Substitutes, melts and moulds of glass, glass fibres and artificial mineral fibres, or

Cleaning of the exhaust air from activities according to Z 1 using aqueous media

chemical processing (acid polishing, etching, matting) of special glass, optical glass or lead glass, or

Cleaning of the exhaust air from activities according to Z 1 with aqueous media

Silverware and copper in flat glass (mirror making),

Silverware of small pieces of glass

further processing of glass fibres or artificial mineral fibres for textile glass products or insulating materials,

Cleaning of the exhaust air from activities according to Z 1 using aqueous media

Waste water from cooling systems and steam generators (§ 4 para. 2 Z 4.1 of the General Waste Water Emissions Ordinance (AAEV), BGBl. No 186/1996),

Waste water from water treatment (§ 4 para. 2 Z 4.4 AAEV),

Wastewater from the electrochemical deposition of metals on glass (§ 4 para. 2 Z 6.4 AAEV),

Wastewater from the production of artificial glass based on organic polymers and

domestic waste water from establishments according to para. 1 to 5.

for establishments or Annexes according to paragraph 1

minimization of leakages and losses,

Recirculation of wash water from the cleaning of the plant and from the exhaust air purification,

Circulation of cooling lubricant emulsions from the design; preferred use of biodegradable coolants; waste water disposal of used non-renewable cooling lubricant emulsions,

Use of physico-chemical waste water purification processes such as removal, sieving, neutralization, filtration, ventilation, precipitation, coagulation and flocculation; waste water disposal of the residues from the waste water purification as waste,

Use of standard techniques of good practice for the reduction of emissions from the storage of liquid raw materials and intermediate products, such as safety containers, inspection/testing of tanks, overfill fuses.

for establishments or Annexes according to paragraph 2

Recirculation of cooling water or cooling emulsions, if necessary with the introduction of purification measures; preferred use of biodegradable coolants in the cooling emulsions,

Use of detergents and cleaners which comply with the requirements of Regulation (EC) No 648/2004 on detergents, OJ L 327, 30.11.2004, p. No. L 104 of 8.4.2004; compliance with ecotoxicological data in the safety data sheets of the working materials used; waiving of organic working and auxiliary substances, in particular organic complexing agents, of which the Total compatibility with aerobic micro-organisms in an aqueous medium after a test period of 28 days is not greater than 80% (ÖNORM EN ISO 7827:2013 04 15),

the most extensive recycling of waste water from mechanical processing, if necessary with the introduction of waste water purification systems into the water cycle; use of carbon dioxide for wastewater neutralization; re-use of Abrasives,

the use of physico-chemical wastewater purification processes,

Separate disposal of contaminated organic solvents, grinding sludges and residues from waste water purification as waste.

for establishments or Annexes in accordance with paragraph 3

use of recovery techniques to re-use the working materials used in the polishing, matting or etching baths;

the most extensive extension of the service life of polishing, matting or etching baths by using regeneration or concentration techniques;

closed circulation of washing water from the exhaust air purification; the most extensive circulation of rinsing waters from the cleaning of the work piece,

the use of physico-chemical wastewater purification processes,

Separate disposal of etch sludges, protective coatings or resins, residues from waste water purification and used non-renewable baths as waste.

for establishments or Annexes pursuant to paragraph 4

the use of recovery techniques for the working materials used (silver in particular),

separate collection of copper-containing and ammoniacal effluents in order to avoid the formation of copper tetramine complexes,

Circulation of rinsing and washing water,

the use of physico-chemical wastewater purification processes,

Separate disposal of silver-or copper-containing sludges as well as residues from waste water purification as waste from wastewater.

for establishments or Annexes pursuant to paragraph 5

Closed circulation of the production water as well as the washing water from the exhaust air cleaning and the cleaning of the plant,

the preferred use of biodegradable fibre binders,

Use of physical-chemical, in the case of direct conductors also biological wastewater purification processes such as e.g. B. Activated Sludge (process) and biofiltration; waste water disposal of the residues of production as well as residues from waste water purification as waste. "

