de - Beste verfügbare Techniken (BVT) - Umweltbundesamt
de - Beste verfügbare Techniken (BVT) - Umweltbundesamt de - Beste verfügbare Techniken (BVT) - Umweltbundesamt
Chapter 2 2.3.7 Recovery/abatement of exhaust gases [15, Köppke, 2000]; [31, European Commission, 2003], *019A,I* Figure 2.6 gives an overview of the recovery/abatement techniques applied to exhaust gases. Oxidisers include thermal and catalytic oxidation. The choice of a particular technique or a particular combination of techniques depends on the contaminants present and especially on the VOC concentration, flow and the variations in concentration and flow. Additionally, various types of filters can be used to recover particulates. Events of planned or emergency shutdowns may require back-up systems or modifications of schedules and hours of operation. Primary and secondary condensers (non-cryogenic) are directly attached to the reactors. If VOC rich exhaust gases are treated by thermal oxidation, other streams can be used as the oxygen source, e.g. VOC lean or odorous streams. Thermal oxidisers and incinerators In this document, the term “thermal oxidation” is used where applied to the gas phase, however, where co-treatment of gas, liquids and/or solids is carried out, then “incineration” is used. The gas collection system consists of the source enclosure, vents and pipes. The gas flowrate is minimised by encasing the source as far as feasible. Explosion risks are controlled by the installation of flammability detectors inside the collection system and by keeping the gas mixture securely below the lower explosion limit (“LEL”, usually below 25 % LEL), above the higher explosion limit or by inertisation. Waste gas containing VOC and possibly other pollutants Selection of techniques or combinations of techniques based on pollutant concentration, flow and the variations in concentration and flow Thermal oxidiser DeNO x Particulate removal Other pollutants, no VOC Scrubber Cryogenic Condenser Adsorber Condenser Waste gas emission Figure 2.6: Typically applied recovery/abatement techniques for exhaust gases on OFC sites 30 Dezember 2005 OFC_BREF Scrubber Scrubber
2.3.8 Recovery/abatement applied to waste water streams Chapter 2 Figure 2.7 gives an overview of the applied recovery/abatement techniques applied to waste water streams. The total effluent is normally treated in a biological WWTP, on-site or together with other waste water in off-site plants (in most cases municipal). Particular waste water streams which are not suitable for biological treatment are segregated and separately pretreated or disposed of as waste (e.g. incineration). In order to ensure a uniform input level for the biological WWTP as much as possible, a sufficient buffer volume is provided. Providing equalisation can often efficiently reduce toxicity to a level where it will not adversely impact the operations of a biological WWTP. Other Precipitation Ion-exchange Extraction Adsorption Stripping Distillation Permeation Low biodegradable Heavy metals Toxic/inhibiting Exceptional high loads ? Buffer Incineration Chemical oxidation Low pressure wet oxidation Wet oxidation Biological WWTP Waste water emission Figure 2.7: Typically applied recovery/abatement techniques for waste water streams on OFC sites OFC_BREF Dezember 2005 31
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- Seite 24 und 25: 5.2.3.5 Removal of SOx from exhaust
- Seite 26 und 27: Abbildung 4.1: : Behandlungsschritt
- Seite 28 und 29: Verzeichnis der Tables bzw. Tabelle
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- Seite 86 und 87: Chapter 2 2.5.9 Oxidation with inor
- Seite 88 und 89: Chapter 2 2.5.11 Reduction of aroma
- Seite 90 und 91: Chapter 2 2.5.11.3 Alkali sulphide
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Chapter 2<br />
2.3.7 Recovery/abatement of exhaust gases<br />
[15, Köppke, 2000]; [31, European Commission, 2003], *019A,I*<br />
Figure 2.6 gives an overview of the recovery/abatement techniques applied to exhaust gases.<br />
Oxidisers inclu<strong>de</strong> thermal and catalytic oxidation. The choice of a particular technique or a<br />
particular combination of techniques <strong>de</strong>pends on the contaminants present and especially on the<br />
VOC concentration, flow and the variations in concentration and flow. Additionally, various<br />
types of filters can be used to recover particulates.<br />
Events of planned or emergency shutdowns may require back-up systems or modifications of<br />
schedules and hours of operation.<br />
Primary and secondary con<strong>de</strong>nsers (non-cryogenic) are directly attached to the reactors. If VOC<br />
rich exhaust gases are treated by thermal oxidation, other streams can be used as the oxygen<br />
source, e.g. VOC lean or odorous streams.<br />
Thermal oxidisers and incinerators<br />
In this document, the term “thermal oxidation” is used where applied to the gas phase, however,<br />
where co-treatment of gas, liquids and/or solids is carried out, then “incineration” is used.<br />
The gas collection system consists of the source enclosure, vents and pipes. The gas flowrate is<br />
minimised by encasing the source as far as feasible. Explosion risks are controlled by the<br />
installation of flammability <strong>de</strong>tectors insi<strong>de</strong> the collection system and by keeping the gas<br />
mixture securely below the lower explosion limit (“LEL”, usually below 25 % LEL), above the<br />
higher explosion limit or by inertisation.<br />
Waste gas<br />
containing<br />
VOC and<br />
possibly other<br />
pollutants<br />
Selection of<br />
techniques or<br />
combinations of<br />
techniques based<br />
on pollutant<br />
concentration,<br />
flow and the<br />
variations in<br />
concentration<br />
and flow<br />
Thermal<br />
oxidiser<br />
DeNO x<br />
Particulate<br />
removal<br />
Other<br />
pollutants,<br />
no VOC Scrubber<br />
Cryogenic<br />
Con<strong>de</strong>nser<br />
Adsorber<br />
Con<strong>de</strong>nser<br />
Waste gas<br />
emission<br />
Figure 2.6: Typically applied recovery/abatement techniques for exhaust gases on OFC sites<br />
30 Dezember 2005 OFC_BREF<br />
Scrubber<br />
Scrubber