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Clean Air Regulations 2014

Key Information

Regulations that are made further to set emission limits, require pollution control systems, and mandate continuous monitoring for industrial and trade premises to reduce air pollution impacts.


Source: AGC - P.U. (A) 151

Regulation 1. Citation

Regulation 2. Interpretation

Regulation 3. Application

Regulation 4. Obligation to comply

Regulation 5. Obligation to notify

Regulation 6. Measures to reduce emission

Regulation 7. Air pollution control system

Regulation 8. Failure in operations of air pollution control system

Regulation 9. Performance monitoring of air pollution control system

Regulation 10. Maintenance of records

Regulation 11. Change in occupancy

Regulation 12. Opacity

Regulation 13. Limit values and technical standards

Regulation 14. Prohibition on emission dilution

Regulation 15. Hazardous substances

Regulation 16. Periodic monitoring

Regulation 17. Continuous emission monitoring

Regulation 18. Emission declaration

Regulation 19. Owner or occupier of premises to render assistance

Regulation 20. Failure of control equipment and emergency requirement

Regulation 21. Accidental emission

Regulation 22. Installation and operation as required by Director General

Regulation 23. Standard method of sampling and analysis of emissions

Regulation 24. Prohibition order

Regulation 25. Licence required to contravene acceptable conditions for emitting emissions into atmosphere

Regulation 26. Schedule of required actions

Regulation 27. Fees

Regulation 28. False or misleading information

Regulation 29. Penalty

Regulation 30. Revocation

FIRST SCHEDULE [Regulations 6 and 13] - ACTIVITIES AND INDUSTRIES SUBJECT TO THE BEST AVAILABLE TECHNIQUES ECONOMICALLY ACHIEVABLE (BAT)

SECOND SCHEDULE [Regulation 13] - LIMIT VALUES AND TECHNICAL STANDARDS (GENERAL)

(I) Control of fuel burning equipment, incinerators and crematoria

Fuel typeFuelFuel quality parameter
Liquid
All
Sulphur content < 500 ppm (per weight)
Solid
Coal
Sulphur content < 1% (per weight)
Biomass
Wood, agricultural waste, etc.: air dry and in its natural composition (e.g. wood without coating, paint or other treatment)
Residues from wood-based industries: without wood preservatives

The CO₂ reference content is 12%.

Fuel typePollutantLimit valueMonitoring
Liquid
Total particulate matter (PM)
Where dust load emitted:
(a) > 0.33 < 1.0 kg/h
(b) ≥ 1.0 kg/h
50 mg/m³
Once/year
2 times/year
Solid
Total particulate matter (PM)
Where dust load emitted:
(a) > 0.44 < 1.0 kg/h
(b) ≥ 1.0 < 1.5 kg/h
(c) ≥ 1.5 < 2.0 kg/h
(d) ≥ 2.0 < 2.5 kg/h
(e) ≥ 2.5 kg/h
150 mg/m³
Once/year
2 times/year
3 times/year
4 times/year
Continuous*
Carbon monoxide (CO)
1000 mg/m³
Periodic

*Averaging time for continuous monitoring is 30 minutes.

NOTE

In the case of boilers, the thermal efficiency shall be at least 90%.

(II) Control of NMVOC emissions

(III) Control of fugitive emissions

Fugitive emissions of NMVOC and dust shall be minimized in accordance with the Guidance Document on Fugitive Emission Control.

(A) Fugitive emissions of NMVOC

(B) Fugitive emissions of dust

THIRD SCHEDULE [Regulation 13] - LIMIT VALUES AND TECHNICAL STANDARDS (BY ACTIVITY OR INDUSTRY)

In this Schedule, “Toxicity Equivalents” or "TEQ” means toxicity equivalents in comparison to 2, 3, 7, 8 tetrachlorinateddibenzo-para-dioxin which is also known as 2, 3, 7, 8 tetrachlorodibenzodioxin or 2, 3, 7, 8 TCDD.

A. HEAT AND POWER GENERATION

  1. Boilers

*The O₂ reference content is 6% for solid fuels and 3% for others.