Substitutes, melts and moulds of glass, glass fibres and artificial mineral fibres, or

Cleaning of the exhaust air from activities according to Z 1 using aqueous media

chemical processing (acid polishing, etching, matting) of special glass, optical glass or lead glass, or

Cleaning of the exhaust air from activities according to Z 1 with aqueous media

Silverware and copper in flat glass (mirror making),

Silverware of small pieces of glass

further processing of glass fibres or artificial mineral fibres for textile glass products or insulating materials,

Cleaning of the exhaust air from activities according to Z 1 using aqueous media

Waste water from cooling systems and steam generators (§ 4 para. 2 Z 4.1 of the General Waste Water Emissions Ordinance (AAEV), BGBl. No 186/1996),

Waste water from water treatment (§ 4 para. 2 Z 4.4 AAEV),

Wastewater from the electrochemical deposition of metals on glass (§ 4 para. 2 Z 6.4 AAEV),

Wastewater from the production of artificial glass based on organic polymers and

domestic waste water from establishments according to para. 1 to 5.

for establishments or Annexes according to paragraph 1

minimization of leakages and losses,

Recirculation of wash water from the cleaning of the plant and from the exhaust air purification,

Circulation of cooling lubricant emulsions from the design; preferred use of biodegradable coolants; waste water disposal of used non-renewable cooling lubricant emulsions,

Use of physico-chemical waste water purification processes such as removal, sieving, neutralization, filtration, ventilation, precipitation, coagulation and flocculation; waste water disposal of the residues from the waste water purification as waste,

Use of standard techniques of good practice for the reduction of emissions from the storage of liquid raw materials and intermediate products, such as safety containers, inspection/testing of tanks, overfill fuses.

for establishments or Annexes according to paragraph 2

Recirculation of cooling water or cooling emulsions, if necessary with the introduction of purification measures; preferred use of biodegradable coolants in the cooling emulsions,

Use of detergents and cleaners which comply with the requirements of Regulation (EC) No 648/2004 on detergents, OJ L 327, 30.11.2004, p. No. L 104 of 8.4.2004; compliance with ecotoxicological data in the safety data sheets of the working materials used; waiving of organic working and auxiliary substances, in particular organic complexing agents, of which the Total compatibility with aerobic micro-organisms in an aqueous medium after a test period of 28 days is not greater than 80% (ÖNORM EN ISO 7827:2013 04 15),

the most extensive recycling of waste water from mechanical processing, if necessary with the introduction of waste water purification systems into the water cycle; use of carbon dioxide for wastewater neutralization; re-use of Abrasives,

the use of physico-chemical wastewater purification processes,

Separate disposal of contaminated organic solvents, grinding sludges and residues from waste water purification as waste.

for establishments or Annexes in accordance with paragraph 3

use of recovery techniques to re-use the working materials used in the polishing, matting or etching baths;

the most extensive extension of the service life of polishing, matting or etching baths by using regeneration or concentration techniques;

closed circulation of washing water from the exhaust air purification; the most extensive circulation of rinsing waters from the cleaning of the work piece,

the use of physico-chemical wastewater purification processes,

Separate disposal of etch sludges, protective coatings or resins, residues from waste water purification and used non-renewable baths as waste.

for establishments or Annexes pursuant to paragraph 4

the use of recovery techniques for the working materials used (silver in particular),

separate collection of copper-containing and ammoniacal effluents in order to avoid the formation of copper tetramine complexes,

Circulation of rinsing and washing water,

the use of physico-chemical wastewater purification processes,

Separate disposal of silver-or copper-containing sludges as well as residues from waste water purification as waste from wastewater.

