[0001] The present invention relates to a method and a device for the treatment of suspensions
of cellulose fibers, which are to be cleaned and concentrated, wherein the cleaning
also encompasses the elimination of light impurities.
[0002] The cleaning of cellulose suspensions from heavy impurities, such as sand, bark
and short shives, is now normally done in hydrocyclones, in which the impurities are
taken out in the apex fraction and the purified suspension in the base fraction. Such
cleaning presupposes a low fiber content, 0.1-3%, preferably 0.2-2%.
[0003] Cleaning out light impurities by means of hydroclones is also previously known, particularly
in the treatment of recycled paper, which often contains significant amounts of waste
plastic and ink etc. The hydrocyclones normally used in this case are dimensioned
and disposed in such a way that the base fraction contains the light impurities and
the apex fraction the major portion of the input cellolose fibers. Hydrocyclones for
this purpose are also known in which both fractions are taken out at the same end
through separate outlets.
[0004] The first mentioned type of hydrocyclone is referred to below as an A-cyclone, while
the second is referred to as a B-cyclone.
[0005] Since hydrocyclones are not perfect separators, recycling units are always required
for economic reasons, which recover cellulose fibers from the reject material. Such
recovering is previously known. As regards recycling with B-cyclones, reference is
made to Swedish patent applica tion 8802580-4 from 8 July 1988, which describes hydrocyclones
particularly suited for such recycling.
[0006] In plants presently used for manufacturing paper and market pulp, it is usual that
the suspension produced by whatever method (cooking, defibration, bleaching, beating
of recycled paper) is first diluted to be able to be screened and/or cyclontreated,
whereafter the cleaned suspension is thickened to be able to be intermediately stored.
This thickening is normally done in open thickeners. In order to thereafter be able
to conduct the pulp to a wet machine it must be diluted once again, as a rule to a
concentration which is higher that that used for the cleaning step. This thickening,
intermediate storage and dilution involves extra costs, which can be eliminated by
concentrating the pulp coming from the cycloning step and directly leading it to the
wet machine, particularly by using the same pump for the primary cycloning step and
a closed thickener working under pressure, as disclosed in Swedish Lay-Open Print
8305036-9.
[0007] As mentioned aboved, however, there is an increasing need for removal of light impurities,
especially plastic, and this applies not only to recycled paper but also to wood,
particularly from populated areas, which contains increasing amounts of plastic impurities.
Plastic particles can also come in during production in the plant. Even small amounts
of these impurities can present difficulties in paper production. Stripes in the paper
web can appear for example when coating.
[0008] One purpose of the present invention is to provide an improved system for manufacturing
paper pulp of good quality, especially as regards elimination of impurities, both
in the form of heavy and light particles. (Light particles are meant to include not
only particles of low density, but also particles which due to their shape perform
as lighter than cellulose fibers in hydrocyclones).
[0009] Another purpose is to provide a system which eliminates the need for thickening for
intermediate storage of already cleaned pulp suspension. Instead, the invention provides
an essentially continuous process which performs, in one sequence, cleaning, concentration
and final treatment in a wet machine or paper machine.
[0010] These and other purposes and advantages are achieved according to the invention by
the process according to claim 1 and by a device according to claim 8.
[0011] One particular advantage of the invention is the synergetic effect achieved by the
combination of the functions of thickening and cleaning from light impurities, preferably
whilst simultaneously eliminating an intermediate storage step and a diluting step.
[0012] What makes the invention possible is the fact that the suspension fraction coming
from the apex in a hydrocyclone designed for eliminating lighter impurities has a
consistency which is increased in relation to that of the suspension supplied, since
much water accompanies the light impurities in the base fraction.
[0013] A particularly high consistency can be achieved, with very good separation of light
impurities, if one can accept that some cellulose fibres will accompany the base fraction,
whereby the recovery is simplified by reducing the number of recycling steps by using
hydrocyclones of the type described in Swedish patent application 8802580-4 (not yet
publicly available).
[0014] According to the invention, it is possible to achieve a consistency of between 1
and 3% after combined cleaning of the light impurities and thickening, which is a
suitable starting consistency for many types of wet machines and paper machines.
Hydrocyclones must of course be operated with an essentially constant flow of liquid,
and the output consistency is determined by the consistency of the pulp flow supply.
The flow to the wet machine or paper machine can then be additionally varied by a
feedback which feeds a controllable portion of the output flow to the input side of
the cleaning system.
