BVT-Merkblatt zu Abwasser- und Abgasbehandlung
BVT-Merkblatt zu Abwasser- und Abgasbehandlung BVT-Merkblatt zu Abwasser- und Abgasbehandlung
Annexes Process water may only be discharged into an open system after degassing. The gaseous effluents collected here must be cleaned by washing or incineration. § 5. As a derogation from § 1, the emission in the gaseous effluent of installations for the catalytic cracking according to the 'fluid bed' procedure with the regeneration of the catalyst may not exceed the following emission limit value for suspended particulates: 1. until 1 January 2005: 300 mg/Nm 3 as monthly average 2. from 1 January 2005: 50 mg/Nm 3 as monthly average. § 6. The concentration of polychlorinated dibenzo-p-dioxins (PCDD’s) and polychlorinated dibenzo-p-furans (PCDF’s), calculated according to article 5.2.3.1.5, § 6, expressed as nanograms dioxin toxic equivalent per Nm 3 (ng TEQ/Nm 3 ), may not exceed a limit value of 0.5 ng TEQ/Nm 3 for all average values over a sampling period of at least 6 hours and a maximum of 8 hours. The emission guide value is 0.1 ng TEQ/Nm 3 . As a derogation from the provisions of the first subsection, the following applies for existing establishments: - an emission guide value of 0.4 ng TEQ/Nm 3 ; - an emission limit value of 2.5 ng TEQ/Nm 3 as of 1 January 2002. The aforementioned guide values must be striven for by the application of the best available techniques. The mass concentration of PCDD’s and PCDF’s is to be measured according to the requirements referred to in the Belgian standard T95-R-NBN EN 1948-1, 2 or 3. This concentration is to be measured at least once a year by an environmental expert accredited for these measurements. This measurement is not compulsory for constituent flows which do not or do not significantly contribute to the emissions. Unless specified otherwise in the environmental licence, the omission of the measurements of specific constituent flows is only accepted providing that this has been approved of in advance by the supervisory authority. Each measurement performed according to the above-mentioned method must, after the calculation of the accuracy as referred to in article 4.4.4.2, § 5, comply with the prescribed emission limit value. If the measured concentration, after the calculation of the aforementioned accuracy, exceeds the emission limit value, within three months new sampling and analysis will take place. Art. 5.20.2.3 Immission control procedures § 1. Without prejudice to the provisions of chapter 4.4, each time the weather conditions appear unfavourable for the good dispersion of the combustion gases, in particular at the establishment, the operator will take all necessary steps to maximally restrict the emissions of SO 2 as well as of NO x from this installation. § 2. Each change of fuel, sulphur content of the liquid fuel, as well as the times of putting out of use are recorded in a register that the operator keeps available to the official charged with supervision. § 3. When the total installed nominal thermal capacity at one establishment amounts to more than 300 MW, in the surrounding area of the installations appliances for the measuring of the immissions of SO 2 and NO 2 in the air at the ground will be installed and maintained at the operator’s expense. The type, the place of measurement, the method of control and the other conditions for use for the appliances are determined in the environmental licence. § 4. Without prejudice to the provisions of § 1, each time the average immission value over 24 hours measured with the equipment specified in § 3, amounts to more than 300 mg/m 3 for SO2 and/or 150 mg/m 3 for NO2, the operator will take the steps prescribed in § 1, and maintain these measures for as long as the measured average immission values over 24 hours of SO2 and of NO2 amount to more than 300 mg/m 3 for SO2 and/or 150 mg/m 3 for NO2. 404 Waste Water and Waste Gas Treatment