Fuel typePollutantCapacityLimit valueMonitoring
Solid and liquid fuels
Sum of SO₂ and SO₃, expressed as SO₂
> 10 MWe
500 mg/m³
Continuous*
Sum of NO and NO₂ expressed as NO₂
> 10 MWe
500 mg/m³
Continuous*
Hydrogen chloride (HCl)
> 10 – < 100 MWe
200 mg/m³
Periodic
Hydrogen chloride (HCl)
≥ 100 MWe
100 mg/m³
Periodic
Hydrogen fluoride (HF)
> 10 – < 100 MWe
30 mg/m³
Periodic
Hydrogen fluoride (HF)
≥ 100 MWe
15 mg/m³
Periodic
Carbon monoxide (CO)
> 10 MWe
200 mg/m³
Continuous*
Total PM
> 10 MWe
50 mg/m³
Continuous*
Mercury (Hg)
> 10 MWe
0.03 mg/m³
Periodic
PCDD/PCDF
> 10 MWe
0.1 ng TEQ/m³
Periodic
Gaseous fuels
Sum of NO and NO₂ expressed as NO₂
> 10 MWe
350 mg/m³
Continuous*
Carbon monoxide (CO)
> 10 MWe
50 mg/m³
Continuous*
Total PM
> 10 MWe
5 mg/m³
Periodic

*Averaging time for continuous monitoring is 30 minutes.

  1. Combustion turbines

The O₂ reference content is 15%.

Fuel typePollutantCapacity at ISO conditionsLimit valueMonitoring
Gaseous fuels
Sum of NO and NO₂ expressed as NO₂
> 10 MWe
150 mg/m³
Continuous*
Carbon monoxide (CO)
> 10 MWe
100 mg/m³
Continuous*
Liquid fuels
Sum of NO and NO₂ expressed as NO₂
> 10 MWe
200 mg/m³
Continuous*
Carbon monoxide (CO)
> 10 MWe
100 mg/m³
Continuous*

*Averaging time for continuous monitoring is 30 minutes.

  1. Generator sets for combined heat and power production with a total thermal output ≥ 3 MWe:

The O₂ reference content is 5%.

Fuel typePollutantCapacityLimit valueMonitoring
Liquid or gas fuels
Sum of NO and NO₂ expressed as NO₂
≥ 3 MWe
600 mg/m³
Periodic
Carbon monoxide (CO)
≥ 3 MWe
650 mg/m³
Periodic
Total PM
≥ 3 MWe
80 mg/m³
Periodic

B. PRODUCTION AND PROCESSING OF FERROUS METALS (IRON AND STEEL MILLS)

SourcePollutantLimit valueMonitoring
Sinter plants (waste gas from the sintering belt)
Sum of SO₂ and SO₃, expressed as SO₂
500 mg/m³
Continuous*
Sum of NO and NO₂ expressed as NO₂
400 mg/m³
Continuous*
Total PM
50 mg/m³
Continuous*
Total lead as Pb
1 mg/m³
Periodic
NMVOC
75 mg/m³
Periodic
PCDD/PCDF
0.1 ng TEQ/m³
Periodic
Coke ovens (@ 5% O₂)
Total PM
10 mg/m³
Continuous*
Sum of NO and NO₂ expressed as NO₂
500 mg/m³
Periodic
Sulphur compounds as S
800 mg/m³
Periodic
Blast furnace (Regenerator; @ 3% O₂)
Total PM
50 mg/m³
Continuous*
Basic oxygen furnace (converter gas)
Total PM
50 mg/m³
Continuous*
Electric arc furnaces
Total PM
50 mg/m³
Continuous*
Rolling mill: Thermal treatment furnace (@ 5% O₂)
Sum of NO and NO₂ expressed as NO₂
500 mg/m³
Periodic

*Averaging time for continuous monitoring is 30 minutes.

NOTE
  1. Blast furnace top gas and converter gas shall be actively recycled. If these gases cannot be recycled for safety reasons or in emergencies, they shall be fed into a flare.
  2. Emissions from iron and steel industry shall be minimized by using techniques described in the Best Available Techniques Guidance Document.
  3. These measures include low emission procedures such as dry coke cooling.
  4. Gaseous and volatile organic compounds shall be indicated as total organic carbon.

C. FERROUS METAL FOUNDRIES WITH A CAPACITY ≥ 1 TON MOLTEN METAL PER DAY

SourcePollutantLimit valueMonitoring
Cupola furnace
Sum of SO₂ and SO₃, expressed as SO₂
500 mg/m³
Periodic
Carbon monoxide (CO)
150 mg/m³
Periodic
Core production and casting
Amine
5 mg/m³
Periodic
Benzene
5 mg/m³
Periodic
NOTE

Gaseous and volatile organic compounds shall be indicated as total organic carbon.

