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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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LIQUID WASTE<br />

IN<br />

VOLUME/WEIGHT<br />

0.7 a -5 m 3 /t<br />

POLLUTING<br />

LOAD<br />

COMPOSITION<br />

*BOD: 20000 - 35000 mg/l<br />

*COD: 30.000 - 60000 mg/l<br />

*Oils & fats: 5000 - 10000 mg/l<br />

*Organic N: 500 - 800 mg/l<br />

a Polyphenols: 80000 mg/l<br />

TSS: 20000 mg/l<br />

COD: 200000 mg/l<br />

pH: 3 - 5.9<br />

WASTE<br />

WATER<br />

Waste water<br />

Waste water<br />

VEGETABLE OIL<br />

PRODUCTION<br />

Cleaning / Storage<br />

Hulling b<br />

Breaking/Flaking/<br />

Crushing<br />

Cooking/<br />

Conditioning<br />

Pressing /<br />

Centrifugation<br />

Solvent extraction<br />

Crude oil<br />

Degumming<br />

Neutralisation<br />

Bleaching<br />

Deodorisation c<br />

Refined oil<br />

Stalks<br />

Leaves<br />

Stones, sand<br />

Hulls<br />

Hulls<br />

Chapter 3<br />

RHC/EIPPCB/FDM_BREF_FINAL January 2006 183<br />

Dust<br />

Gums<br />

SOLID WASTE/<br />

BY-PRODUCT<br />

Crude cake<br />

Olive stones a<br />

Extracted cake or<br />

spent meal b<br />

Soapstock<br />

Spent<br />

bleaching earth<br />

Distillate<br />

% SOLID<br />

WASTE IN<br />

WEIGHT<br />

5 a<br />

33 a -59<br />

0.4 - 2<br />

0.5 - 5<br />

TOTAL: 40 - 70<br />

a For olive oil production.<br />

b For rape seed oil production, hulling is not applied. The solvent extraction is the step from which the main solid waste is generated.<br />

c Most of the water is generated during deodorization, in the case of rape seed oil, the amount can be three times as much as waste water<br />

from raw oil production.<br />

Figure 3.10: Types and quantities of wastes and by-products generated in vegetable oil processing<br />

[134, AWARENET, 2002]<br />

3.3.4.4.1 Oilseed<br />

Typically the yield from oilseed processing is almost 100 %. Products from oilseed processing<br />

and vegetable oil refining are mainly vegetable oil, protein rich meal, lecithin and ffa (acid oil).<br />

Ffa may contain tocopherol, a natural antioxidant. They can be used as a feedstock for the<br />

production of vitamin E. By-products may either be used as animal feed or burnt as fuels [182,<br />

Germany, 2003, 185, CIAA-FEDIOL, 2004].<br />

Chemical refining produces soap stock during the neutralisation of crude oil. This consists<br />

mainly of the sodium salts of the separated ffa, but also includes triacylglycerols, phosphatides,<br />

proteins, pigments and other compo<strong>und</strong>s. Normally soap stock is further processed in the<br />

refinery by splitting the soaps and regaining the ffa. It is possible to mix the soap stock from the<br />

chemical refining of vegetable oil with other ingredients to produce low quality soaps or for use<br />

in meal for animal feed [182, Germany, 2003, 185, CIAA-FEDIOL, 2004].<br />

Crude cake and spent meal are either incinerated or used in the production of fuels and other<br />

products such as kernel oil and activated carbon. They can also be used in animal feed.<br />

Exhausted cake, which has an oil content lower than 1 %, is usually formed into pellets or<br />

briquettes and its main application is animal feed, but it may also be composted or burnt.<br />

Lecithin is an edible by-product consisting of a mixture of phosphatides with minor quantities<br />

of glycolipids and oligosaccharides. It is known to have outstanding functional characteristics,<br />

such as emulsification properties, spreadability and wetting ability. After a very simple and<br />

inexpensive purification, it can be used in a number of applications in food, cosmetics and<br />

pharmaceuticals. Soybean oil is the most important source of lecithin, although other vegetable<br />

oils such as maize, sunflower or gro<strong>und</strong>-nut oil also yield suitable lecithin.

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