CA2027564A1 - Appliance for sorting and deflaking fibre suspensions - Google Patents
Appliance for sorting and deflaking fibre suspensionsInfo
- Publication number
- CA2027564A1 CA2027564A1 CA002027564A CA2027564A CA2027564A1 CA 2027564 A1 CA2027564 A1 CA 2027564A1 CA 002027564 A CA002027564 A CA 002027564A CA 2027564 A CA2027564 A CA 2027564A CA 2027564 A1 CA2027564 A1 CA 2027564A1
- Authority
- CA
- Canada
- Prior art keywords
- rotor
- region
- screen
- sorting
- deflaking
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D5/00—Purification of the pulp suspension by mechanical means; Apparatus therefor
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D5/00—Purification of the pulp suspension by mechanical means; Apparatus therefor
- D21D5/02—Straining or screening the pulp
- D21D5/023—Stationary screen-drums
- D21D5/026—Stationary screen-drums with rotating cleaning foils
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D5/00—Purification of the pulp suspension by mechanical means; Apparatus therefor
- D21D5/18—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force
- D21D5/20—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force in apparatus with a horizontal axis
Abstract
ABSTRACT
An appliance for sorting and deflaking fibre suspensions has a rotor with a horizontal axis rotatively mounted in a housing. In a first, inlet rotor zone the rotor is provided with entraining means for extracting by centrifugation contaminating particles of high relative density. The rotor is surrounded downstream by a screening cylinder and is also provided with entraining means for the fibre suspension, which deflake and sort out the fibre suspension in a second rotor zone. In a third rotor zone the fibres are washed out of the rejects after water has been added and in a fourth zone the rejects are dehydrated.
An appliance for sorting and deflaking fibre suspensions has a rotor with a horizontal axis rotatively mounted in a housing. In a first, inlet rotor zone the rotor is provided with entraining means for extracting by centrifugation contaminating particles of high relative density. The rotor is surrounded downstream by a screening cylinder and is also provided with entraining means for the fibre suspension, which deflake and sort out the fibre suspension in a second rotor zone. In a third rotor zone the fibres are washed out of the rejects after water has been added and in a fourth zone the rejects are dehydrated.
Description
~7~
APPARATUS FOR SORTING AND DEFLAKING FIBROUS SUSPENSIONS
The invention relates to an apparatus for sorting and deflaking fibrous suspensions and, in particular, a so-called pressureless sorter for heavily soiled fibrous suspensions such as those resulting as rejected material from the most varied sorting systems.
Known open sorting apparatuses, such as, for example, vibratlon sorters often used as the final stage in a multistage sorting system, do not generally lead to a rejected material which is dewatered to any great extent and result, in addition, in relatively high losses of usable fibers remaining in the rejected material. The high costs connected with the storage of the rejected material, above all the requirement of a high dry content of the rejected material, often necessitate the purchase of additional apparatus, such as piston-type presses and worm compressors, to further dewater the re;ected material in a paper mill .
E~nown sorting apparatuses comprising a rotor are, however, subject to considerable wear and tear when processing heavily soiled fibrous suspensions, insofar as an apparatus for separating out dirt particles having a heavy specific weight is not connected to their inlet sides. These dirt particles having a heavy specific weight do have an extremely abrasive effect in these apparatuses between rotor and screen.
The object underlying the invention was therefore to provide a sorting apparatus which is also suitable for processing heavily soiled fibrous suspensions and fulfills the requirement for a r,e~ected material which has a high dry content and is as free of f;ibers as possible.
