vessels and tanks fitted with level control, closed pipes, sealed drainage systems, and planned maintenance programmes |
|
b |
Reaction vessels and tanks connected to a common ductwork system with off-gas extraction (automatic standby/back-up unit available in case of failure) |
BAT 138. In order to reduce diffuse emissions to air from incineration, calcining and drying, BAT is to use all of the techniques given below.
|
|
Technique |
|
a |
Connect all calcining furnaces, incinerators and drying ovens to a ductwork system extracting process exhaust gases |
|
b |
Scrubber plant on a priority electricity circuit which is served by a back-up generator in the event of power failure |
|
c |
Operating start-up and shutdown, spent acid disposal, and fresh acid make-up of scrubbers via an automated control system |
BAT 139. In order to reduce diffuse emissions to air from the melting of final metal products during refining, BAT is to use both of the techniques given below.
|
|
Technique |
|
a |
Enclosed furnace with negative pressure |
|
b |
Appropriate housing, enclosures and capture hoods with efficient extraction/ventilation |
1.6.1.2. Channelled dust emissions
BAT 140. In order to reduce dust and metal emissions to air from all dusty operations, such as crushing, sieving, mixing, melting, smelting, incineration, calcining, drying and refining, BAT is to use one of the techniques given below.
|
|
Technique (111) |
Applicability |
|
a |
Bag filter |
May not be applicable for off-gases containing a high level of volatilised selenium |
|
b |
Wet scrubber in combination with an ESP, allowing the recovery of selenium |
Only applicable to off-gases containing volatilised selenium (e.g. Doré metal production) |
BAT-associated emission levels: See Table 39.
Table 39
BAT-associated emission levels for dust emissions to air from all dusty operations, such as crushing, sieving, mixing, melting, smelting, incineration, calcining, drying and refining
|
Parameter |
BAT-AEL (mg/Nm3) (112) |
|
Dust |
2-5 |
The associated monitoring is in BAT 10.
1.6.1.3. NOX emissions
BAT 141. In order to reduce NOX emissions to air from a hydrometallurgical operation involving dissolving/leaching with nitric acid, BAT is to use one or both of the techniques given below.
|
|
Technique (113) |
|
a |
Alkaline scrubber with caustic soda |
|
b |
Scrubber with oxidation agents (e.g. oxygen, hydrogen peroxide) and reducing agents (e.g. nitric acid, urea) for those vessels in hydrometallurgical operations with the potential to generate high concentrations of NOX. It is often applied in combination with BAT 141(a) |
BAT-associated emission levels: See Table 40.
Table 40
BAT-associated emission levels for NOX emissions to air from a hydrometallurgical operation involving dissolving/leaching with nitric acid
|
Parameter |
BAT-AEL (mg/Nm3) (114) |
|
NOX |
70-150 |
The associated monitoring is in BAT 10.
1.6.1.4. Sulphur dioxide emissions
BAT 142. In order to reduce SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from a melting and smelting operation for the production of Doré metal, including the associated incineration, calcining and drying operations, BAT is to use one or a combination of the techniques given below.
|
|
Technique (115) |
Applicability |
||||
|
a |
Lime injection in combination with a bag filter |
Generally applicable |
||||
|
b |
Wet scrubber |
Applicability may be limited in the following cases:
|
BAT-associated emission levels: See Table 41.
Table 41
BAT-associated emission levels for SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from a melting and smelting operation for the production of Doré metal, including the associated incineration, calcining and drying operations
|
Parameter |
BAT-AEL (mg/Nm3) (116) |
|
SO2 |
50-480 |
The associated monitoring is in BAT 10.
BAT 143. In order to reduce SO2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use a wet scrubber.
BAT-associated emission levels: See Table 42.
Table 42
BAT-associated emission levels for SO2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations
|
Parameter |
BAT-AEL (mg/Nm3) (117) |
|
SO2 |
50-100 |
The associated monitoring is in BAT 10.
1.6.1.5. HCl and Cl2 emissions
BAT 144. In order to reduce HCl and Cl2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations, BAT is to use an alkaline scrubber.
BAT-associated emission levels: See Table 43.
Table 43
BAT-associated emission levels for HCl and Cl2 emissions to air from a hydrometallurgical operation, including the associated incineration, calcining and drying operations
|
Parameter |
BAT-AEL (mg/Nm3) (118) |
|
HCl |
≤ 5-10 |
|
Cl2 |
0,5-2 |
The associated monitoring is in BAT 10.
1.6.1.6. NH3 emissions
BAT 145. In order to reduce NH3 emissions to air from a hydrometallurgical operation using ammonia or ammonium chloride, BAT is to use a wet scrubber with sulphuric acid.
BAT-associated emission levels: See Table 44.
Table 44
BAT-associated emission levels for NH3 emissions to air from a hydrometallurgical operation using ammonia or ammonium chloride
|
Parameter |
BAT-AEL (mg/Nm3) (119) |
|
NH3 |
1-3 |
The associated monitoring is in BAT 10.
1.6.1.7. PCDD/F emissions
BAT 146. In order to reduce PCDD/F emissions to air from a drying operation where the raw materials contain organic compounds, halogens or other PCDD/F precursors, from an incineration operation, and from a calcining operation, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Afterburner or regenerative thermal oxidiser (120) |
|
b |
Injection of adsorption agent in combination with an efficient dust collection system (120) |
|
c |
Optimise combustion or process conditions for the abatement of emissions of organic compounds (120) |
|
d |
Avoid exhaust systems with a high dust build-up for temperatures > 250 °C (120) |
|
e |
Rapid quenching (120) |
|
f |
Thermal destruction of PCDD/F in the furnace at high temperatures (> 850 °C) |
|
g |
Use of oxygen injection in the upper zone of the furnace |
|
h |
Internal burner system (120) |
BAT-associated emission levels: See Table 45.
