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Paper Technology Journal 17 - Voith

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8<br />

Fig. 1: Previous AK design.<br />

Fig. 2: New CompactPulper design.<br />

Fig. 3: 3D presentation of the new Compact-<br />

Pulper.<br />

Fig. 4: Chest widths: comparison between<br />

conventional and new design.<br />

At sheet breaks the broke pulper must<br />

reach full operating speed from start-up<br />

in the shortest possible time. The procedure<br />

is as follows:<br />

As soon as a sheet break is detected, the<br />

sheet is diverted directly into the broke<br />

pulper located ahead of the sheet break.<br />

At the same time the showers open, and<br />

the sheet is wetted and pulled down with<br />

the water flow. In the meantime, the<br />

pulper rotors have reached full speed,<br />

generating enough circulation energy to<br />

draw in the sheet, which is then rapidly<br />

pulped down and pumped off through the<br />

pulper screenplate.<br />

Based on <strong>Voith</strong>’s long experience, with<br />

over 375 AK series pulpers delivered<br />

since 1990, the objective of this development<br />

project was to further increase<br />

broke pulper efficiency whilst at the same<br />

time reducing investment costs.<br />

Slushing conditions in the broke pulper<br />

1 2<br />

<strong>17</strong>/04<br />

seem simple at first sight, but a closer<br />

look quickly reveals just how many<br />

boundary conditions have to be simultaneously<br />

taken into account in order to ensure<br />

reliable operation:<br />

● <strong>Paper</strong> machine width and speed<br />

● <strong>Paper</strong> grade, basis weight and location<br />

of the sheet break in the machine<br />

● Pulping intensity and suspension level<br />

● Dwelltime<br />

● Broke removal rate through the pulper<br />

screenplate.<br />

Additionally, the pulping consistency has<br />

to keep within certain limits to ensure a<br />

reliable sheet draw-in, good pulping and<br />

stable pump operation.<br />

The development project was carried out<br />

on two levels due to the complexity of the<br />

process and also the need for field trials:<br />

● A full-size trial pulper, incorporating<br />

the new optimized geometry of the<br />

CompactPulper, was tested in <strong>Voith</strong><br />

<strong>Paper</strong>’s <strong>Technology</strong> Center. This<br />

enabled intensive investigation of<br />

machine parameters which usually<br />

cannot be changed in mill operation<br />

● Extensive mill trials and comparison<br />

with the <strong>Technology</strong> Center’s trial<br />

results.<br />

Figs. 1 and 2 show the differences<br />

between the conventional broke pulper<br />

design and the new CompactPulper.<br />

The trials clearly showed that a large part<br />

of broke pulping energy is used for moving<br />

the stock round. Compared with<br />

pulpers for slushing recovered paper or<br />

virgin fiber pulp, in broke pulpers the<br />

sheet is brought into the pulper in a<br />

clearly defined way. It has already been<br />

thoroughly wetted on both sides by the<br />

showers. This means that pulper dwelltime<br />

is reduced by the time otherwise required<br />

for breaking down and wetting the<br />

paper when presented in bale form.The<br />

pulper chest can therefore be much<br />

smaller, as confirmed by the trial results.

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