for establishments or Annexes pursuant to paragraph 5

Closed circulation of the production water as well as the washing water from the exhaust air cleaning and the cleaning of the plant,

the preferred use of biodegradable fibre binders,

Use of physical-chemical, in the case of direct conductors also biological wastewater purification processes such as e.g. B. Activated Sludge (process) and biofiltration; waste water disposal of the residues of production as well as residues from waste water purification as waste. "

Unless otherwise provided for in Z 2 to 4, an emission limit for a waste water parameter of Annexes A to E shall be deemed to be complied with if, for five consecutive measurements, four measured values are no greater than those of the Emission limitation and only a measured value does not exceed the emission limit by more than 50% ("4 of 5" rule). "

If no other arrangements are made in Z 2, the measurement should be repeated if a measurement of a wastewater parameter of the installations A to E is determined for up to four times a year of external monitoring of an introduction, the between the emission limit and its 1.5fachem. If the measured value is no greater than the emission limit during the repetition measurement, the emission limit is considered to be complied with. In the case of more frequent external monitoring, the "4 of 5" rule shall apply in accordance with paragraph 2. "

with the day following the event:

Section 1, as amended by Z 1 of the above-mentioned Regulation,

§ 2 in the version of the Z 3 of the above-mentioned regulation, § 3 (2) and (3), § 4 (1), (2) (1) and (2) and (3) (1), § 5 (2) and (4) and (6) and (6) and

Annexes A to F, as amended by Z 13 of the said Regulation,

three years after the end of the day of the event:

Section 1, as amended by Z 2 of the above-mentioned Regulation,

§ 2, as amended by Z 4 of the above-mentioned Regulation; and

Annexes B and C in the version of Z 14 of the said Regulation.

If the initial general adjustment in accordance with § 33c WRG 1959 has never been triggered for the introduction and is not an installation according to § 33c (6) Z 1 WRG 1959, it has pursuant to § 33c (1) WRG 1959 pursuant to section 33c (6) WRG 1959 within five years of the entry into force of the Regulation, to comply with the emission limits of Annexes A to H (for a different waste water parameter in accordance with Article 4 (3) of the AAEV of the corresponding emission limit of Appendix A of the AAEV). If an initial general adjustment according to § 33c WRG 1959 has never been initiated for the introduction and is an installation according to § 33c (6) Z 1 WRG 1959, the introduction pursuant to Section 33c (1) of the WRG 1959 according to section 33c (6) of the German WRG (WRG) 1959 within four years following the publication of the Commission's implementing decision on conclusions on best available techniques (BAT) in accordance with Directive 2010 /75/EU on industrial emissions (integrated prevention and control). Reduction of pollution) ('the IE Directive '), OJ C 327, 30.4.2002, p. No. OJ L 334, 17.12.2010, as amended by the corrigendum OJ L 327, 22.12.2010, p. No. OJ L 158, 19.06.2012, p. 25, with regard to glass production (OJ L 158, 30.4.2012, p 1) must comply with the emission limits of Annexes A to H (for a different waste water parameter in accordance with Article 4 (3) of the AAEV of the corresponding emission limit of Appendix A of the AAEV).

If a general adjustment obligation pursuant to section 33c (1) WRG 1959 has already been triggered for the introduction and is an installation according to § 33c (6) Z 1 WRG 1959, the introduction pursuant to Section 33c (1) of the WRG 1959 according to § 33c (1) of the German WRG Act (WRG 1959) 6 WRG 1959 within four years following the publication of the Commission's implementing decision on the conclusions on best available techniques (BAT) in accordance with the IE Directive concerning the manufacture of glass Emission limits of installations A to E (for a different waste water parameter according to § 4 para. 3 AAEV of the the corresponding emission limit of Appendix A of the AAEV. "

IE Directive;

Implementing decision of the Commission on the best available techniques (BAT) in accordance with the IE Directive in relation to glass production. "

Substitutes, melts and moulds of glass, glass fibres and artificial mineral fibres;

Cleaning of the exhaust air from activities according to Z 1 using aqueous media

The definition of the parameter to be filtered shall not be subject to the definition of the parameters which can be set down.