Table 45
BAT-associated emission levels for PCDD/F emissions to air from a drying operation where the raw materials contain organic compounds, halogens or other PCDD/F precursors, from an incineration operation, and from a calcining operation
|
Parameter |
BAT-AEL (ng I-TEQ/Nm3) (121) |
|
PCDD/F |
≤ 0,1 |
The associated monitoring is in BAT 10.
1.6.2. Soil and groundwater protection
BAT 147. In order to prevent soil and groundwater contamination, BAT is to use a combination of the techniques given below.
|
|
Technique |
|
a |
Use of sealed drainage systems |
|
b |
Use of double-walled tanks or placement in resistant bunds |
|
c |
Use of impermeable and acid-resistant floors |
|
d |
Automatic level control of reaction vessels |
1.6.3. Waste water generation
BAT 148. In order to prevent the generation of waste water, BAT is to use one or both of the techniques given below.
|
|
Technique |
|
a |
Recycling of spent/recovered scrubbing liquids and other hydrometallurgical reagents in leaching and other refining operations |
|
b |
Recycling of solutions from leaching, extraction and precipitation operations |
1.6.4. Waste
BAT 149. In order to reduce the quantities of waste sent for disposal, BAT is to organise operations on site so as to facilitate process residues reuse or, failing that, process residues recycling, including by using one or a combination of the techniques given below.
|
|
Technique |
Process |
|
a |
Recovery of the metal content from slags, filter dust and residues of the wet dedusting system |
Doré production |
|
b |
Recovery of the selenium collected in the wet dedusting system’s off-gases containing volatilised selenium |
|
|
c |
Recovery of silver from spent electrolyte and spent slime washing solutions |
Silver electrolytic refining |
|
d |
Recovery of metals from residues from electrolyte purification (e.g. silver cement, copper carbonate-based residue) |
|
|
e |
Recovery of gold from electrolyte, slimes and solutions from the gold leaching processes |
Gold electrolytic refining |
|
f |
Recovery of metals from spent anodes |
Silver or gold electrolytic refining |
|
g |
Recovery of platinum group metals from platinum group metal-enriched solutions |
|
|
h |
Recovery of metals from the treatment of process end liquors |
All processes |
1.7. BAT CONCLUSIONS FOR FERRO-ALLOYS PRODUCTION
1.7.1. Energy
BAT 150. In order to use energy efficiently, BAT is to recover energy from the CO-rich exhaust gas generated in a closed submerged arc furnace or in a closed plasma dust process using one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Use of a steam boiler and turbines to recover the energy content of the exhaust gas and produce electricity |
Applicability may be restricted depending on energy prices and the energy policy of the Member State |
|
b |
Direct use of the exhaust gas as fuel within the process (e.g. for drying raw materials, preheating charging materials, sintering, heating of ladles) |
Only applicable if a demand for process heat exists |
|
c |
Use of the exhaust gas as fuel in neighbouring plants |
Only applicable if an economically viable demand for this type of fuel exists |
BAT 151. In order to use energy efficiently, BAT is to recover energy from the hot exhaust gas generated in a semi-closed submerged arc furnace using one or both of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Use of a waste heat boiler and turbines to recover the energy content of the exhaust gas and produce electricity |
Applicability may be restricted depending on energy prices and the energy policy of the Member State |
|
b |
Use of a waste heat boiler to produce hot water |
Only applicable if an economically viable demand exists |
BAT 152. In order to use energy efficiently, BAT is to recover energy from the exhaust gas generated in an open submerged arc furnace via the production of hot water.
Applicability
Only applicable if an economically viable demand for hot water exists.
1.7.2. Air emissions
1.7.2.1. Diffuse dust emissions
BAT 153. In order to prevent or reduce and collect diffuse emissions to air from tapping and casting, BAT is to use one or both of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Use of a hooding system |
For existing plants, applicable depending on the configuration of the plant |
|
b |
Avoid casting by using ferro-alloys in the liquid state |
Only applicable when the consumer (e.g. steel producer) is integrated with the ferro-alloy producer |
1.7.2.2. Channelled dust emissions
BAT 154. In order to reduce dust and metal emissions to air from the storage, handling and transport of solid materials, and from pretreatment operations such as metering, mixing, blending and degreasing, and from tapping, casting and packaging, BAT is to use a bag filter.
BAT-associated emission levels: See Table 46.
BAT 155. In order to reduce dust and metal emissions to air from crushing, briquetting, pelletising and sintering, BAT is to use a bag filter or a bag filter in combination with other techniques.
Applicability
The applicability of a bag filter may be limited in the case of low ambient temperatures (– 20 °C to – 40 °C) and high humidity of the off-gases, as well as for the crushing of CaSi due to safety concerns (i.e. explosivity).
BAT-associated emission levels: See Table 46.
BAT 156. In order to reduce dust and metal emissions to air from an open or a semi-closed submerged arc furnace, BAT is to use a bag filter.
BAT-associated emission levels: See Table 46.
BAT 157. In order to reduce dust and metal emissions to air from a closed submerged arc furnace or a closed plasma dust process, BAT is to use one of the techniques given below.
|
|
Technique (122) |
Applicability |
|
a |
Wet scrubber in combination with an ESP |
Generally applicable |
|
b |
Bag filter |
Generally applicable unless safety concerns exist related to the CO and H2 content in the exhaust gases |
BAT-associated emission levels: See Table 46.
