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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 />

In some seeds, e.g. rapeseed, the sulphur content may be high. Enzymatic and biological<br />

processes may convert sulphur compo<strong>und</strong>s into hydrogen sulphide. No emission data have been<br />

reported yet during storage but significant hydrogen sulphide concentrations have been detected<br />

in the exhaust air of extractors [65, Germany, 2002]. Air emission types during the manufacture<br />

of crude vegetable oils are shown in Table 3.45.<br />

Degumming Neutralisation Bleaching Deodorisation Hardening<br />

Volatile<br />

compo<strong>und</strong>s<br />

Odour Ffa<br />

Volatile<br />

compo<strong>und</strong>s<br />

Odours<br />

Table 3.45: Summary of air emissions in the manufacturing of crude vegetable oils<br />

[10, Environment Agency of England and Wales, 2000, 74, Greek Ministry for the Environment,<br />

2001]<br />

Odour is produced in all steps where heating is involved. It results from the volatile fatty acids,<br />

organic nitrogen compo<strong>und</strong>s and, in the case of rapeseed, hydrogen sulphide and organic<br />

sulphur compo<strong>und</strong>s.<br />

3.3.4.4 Solid output<br />

Depending on the type of vegetable, i.e. oilseed or oilfruit, the raw materials for vegetable oil<br />

production can almost completely be converted into products, e.g. vegetable oil, protein rich<br />

meal, fatty acids and lecithin, or by-products, e.g. for human food, animal feed and<br />

pharmaceutical products.<br />

Solid waste, e.g. leaves, wood, pieces of metal and stones, is generated in the raw material’s<br />

primary treatment step (cleaning and hulling). This is separated during the cleaning of the raw<br />

material by wind sifters, magnet separators and sieves. In oilseed production, this fraction is less<br />

than 1 % of the processed seed. Metals are sent for recycling or disposal and the remain<strong>der</strong>,<br />

such as stones and sand, is disposed of. Dust may be incinerated. In the pressing/centrifuging<br />

step, used filter clothes from seed pressing are produced and are also disposed of [161, Verband<br />

Deutscher Oelmuehlen, 2003].<br />

In the case of chemical refining, soap stock is produced during the neutralisation of crude oil.<br />

This consists mainly of NaOH saponified ffa, but also contains phosphatides, proteins and other<br />

compo<strong>und</strong>s. Normally, it is further processed in the refinery by splitting the soaps and regaining<br />

the fatty acids (acid oil). In some countries, it is possible to mix the soap stock from the<br />

chemical refining of vegetable oil with other ingredients for the production of low quality soaps<br />

or for use in meal for animal feed.<br />

The production of solid wastes from vegetable oil refining and processing is dependent on the<br />

specific site. In bleaching operations, spent bleaching earth containing 20 – 40 % fat is<br />

produced. This makes the waste prone to spontaneous combustion. In production installations,<br />

which exclusively refine and modify edible oil, the spent bleaching earth is utilised by third<br />

parties for energy production by co-fermentation to produce biogas or to make bricks [182,<br />

Germany, 2003]. The spent catalyst is recycled to third parties for regeneration.<br />

In mixed production installations, which produce crude oil and meal, and refine/modify the<br />

edible oil, there are further opportunities for utilisation of components of the raw material and of<br />

wastes. For example, utilisation of phospholipids in meal and utilisation of spent bleaching earth<br />

in meal, both as animal feed. The precondition for the latter example is the absence of nickel<br />

catalyst residues [161, Verband Deutscher Oelmuehlen, 2003].<br />

RHC/EIPPCB/FDM_BREF_FINAL January 2006 181

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