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Generally the cleaning is done as follows:
Precipitate
The metals are precipitated as hydroxides, by raising the pH to 8-10. To manage
the low emission values for mercury and cadmium, these are precipitated as
sulphides. De-gasification
Is done by "stripping" the liquid with combustion air. This is done in
a reactor with a surface enlarging inset, where the liquid is finely dispersed
over the inset and meets the air on it's way through the stripping tower. Flocking
Precipitated metals, fine grain ash and dioxin most often appear as small
particles difficult to separate. By using additives the particles agglomerate
into larger clusters, where after these are separated gravimetrically or by
sieving. Particle separation
Gravimatic separators
In these the flow of liquid is laminar with such low velocity, that the
particles settle. The average distance between particle and sediment surface is
kept narrow, which promotes sedimentation. The remaining particle content after
the gravimatical separation is normally 20-40 mg / l.
Sieves
When filtering using the sieve effect, cartridge filter drum sieves
etc., are used. Cartridge filter can be selected to give a remaining particle
content after filter of 10 mg / l. The automatically cleaned drum sieve RECO-LW
is suitable for high liquid flows and high particle load. It can be selected to
separate particles down to 20 mm. Sandfilter
With demand of very low particle emissions, (less than 10 mg /l), sand filter is
used, either alone or as a final filter after gravimatical separators or sieves. Carbon filter
For example. mercury, cadmium and dioxins the demands are so stringent, that
further process stages in some cases are necessary, e.g. adsorption with
activated carbon.
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