BAT 158. In order to reduce dust and metal emissions to air from a refractory-lined crucible for the production of ferro-molybdenum and ferro-vanadium, BAT is to use a bag filter.
BAT-associated emission levels: See Table 46.
Table 46
BAT-associated emission levels for dust emissions to air from ferro-alloys production
|
Parameter |
Process |
BAT-AEL (mg/Nm3) |
||||||
|
Dust |
|
2-5 (123) |
||||||
|
Crushing, briquetting, pelletising and sintering |
||||||||
|
Open or semi-closed submerged arc furnace |
||||||||
|
2-5 (124) |
The associated monitoring is in BAT 10.
1.7.2.3. PCDD/F emissions
BAT 159. In order to reduce PCDD/F emissions to air from a furnace producing ferro-alloys, BAT is to inject adsorbents and to use an ESP and/or a bag filter.
BAT-associated emission levels: See Table 47.
Table 47
BAT-associated emission levels for PCDD/F emissions to air from a furnace producing ferro-alloys
|
Parameter |
BAT-AEL (ng I-TEQ/Nm3) |
|
PCDD/F |
≤ 0,05 (128) |
The associated monitoring is in BAT 10.
1.7.2.4. PAH and organic compound emissions
BAT 160. In order to reduce PAH and organic compound emissions to air from the degreasing of titanium swarf in rotary kilns, BAT is to use a thermal oxidiser.
1.7.3. Waste
BAT 161. In order to reduce the quantities of slag sent for disposal, BAT is to organise operations on site so as to facilitate slag reuse or, failing that, slag recycling, including by using one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Use of slag in construction applications |
Only applicable to slags from high-carbon FeCr and SiMn production, slags from alloy recovery from steel mill residues and standard exhaust slag from FeMn and FeMo production |
|
b |
Use of slag as sandblasting grit |
Only applicable to slags from high-carbon FeCr production |
|
c |
Use of slag for refractory castables |
Only applicable to slags from high-carbon FeCr production |
|
d |
Use of slag in the smelting process |
Only applicable to slags from silico-calcium production |
|
e |
Use of slag as raw material for the production of silico-manganese or other metallurgical applications |
Only applicable to rich slag (high content of MnO) from FeMn production |
BAT 162. In order to reduce the quantities of filter dust and sludge sent for disposal, BAT is to organise operations on site so as to facilitate filter dust and sludge reuse or, failing that, filter dust and sludge recycling, including one or a combination of the techniques given below.
|
|
Technique |
Applicability (129) |
|
a |
Use of filter dust in the smelting process |
Only applicable to filter dust from FeCr and FeMo production |
|
b |
Use of filter dust in stainless steel production |
Only applicable to filter dust from crushing and screening operations in high-carbon FeCr production |
|
c |
Use of filter dust and sludge as a concentrate feed |
Only applicable to filter dust and sludge from the off-gas cleaning in Mo roasting |
|
d |
Use of filter dust in other industries |
Only applicable to FeMn, SiMn, FeNi, FeMo and FeV production |
|
e |
Use of micro-silica as an additive in the cement industry |
Only applicable to micro-silica from FeSi and Si production |
|
f |
Use of filter dust and sludge in the zinc industry |
Only applicable to furnace dust and wet scrubber sludge from the alloy recovery from steel mill residues |
1.8. BAT CONCLUSIONS FOR NICKEL AND/OR COBALT PRODUCTION
1.8.1. Energy
BAT 163. In order to use energy efficiently, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Use of oxygen-enriched air in smelting furnaces and oxygen converters |
|
b |
Use of heat recovery boilers |
|
c |
Use of the flue-gas generated in the furnace within the process (e.g. drying) |
|
d |
Use of heat exchangers |
1.8.2. Air emissions
1.8.2.1. Diffuse emissions
BAT 164. In order to reduce diffuse dust emissions to air from the charging of a furnace, BAT is to use enclosed conveyor systems.
BAT 165. In order to reduce diffuse dust emissions to air from smelting, BAT is to use covered and hooded launders connected to an abatement system.
BAT 166. In order to reduce diffuse dust emissions from converting processes, BAT is to use operation under negative pressure and capture hoods connected to an abatement system.
BAT 167. In order to reduce diffuse emissions from atmospheric and pressure leaching, BAT is to use both of the techniques given below.
|
|
Technique |
|
a |
Sealed or closed reactors, settlers and pressure autoclaves/vessels |
|
b |
Use of oxygen or chlorine instead of air in leaching stages |
BAT 168. In order to reduce diffuse emissions from solvent extraction refining, BAT is to use one of the techniques given below.
|
|
Technique |
|
a |
Use of a low or a high shear mixer for the solvent/aqueous mixture |
|
b |
Use of covers for the mixer and separator |
|
c |
Use of completely sealed tanks connected to an abatement system |
BAT 169. In order to reduce diffuse emissions from electrowinning, BAT is to use a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Collection and reuse of chlorine gas |
Only applicable to chloride-based electrowinning |
|
b |
Use of polystyrene beads to cover cells |
Generally applicable |
|
c |
Use of foaming agents to cover the cells with a stable layer of foam |
Only applicable to sulphate-based electrowinning |
BAT 170. In order to reduce diffuse emissions from the hydrogen reduction process when producing nickel powder and nickel briquettes (pressure processes), BAT is to use a sealed or closed reactor, a settler and a pressure autoclave/vessel, a powder conveyor and a product silo.