Annexes § 5. To guarantee compliance with the emission limit values for nitrogen oxides of art. 5.20.2.2, more appropriate technical construction conditions can be imposed in the environmental licences. If from control measurements it appears that the emission limit value is not being complied with due to unforeseen circumstances, the operator must take all suitable primary measures to ensure compliance with the emission limit values as soon as possible. The operator must report this to the Environmental Inspection Department together with the mentioning of measures taken for improvement. The European Commission is to be immediately informed through the usual channels of such events, as well as of the work carried out for improvement. Section 5.20.3 Installations for the dry distillation of coal (coke ovens) Art. 5.20.3.1 Underfiring, coke oven gas and heating installations § 1. Reference value The emission values for waste gases from heating concern a volume level of oxygen in the spent gas of 5 %. § 2. Coke oven gas and fuel As a derogation from the general emission limit value for SO2 as specified in article 4.4.3.1, the weighed average of the mass concentration of sulphur compounds in the gas from the underfiring, as well as in the gases originating from the coke ovens used as fuel, may over a calendar year not exceed 0.80 g/m 3 expressed in sulphur. § 3. Nitrogen oxides With the first time of measuring, the emissions of nitrogen monoxide and nitrogen dioxide in the gaseous effluent from the underfiring may not exceed 0.50 g/m 3 expressed in nitrogen dioxide. The best available techniques to reduce the increase of emissions due to ageing must be applied. The measurements to be conducted for the first time after foundation or significant modification must be carried out after the installation has reached uninterrupted operation, but at the earliest after three months in operation and at the latest twelve months after being in operation. Art. 5.20.3.2 Filling the coke ovens With the unloading of the coal from the coal bunker in the larry car, dust emissions must be avoided. The filling gases must be collected. When dumping, the filling gases must be transferred to the raw gas or an oven close by to the extent possible, with the further processability of the raw coal tar in mind. With stamping, the filling gases must be transferred in the raw gas to the extent possible. Filling gases which cannot be transferred must be taken to an incineration facility. Dustcontaining emissions in the gaseous effluent of the incineration may not exceed 25 mg/m 3 . With the levelling activities with the dumping of coal, the emissions of filling gases must be reduced by the sealing of the levelling opening. Art. 5.20.3.3 Filling opening covers Emissions with filling opening covers must be avoided to the extent possible, for example by using filling opening covers with large sealing surfaces, coating the filling opening covers will loam each time after filling the ovens and the regular cleaning of the filling opening frames and filling opening covers before the filling openings are closed. Coal remains must be regularly removed from the oven roof. Waste Water and Waste Gas Treatment 405
- Seite 389 und 390: Annexes Luftreinhaltegesetz and
- Seite 391 und 392: Emission standards for the producti
- Seite 393 und 394: Annexes The ordinance “Verordnung
- Seite 395 und 396: Annexes 7. CHEMICALS (see also sect
- Seite 397 und 398: Annexes 17 Hazardous Products 1 (di
- Seite 399 und 400: Annexes 3. with respect to BFCs, no
- Seite 401 und 402: Art. 5.7.2.2 Annexes § 1. The dump
- Seite 403 und 404: Annexes sponding to the conversion
- Seite 405 und 406: Annexes § 2. The waste gases of pl
- Seite 407 und 408: Section 5.7.11 The production of po
- Seite 409 und 410: Annexes From 1 January 2002, and as
- Seite 411 und 412: Art. 5.17.1.3 Annexes § 1. Unless
- Seite 413 und 414: Annexes an equivalent fire-resistan
- Seite 415 und 416: Annexes § 2. The register or alter
- Seite 417 und 418: Annexes a) provide sufficient stren
- Seite 419 und 420: Annexes § 4. In the event of possi
- Seite 421 und 422: Art. 5.17.2.5 § 1. Storage in cont
- Seite 423 und 424: Annexes § 2. Except for containers
- Seite 425 und 426: Annexes 1. single-walled containers
- Seite 427 und 428: Art. 5.17.3.5 Annexes § 1. An iden
- Seite 429 und 430: Annexes 1. the storage must be prot
- Seite 431 und 432: Art. 5.17.3.15 Annexes § 1. The op
- Seite 433 und 434: Annexes These containers continue t
- Seite 435 und 436: Annexes 2. from 1 January 2002 for
- Seite 437 und 438: Art. 5.17.5.5 Annexes Fuelling plac
- Seite 439: Annexes For new, large heating inst
- Seite 443 und 444: Art. 5.20.3.10 Existing installatio
- Seite 445 und 446: 5. FRANCE The legislation for the c
- Seite 447 und 448: Annexes Specific emission control r
- Seite 449 und 450: Annexes b) more than 750 mg/l, a CO
- Seite 451 und 452: Annexes (4) Notwithstanding part D,
- Seite 453 und 454: Emission Limit Values for Fertilise
- Seite 455 und 456: Annexes d Fugitive solvent emission
- Seite 457 und 458: ANNEX 2 (SPECIFIC EMISSION LIMITS F
- Seite 459 und 460: Benzo(a)anthracene Benzo(b)fl
- Seite 461 und 462: Class III Annexes If the mass flow
