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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 2<br />

The neutralised oil is bleached to remove colouring matter, such as carotenoids and other minor<br />

constituents, such as oxidative degradation products or traces of transition metals. Bleaching<br />

uses activated Fuller’s earth with treatments typically in the 90 to 130 ºC range for<br />

10 to 60 minutes. The earth is sucked into the oil <strong>und</strong>er vacuum and is removed by filtration.<br />

The bleached oil is steam distilled at low pressure to remove volatile impurities including<br />

<strong>und</strong>esirable odours and flavours. This process, known as deodorisation, takes place in the<br />

temperature range of 180 to 270 ºC and may last from 15 minutes to 5 hours depending upon the<br />

nature and the quantity of the oil, and the type of equipment used. For example, if a batch<br />

deodoriser is used, it would take between 4.5 to 5 hours depending on the oil type and the<br />

quantity. However, if the same oils were processed in a semi-continuous deodoriser it would<br />

take about 15 minutes. Figure 2.8 shows a flow diagram of crude oil chemical refining. Olive oil<br />

and husk from pomace oil refining is similar to oilseed oil refining.<br />

INPUT:<br />

Crude<br />

vegetable<br />

oil<br />

OUTPUT:<br />

Auxiliary<br />

material<br />

1. Neutralisation/<br />

and/or final<br />

degumming<br />

Waste water<br />

Adsorbent<br />

2. Bleaching<br />

Internal<br />

recycling or<br />

waste<br />

Figure 2.8: Crude oil chemical refining<br />

[79, Italian contribution, 2001]<br />

Electricity<br />

Fuel / Steam<br />

Water<br />

Catalyst<br />

3.<br />

Hardening<br />

Waste (if<br />

applicable)<br />

Auxiliary<br />

material<br />

4. Interesterification<br />

5.<br />

Deodorising<br />

Waste water<br />

Finished<br />

product<br />

Physical refining is a simpler process in which the crude oil is degummed and bleached,<br />

followed by steam stripping which removes ffa, odours and volatiles in one step. The oil is<br />

heated to temperatures of up to 270 ºC and then refined by the oil flowing over a series of trays<br />

countercurrent to the flow of the stripping steam. The advantages of physical refining are the<br />

higher yield, the lower cost and the fewer chemicals used. One of the disadvantages, compared<br />

to chemical neutralisation, can be a lower quality of the end-product.<br />

There are three other processes which may be carried out during oil refining, depending upon<br />

the oil source. These are winterisation, which essentially is the removal of wax which would<br />

otherwise cause cloudiness. This is carried out on, e.g. sunflower oil. The process involves<br />

cooling the oil followed by filtration, using a filter aid to remove wax. The second process is<br />

fractionation. Typically this may be carried out on crude or refined oil. This involves<br />

completely melting the solid oil, followed by cooling to yield solid and liquid fractions which<br />

have different functional properties (see Section 2.2.5.3.). The third process is<br />

interesterification. This involves the separation of triglycerides into fatty acids and glycerol<br />

followed by recombination. The reaction is carried out using citric or phosphoric acid plus a<br />

catalyst, typically sodium methoxide. Interesterification modifies the functional properties of<br />

the treated oil and may be carried out after neutralisation or deodorisation.<br />

RHC/EIPPCB/FDM_BREF_FINAL January 2006 77

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