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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 />

Before bottling, the beer is filtered through a filter cake. Proven materials for this purpose are<br />

mud-free kieselguhr; calcined and screened diatomaceous earth of various particle size<br />

distribution; and perlite from gro<strong>und</strong> and calcined glassy rock of volcanic origin. Activated<br />

carbon may be used to correct a mild off-taste. For example, it is usually used in the treatment<br />

of rest beers. Shortly before filtration, hydro- and xero-silica gels may be added to contribute to<br />

the build-up of the filter cake. Fining, by the addition of, e.g cross-linked polyvinylpyrrolidone<br />

(PVP) and polyvinylpolypyrrolidine (PVPP) is carried out to clarify the beer and, e.g. reduce the<br />

polyphenol concentration.<br />

Cleaning agents and disinfectants are also used.<br />

2.2.17 Distilling<br />

The use of distillation in the FDM sector can be illustrated by the following two examples; the<br />

distillations of Scotch whisky and cognac.<br />

2.2.17.1 Scotch whisky<br />

Distillation units in the production of scotch whisky range from simple pot stills to continuous<br />

multicolumn stills. Energy is introduced in the form of steam to the bottom of the still and<br />

selectively volatilises the alcohol and other components from the fermented liquids and predistilled<br />

alcohol/water mixtures. The volatile components are recirculated within the still to<br />

achieve the correct separation, selection and concentration of alcoholic/aqueous compo<strong>und</strong>s for<br />

the many varied and desirable congener profiles required by the various types and brands of<br />

products. Stills can be operated singly or in series. The volatile components are condensed by<br />

heat-exchange with water in condensers and removed as a liquid spirit. The residual material<br />

known as pot ale, spent lees, stillage or spent wash, is discharged from the bottom of the still. In<br />

column stills other fractions are also removed such as fusel oils and high feints. The high feints<br />

are fed back into the stills and the fusel oils, which are mainly amyl alcohol, are sold as a coproduct.<br />

2.2.17.2 Cognac<br />

Cognac is obtained by the distillation of white wines harvested in the controlled appellation<br />

area. The distillation of Cognac is a two-stage process. In the first stage, a first distillate, known<br />

as “brouillis” is obtained. This has an alcoholic strength of between 28 to 32 % volume. In the<br />

second stage, the brouillis is returned to the boiler for a second heating, known as “la bonne<br />

chauffe”. The distillation heads, secondes and tails are separated, leaving only the heart of the<br />

spirit. There is a restriction on the maximum strength of distillation, which must not exceed<br />

72 vol-% alcohol. The time of each stage is about 12 hours.<br />

Distillation is carried out in two separate heatings or chauffes in a special Charentais copper pot<br />

still comprising a characteristically shaped boiler, heated with a naked flame and topped with a<br />

cowl shaped like a turban, an olive or an onion. A Charentais still often has an energy saving<br />

wine reheater. This device, in which the heat is provided by the alcohol vapours passing through<br />

it, preheats the wine, which is to be distilled in the next cycle. The final day for distillation is<br />

31 March of the year following harvesting.<br />

Maturation must be carried out in Limousin or Tronçais oak casks. As with other brandies and<br />

matured wine spirits, maturation was aided by the use of oak extracts, but this practice is<br />

becoming less common in Cognac. French regulations prohibit the use of additives in the final<br />

product, other than water and sugar or caramel, and restrict the minimum strength to 40 vol-%<br />

alcohol.<br />

108 January 2006 RHC/EIPPCB/FDM_BREF_FINAL

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