A sorting apparatus, in which the fiber content of the fibrous suspension to be processed is reduced and which is intended to result in a rejected material having a relatively high dry content, is known from EP-0 235 605~A2. this sorting apparatus has a housing surrounding a rotor with a horizontal axis, the housing having a housing portion on the inlet side with a larger di.ameter and a housing portion on the outlet side with a smaller diameter. In the housing portion on the inlet side the rotor comprises a first rotor region which is designed as an impeller having a relatively large diameter and is intended to effect de!flaking, whereas a second rotor reglon located in the housing portion at the outlet side is designed as a cylinder having a cc,nsiderably smaller diameter and is surrounded by a cylindrical screen, through which the accepted material and the majority of the water pass in order to provide a relatively dry rejected material. A screen plate is located on the side of the impeller opposite the housing portion on the outlet side having a smaller diameter and at a very slight axial distance from the impeller, and is followed by an accepted material chamber provided with an accepted material outlet. If this known apparatus is used for processing fibrous suspensions recovered from mixed waste paper, it is intended to be utilized for the last stage of the sorting process. If it were to form the first stage of the sorting process, the dirt particles, such as sand and metal parts, contained in the fibrous suspension would quickly lead to wear and tear on the impeller, the screen plate, the vanes arranged `~ 2 7 at the periphery of the second rotor region and the cylindrical screen surrounding the second rotor region.
DE-26 11 886-8 of the applicant discloses an apparatus for sorting and deflaking fibrous suspensions, which comprises a housing surrounding a rotor arranged with its axis horizontal, the housing having in a front housing end region an inlet for th,e fibrous suspension to be processed, in a central region at the bottom an accepted material outlet for the sorted fibrous suspension and in a rear housing end region at the bottom a rejected material outlet. The rotor has the form of a hollow, approximately drum-shaped, rotationally symmetrical body and comprises three regions arranged one behind the other in the dLrection of the rotor axis, namely a first rotor region on the inlet side, a central, second rotor region and a third rotor rlgion on the outlet side. Web-like accelerator strips are attached at the rotor periphery in the first and third rotor r,eglons to accelerate the fibrous suspension in the circumferential direction while the second rotor region is provided at the perlphery with ribs extending in axial direction, these ribs being designed such that they develop a deflaking effect together with a screen cylinder encircling the rotor at a slight radial distance. Together with this screen cylinder, the first rotor region effects a dewatering of the fibrous suspension while, at the same time, accepted material is separated out. In other words, the first rotor region is a sorting and dewatering region, the second rotor region brings a,bout, as already mentioned, a deflaking of the fibrous suspenslon, and in the annular space between third rotor region and screen cylinder usable fibers are washed out of the rejected material and sorted, for which purpose a supply of diluting water ls directed from outside in radial direction onto the 2~ F;~U é
screen cylinder. Behind the rotor the rejected material leaves the apparatus housing through the rejected material outlet already mentioned.
When a fibrous suspension recovered from mixed waste paper is sorted and deflaked with this known apparatus, sand, metal particles and the like result in considerable wear and tear on the screen cylinder and on the accelerator and deflaking ribs attached at the rotor periphery. In addition, this known apparatus supplies an undesirably thin rejected material because in the third rotor region the still usable fibers are washed out of the rejected material by diluting water. The aforementioned object cannot, therefore, be accomplished with this known apparatus.
