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Since efficient centrifugal cleaning requires low pulp consistency and small-sized
hydrocyclones, a large number of units is required to deal with the considerable
flow rates. This has formerly resulted in long rows of cleaners with atmospheric
reject discharge. Today, the established arrangement of large numbers of pressurized
hydrocyclones is in canisters.
Figure 6.39 shows a Noss Radiclone, where the hydrocyclones are installed
radially in a pressurized cylindrical canister with vertical axis. Depending on the
cleaning capacity, one canister can hold several hundred cyclones. The feed enters
the canister centrically from the bottom and the pulp flows to the individual
hydrocyclones, where the separation takes place. The rejects and accepts from the
individual cyclones are then collected in separate compartments and leave the canister
through nozzles at the bottom. Typical cyclone diameters range from 80 to
125 mm. The pressure drop from the feed side to the accept side is between 1 and
2 bar [39]. In order to reduce the fiber loss from the last stage of cleaning, hydrocyclones
can be equipped with apex dilution.
The above-mentioned type of hydrocyclone used for the separation of heavyweight
particles is also called a forward cyclone. Cleaners for the separation of
light-weight contaminants are often termed reverse cyclones, accounting for the
6.9 Screening and Cleaning Equipment 605
inversion of accept and reject positions. Reverse cleaners can also be arranged in
canisters. The flow pattern in such canisters is similar to that illustrated in
Fig. 6.39, but the dimensions of the flow channels are adapted to the comparatively
larger apex flow rate and smaller base flow rate. In contrast to forward
cyclones, reverse cleaners do not thicken the reject, but lift the accept consistency
considerably above the feed consistency. Typical thickening factors are between
1.5 and 3.0 [40].
Larger-diameter, individual cyclones are sometimes employed for the separation
of heavy-weight contaminants to protect screen baskets or refiners from detrimental
feed components. These cyclones are typically 200–500 mm in diameter, and
may extend some meters in an axial direction. An example of a larger-diameter
cyclone separator, the Metso HC cleaner, is shown in Fig. 6.40. The cleaner can be
operated either on a continuous basis or with intermittent reject discharge as a
junk trap. HC cleaners are designed to work with feed consistencies up to 5%, but
are normally operated in the 1.5–2.5% range [41].
606 6 Pulp Screening, Cleaning, and Fractionation
Fig. 6.39 The Noss Radiclone AM [39]. Fig. 6.40 The Metso HC cleaner [41].
References 607
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