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Integrierte Vermeidung und Verminderung der Umweltverschmutzung

Integrierte Vermeidung und Verminderung der Umweltverschmutzung

Integrierte Vermeidung und Verminderung der Umweltverschmutzung

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Chapter 3<br />

3.2.52.3 Solid output<br />

Ashes from solid fuel fired boilers and scale and inert soot deposits which are removed during<br />

periodic boiler maintenance and cleaning, are produced. They are sent for landfill.<br />

3.2.52.4 Noise<br />

Normal boiler operations do not give rise to noise outside the installation, but this depends on<br />

the measures taken to contain the noise and the proximity of neighbouring premises. During<br />

process interruptions, and during periods of testing and commissioning, there may be short<br />

periods when the boiler safety relief valve operates. This effect is likely to be local to the<br />

installation but could be a source of nuisance during that period. Large relief valves can be<br />

provided with silencers.<br />

3.2.53 Water use (U.3)<br />

3.2.53.1 Water<br />

Waste water from water regeneration and residues from other processes are discharged to water.<br />

Minimisation of water consumption by process optimisation and water recycling can be applied.<br />

3.2.53.2 Solid output<br />

Mineral sludges and spent resins from water treatment processes need to be disposed of.<br />

3.2.54 Vacuum generation (U.4)<br />

3.2.54.1 Water<br />

Water is used in water-ring type vacuum pumps for cooling and for sealing. To reduce water<br />

consumption, the water is normally recirculated in closed-circuit systems with a bleed off<br />

determined by the condensable matter. Waste water is produced which contains soluble organic<br />

material.<br />

If steam jet ejectors are used for vacuum production, not only the media coming from the<br />

evacuated plant has to be condensed, but also the driving steam of the jet ejector. This is<br />

normally done in spray condensers. Here, water is used to condense the steam along with any<br />

volatiles carried over. For large installations, the volume of water used to condense the steam<br />

can be significant, i.e. during refining of sugar or edible oil. The volatile material carried over is<br />

condensed in the water thereby increasing the level of dissolved organic material. To reduce<br />

water consumption, water can be recirculated over cooling towers. In this case a bleed from the<br />

system is required for the condensed steam. This can lead to a concentration of the organic<br />

material condensed in the water. With indirect condensers or heat-exchangers, the volume of<br />

condensate is equivalent to the condensed live steam and other condensable matter, and will<br />

contain any organic volatiles carried over. With chilling or freezing systems, the volume of<br />

condensate is reduced further.<br />

3.2.54.2 Air emissions<br />

Depending on the material being processed, air evacuated by vacuum pumps may contain<br />

volatile material, which, if not properly controlled, may result in odour problems.<br />

Non-condensable material may be discharged into the air with steam jet ejectors. Depending on<br />

the material being processed, this discharge may result in odour emissions. If condenser water is<br />

recirculated over cooling towers, the drift/mist from the towers may result in odour emissions.<br />

Indirect recirculation with heat-exchangers with two cycles may be used in this case. Heatexchangers<br />

have to be cleaned regularly.<br />

146 January 2006 RHC/EIPPCB/FDM_BREF_FINAL

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