1.8.2.2. Channelled dust emissions
BAT 171. When processing sulphidic ores, in order to reduce dust and metal emissions to air from the handling and storage of raw materials, material pretreatment processes (such as ore preparation and ore/concentrate drying), furnace charging, smelting, converting, thermal refining and nickel powder and briquette production, BAT is to use a bag filter or a combination of an ESP and a bag filter.
BAT-associated emission levels: See Table 48.
Table 48
BAT-associated emission levels for dust emissions to air from the handling and storage of raw materials, material pretreatment processes (such as ore preparation and ore/concentrate drying), furnace charging, smelting, converting, thermal refining and nickel powder and briquette production when processing sulphidic ores
|
Parameter |
BAT-AEL (mg/Nm3) (130) |
|
Dust |
2-5 |
The associated monitoring is in BAT 10.
1.8.2.3. Nickel and chlorine emissions
BAT 172. In order to reduce nickel and chlorine emissions to air from the atmospheric or pressure leaching processes, BAT is to use a wet scrubber.
BAT-associated emission levels: See Table 49.
Table 49
BAT-associated emission levels for nickel and chlorine emissions to air from the atmospheric or pressure leaching processes
|
Parameter |
BAT-AEL (mg/Nm3) (131) |
|
Ni |
≤ 1 |
|
Cl2 |
≤ 1 |
The associated monitoring is in BAT 10.
BAT 173. In order to reduce nickel emissions to air from the nickel matte refining process using ferric chloride with chlorine, BAT is to use a bag filter.
BAT-associated emission levels: See Table 50.
Table 50
BAT-associated emission levels for nickel emissions to air from the nickel matte refining process using ferric chloride with chlorine
|
Parameter |
BAT-AEL (mg/Nm3) (132) |
|
Ni |
≤ 1 |
The associated monitoring is in BAT 10.
1.8.2.4. Sulphur dioxide emissions
BAT 174. When processing sulphidic ores, in order to reduce SO2 emissions to air (other than those that are routed to the sulphuric acid plant) from smelting and converting, BAT is to use one of the techniques given below.
|
|
Technique (133) |
|
a |
Lime injection followed by a bag filter |
|
b |
Wet scrubber |
1.8.2.5. NH3 emissions
BAT 175. In order to reduce NH3 emissions to air from nickel powder and briquette production, BAT is to use a wet scrubber.
1.8.3. Waste
BAT 176. In order to reduce the quantities of waste sent for disposal, BAT is to organise operations on site so as to facilitate process residues reuse or, failing that, process residues recycling, including by using one or a combination of the techniques given below.
|
|
Technique |
Applicability |
|
a |
Use of the granulated slag generated in the electric arc furnace (used in smelting) as an abrasive or construction material |
Applicability depends on the metal content of the slag |
|
b |
Use of the off-gas dust recovered from the electric arc furnace (used in smelting) as a raw material for zinc production |
Generally applicable |
|
c |
Use of the matte granulation off-gas dust recovered from the electric arc furnace (used in smelting) as a raw material for the nickel refinery/re-smelting |
Generally applicable |
|
d |
Use of the sulphur residue obtained after matte filtration in the chlorine-based leaching as a raw material for sulphuric acid production |
Generally applicable |
|
e |
Use of the iron residue obtained after sulphate-based leaching as a feed to the nickel smelter |
Applicability depends on the metal content of the waste |
|
f |
Use of the zinc carbonate residue obtained from the solvent extraction refining as a raw material for zinc production |
Applicability depends on the metal content of the waste |
|
g |
Use of the copper residues obtained after leaching from the sulphate- and chlorine-based leaching as a raw material for copper production |
Generally applicable |
1.9. BAT CONCLUSIONS FOR CARBON AND/OR GRAPHITE PRODUCTION
1.9.1. Air emissions
1.9.1.1. Diffuse emissions
BAT 177. In order to reduce diffuse PAH emissions to air from the storage, handling and transport of liquid pitch, BAT is to use one or a combination of the techniques given below.
|
|
Technique |
|
a |
Back-venting of the liquid pitch storage tank |
|
b |
Condensation by external and/or internal cooling with air and/or water systems (e.g. conditioning towers), followed by filtration techniques (adsorption scrubbers or ESP) |
|
c |
Collection and transfer of collected off-gases to abatement techniques (dry scrubber or thermal oxidiser/regenerative thermal oxidiser) available at other stages of the process (e.g. mixing and shaping or baking) |
1.9.1.2. Dust and PAH emissions
BAT 178. In order to reduce dust emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining, BAT is to use a bag filter.
BAT-associated emission levels: See Table 51.
Table 51
BAT-associated emission levels for dust and BaP (as an indicator of PAH) emissions to air from the storage, handling and transportation of coke and pitch, and mechanical processes (such as grinding) and graphitising and machining
|
Parameter |
BAT-AEL (mg/Nm3) (134) |
|
Dust |
2-5 |
|
BaP |
≤ 0,01 (135) |
The associated monitoring is in BAT 10.
BAT 179. In order to reduce dust and PAH emissions to air from the production of green paste and green shapes, BAT is to use one or a combination of the techniques given below.
|
|
Technique (136) |
|
a |
Dry scrubber using coke as the adsorbent agent and with or without precooling, followed by a bag filter |
|
b |
Coke filter |
|
c |
Regenerative thermal oxidiser |
|
d |
Thermal oxidiser |
BAT-associated emission levels: See Table 52.
Table 52
BAT-associated emission levels for dust and BaP (as an indicator of PAH) emissions to air from the production of green paste and green shapes
|
Parameter |
BAT-AEL (mg/Nm3) (137) |
|
Dust |
2-10 (138) |
|
BaP |
0,001-0,01 |
The associated monitoring is in BAT 10.