In individual cases, a higher emission limit shall be permitted if it is ensured that there is no deposit as a result of an introduction pursuant to Article 1 (1), which is the operation of the public sewerage system or the public sector. Disturb the wastewater treatment plant.

The concentration of arsenic in the sum shall not exceed 0,3 mg/l.

For waste water from the production of lead glass and packaging glass, an emission limit of 0.3 mg/l shall be maintained.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the Bor parameter shall be subject to an emission limit of 3.0 mg/l.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, a maximum emission limit of 6.0 mg/l shall be established for the parameter fluoride-total.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 1 000 mg/l shall be laid down for the sulphate parameter.

The emission limit is to be determined on a case-by-case basis with regard to the risk of corrosion for cement-bound materials in the sewage treatment and sewage treatment plant sector (ÖNORM B 2503: 2012 08 01).

For the TOC and CSB parameters, the parameters for the parameters of biochemical oxygen demand are also determined. Either the TOC parameter or the CSB parameter can be used for the monitoring of the waste water quality.

The definition of the parameter to be filtered shall not be subject to the definition of the parameters which can be set down.

In individual cases, a higher emission limit shall be permitted if it is ensured that there will be no deposits as a result of an introduction pursuant to Article 1 (2), which will result in the operation of the public sewerage system or the public sector. Disturb the wastewater treatment plant.

The concentration of Arsen (ber. as an As) in the sum shall not exceed 0,3 mg/l.

For establishments and installations which carry out an industrial activity referred to in Annex I to the IE Directive, the lead parameter shall be subject to an emission limit of 0.05 mg/l. For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive and working on lead glass and packaging glass, the lead parameter shall be subject to an emission limit of 0.3 mg/l.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 0.05 mg/l shall be established for the cadmium parameter.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 0.3 mg/l shall be established for the total chromium parameter.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the copper parameter shall be subject to an emission limit of 0.3 mg/l.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the Bor parameter shall be subject to an emission limit of 3.0 mg/l. For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive and working on borosilicate glass, a limit of 6.0 mg/l shall be established for the Bor parameter.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, a maximum emission limit of 6.0 mg/l shall be established for the parameter fluoride-total.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 1 000 mg/l shall be laid down for the sulphate parameter.

The emission limit is to be determined on a case-by-case basis with regard to the risk of corrosion for cement-bound materials in the sewage treatment and sewage treatment plant sector (ÖNORM B 2503: 2012 08 01).

For the TOC and CSB parameters, the parameters for the parameters of biochemical oxygen demand are also determined. Either the TOC parameter or the CSB parameter can be used for the monitoring of the waste water quality.

The setting for the AOX parameter does not need to be set for the POX parameter. The emission limit for the AOX parameter shall also be considered to be complied with in the context of self-monitoring and in the context of external monitoring, if the water rights authority is proved that the auxiliaries or additives used (e.g. Cooling lubricants) do not contain halogenated hydrocarbons.

Chemical processing (acid polishing, etching, matting) of special glass, optical glass or lead glass;

Cleaning of the exhaust air from activities according to Z 1 with aqueous media

The definition of the parameter to be filtered shall not be subject to the definition of the parameters which can be set down.

The concentration of Arsen (ber. as an As) in the sum shall not exceed 0,3 mg/l.