D. PRODUCTION AND PROCESSING OF NON-FERROUS METALS WITH A CAPACITY ≥ 0.5 TONS PER DAY FOR LEAD OR CADMIUM OR ≥ 2 TONS PER DAY FOR OTHER METALS

SourcePollutantLimit valueMonitoring
Sinter plants (waste gas from the sintering belt)
Sum of SO₂ and SO₃, expressed as SO₂
500 mg/m³
Continuous*
Sum of NO and NO₂ expressed as NO₂
400 mg/m³
Continuous*
Total PM
50 mg/m³
Continuous*
Total lead as Pb
1 mg/m³
Periodic
NMVOC
75 mg/m³
Periodic
PCDD/PCDF
0.1 ng TEQ/m³
Periodic
Production of copper and zinc
Total PM
20 mg/m³
Continuous*
Production of lead
Total PM
10 mg/m³
Continuous*
Primary aluminium
Total PM
10 mg/m³
Periodic
Fluorine compounds as HF
1 mg/m³
Periodic
Total Fluoride
1.5 mg/m³
Periodic
Sum of SO₂ and SO₃ expressed as SO₂
100 mg/m³
Continuous*
Secondary aluminium(1)
Sum of NO and NO₂ expressed as NO₂
500 mg/m³
Periodic
Smelting, alloying and refining of aluminium(2)
Total PM
10 mg/m³
Continuous*
Smelting, alloying and refining of other non-ferrous metals
Total PM
5 mg/m³
Continuous*

*Averaging time for continuous monitoring is 30 minutes.

NOTE
  1. Gaseous and volatile organic compounds shall be indicated as total organic carbon.
  2. For non-ferrous metal foundries, limit values of ferrous metal foundries apply.
  3. Fugitive dust emissions shall be minimized using Best Available Techniques Economically Achievable Guidance Document.

E. OIL AND GAS INDUSTRIES: REFINERIES (ALL SIZES); NATURAL GAS PROCESSING AND STORAGE; STORAGE AND HANDLING OF PETROLEUM PRODUCTS

SourcePollutantLimit valueMonitoring
Claus plant
Sulphur
Recovery > 95%
Periodic
Catalytic cracking
Total PM
40 mg/m³
Continuous*
Sum of SO₂ and SO₃, expressed as SO₂
1200 mg/m³
Continuous*
Calcination
Total PM
40 mg/m³
Continuous*

*Averaging time for continuous monitoring is 30 minutes.

NOTE
  1. Gases and vapors of organic substances which escape from pressure relief fittings and blow-down systems shall be fed into a gas collecting system.
  2. The collected gases shall be combusted in process furnaces if this is feasible. If this is not feasible, the gases shall be fed into a flare.
  3. Waste gases continually produced by processing systems and waste gases occurring during the regeneration of catalysts, inspections and cleaning operations shall be fed into a post-combustion facility, or equivalent measures to reduce emissions shall be applied.
  4. Gaseous and volatile organic compounds shall be indicated as total organic carbon.
  5. Fugitive emissions of volatile organic substances shall be minimized according to the respective Best Available Techniques Economically Achievable Guidance Document.
  6. For compliance check, a “Leakage Detection and Repair Programme” shall be implemented as outlined in the Guidance Document on Leak Detection and Repair in a manner as specified and approved by the Director General.
  7. Combustion installations using refinery gas or other by-products shall comply with the standards of Fuel Burning Equipment in the Second Schedule or Third Schedule, depending on the thermal output.

F. NON-METALLIC (MINERAL) INDUSTRY: CEMENT PRODUCTION (ALL SIZES); MANUFACTURE OF GLASS INCLUDING GLASS FIBRE WITH A MELTING CAPACITY ≥ 1 TON OF PRODUCT PER DAY; MANUFACTURE OF CERAMIC PRODUCTS BY FIRING, ROOFING TILES, BRICKS, REFRACTORY BRICKS, TILES, CERAMIC GLASS, STONEWARE OR PORCELAIN, WITH A PRODUCTION CAPACITY ≥ 10 TONS OF PRODUCT PER DAY

The O₂ reference content for:
(a) cement kilns is 10%
(b) flame-heated glass melting furnaces is 8%
(c) flame-heated pot furnaces and day tanks furnaces is 13%
(d) ceramic furnaces is 17%