BAT 180. In order to reduce dust and PAH emissions to air from baking, BAT is to use one or a combination of the techniques given below.
|
|
Technique (139) |
Applicability |
|
a |
ESP, in combination with a thermal oxidation step (e.g. regenerative thermal oxidiser) when highly volatile compounds are expected |
Generally applicable |
|
b |
Regenerative thermal oxidiser, in combination with a pretreatment (e.g. ESP) in cases of a high dust content in the exhaust gas |
Generally applicable |
|
c |
Thermal oxidiser |
Not applicable to continuous ring furnaces |
BAT-associated emission levels: See Table 53.
Table 53
BAT-associated emission levels for dust and BaP (as an indicator of PAH) emissions to air from baking and rebaking
|
Parameter |
BAT-AEL (mg/Nm3) (140) |
|
Dust |
2-10 (141) |
|
BaP |
The associated monitoring is in BAT 10.
BAT 181. In order to reduce dust and PAH emissions to air from impregnation, BAT is to use one or a combination of the techniques given below.
|
|
Technique (144) |
|
a |
Dry scrubber followed by a bag filter |
|
b |
Coke filter |
|
c |
Thermal oxidiser |
BAT-associated emission levels: See Table 54.
Table 54
BAT-associated emission levels for dust and BaP (as an indicator of PAH) emissions to air from impregnation
|
Parameter |
BAT-AEL (mg/Nm3) (145) |
|
Dust |
2-10 |
|
BaP |
0,001-0,01 |
The associated monitoring is in BAT 10.
1.9.1.3. Sulphur dioxide emissions
BAT 182. In order to reduce SO2 emissions to air when there is a sulphur addition in the process, BAT is to use a dry and/or wet scrubber.
1.9.1.4. Organic compound emissions
BAT 183. In order to reduce emissions of organic compounds to air, including phenol and the formaldehyde from the impregnation stage where special impregnation agents such as resins and biodegradable solvents are used, BAT is to use one of the techniques given below.
|
|
Technique (146) |
|
a |
Regenerative thermal oxidiser in combination with an ESP for the mixing, baking and impregnation stages |
|
b |
Biofilter and/or bioscrubber for the impregnation stage where special impregnation agents such as resins and biodegradable solvents are used |
BAT-associated emission levels: See Table 55.
Table 55
BAT-associated emission levels for TVOC emissions to air from mixing, baking and impregnation
|
Parameter |
|
|
TVOC |
≤ 10-40 |
The associated monitoring is in BAT 10.
1.9.2. Waste
BAT 184. In order to reduce the quantities of waste sent for disposal, BAT is to organise operations on site so as to facilitate process residues reuse or, failing that, process residues recycling, including by reuse or recycling of carbon and other residues from the production processes within the process or in other external processes.
1.10. DESCRIPTION OF TECHNIQUES
1.10.1. Air emissions
The techniques described below are listed according to the main pollutant(s) they are aimed to abate.
1.10.1.1. Dust emissions
|
Technique |
Description |
|
Bag filter |
Bag filters, often referred to as fabric filters, are constructed from porous woven or felted fabric through which gases flow to remove particles. The use of a bag filter requires a fabric material selection suited to the characteristics of the off-gases and the maximum operating temperature. |
|
Electrostatic precipitator (ESP) |
Electrostatic precipitators operate such that particles are charged and separated under the influence of an electrical field. They are capable of operating over a wide range of conditions. In a dry ESP, the collected material is mechanically removed (e.g. by shaking, vibration, compressed air), while in a wet ESP it is flushed with a suitable liquid, usually water. |
|
Wet scrubber |
Wet scrubbing entails separating the dust by intensively mixing the incoming gas with water, usually combined with the removal of the coarse particles through the use of centrifugal force. The removed dust is collected at the bottom of the scrubber. Also, substances such as SO2, NH3, some VOC and heavy metals may be removed |
1.10.1.2. NOX emissions
|
Technique |
Description |
|
Low-NOX burner |
Low-NOX burners reduce the formation of NOX by reducing peak flame temperatures, delaying but completing the combustion and increasing the heat transfer (increased emissivity of the flame). The ultra-low-NOx burners includes combustion staging (air/fuel) and flue-gas recirculation |
|
Oxy-fuel burner |
The technique involves the replacement of the combustion air with oxygen, with the consequent elimination/reduction of thermal NOX formation from nitrogen entering the furnace. The residual nitrogen content in the furnace depends on the purity of the oxygen supplied, on the quality of the fuel and on the potential air inlet |
|
Flue-gas recirculation |
This implies the reinjection of flue-gas from the furnace into the flame to reduce the oxygen content and therefore the temperature of the flame. The use of special burners is based on internal recirculation of combustion gases which cool the root of the flames and reduce the oxygen content in the hottest part of the flames |
1.10.1.3. SO2, HCl, and HF emissions
|
Technique |
Description |
|
Dry or semi-dry scrubber |
Dry powder or a suspension/solution of an alkaline reagent (e.g. lime or sodium bicarbonate) is introduced and dispersed in the off-gas stream. The material reacts with the acidic gaseous species (e.g. SO2) to form a solid which is removed by filtration (bag filter or electrostatic precipitator). The use of a reaction tower improves the removal efficiency of the scrubbing system. Adsorption can also be achieved by the use of packed towers (e.g. coke filter). For existing plants, the performance is linked to process parameters such as temperature (min. 60 °C), moisture content, contact time, gas fluctuations and to the capability of the dust filtration system (e.g. bag filter) to cope with the additional dust load |
|
Wet scrubber |
In the wet scrubbing process, gaseous compounds are dissolved in a scrubbing solution (e.g. an alkaline solution containing lime, NaOH, or H2O2). Downstream of the wet scrubber, the off-gases are saturated with water and a separation of the droplets is carried out before discharging the off-gases. The resulting liquid is further treated by a waste water process and the insoluble matter is collected by sedimentation or filtration. For existing plants, this technique may require significant space availability |
|
Use of low-sulphur fuels |
The use of natural gas or low-sulphur fuel oil reduces the amount of SO2 and SO3 emissions from the oxidation of sulphur contained in the fuel during combustion |
|