The emission limit for the specific cargo is to be specified in addition to the emission limit for the concentration; it refers to the installed capacity for hydrofluoric acid (calculated as HF) installed.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the lead parameter shall be subject to an emission limit of 0.05 mg/l and a specific freight rate of 0.005 kg/tonne. For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive and working on lead glass and packaging glass, the lead parameter shall be subject to an emission limit of 0.3 mg/l and a specific cargo of 0.03 kg/t.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 0.05 mg/l shall be laid down for the cadmium parameter

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 0.3 mg/l shall be established for the total chromium parameter.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the copper parameter shall be subject to an emission limit of 0.3 mg/l.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the zinc parameter shall be subject to an emission limit of 0.5 mg/l.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the Bor parameter shall be subject to an emission limit of 3.0 mg/l. For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive and working on borosilicate glass, a limit of 6.0 mg/l shall be established for the Bor parameter.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, a maximum emission limit of 6.0 mg/l shall be established for the parameter fluoride-total.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 1 000 mg/l shall be laid down for the sulphate parameter.

The emission limit is to be determined on a case-by-case basis with regard to the risk of corrosion for cement-bound materials in the sewage treatment and sewage treatment plant sector (ÖNORM B 2503: 2012 08 01).

For the TOC and CSB parameters, the parameters for the parameters of biochemical oxygen demand are also determined. Either the TOC parameter or the CSB parameter can be used for the monitoring of the waste water quality.

The setting for the AOX parameter does not need to be set for the POX parameter. The emission limit for the AOX parameter shall also be considered to be complied with in the context of self-monitoring and in the context of external monitoring, if the water rights authority is proved that the auxiliaries or additives used (e.g. Cooling lubricants) do not contain halogenated hydrocarbons.

Silverware and copper in flat glass (mirror making);

Silverware of small pieces of glass

The definition of the parameter to be filtered shall not be subject to the definition of the parameters which can be set down.

The emission limit for the specific cargo is to be specified in addition to the emission limit for the concentration; it refers to the production capacity of a mirrored glass surface installed on the square meter.

The emission limit for the specific cargo is to be specified in addition to the emission limit for the concentration; it refers to the capacity for silver used for silver in the silting of small pieces of glass.

The emission limit is to be determined on a case-by-case basis with regard to the risk of corrosion for cement-bound materials in the sewage treatment and sewage treatment plant sector (ÖNORM B 2503: 2012 08 01).

For the TOC and CSB parameters, the parameters for the parameters of biochemical oxygen demand are also determined. Either the TOC parameter or the CSB parameter can be used for the monitoring of the waste water quality.

further processing of glass fibres or artificial mineral fibres for textile glass products or insulating materials;

Cleaning of the exhaust air from activities according to Z 1 using aqueous media

The definition of the parameter to be filtered shall not be subject to the definition of the parameters which can be set down.

In individual cases, a higher emission limit shall be permitted if it is ensured that there will be no deposits as a result of an introduction pursuant to Article 1 (5), which will result in the operation of the public sewer system or the public sector. Disturb the wastewater treatment plant.

The emission limit is to be determined on a case-by-case basis with regard to the risk of corrosion for cement-bound materials in the sewage treatment and sewage treatment plant sector (ÖNORM B 2503: 2012 08 01).

For the TOC and CSB parameters, the parameters for the Biochemical oxygen demand parameter are also determined. Either the TOC parameter or the CSB parameter can be used for the monitoring of the waste water quality.

The parameters sum antimony and arsenic, barium, lead, cadmium, chromium-total, copper, nickel, silver, zinc, tin, ammonium, boron, fluoride total, phosphorus-total, sulfate, TOC, COD, AOX, hydrocarbon index and phenol index of the plants A to E are based on a quantity-proportional, non-deposited homogenized daily mixing sample. In the emptying of stacking containers, the sample is considered as a quantity-proportional sampling for the discharged volume of waste water.

The parameters of temperature, filterable substances and pH of Annexes A to E shall be determined on the basis of a sample. The daily frequency and intervals of the sampling frames shall be determined as a function of the drainage behaviour of the waste water constituents (properties); concentrations and rates shall be determined in proportion to the quantity.

The parameters Abfiltratable substances, sum of antimony and arsenic, barium, lead, cadmium, chromium-total, copper, nickel, silver, zinc, tin, boron, total fluoride, phosphorus-total, TOC, COD, AOX, hydrocarbon index and phenol index of plants A to E relate to total contents.