[0015] It is suitable to provide the white water tank of the wet or paper machine with a
spillway to keep the water level constant, and to take the necessary diluting water
from there for the process.
[0016] As a rule, hydrocyclones function best if the liquid flows and pressure ratios are
kept rather constant at the rated values. However, in different operating situations
it can be necessary to vary the flow to a wet machine or paper machine. It is therefore
suitable to arrange a diversion of the treated suspension, which returns the unused
but cleaned and concentrated suspension. This recycling can be done to a point immediately
in front of the main pump, without changing the fiber flow to the wet machine or paper
machine, but with the result that the consistency of the suspension to the headbox
will be increased. Alternatively, the feedback can be to a point prior to the consistency
control in connection with a first dilution, thus keeping the consistency of the suspension
to the headbox constant and reducing the flow to the headbox.
[0017] The invention will now be described with reference to a non-limiting example, shown
schematically in diagram form in the drawing.
[0018] The schematic figure shows an example of a plant functioning in accordance with
the invention. The major portion of the fiber material passing through it flows from
a conventional silo 1 to a wet machine or paper machine 9 along a main path drawn
as a thick line. The pulp with a consistency of 10-12% is diluted in the lower portion
of the silo 1 to about 3.5%, and is diluted at the input side of a pump 103 to a controlled
consistency of 3.0% and is then led to a silo 2, where the level is kept constant.
The diluting water is taken via a pump 12 from the white water of the wet or paper
machine. The person skilled in the art will understand how the level and consistency
in the silo 2 will be controlled and therefore it is sufficient to state that the
dilution is controlled by actuating the valves 100 and 101 by the sensor 102 and the
level by the level sensor 200, which controls the speed regulator 104 to the pump
103. 105 is a control unit which opens the valves 100 and 101 in parallel and controls
the flow therethrough in a predetermined ratio. In the silo 2, there is thereby achieved
a constant level and a constant consistency for the suspension.
[0019] The suction side of the pump 3 is connected to the silo 2, and it receives diluting
water from the pump 12 via the valve 300, which is controlled by the sensor 301, which
senses the consistency of the suspension exiting from the pressure side of the pump
3. The consistency is controlled thereby to 2.5%. The flow of the suspension supplied
is led through a valve 400 under the control of a flow sensor 401 at a desired level.
The flow of fibers through the valve 400 is thus kept constant.
[0020] A controlled flow of suspension with a controlled consistency (fiber concentration)
is thus led to the suction side of the pump 4.
[0021] For the present, one can disregard the line 13, which refers to a particular aspect
of the invention which will be described in more detail below. The pump 4, a centrifugal
pump, provides an essentially constant flow, and the pressure on the suction side
is determined by the level in the white water tank 10, the level of which is kept
constant in a known manner. The pump 4, as long as its counterpressure is stable,
gives a predetermined flow with a consistency determined by the amount of fibers per
unit of time which passes through the valve 400. With the values according to the
example, a consistency of 0.5% is attained on the pressure side of the pump 4, which
is a suitable value for cycloning, even though thinner and thicker consistencies
are possible to work with.
[0022] The suspension thus diluted is led through a screen 5, which is primarily intended
to eliminate scrap particles and other larger particles, which could damage the cyclones,
to a multi-hydrocyclone unit 6 with A-cyclones, the base fraction of which is conducted
further. The consistency of the base fraction will be 0.45%, i.e. somewhat thinner
than the suspension supplied. This base fraction is moved on without intermediate
pumping to a multi-hydrocyclone unit 7 with B-cyclones, where the fiber is removed
as an apex fraction, which the lighter particles go into the base fraction. In this
apex fraction, the cellulose fibers are enriched to a higher consistency, in the example
to 1.5%, thus thickened by a factor of 3.33. This consistency is suitable for the
following wet or paper machine 9, to the headbox 8 of which the suspension is conducted
via a valve 800, controlled by a sensor 801, in this case a pressure sensor. The headbox
thus receives the suspension at a controlled pressure. If so desired, the sensor 801
can be a level sensor or a flow sensor.
