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Rotary drum washers were the first pieces of continuous washing equipment to
be developed. They have undergone continuous improvement over the decades,
and today exist in a wide variety of designs. Conventional drum washers can be
categorized into vacuum washers and pressure washers.
5.6 Washing Equipment 547
Pulp of typically 0.5–1.8% consistency is fed to the washer vat. As the liquor
flows through the washer wire attached to the drum, the pulp mat is formed. The
pulp mat is lifted out of the vat with the rotation of the drum and enters the washing
zone, where several showers layer the wash liquor onto the mat. At the end of
the washing zone, the drainage may be supported by press rolls. Finally, the pulp
mat is released from the wire in the discharge zone and falls from the take-off
into the repulper, a shredding screw conveyor (Fig. 5.25).
Fig. 5.25 Impco Coru-Dek vacuum washer [33].
In a vacuum washer, the vacuum which causes the liquor to flow through the
pulp mat and washer wire is usually created by the downfalling filtrate in the drop
leg, a vertical pipe of adequate length. This set-up requires the vacuum washer to
be located at a higher level in the building. It also requires that the temperature of
the filtrate does not exceed about 80–85 °C, because above this temperature the
vapor pressure of water becomes a threat to the vacuum.
In pressure washers, the differential pressure across the pulp mat is created by
a gas pressure maintained in the hood by a fan. No drop leg is required, and pressure
washers can be operated much closer to the boiling point of the liquor than
vacuum washers. The pulp enters the vat, is taken up by the drum, and is then
washed in up to three countercurrent stages. After the pulp has passed the seal
roll, the take-off is provoked by the pressure inside the drum which blows the
pulp off the face wire. The encapsulated design minimizes emissions to the air.
548 5 Pulp Washing
Fig. 5.26 Two-stage Sunds Rauma pressure washer [34].
The washing efficiency on a conventional drum washer depends mainly on the
shower arrangement and on the washer’s capability to avoid rewetting of the pulp
mat with filtrate from the pockets of the drum before discharge.
As a rule of thumb, the outlet consistency is around 12%. However, it may fall
well below 10% for pulp with unfavorable drainage behavior, yet may be as high
as 18% for easy-draining pulp after press rolls. The E factors range from 1.5 and
3.0.
As a consequence of the design principle, conventional drum washers tend to
let air through the pulp mat towards the end of the washing zone. The entrained
air induces foaming in the filtrate tank, and would adversely affect drainage if
recycled back with dilution filtrate before the washer. In order to avoid the latter
situation, air must be given sufficient time to leave the filtrate in the filtrate tank,
and this is done by providing adequate retention time and surface area.
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