A pulper
A pulper for producing paper pulp from waste paper containing undesired scrap particles includes a container (
1) forming a chamber (
4) defined by a bottom wall (
5) and a cylindrical circumferential wall (
6). A paper tearing member (
7)
is arranged in the chamber closed to the bottom wall and is rotatable
in a horizontal direction of rotation about the centre axis of the
cylindrical wall. The bottom wall and the circumferential wall forms a
substantially circular peripheral reject chute (
11) situated
under the paper tearing member for collecting reject including undesired
scrap particles. The reject chute extends helically in the direction of
rotation of the paper tearing member from an upper end (
12) of the reject chute downwardly to a lower end (
13) of the reject chute. The circumferential wall (
6) has a substantially cylindrical shape and extends vertically to the reject chute (
11). A discharge element (
2) is adapted to discharge reject in batches from the reject chute.
1. A pulper for producing paper pulp from waste paper containing
undesired scrap particles, comprising: a container forming a chamber
for receiving waste paper and water, said chamber being defined by a
bottom wall and a substantially cylindrical circumferential wall, a
paper tearing member, which is arranged in said chamber close to said
bottom wall and which is rotatable in a horizontal direction of rotation
about a center axis of said cylindrical wall, said bottom wall and said
circumferential wall forming a substantially circular peripheral reject
chute, which is situated under said paper tearing member for collecting
reject including undesired scrap particles and which extends helically
in the direction of rotation of said paper tearing member from an upper
end of said reject chute downwardly to a lower end of said reject chute,
a horizontal discharge pipe connected to said reject chute at said
lower end thereof, and a coreless conveyer screw in said horizontal
discharge pipe for discharging reject in batches from said reject chute,
said coreless conveyor screw having an inlet end and an outlet end,
wherein said conveyor screw is journalled in such a manner at said inlet
end so that said conveyor screw is radially moveable at said outlet
end.
2. A pulper according to claim 1, wherein the interior
of said discharge pipe is connected to said reject chute at said lower
end thereof via an upper hole in said discharge pipe, whereby reject
passes from said reject chute into said discharge pipe via said upper
hole.
3. A pulper according to claim 1, wherein said discharge
pipe extends substantially tangentially toward said circular
circumferential wall of said container.
4. A pulper according to claim 1, further comprising a
drive means adapted to intermittently rotate said conveyor screw to
discharge reject in batches from said reject chute.
5. A pulper according to claim 1, further comprising a
dewatering means for dewatering reject that is fed out of said discharge
pipe.
6. A pulper according to claim 5, wherein said
dewatering means comprises a declining pipe, which at its lower end is
connected to said discharge pipe, a dewatering screw extending in said
declining pipe for feeding reject to the upper end of said declining
pipe, and a strainer arranged on said declining pipe at its upper end
for separating water from the reject.
7. A pulper according to claim 1, wherein said
substantially cylindrical wall comprises a wall portion forming a radial
constriction in said chamber of said container.
8. A pulper according to claim 7, wherein said wall portion is plane.
Description:
BACKGROUND OF THE INVENTION
The
present invention relates to a pulper for producing paper pulp from
waste paper containing undesired scrap particles. The pulper comprises a
container forming a chamber for receiving waste paper and water. The
chamber is defined by a bottom wall and a substantially cylindrical
circumferential wall. The pulper further comprises a paper tearing
member provided in the chamber closed to the bottom wall and rotatable
in a horizontal direction of rotation about the centre axis of the
cylindrical wall. The bottom wall and the circumferential wall form a
substantially circular peripheral reject chute situated under the paper
tearing member for collecting reject including undesired scrap particles
and extending helically in the direction of rotation of the paper
tearing member from an upper end of the reject chute to a lower end of
the reject chute, the circumferential wall extending vertically to the
reject chute. A discharge pipe is connected to the reject chute at the
lower end thereof and a conveyer screw is arranged in the discharge pipe
for discharging reject in batches from the reject chute.
Traditionally,
pulpers are used in the pulp and paper making industry as a first
process step to initially fragmentize and disintegrate the waste paper,
which usually is delivered in bales, in water, so that a primary paper
pulp is obtained. The primary paper pulp usually contains a great deal
of undesired relatively large scrap particles, such as glass, stone,
metal, plastic and the like. Such undesired scrap particles are removed
from the primary paper pulp already in the pulper with the aid of a
strainer that only permits passage of paper pulp and smaller impurities.
A
problem of the traditional pulpers however is that also relatively
large scrap particles are disintegrated by the rotating paper tearing
member into smaller particles that are able to pass through the strainer
of the pulper, which makes it more difficult to clean the primary paper
pulp in the subsequent cleaning steps. EP 0414602 A2 discloses a known
pulper of the kind initially described that partly eliminates this
problem. Thus, the container according to the known pulper has a
traditional, conically designed wall portion of the circumferential wall
extending downwardly to the reject chute, and a reject outlet for
continuous discharge of reject from the reject chute. Undesired large
scrap particles are intended to separate to the reject chute and be
discharged continuously from this via the outlet.
However, the
known pulper is not capable of satisfactorily preventing large scrap
particles from being disintegrated by the paper tearing member. In
addition, some released fibres are lost through the reject outlet, which
is a drawback.
SUMMARY OF THE INVENTION
The object of the
present invention is to provide a pulper that efficiently prevents
disintegration of relatively large scrap particles and minimises the
lost of fibres.
This object is obtained by a pulper of the kind
initially described characterised in that the conveyer screw comprises a
coreless conveyer screw and that the discharge pipe is horizontal.