SourcePollutantLimit valueMonitoring
Cement kilns
Sum of NO and NO₂ expressed as NO₂
800 mg/m³
Continuous*
Total PM
50 mg/m³
Continuous*
Mercury
0.05 mg/m³
Periodic
PCDD/PCDF
0.1 ng TEQ/m³
Periodic
Rotary furnaces for the manufacture of hard quicklime or sintering dolomite
Sum of NO and NO₂ expressed as NO₂
1500 mg/m³
Continuous*
Total PM
50 mg/m³
Continuous*
Mercury
0.05 mg/m³
Periodic
PCDD/PCDF
0.1 ng TEQ/m³
Periodic
Glass furnaces
Sum of SO₂ and SO₃ expressed as SO₂
800 mg/m³
Continuous*
Sum of NO and NO₂ expressed as NO₂
800 mg/m³
Continuous*
Total lead as Pb
5 mg/m³
Periodic
Total PM
50 mg/m³
Continuous*
Ceramic furnaces
Sum of SO₂ and SO₃ expressed as SO₂
800 mg/m³
Periodic
Sum of NO and NO₂ expressed as NO₂
800 mg/m³
Periodic
Total PM
Where dust load emitted:
(a) > 0.33 < 1.0 kg/h
(b) ≥ 1.0 < 2.0 kg/h
(c) ≥ 2.0 kg/h
50 mg/m³
Once/year 2 times/year Continuous*

*Averaging time for continuous monitoring is 30 minutes.

NOTE
  1. Glass furnaces: If nitrate purification is required for reasons of glass product quality, sum of NO and NO₂ emissions expressed as NO₂ in waste gas shall not exceed a mass concentration of 1000 mg/m³.
  2. The best available techniques to further reduce emissions, particularly by using improved combustion, shall be applied.
  3. Emission limits for furnaces with oxy-fuel burners shall be considered on a case-by-case basis in accordance with the Best Available Techniques Economically Achievable Guidance Document.
  4. Facilities for the melting of mineral substances including the production of mineral fibres shall comply with a limit value for sum of SO₂ and SO₃, expressed as SO₂ of 1500 mg/m³ corrected to O₂ reference content at 8%.

G. ASPHALT MIXING PLANTS (STATIONARY INSTALLATIONS)

The O₂ reference content is 17%.

Fuel typePollutantLimit valueMonitoring
Liquid and gaseous
Carbon monoxide (CO)
0.50 g/m³
Periodic
Solid
Carbon monoxide (CO)
1.0 g/m³
Periodic
All fuels
Total PM
50 mg/m³
Periodic
NMVOC
50 mg/m³
Periodic
NOTE
  1. Waste gases containing dust from the mineral rotary dryer, the asphalt granulate dryer (parallel dryer), the transport units for hot minerals, the washer and the mixer shall be collected and fed into a de-dusting system.
  2. Crushers for recycled asphalt shall be encapsulated and equipped with effective control equipment to reduce dust emissions, e.g., water sprinklers.
  3. Waste gases from the vicinity of the mixer outflow, the transfer points to the mixer, the transport units for the bituminous mixture and the transfer points to the loading silos which contain organic substances shall be collected and fed into a suitable waste gas purification facility, by feeding the waste gases into the mineral rotary dryer as combustion air.
  4. Emissions of organic substances when the bitumen storage tanks are filled shall preferably be avoided by using the vapor recovery technique.
  5. Gaseous and volatile organic compounds shall be indicated as total organic carbon.

H. PULP AND PAPER INDUSTRY INCLUDING PAPER RECYCLING FACILITIES IN ALL SIZES

SourcePollutantLimit valueMonitoring
Recovery furnaces
PM
150 mg/m³
Periodic
Sum of NO and NO₂ expressed as NO₂
2 kg/t Air Dried Pulp (ADP)
Periodic
Lime kilns
Hydrogen sulfide (H₂S)
15 mg/m³
Periodic
Sum of NO and NO₂ expressed as NO₂
2 kg/t Air Dried Pulp (ADP)
Periodic
Sulfite mills
Total sulfur
1.5 kg/t Air Dried Pulp (ADP)
Periodic
Kraft and others
Total sulfur
1.0 kg/t Air Dried Pulp (ADP)
Periodic
NOTE
  1. Through good planning and construction, as well as optimization of process technology and plant management, emissions of odour-intensive substances such as from waste paper stock, waste paper treatment, interim storage and transportation of waste from waste paper treatment, process water cycles, the water treatment plant and sludge dewatering, shall be prevented as far as possible.
  2. If odour impacts are to be expected in the vicinity of a facility, the best available more extensive techniques to reduce odours shall be used, for example enclosure of the facility components, collection of waste gases and feeding them to a waste gas purification facility.
  3. Emissions of dust and Total Reduced Sulphur (TRS) shall be minimized by using Best Available Techniques Economically Achievable as outlined in the Best Available Techniques Economically Achievable Guidance Document.