- Seite 463 und 464: Class IV If the mass flow equals or
- Seite 465 und 466: Parameter Unit Discharge into surfa
- Seite 467 und 468: Annexes General Environmental Perfo
- Seite 469 und 470: Annexes Classification of organic s
- Seite 471 und 472: GLOSSAR DER BEGRIFFE UND ABKÜRZUNG
- Seite 473 und 474: Ω ohm = Ohm Glossar Abkürzungen /
- Seite 475 und 476: Glossar PSA Pressure-swing Adsorpti
- Seite 477: Fugitive emissions = Emission von f
Annexes<br />
Process water may only be discharged into an open system after degassing. The gaseous effluents<br />
collected here must be cleaned by washing or incineration.<br />
§ 5. As a derogation from § 1, the emission in the gaseous effluent of installations for the catalytic<br />
cracking according to the 'fluid bed' procedure with the regeneration of the catalyst may<br />
not exceed the following emission limit value for suspended particulates:<br />
1. until 1 January 2005: 300 mg/Nm 3 as monthly average<br />
2. from 1 January 2005: 50 mg/Nm 3 as monthly average.<br />
§ 6. The concentration of polychlorinated dibenzo-p-dioxins (PCDD’s) and polychlorinated<br />
dibenzo-p-furans (PCDF’s), calculated according to article 5.2.3.1.5, § 6, expressed as<br />
nanograms dioxin toxic equivalent per Nm 3 (ng TEQ/Nm 3 ), may not exceed a limit value of<br />
0.5 ng TEQ/Nm 3 for all average values over a sampling period of at least 6 hours and a maximum<br />
of 8 hours. The emission guide value is 0.1 ng TEQ/Nm 3 .<br />
As a derogation from the provisions of the first subsection, the following applies for existing<br />
establishments:<br />
- an emission guide value of 0.4 ng TEQ/Nm 3 ;<br />
- an emission limit value of 2.5 ng TEQ/Nm 3 as of 1 January 2002.<br />
The aforementioned guide values must be striven for by the application of the best available<br />
techniques.<br />
The mass concentration of PCDD’s and PCDF’s is to be measured according to the requirements<br />
referred to in the Belgian standard T95-R-NBN EN 1948-1, 2 or 3. This concentration is<br />
to be measured at least once a year by an environmental expert accredited for these measurements.<br />
This measurement is not compulsory for constituent flows which do not or do not significantly<br />
contribute to the emissions. Unless specified otherwise in the environmental licence,<br />
the omission of the measurements of specific constituent flows is only accepted providing that<br />
this has been approved of in advance by the supervisory authority.<br />
Each measurement performed according to the above-mentioned method must, after the calculation<br />
of the accuracy as referred to in article 4.4.4.2, § 5, comply with the prescribed emission<br />
limit value. If the measured concentration, after the calculation of the aforementioned accuracy,<br />
exceeds the emission limit value, within three months new sampling and analysis will take<br />
place.<br />
Art. 5.20.2.3 Immission control procedures<br />
§ 1. Without prejudice to the provisions of chapter 4.4, each time the weather conditions appear<br />
unfavourable for the good dispersion of the combustion gases, in particular at the establishment,<br />
the operator will take all necessary steps to maximally restrict the emissions of SO 2 as<br />
well as of NO x from this installation.<br />
§ 2. Each change of fuel, sulphur content of the liquid fuel, as well as the times of putting out of<br />
use are recorded in a register that the operator keeps available to the official charged with supervision.<br />
§ 3. When the total installed nominal thermal capacity at one establishment amounts to more<br />
than 300 MW, in the surro<strong>und</strong>ing area of the installations appliances for the measuring of the<br />
immissions of SO 2 and NO 2 in the air at the gro<strong>und</strong> will be installed and maintained at the operator’s<br />
expense. The type, the place of measurement, the method of control and the other conditions<br />
for use for the appliances are determined in the environmental licence.<br />
§ 4. Without prejudice to the provisions of § 1, each time the average immission value over<br />
24 hours measured with the equipment specified in § 3, amounts to more than 300 mg/m 3 for<br />
SO2 and/or 150 mg/m 3 for NO2, the operator will take the steps prescribed in § 1, and maintain<br />
these measures for as long as the measured average immission values over 24 hours of SO2 and<br />
of NO2 amount to more than 300 mg/m 3 for SO2 and/or 150 mg/m 3 for NO2.<br />
404 Waste Water and Waste Gas Treatment