Polyether-based absorption/desorption system |
A polyether-based solvent is used to selectively absorb the SO2 from the exhaust gases. Then the absorbed SO2 is stripped in another column and the solvent is fully regenerated. The stripped SO2 is used to produce liquid SO2 or sulphuric acid |
1.10.1.4. Mercury emissions
|
Technique |
Description |
|
Activated carbon adsorption |
This process is based on the adsorption of mercury onto the activated carbon. When the surface has adsorbed as much as it can, the adsorbed content is desorbed as part of the regeneration of the adsorbent |
|
Selenium adsorption |
This process is based on the use of selenium-coated spheres in a packed bed. The red amorphous selenium reacts with the mercury in the gas to form HgSe. The filter is then treated to regenerate the selenium. |
1.10.1.5. VOC, PAH, and PCDD/F emissions
|
Technique |
Description |
|
Afterburner or thermal oxidiser |
Combustion system in which the pollutant within the exhaust gas stream reacts with oxygen in a temperature-controlled environment to create an oxidation reaction |
|
Regenerative thermal oxidiser |
Combustion system that employs a regenerative process to utilise the thermal energy in the gas and carbon compounds by using refractory support beds. A manifold system is needed to change the direction of the gas flow to clean the bed. It is also known as a regenerative afterburner |
|
Catalytic thermal oxidiser |
Combustion system where the decomposition is carried out on a metal catalyst surface at lower temperatures, typically from 350 °C to 400 °C. It is also known as a catalytic afterburner |
|
Biofilter |
It consists of a bed of organic or inert material, where pollutants from off-gas streams are biologically oxidised by microorganisms |
|
Bioscrubber |
It combines wet gas scrubbing (absorption) and biodegradation, the scrubbing water containing a population of microorganisms suitable to oxidise the noxious gas components |
|
Select and feed the raw materials according to the furnace and the abatement techniques used |
The raw materials are selected in such a way that the furnace and the abatement system used to achieve the required abatement performance can treat the contaminants contained in the feed properly |
|
Optimise combustion conditions to reduce the emissions of organic compounds |
Good mixing of air or oxygen and carbon content, control of the temperature of the gases and residence time at high temperatures to oxidise the organic carbon comprising PCDD/F. It can also include the use of enriched air or pure oxygen |
|
Use charging systems, for a semi-closed furnace, to give small additions of raw material |
Add raw material in small portions in semi-closed furnaces to reduce the furnace cooling effect during charging. This maintains a higher gas temperature and prevents the reformation of PCDD/F |
|
Internal burner system |
The exhaust gas is directed through the burner flame and the organic carbon is converted with oxygen to CO2 |
|
Avoid exhaust systems with a high dust build-up for temperatures > 250 °C |
The presence of dust at temperatures above 250 °C promotes the formation of PCDD/F by de novo synthesis |
|
Injection of adsorption agent in combination with efficient dust collection system |
PCDD/F may be adsorbed onto dust and hence emissions can be reduced using an efficient dust filtration system. The use of a specific adsorption agent promotes this process and reduces the emissions of PCDD/F |
|
Rapid quenching |
PCDD/F de novo synthesis is prevented by rapid gas cooling from 400 °C to 200 °C |
1.10.2. Water emissions
|
Techniques |
Descriptions |
|
Chemical precipitation |
The conversion of dissolved pollutants into an insoluble compound by adding chemical precipitants. The solid precipitates formed are subsequently separated by sedimentation, flotation or filtration. If necessary, this may be followed by ultrafiltration or reverse osmosis. Typical chemicals used for metal precipitation are lime, sodium hydroxide, and sodium sulphide. |
|
Sedimentation |
The separation of suspended particles and suspended material by gravitational settling |
|
Flotation |
The separation of solid or liquid particles from waste water by attaching them to fine gas bubbles, usually air. The buoyant particles accumulate at the water surface and are collected with skimmers |
|
Filtration |
The separation of solids from waste water by passing them through a porous medium. Sand is the most commonly used filtering medium |
|
Ultrafiltration |
A filtration process in which membranes with pore sizes of approximately 10 μm are used as the filtering medium |
|
Activated carbon filtration |
A filtration process in which activated carbon is used as the filtering medium |
|
Reverse osmosis |
A membrane process in which a pressure difference applied between the compartments separated by the membrane causes water to flow from the more concentrated solution to the less concentrated one |
1.10.3. Other
|
Techniques |
Descriptions |
|
Demister |
Demisters are filter devices that remove entrained liquid droplets from a gas stream. They consist of a woven structure of metal or plastic wires, with a high specific surface area. Through their momentum, small droplets present in the gas stream impinge against the wires and coalesce into bigger drops |
|
Centrifugal system |
Centrifugal systems use inertia to remove droplets from off-gas streams by imparting centrifugal forces |
|
Boosted suction system |
Systems designed to modify the extraction fan capacity based on the sources of the fumes which change over the charging, melting and tapping cycles. Automated control of the burner rate during charging is also applied to ensure a minimum gas flow during operations with the door opened |
|
Centrifugation of swarf |
Centrifugation is a mechanical method to separate the oil from the swarf. To increase the velocity of the sedimentation process, a centrifugation force is applied to the swarf and the oil is separated |
|
Drying of swarf |
The swarf drying process uses an indirectly heated rotary drum. To remove the oil, a pyrolytic process takes place at a temperature between 300 °C and 400 °C |
|
Sealed furnace door or furnace door sealing |
The furnace door is designed to provide efficient sealing to prevent diffuse emissions escaping and to maintain the positive pressure inside the furnace during the smelting/melting stage |
(1) For batch processes, the average of a representative number of measurements taken over the total batch time or the result of a measurement carried out over the total batch time can be used.