The
conveyer screw has an inlet end and an outlet end, wherein the conveyer
screw is journalled at the inlet end thereof in a manner such that it
is radially moveable at its outlet end. The fact that the conveyor screw
is coreless and radially moveable at its outlet end means that the
discharged pipe is efficiently prevented from being clogged by long
particles such as plastic shreds that rotate along with the conveyor
screw. Suitably, a drive means is adapted to intermittently rotate the
conveyor screw to discharge reject in batches from the reject chute.
The
discharge pipe preferably extends substantially tangentially towards
the circular reject chute and at its lower end is provided with an upper
radial hole, through which reject passes from the reject chute into the
discharge pipe. A dewatering means for dewatering reject fed out from
the discharge pipe may comprise an inclined pipe, which at is lower end
is connected to the discharge pipe, a dewatering screw extending in the
pipe for feeding reject to the upper end of the pipe, and a strainer
arranged on the pipe at its upper end for separating water from the
reject.
To disturb the vortex generated in the mixture of torn
paper and water in the container of the pulper, as the paper tearing
member is rotated, the generally cylindrical wall may comprise a
preferably plane wall portion forming a radial constriction in the
chamber of the container. The constriction makes it difficult for the
vortex to form a central air column that reaches down to the strainer
that normally is arranged under the rotating paper tearing member. As a
result a large volume of finished paper pulp can be pumped from the
container before air from the air column of the vortex disturbs the
function of the used pump.
BRIEF DESCRIPTION OF THE DRAWINGS
The invention is explained in more detail in the following reference to the accompanying drawings, in which
FIG. 1 shows a side view of a pulper according to the invention,
FIG. 2 shows a view from above of the pulper according to FIG. 1, and
FIG. 3 shows a sectional side view of an enlarged detail of the pulper according to FIG.
1.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
FIG. 1 shows a pulper according to the invention comprising a container
1 for receiving waste paper bales in batches, a discharge means
2 for discharging reject in batches from the container
1 and a dewatering means
3 for dewatering discharge reject. The container
1 forms a chamber
4 defined by a bottom wall
5 and a vertical cylindrical circumferential wall
6, see FIG.
3. The cylindrical circumferential wall
6 has a diameter of about 5 meter and comprises a plane wall portion
24, which forms a radial constriction in the chamber
4. A paper tearing member
7 with five knife blades
8 is attached to a vertical rotor shaft
9 journalled centrally on the bottom wall
5 and rotatable by a motor
10.
The bottom wall
5 and the cylindrical circumferential wall
6 form a circular peripheral reject chute
11 situated under the paper tearing member
7. The reject chute
11 extends helically in the direction of rotation of the paper tearing member
7 from an upper end
12 of the reject chute
11 to a lower end
13 of the reject chute
11.
The discharge means
2 comprises a straight horizontal discharge pipe
14 extending substantially tangentially towards the cylindrical circumferential wall
6 and situated under the reject chute
11. The interior of the discharge pipe
14 is connected to the reject chute
11 at its lower end
13 via an upper hole
15 in the discharge pipe
14. A coreless conveyor screw
16 extends in the discharge pipe
11 and is rotatable by a motor
17. At its inlet end the conveyor screw
16 is journalled on the shaft of the motor
17 in such a manner that it is somewhat radially moveable at its outlet end.
The dewatering means
3 comprises a pipe
18 extending obliquely upwardly from the discharge pipe
14, a dewatering screw arranged in the pipe
18 and a strainer
19 arranged on the under side of the pipe
18 close to the upper end of the pipe
18. The dewatering screw is driven by a motor
20 situated at the lower end of the pipe
18. The discharge pipe
14 and the obliquely upwardly extending pipe
18 are connected to each other so that a closed passage for reject is formed in the latter. A screw press
21 is arranged to receive reject that is conveyed out of the pipe
18. A reject container
22 is placed under the screw press
21 for receiving compressed reject.
In operation, the paper tearing member
7 is rotated by the motor
10 at a speed of about 100-200 rpm and the container
1
is filled with a number of waste paper bales. Water is supplied to the
container concurrently with the continuous disintegration of the paper,
so that finally a primary paper pulp with a desired fibre concentration
has been obtained, for example between 8-15%. Then valves, not shown,
are opened so that the paper pulp can be pumped out from the container
through the coreless strainer
23 situated centrally under the paper tearing member
7. During the discharge of the paper pulp the vortex in the paper pulp is disturbed by the plane wall portion
24, so that substantially all of the paper pulp can be pumped out from the container
1. The course of events described above can normally take about 90 minutes.
During
the disintegration of the paper pulp present scrap particles are
released, which scrap particles are pulled by centrifugal force radially
outwardly to the vertical circumferential wall where they sink by
gravity down to and accumulate in the reject chute
11. After discharge of paper pulp and before a new batch of waste paper is supplied to the container
1 accumulated reject may be discharged. Discharge of reject takes place by activating the motors
17 and
20 at the same time as rinsing water is supplied to the container
1 and the paper tearing member
7 is rotated. The reject in the lower end
13 of the reject chute
11 is pressed down through the hole
15 and its captured by the conveyor screw
16, which conveys the reject to the upwardly obliquely extending pipe
18. In this the dewatering screw feeds the reject further up to a level above the liquid mixture in the container
1. At this level the reject is dewatered when it passes the strainer
19. The dewatered reject is discharged from the upper end of the pipe
18 to the screw press
21, which compresses the reject. Finally the compressed reject is discharged from the screw press
21 to the reject container
22. After accomplished reject discharge the motors
17 and
20 are stopped, and then a new batch of waste paper can be supplied to the container
1.