I. CHEMICAL AND PETROCHEMICAL INDUSTRY IN ALL SIZES

PollutantLimit valueMonitoring
Hydrogen chloride (HCl)
200 mg/m³
Periodic
Sum of NO and NO₂ expressed as NO₂
700 mg/m³
Periodic
Ammonia (NH₃)
76 mg/m³
Periodic
Chlorine (Cl)
32 mg/m³
Periodic
Sum of SO₂ and SO₃, expressed as SO₂
100 mg/m³
Periodic
Mercury (Hg)
0.05 mg/m³
Periodic
Hydrogen sulphide (H₂S)
7.5 mg/m³
Periodic
Total PM
50 mg/m³
Periodic
NOTE

J. SOLVENT USE IN INDUSTRY: FACILITIES FOR THE SURFACE TREATMENT OF SUBSTANCES, OBJECTS OR PRODUCTS USING ORGANIC SOLVENTS, IN PARTICULAR FOR DRESSING, PRINTING, COATING, DEGREASING, WATERPROOFING, SIZING, PAINTING, CLEANING OR IMPREGNATING, FAT EXTRACTION, WITH A SOLVENT CONSUMPTION CAPACITY OF MORE THAN 200 TONNES PER YEAR

  1. Facilities of this category shall establish a solvent management plan in order to set-up a reduction strategy.
  2. Solvent losses shall be reduced in accordance with Best Available Techniques Economically Achievable limiting these losses to not more than 30% of the solvent input as a general rule.
  3. Actual reduction targets and their time frame shall be set on a case-by-case basis as outlined in the Guidance Document on Fugitive Emission Control.

K. WASTE INCINERATORS IN ALL SIZES

Air pollutant emission from incineration process shall not exceed the concentration limits tabulated below.

The O₂ reference content is 11%.

PollutantLimit valueMonitoring
Total PM
100 mg/m³
Continuous*
NMVOC as total organic carbon
10 mg/m³
Continuous*
Hydrogen chloride (HCl)
40 mg/m³
Continuous*
Hydrogen fluoride (HF)
1 mg/m³
Continuous*
Sum of SO₂ and SO₃ expressed as SO₂
50 mg/m³
Continuous*
Sum of NO and NO₂ expressed as NO₂
200 mg/m³
Continuous*
Carbon monoxide (CO)
50 mg/m³
Continuous*
Cadmium and its compounds, expressed as cadmium (Cd)
0.05 mg/m³
Periodic
Thallium and its compounds, expressed as thallium (Tl)
Mercury and its compounds, expressed as mercury (Hg)
0.05 mg/m³
Periodic
Antimony (Sb), Arsenic (As), Lead (Pb), Chromium (Cr), Cobalt (Co), Copper (Cu), Manganese (Mn), Nickel (Ni), Vanadium (V), and their compounds expressed as the element
Total 0.5 mg/m³
Periodic
PCDD/PCDF
0.1 ng TEQ/m³
Periodic

*Averaging time for continuous monitoring is 30 minutes.

FOURTH SCHEDULE [Regulation 13] - TOXICITY EQUIVALENTS FACTOR (TEFs) FOR DIOXIN AND FURAN

DIOXIN

Chlorine PositionComponentEquivalents Factor
(a)
2,3,7,8 Tetrachlorodibenzodioxin (TCDD)
1
(b)
1,2,3,7,8 Pentachlorodibenzodioxin (PeCDD)
0.5
(c)
1,2,3,4,7,8 Hexachlorodibenzodioxin (HxCDD)
0.1
(d)
1,2,3,7,8,9 Hexachlorodibenzodioxin (HxCDD)
0.1
(e)
1,2,3,6,7,8 Hexachlorodibenzodioxin (HxCDD)
0.1
(f)
1,2,3,4,6,7,8 Heptachlorodibenzodioxin (HpCDD)
0.01
(g)
1,2,3,4,6,7,8,9 Octachlorodibenzodioxin (OCDD)
0.001

