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Separator's Digest 2009/1 min. - GEA Westfalia Separator Group

Separator's Digest 2009/1 min. - GEA Westfalia Separator Group

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The ceramic membrane in<br />

cross-flow filtration is the<br />

most efficient method of<br />

juice filtration.<br />

Avoiding retentate<br />

Membrane technology is suitable for maximum concentration of the solids in the<br />

retentate, thereby reducing the overall retentate volume.<br />

The quantity of retentate is reduced if decanters are used for juicing<br />

in normal processing. In principle, this use of centrifugal technology<br />

with decanters features the lowest trub level. However, the solids<br />

content can also be reduced to a <strong>min</strong>imum with a separator for<br />

clarifying the juice. This means that the quantity of trub, which<br />

forms the subsequent retentate, is limited right from the very<br />

beginning.<br />

In the next stage, the process of continuing this idea for reducing<br />

the general volume of retentate results in maximum concentration<br />

of the solids in the retentate. Polymer and ceramic membranes are<br />

suitable for this purpose, with system-related differences. A ceramic<br />

membrane is much more stable with regard to pressure, and is thus<br />

able to provide a retentate with a solids content of up to 90 percent<br />

(by volume). Compared with a plastic membrane, the concentration<br />

factor is thus three times as high. Such a high concentration of<br />

the solids requires no further treatment of the retentate. A ceramic<br />

membrane in cross-flow filtration is thus the most efficient method<br />

used for juice filtration. The use of decanters and ceramic filtration<br />

is therefore always recommended for a new installation or<br />

whenever an existing operation is extended.<br />

Solids content reduced by a centrifuge<br />

upstream of filtration<br />

Diafiltration is the simplest way to achieve an additional benefit<br />

from the retentate, in order to generate a profit from waste costs.<br />

In many areas, it is better known as desweetening. At the end of<br />

the filtration stage, water instead of turbid juice is added to<br />

the filtration cycle. The cost-effectiveness of desweetening must be<br />

deter<strong>min</strong>ed for each individual case. Process engineering measures<br />

enable the filtration cycles to be extended and thus the number of<br />

cleaning and diafiltration runs to be reduced.<br />

24<br />

<strong>Separator</strong>’s <strong>Digest</strong> 1 | <strong>2009</strong><br />

<strong>GEA</strong> <strong>Westfalia</strong> <strong>Separator</strong> Process

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