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Integrierte Vermeidung und Verminderung der Umweltverschmutzung

Integrierte Vermeidung und Verminderung der Umweltverschmutzung

Integrierte Vermeidung und Verminderung der Umweltverschmutzung

MEHR ANZEIGEN
WENIGER ANZEIGEN

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Chapter 3<br />

Source Volume<br />

m 3 /t 1<br />

BOD5<br />

mg/l<br />

COD<br />

mg/l<br />

FOG<br />

mg/l<br />

SS<br />

mg/l<br />

Neutral oil washing 0.1 1000 15000 100 - 500 n.d. 3<br />

Neutralisation reaction<br />

pH = 10 – 12<br />

2.1 2<br />

4300 7200 670 2900<br />

Barometric condensers<br />

pH = 6.5 – 7.5<br />

2 140 – 200 500 – 600 20 – 200 40 – 100<br />

Steam boiler 10 % of<br />

steam<br />

20 40 – 100<br />

Water softening 5 % of<br />

steam<br />

20 40 – 100<br />

Floor and equipment cleaning 0.1 1500 2000 n.d. 300<br />

1 2 3<br />

per t of crude oil per t of ffa n.d. = no data<br />

Table 3.42: Reported untreated waste water characteristics in vegetable oil refining (cornflower,<br />

cottonseed and sunflower)<br />

[74, Greek Ministry for the Environment, 2001]<br />

3.3.4.2.1 Olive oil<br />

Traditional olive oil production, also called pressing, generates about 2 to 5 litres of waste water<br />

per litre of oil produced, the three-phase continuous olive oil extraction generates about<br />

6 to 8 litres of waste water per litre of oil produced, whereas the two-phase continuous olive oil<br />

extraction generates only about 0.33 – 0.35 litres of waste water per litre of oil produced. Table<br />

3.43 shows the characteristics of olive oil waste water using different extraction techniques.<br />

Technology<br />

Traditional<br />

extraction<br />

(pressing)<br />

Three-phase<br />

extraction<br />

Two-phase<br />

extraction<br />

Waste water<br />

volume<br />

(m 3 /t olive oil)<br />

BOD5<br />

(mg/l)<br />

COD<br />

(mg/l)<br />

TSS<br />

(mg/l)<br />

2 – 5 22000 – 62000 59000 – 162000 65000 4.6 – 4.9<br />

6 – 8 13000 – 14000 39000 – 78000 65000 5.2<br />

0.33 – 0.35 90000 – 100000 120000 – 130000 120000 4.5 – 5.0<br />

Table 3.43: Characteristics of olive oil mill waste water<br />

[74, Greek Ministry for the Environment, 2001, 86, Junta de Andalucia and Agencia de Medio<br />

Ambiente, 1994]<br />

3.3.4.3 Air emissions<br />

Dry dust is generated during seed delivery, silo storage, seed cleaning, seed preparation, meal<br />

shipment and indoor transportation/conveying. Wet dust can arise during seed preparation, meal<br />

drying and cooling, and indoor transportation/conveying.<br />

If solvent extraction is applied, leakages and transportation can cause losses to the air.<br />

Following the extraction step, emissions of solvent (hexane) may occur during drying, cooling,<br />

storage and the transportation of meal and crude oil. Air emission levels for hexane, associated<br />

with various seed feedstocks, are shown in Table 3.44.<br />

Table 3.44: Hexane emission to air<br />

[65, Germany, 2002]<br />

Feedstock Hexane output<br />

(kg hexane/t raw seed)<br />

Soy beans 0.5 – 1.0<br />

Rapeseed 0.5 – 1.2<br />

Sunflowerseed 0.5 – 1.2<br />

Linseed about 2.0<br />

Castor >3.0<br />

180 January 2006 RHC/EIPPCB/FDM_BREF_FINAL<br />

pH

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