(2) For discontinuous flows, a different sampling procedure yielding representative results (e.g. spot sampling) can be used.
(3) For sources of high emissions, BAT is continuous measurement or, where continuous measurement is not applicable, more frequent periodic monitoring.
(4) For small sources (< 10 000 Nm3/h) of dust emissions from the storage and handling of raw materials, monitoring could be based on the measurement of surrogate parameters (such as the pressure drop).
(5) The metals to be monitored depend on the composition of the raw materials used.
(6) Related to BAT 69(a), a mass balance can be used to calculate SO2 emissions, based on the measurement of the sulphur content of each of the anode batches consumed.
(7) Where relevant in view of factors such as the halogenated organic compounds content of the raw materials used, the temperature profile, etc.
(8) Monitoring is relevant when the raw materials contain sulphur.
(9) Monitoring may not be relevant for hydrometallurgical processes.
(10) Where relevant in view of the organic compounds content of the raw materials used.
(11) Descriptions of the techniques are given in Section 1.10.
(12) As a daily average or as an average over the sampling period.
(13) The lower end of the range is associated with the use of adsorbents (e.g. activated carbon, selenium) in combination with dust filtration, except for processes using Waelz kilns.
(14) Descriptions of the techniques are given in Section 1.10.
(15) The monitoring frequency may be adapted if the data series clearly demonstrate sufficient stability of the emissions.
(16) Note: ‘other non-ferrous metals’ means the production of non-ferrous metals other than those dealt with specifically in Sections 1.2 to 1.8.
(17) The metals monitored depend on the composition of the raw material used.
(18) Descriptions of the techniques are given in Section 1.10.
(19) In the case of a high arsenic content in the total input of the plant, the BAT-AEL may be up to 0,2 mg/l.
(20) Description of the technique is given in Section 1.10.
(21) Description of the technique is given in Section 1.10.
(22) Description of the technique is given in Section 1.10.
(23) Description of the technique is given in Section 1.10.
(24) Description of the technique is given in Section 1.10.
(25) As an average over the sampling period.
(26) As a daily average or as an average over the sampling period.
(27) As a daily average.
(28) Dust emissions are expected to be towards the lower end of the range when emissions of heavy metals are above the following levels: 1 mg/Nm3 for lead, 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium.
(29) When the concentrates used have a high organic carbon content (e.g. around 10 wt-%), emissions of up to 10 mg/Nm3 can be expected.
(30) Dust emissions are expected to be towards the lower end of the range when emissions of lead are above 1 mg/Nm3.
(31) The lower end of the range is associated with the use of a bag filter.
(32) Dust emissions are expected to be towards the lower end of the range when emissions of copper are above 1 mg/Nm3.
(33) Descriptions of the techniques are given in Section 1.10.
(34) As a daily average or as an average over the sampling period.
(35) The lower end of the range is associated with the use of a regenerative thermal oxidiser.
(36) Descriptions of the techniques are given in Section 1.10.
(37) As an average over a sampling period of at least six hours.
(38) As a daily average or as an average over the sampling period.
(39) In the case of using a wet scrubber or a concentrate with a low sulphur content, the BAT-AEL can be up to 350 mg/Nm3.
(40) Descriptions of the techniques are given in Section 1.10.
(41) As a daily average or as an average over the sampling period.
(42) As an average over the sampling period.
(43) Descriptions of the techniques are given in Section 1.10.
(44) As a daily average or as an average over the sampling period.
(45) As an average over the sampling period.
(46) As a daily average.
(47) As an average over the sampling period.
(48) As an average over the sampling period.
(49) Descriptions of the techniques are given in Section 1.10
(50) As a daily average or as an average over the sampling period.
(51) As an average over the sampling period.
(52) As mass of pollutant emitted during a year from the electrolysis house divided by the mass of liquid aluminium produced in the same year.
(53) These BAT-AELs are not applicable to plants that due to their configuration cannot measure roof emissions.
(54) Description of the technique is given in Section 1.10.
(55) As an average of the samples obtained over a year.
(56) The lower end of the range is associated with the use of a bag filter.
(57) Description of the technique is given in Section 1.10.
(58) As mass of pollutant emitted during a year divided by the mass of liquid aluminium produced in the same year.
(59) The lower end of the range is associated with the use of a wet scrubber. The higher end of the range is associated with the use of low-sulphur anodes.
(60) Description of the techniques are given in Section 1.10.
(61) Description of the technique is given in Section 1.10.
(62) As an average over the sampling period.
(63) As a daily average or as an average over the sampling period.
(64) As an average over the sampling period.
(65) For furnaces designed to use and using only uncontaminated raw material, for which dust emissions are below 1 kg/h, the upper end of the range is 25 mg/Nm3 as an average of the samples obtained over a year.
(66) Descriptions of the techniques are given in Section 1.10.
(67) As a daily average or as an average over the sampling period.
(68) As an average over a sampling period of at least six hours.
(69) Description of the techniques are given in Section 1.10.