FURAN

Chlorine PositionComponentEquivalents Factor
(a)
2,3,7,8 Tetrachlorodibenzofuran (TCDF)
0.1
(b)
2,3,4,7,8 Pentachlorodibenzofuran (PeCDF)
0.5
(c)
1,2,3,7,8 Pentachlorodibenzofuran (PeCDF)
0.05
(d)
1,2,3,4,7,8 Hexachlorodibenzofuran (HxCDF)
0.1
(e)
1,2,3,7,8,9 Hexachlorodibenzofuran (HxCDF)
0.1
(f)
2,3,4,6,7,8 Hexachlorodibenzofuran (HxCDF)
0.1
(g)
1,2,3,4,6,7,8 Heptachlorodibenzofuran (HpCDF)
0.01
(h)
1,2,3,4,7,8,9 Heptachlorodibenzofuran (HpCDF)
0.01
(i)
1,2,3,4,6,7,8,9 Octachlorodibenzofuran (OCDF)
0.001

FIFTH SCHEDULE [Regulation 15] - EMISSION STANDARDS FOR HAZARDOUS SUBSTANCES

Category (1) Extremely hazardous substances

A substance is categorized as extremely hazardous on the basis of extreme toxicity, persistence and tendency towards accumulation. For extremely hazardous substances no limit mass flow or emissions standard applies but the requirement to minimize emissions applies instead. In general, for unintentional releases of Category (1) substances a limit value of 0.1 ng TEQ/m³ shall apply.

Category (2) Carcinogenic substances

For substances classified as hazardous the following limit value shall apply to the sum of all occurring carcinogenic substances in a gas flow:

Class (1)

In the case of an untreated mass flow of 0.5 grams/hour or more an emission standard of 0.10 mg/m³ applies.

Class (2)

In the case of an untreated mass flow of 5 grams/hour or more an emission standard of 1 mg/m³ applies.

Class (3)

In the case of an untreated mass flow of 25 grams/hour or more an emission standard of 5 mg/m³ applies.

Category (3) Gaseous and volatile organic substances

Class (1)

In the case of an untreated mass flow of 0.10 kilograms/hour or more an emission standard of 20 mg/m³ applies.

Class (2)

In the case of an untreated mass flow of 2.0 kilograms/hour or more an emission standard of 100 mg/m³ applies.

Class (3)

In the case of an untreated mass flow of 3.0 kilograms/hour or more an emission standard of 150 mg/m³ applies.

If more than one emission standard applies to a group of substances, the lowest standard will be the norm for the sum of all substances in accordance with the cumulation rule.

Fugitive NMVOC emissions shall be minimized by suitable control measures such as those mentioned in the Guidance Document on Fugitive Emission Control.

Category (4) Gaseous and volatile inorganic substances

(a) Volatile inorganic substances other than Oxides of Sulfur and Oxides of Nitrogen

Class (1)

In the case of an untreated mass flow of 10 grams/hour or more for each substance an emission standard of 1.0 mg/m³ applies.

Class (2)

In the case of an untreated mass flow of 50 grams/hour or more for each substance an emission standard of 5.0 mg/m³ applies.

Class (3)

In the case of an untreated mass flow of 300 grams/hour or more for each substance an emission standard of 30 mg/m³ applies.

In the case of gaseous and volatile inorganic substances the cumulation rule shall not apply.

(b) Oxides of Sulfur and Oxides of Nitrogen

General limit values for oxides of sulphur (sum of SO₂ and SO₃ expressed as SO₂) and oxides of nitrogen (sum of NO and NO₂ expressed as NO₂):

In the case of an untreated mass flow of 5.0 kilograms/hour or more for each substance, an emission standard of 400 mg/m³ shall apply if not stated otherwise in the Third Schedule.

Category (5) Particulate inorganic substances

Class (1)

In the case of an untreated mass flow of 1.0 grams/hour or more an emission standard of 0.20 mg/m³ applies.

Class (2)

In the case of an untreated mass flow of 5.0 grams/hour or more an emission standard of 1.0 mg/m³ applies.

Class (3)

In the case of an untreated mass flow of 25 grams/hour or more an emission standard of 5.0 mg/m³ applies.

If more than one emission standard applies to a group of substances, the lowest value will be the norm for the sum of all substances in accordance with the cumulation rule.

Fugitive particulate emissions shall be minimized by suitable control measures as determined by the Director General.

Category (6) Fibres

Biopersistent ceramic fibres (for example, consisting of aluminium silicate, aluminium oxide, silicon carbide, potassium titanate) in waste gases shall not exceed 1.5 × 10⁴ fibres/m³.

Fibre here means a particle with a length in excess of 5 μm, a width of less than 3 μm and a length/width ratio of more than 3:1.

SIXTH SCHEDULE [Regulation 24] - LIST OF UNDESIRABLE OCCURRENCE

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