10.12.2012 Aufrufe

Integrierte Vermeidung und Verminderung der Umweltverschmutzung

Integrierte Vermeidung und Verminderung der Umweltverschmutzung

Integrierte Vermeidung und Verminderung der Umweltverschmutzung

MEHR ANZEIGEN
WENIGER ANZEIGEN

Sie wollen auch ein ePaper? Erhöhen Sie die Reichweite Ihrer Titel.

YUMPU macht aus Druck-PDFs automatisch weboptimierte ePaper, die Google liebt.

3.2.20.5 Noise<br />

Chapter 3<br />

Some of the production equipment may emit high noise levels, e.g. during the concentration of<br />

stillage or the dehydration of alcohol by molecular sieve adsorption.<br />

3.2.21 Soaking (D.1)<br />

3.2.21.1 Water<br />

For soaking, water is required and consequently some waste water containing dissolved organic<br />

material and SS is produced.<br />

3.2.21.2 Solid output<br />

Some dirt can be produced, although this is usually removed during soaking. Organic solid<br />

output may also be produced.<br />

3.2.22 Dissolving (D.2)<br />

3.2.22.1 Water<br />

Waste water is generated during cleaning. This waste water may contain product residues, e.g.<br />

pow<strong>der</strong> and oil from rinsing, resulting in dissolved organic material, dissolved solids and SS in<br />

the waste water.<br />

3.2.22.2 Air emissions<br />

Dust emissions may occur during bag tipping. These emissions are typically minor and<br />

generally remain inside buildings.<br />

3.2.22.3 Energy<br />

During the dissolving process, steam and electricity are used.<br />

3.2.23 Solubilisation/alkalising (D.3)<br />

3.2.23.1 Water<br />

Waste water is generated from the cleaning of equipment and typically contains soluble organic<br />

material, SS and FOG.<br />

3.2.23.2 Air emissions<br />

Air emissions typically consist of water vapour containing low concentrations of VOCs and<br />

dust. Odour may also be a problem.<br />

3.2.23.3 Energy<br />

An example of the typical energy requirements per tonne of cocoa is shown in Table 3.8.<br />

Electrical power Electrical power Steam Steam<br />

(kJ/kg) (kWh/kg) (kg/t) (kWh/t)<br />

Liquid process 35 – 70 0.010 – 0.019 300 – 500 233 – 389<br />

Nips alkalising 35 – 550 0.010 – 0.153 700 – 1000 548 – 778<br />

Table 3.8: Typical energy requirement per tonne of cocoa<br />

[1, CIAA, 2002]<br />

RHC/EIPPCB/FDM_BREF_FINAL January 2006 133

Hurra! Ihre Datei wurde hochgeladen und ist bereit für die Veröffentlichung.

Erfolgreich gespeichert!

Leider ist etwas schief gelaufen!