The emission limits of the parameters sum antimony and arsenic and the total fluoride of the plants A to E are based on the following or equivalent analytical methods. For the parameter antimony (sum of antimony and arsenic) or fluoride total of Annexes A to E, an analytical method shall be considered equivalent if its limit of determination is less than the emission limit.

The definition of the parameter to be filtered shall not be subject to the definition of the parameters which can be set down.

In individual cases, a higher emission limit shall be permitted if it is ensured that there will be no deposits as a result of an introduction pursuant to Article 1 (2), which will result in the operation of the public sewerage system or the public sector. Disturb the wastewater treatment plant.

The concentration of Arsen (ber. as an As) in the sum shall not exceed 0,3 mg/l.

For establishments and installations which carry out an industrial activity referred to in Annex I to the IE Directive, the lead parameter shall be subject to an emission limit of 0.05 mg/l. For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive and working on lead glass and packaging glass, the lead parameter shall be subject to an emission limit of 0.3 mg/l.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 0.05 mg/l shall be established for the cadmium parameter.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 0.3 mg/l shall be established for the total chromium parameter.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the copper parameter shall be subject to an emission limit of 0.3 mg/l.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the Bor parameter shall be subject to an emission limit of 3.0 mg/l. For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive and working on borosilicate glass, a limit of 6.0 mg/l shall be established for the Bor parameter.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, a maximum emission limit of 6.0 mg/l shall be established for the parameter fluoride-total.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 1 000 mg/l shall be laid down for the sulphate parameter.

The emission limit is to be determined on a case-by-case basis with regard to the risk of corrosion for cement-bound materials in the sewage treatment and sewage treatment plant sector (ÖNORM B 2503: 2012 08 01).

For the TOC and CSB parameters, the parameters for the parameters of biochemical oxygen demand are also determined. Either the TOC parameter or the CSB parameter can be used for the monitoring of the waste water quality.

Chemical processing (acid polishing, etching, matting) of special glass, optical glass or lead glass;

Cleaning of the exhaust air from activities according to Z 1 with aqueous media

The definition of the parameter to be filtered shall not be subject to the definition of the parameters which can be set down.

The concentration of Arsen (ber. as an As) in the sum shall not exceed 0,3 mg/l.

The emission limit for the specific cargo is to be specified in addition to the emission limit for the concentration; it refers to the installed capacity for hydrofluoric acid (calculated as HF) installed.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the lead parameter shall be subject to an emission limit of 0.05 mg/l and a specific freight rate of 0.005 kg/tonne. For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive and working on lead glass and packaging glass, the lead parameter shall be subject to an emission limit of 0.3 mg/l and a specific cargo of 0.03 kg/t.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 0.05 mg/l shall be laid down for the cadmium parameter

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 0.3 mg/l shall be established for the total chromium parameter.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the copper parameter shall be subject to an emission limit of 0.3 mg/l.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the zinc parameter shall be subject to an emission limit of 0.5 mg/l.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, the Bor parameter shall be subject to an emission limit of 3.0 mg/l. For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive and working on borosilicate glass, a limit of 6.0 mg/l shall be established for the Bor parameter.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, a maximum emission limit of 6.0 mg/l shall be established for the parameter fluoride-total.

For establishments and installations carrying out an industrial activity referred to in Annex I to the IE Directive, an emission limit of 1 000 mg/l shall be laid down for the sulphate parameter.

The emission limit is to be determined on a case-by-case basis with regard to the risk of corrosion for cement-bound materials in the sewage treatment and sewage treatment plant sector (ÖNORM B 2503: 2012 08 01).

For the TOC and CSB parameters, the parameters for the parameters of biochemical oxygen demand are also determined. Either the TOC parameter or the CSB parameter can be used for the monitoring of the waste water quality.