(70) As a daily average or as an average over the sampling period. For refining carried out with chemicals containing chlorine, the BAT-AEL refers to the average concentration during chlorination.
(71) As an average over the sampling period. For refining carried out with chemicals containing chlorine, the BAT-AEL refers to the average concentration during chlorination.
(72) Only applicable to emissions from refining processes carried out with chemicals containing chlorine.
(73) As an average over the sampling period.
(74) As a daily average or as an average over the sampling period.
(75) Descriptions of the techniques are given in Section 1.10.
(76) As an average over the sampling period.
(77) Descriptions of the techniques are given in Section 1.10.
(78) As a daily average or as an average over the sampling period.
(79) As an average over the sampling period.
(80) As a daily average or as an average over the sampling period.
(81) Dust emissions are expected to be towards the lower end of the range when emissions are above the following levels: 1 mg/Nm3 for copper, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium.
(82) As an average over the sampling period.
(83) As a daily average or as an average over the sampling period.
(84) Dust emissions are expected to be towards the lower end of the range when emissions are above the following levels: 1 mg/Nm3 for copper, 1 mg/Nm3 for antimony, 0,05 mg/Nm3 for arsenic, 0,05 mg/Nm3 for cadmium.
(85) As an average over the sampling period.
(86) Descriptions of the techniques are given in Section 1.10.
(87) As a daily average or as an average over the sampling period.
(88) Descriptions of the techniques are given in Section 1.10.
(89) As an average over a sampling period of at least six hours.
(90) Descriptions of the techniques are given in Section 1.10.
(91) As a daily average or as an average over the sampling period.
(92) When wet scrubbers are not applicable, the upper end of the range is 500 mg/Nm3.
(93) As an average over the sampling period.
(94) Descriptions of the techniques are given in Section 1.10.
(95) As an average over the sampling period.
(96) As a daily average or as an average over the sampling period.
(97) When a bag filter is not applicable, the upper end of the range is 10 mg/Nm3.
(98) As a daily average.
(99) As an average over the sampling period.
(100) As a daily average or as an average over the sampling period.
(101) When a bag filter is not applicable, the upper end of the range may be higher, up to 15 mg/Nm3.
(102) Dust emissions are expected to be towards the lower end of the range when emissions of arsenic or cadmium are above 0,05 mg/Nm3.
(103) Descriptions of the techniques are given in Section 1.10.
(104) As a daily average or as an average over the sampling period.
(105) As an average over a sampling period of at least six hours.
(106) Descriptions of the techniques are given in Section 1.10.
(107) As an average over the sampling period.
(108) As an average over the sampling period.
(109) Descriptions of the techniques are given in Section 1.10.
(110) As an average over the sampling period.
(111) Descriptions of the techniques are given in Section 1.10.
(112) As a daily average or as an average over the sampling period.
(113) Descriptions of the techniques are given in Section 1.10.
(114) As an hourly average or as an average over the sampling period.
(115) Descriptions of the techniques are given in Section 1.10.
(116) As a daily average or as an average over the sampling period.
(117) As a daily average or as an average over the sampling period.
(118) As an average over the sampling period.
(119) As an average over the sampling period.
(120) Descriptions of the techniques are given in Section 1.10.
(121) As an average over a sampling period of at least six hours.
(122) Descriptions of the techniques are given in Section 1.10.
(123) As an average over the sampling period.
(124) As a daily average or as an average over the sampling period.
(125) The upper end of the range can be up to 10 mg/Nm3 for cases where a bag filter cannot be used.
(126) The upper end of the range may be up to 15 mg/Nm3 for the production of FeMn, SiMn, CaSi due to the sticky nature of the dust (caused e.g. by its hygroscopic capacity or chemical characteristics) affecting the efficiency of the bag filter.
(127) Dust emissions are expected to be towards the lower end of the range when emissions of metals are above the following levels: 1 mg/Nm3 for lead, 0,05 mg/Nm3 for cadmium, 0,05 mg/Nm3 for chromiumVI, 0,05 mg/Nm3 for thallium.
(128) As an average over a sampling period of at least six hours.
(129) Highly contaminated dusts and sludges cannot be reused or recycled. Reuse and recycling might also be limited by accumulation problems (e.g. reusing dust from FeCr production might lead to Zn accumulation in the furnace).
(130) As a daily average or as an average over the sampling period.
(131) As an average over the sampling period.
(132) As an average over the sampling period.
(133) Descriptions of the techniques are given in Section 1.10.
(134) As an average over the sampling period.
(135) BaP particles are only expected if processing solid pitch.
(136) Descriptions of the techniques are given in Section 1.10.
(137) As an average over the sampling period.
(138) The lower end of the range is associated with the use of a dry scrubber using coke as the adsorbent agent followed by a bag filter. The upper end of the range is associated with the use of a thermal oxidiser.
(139) Descriptions of the techniques are given in Section 1.10.
(140) As an average over the sampling period.
(141) The lower end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser. The higher end of the range is associated with the use of a thermal oxidiser.
(142) The lower end of the range is associated with the use of a thermal oxidiser. The upper end of the range is associated with the use of a combination of an ESP and a regenerative thermal oxidiser.
(143) For cathode production, the upper end of the range is 0,05 mg/Nm3.
(144) Descriptions of the techniques are given in Section 1.10.
(145) As an average over the sampling period.
(146) Descriptions of the techniques are given in Section 1.10.
(147) As an average over the sampling period.
(148) The lower end of the range is associated with the use of an ESP in combination with a regenerative thermal oxidiser. The upper end of the range is associated with the use of a biofilter and/or a bioscrubber.