[0023] Recovery units are connected to the two multi-hydro cyclone units 6 and 7. The recovery
units are shown here as cascade coupled units with individual pumps at the inlets
and with the outlets connected to a common level in the tank 10. Although only two
steps in each unit have been shown, the number of steps is determined by the desired
degree of recovery and purification. The recovery units to the unit 6 consist of A-cyclones,
while the recycling units to unit 7 are B-cyclones. The number of steps in the recycling
from unit 7 is positively affected, as is the number of individual cyclones in the
units, if the latter are constructed in accordance with Swedish patent application
8802580-4.
[0024] In the example, the unit 7 provides both a cleaning from light impurities and a thickening
of the suspension thus cleaned, which combination is the great advantage of the invention.
This thickening can be done in different degrees depending on the cyclone dimensions,
the pressure drop and the distribution of apex and base flows of the incoming suspension.
The thickening factor, which always exceeds 1, and in this example is 3.33, can be
increased to 5 for example, if so required, and this can be done without negatively
effecting the separation of light impurities; on the contrary, the separation effect
will tend to increase. The fiber content in the base fraction may thereby increase,
so that the processing work in the recovery units increases, but this can be dealt
with by using hydrocyclones according to the Swedish patent application 8802580-4.
[0025] The above-mentioned thickening is a result of separation of water and fibers. The
degree of thickening in a hydrocyclone is determined by the effectiveness of this
separation. In order to achieve a high degree of thickening, the hydrocyclone is
made with a smaller base opening than the apex opening. For the separation work, the
conical separa tion chamber should have a largest diameter of less than 125 mm and
preferably less than 100 mm. Furthermore, the diameter of the base opening should
be less than a fifth of the largest diameter of the separation chamber.
[0026] The main flow of fibers has now been explained. The return flows from the recycling
steps go through the line 11′ back to the suction side of the pump 4. This means,
that if the line 13 were not there, the entire flow of fibers, under stability conditions,
coming in via the valve 400, would be fed out to the headbox 8. The flow is then determined
by the capacity of the pump 4 and by the flow-offs, determined by the normally constant
pressure ratios, in the apex fraction of unit 6 and in the base fraction of unit 7.
[0027] For optimal operation, hydrocyclones should be operated with predetermined liquid
flows. However, it is not certain that this is the case with the headbox of a wet
machine or paper machine, where the flow, pressure and consistency may need to be
varied. The consistency, at constant flow, can be controlled by controlling the flow
and consistency of the suspension supplied via the valve 400. The flow to the headbox
8 can be controlled by a return line 13 with the valve 130 controlled by a pressure
sensor 131. This return line 13 can, in accordance with the first embodiment, open
into the suction side of the pump 4, which will cause the fiber flow to the headbox
8 to be unchanged while the consistency is changed.
[0028] In accordance with a second embodiment, drawn with dashed lines in the Figure, the
return flow is effected via a line 13′ back to a point prior to the pump 3, in this
case upstream of the dilution control valve 300, but in any case to a point upstream
of the consistency and flow control which determined the fiber flow supplied to the
suction side of the pump 4. Controlling the liquid flow to the headbox 8 by means
of the valve 130 does not effect the consistency of the suspension supply.
[0029] The invention has now been described on the basis of a non-limiting example, from
which it is clear that such a system can be controlled within side limits. Even if
the flow capacity for the cyclone equipment is given by the design, it is possible
to vary within wide limits the capacity of the pulp flow and the consistency of the
suspension outflow.
[0030] As mentioned, it is also possible by designing control measures within the scope
of the invention to vary for example the degree of thickening in the system.
[0031] One should note in particular that a single main pump 4 pumps the diluted suspension
to the units 6 and 7 coupled in series and then to the headbox 8. In a representative
example, the pressure drop between the inlet and the base in a A-cyclone is 1 bar
and the pressure drop in a B-cyclone between the inlet and the apex is 1.5 bar. These
pressure drops are essentially a function of the flow. The pump 4 is dimensioned so
that it can both compensate these pressure drops and produce sufficient pressure to
the headbox 8.
[0032] Control of the valves 800 and 130 must be done in such a manner that the operating
conditions for the multi-hydrocyclone units are not affected negatively. The main
pump 4 is a centrifugal pump, driven at essentially constant rotational speed, with
falling pressure head as flow increases. The system is designed so that at the rated
flow the pressure head is sufficient for the pressure drops in the multi-hydrocyclone
units 6 and 7 and the valve 800 at a normal work point, and controlling within reasonable
limits of the flow through the valve 800 to keep the pressure or the level in the
headbox 8 does not involve any appreciable disruption. Major changes in the pressure
drop over the valve 800 cannot be tolerated, however, since the working conditions
for the units 6 and 7 would be adversely affected. In order to make significant changes
in the feed flow to the box 8, there must therefore be a diversion via the shunt valve
130 so that the pressure on the suspension can be kept reasonably constant. The shunt
valve 130 can then either be controlled manually with reference to a manometer or
can be pressure controlled in the manner shown in the drawing.
[0033] The various controls in the drawing have been shown as mutually independent local
controls. It will be understood, however, that such controls can be effected by a
common computer.
1. Process for manufacturing cellulose pulp with improved quality properties, especially
as regards the content of light, solid impurities such as particles of plastic and
the like, characterized in that a fiber suspension of low consistency is caused by
a main pump (4) to pass through a first multi-hydrocyclone unit (6) to separate out
heavy particles and a second multi-hydrocyclone unit (7) included in the same pump
circuit for separating out light particles at the same time as the pulp consistency
is made higher during treatment in the second multi-hydrocyclone unit (7), and that
at least a portion of the pulp suspension thus treated is thereafter conducted directly
without intermediate pumping to the headbox (8) of a wet machine or paper machine.
2. Process according to claim 1, characterized in that the suspension conducted to
the wet machine or paper machine passes through a controllable valve (800), which
is controlled by a sensor (801) for pressure, flow or level in the head box (8) of
the wet machine or paper machine.
3. Process according to claim 1, characterized in that a portion of the flow which
emerges cleaned from the second multi-hydrocyclone unit (7) is recycled for intake
upstream of the main pump (4).
4. Process according to claim 3, characterized in that the recycled flow is controlled
by means of a valve (130) to achieve the desired pressure for the cleaned suspension
coming from this second multi-hydrocyclone unit.
5. Process according to claim 3, characterized in that the reintroduction is arranged
at the suction side of the main pump (4).
6. Process according to claim 3, characterized in that the reintroduction is arranged
to a diluting device (300) upstreams of the suction side of the main pump (4).
7. Process according to claim 1, characterized in that to the suction side of the
main pump (4) by means of a second pump (3) there is pumped a suspension which is
controlled as to its flow rate and consistency, the suction side of said main pump
(4) being coupled to a level regulated tank (10) included in the white water system
of the wet machine or paper machine, dilution being effected with white water therefrom.
8. Process according to claim 1, characterized in that the second multi-hydrocyclone
unit is provided with hydrocyclones with conical separation chambers with a greatest
diameter of less than 125 mm and preferably less than 100 mm, and with a base opening
diameter which is less than a fifth of the largest diameter of the separation chamber
and an apex opening which is greater than the base opening.
9. Device for manufacturing cellulose pulp with improved quality properties, particularly
as regards the content of light, solid impurities such as particles of plastic and
the like, characterized by the combination of a pump (4), a first multi-hydrocyclone
unit (6) for separating out heavy particles, a second multi-hydrocyclone unit (7)
for separating out light particles, and the headbox (8) of a wet machine or paper
machine (9) coupled in series with each other, said second multi-hydrocyclone unit
serving at the same time as a means for thickening the cleaned suspension.
10. Device according to claim 9, characterized by a controllable valve (800) which
is coupled between the second multi-hydrocyclone unit (7) and the headbox, and means
(801) for sensing and, by actuating the valve (800), controlling pressure, flow or
the level in the headbox.
11. Device according to claim 9 or 10, characterized by a shunt line (13, 13′) which,
for diverting suspension, is connected at a diversion point between the second multi-hydrocyclone
unit (7) and the headbox (8) and leads to an introduction point which is located upstream
of said pump (4).
12. Device according to claim 11, characterized in that in the shunt line (13, 13′)
there is a valve (130).
13. Device according to claim 12, characterized by a control device (131) which is
disposed to control the valve (130) in response to the pressure at said diversion
point.
14. Device according to claim 11, characterized in that said shunt line (13, 13′)
leads to a diluting device disposed upstream of the pump (4).
15. Device according to claim 9, characterized in that the second multi-hydrocyclone
unit is made of hydrocyclones with conical separation chambers with a largest diameter
of at most 125 mm, preferably at most 100 mm, and with the base opening and an apex
opening, the base opening diameter being less than a fifth of the largest diameter
of the separation chamber and the apex opening being larger than the base opening.