Proceeding on the basis of an apparatus of the generic type, such as that disclosed in DE-26 11 886-8, i.e. an apparatus for sorting and deflaking fibrous suspensions, comprising a housing whlch has in a front housing end region an inlet for the fibrous suspension to be processed, in addition an accepted material outlet for the sorted fibrous suspension as well as a rejected material outlet, and in which a rotor having a horizontal axis is mounted for rotation, this rotor having a plurality of regions disposed one after the other in the direction of the rotor axis and being surrounded by annular chambers having different functions, of these regions a first rotor region on the inlet side and a last rotor region facing the rejected material outlet arranged at a rear housing end region being provided at their periphery with take-along elements for the fibrous suspension, the last rotor region being surrounded by an annular screen, and a deflaking rotor region located upstream of the last rotor region having elevations for effecting deflaking, wherein an additional rotor region surrounded by an 2'at~ v 'I g annular screen is located between said first and said last rotor regions, the object underlying the invention may be accomplished in that the first rotor region is surrounded by an annular housing wall, an outlet for particles of dirt having a heavy specific weight opening into this wall from below, and that the last rotor region is designed as a rejected material thickening region and the additional rotor region is designed as a sorting region. Since, in the inventive apparatus, no screen surrounding the first rotor region has to be provided but rather embodiments are preferred, in which the first rotor region is surrounded by the housing wall which is closed apart from the inlet arranged in the top for the fibrous suspension to be processed and the opening of the outlet for heavy dirt, the dirt particles having a heavy specific weight are, in the inventive apparatus, centrifuged out of the f'ibrous suspension before they can lead to wear and tear on a screen and the rotor parts surrounded by the screen. the fibrous suspension, which is set to rotate quickly by the rotor, catapults the heavy dirt particles against the housing wall where they slide down along this wall and reach the outlet for the dirt particles having a heavy specific weight. Only then is the fibrous suspension deflaked and sorted in the inventive apparatus. It is hereby considered to be a particular advantage for the processes of sorting and thickening not to occur in the same region of the apparatus because in the sorting region, namely, the screen is appropriately acted upon by wash water to clean the screen and wash out usable fibers whereas in the inventive apparatus the rejected material thickening region need not have any wash water supply device.
In an apparatus of a different generic type for sorting and washing out a fibrous suspension as well as thickening the rejected material (DE-28 50 385-~), a rotor having a more or less horizontal axis is surrounded over its entire length by a screen cylinder. At one end of the apparatus housing which also has a more or less horizontal axis and is approximately cylindrical in design, an inlet for the fibrous suspension to be processed is provided. An outlet for the accepted material is located outside the screen cylinder and at the other end of the apparatus housing a reiected material outlet is provided. A
first rotor region on the inlet side is provided with accelerator vanes for the fibrous suspension, a second rotor region with transporting vanes conveying the fibrous suspension in an axial direction and a third rotor region with centrifugal vanes arranged at the rotor periphery. The first rotor region serves to sort the fibrous suspension, the second to wash out the fibrous suspension (by means of wash water outlet openings provided in the rotor casing), and in the third rotor region the rejected material is dewatered. This known apparatus is of a different generic type since it does not relate to a deflaking apparatus. In addition, it does not accomplish the present object since it does not contain any means for removing dirt particles having a heavy specific weight before the fibrous suspension enters an annular space between a rotor and a screen.
A further apparatus of a different generic type (DE-38 20 366-A), in which the fibrous suspension is also not deflaked, relates to an apparatus for sorting cellular material which has an approximately circular-cylindrical housing with a horizontal axis and a rotor arranged concentrically to the housing. The fibrous suspension to be processed is introduced paraxially into the apparatus at one housing end, namely into a chamber formed by the housing wall which is closed around its circumference. A first rotor region designed as a toothed wheel is located in this chamber and followed by a second, circular-cylindrical rotor region which forms, directly behind the toothed wheel, a narrow annular gap with a housing partition wall, the external diameter of the gap being smaller than the external diameter of the toothed wheel. Rib-like vanes extending in axial direction are placed on the second rotor region. A first area of said second rotor region on the inlet side is surrounded by a region of the housing wall designed as a screen so that the fibrous suspension is sorted in this region whereas a second area of the second rotor region remote from the apparatus inlet is surrounded by a closed area of the housing wall into which a rejected material outlet opens from above. In the region of the screen, a diluting water connection leads through the screen. The toothed wheel is intended to be designed such that undesired solid dirt particles are hit by the toothed wheel and catapulted back in a radial direction towards the outside as well as in the direction towards the apparatus inlet in order to prevent the dirt particles from entering the annular gap located behind the toothed wheel. However, DE-38 20 366-A expressly points out that the major portlon of the impurities occurring in the fibrous suspension passes through the apparatus and leaves the apparatus with the re;ected material. In addition, this known apparatus has no rejected material thickening region. To summarize, it can be said that it is inconceivable to process fibrous suspensions recovered from very dirty, mixed waste paper with this known apparatus.
It is obvious that the different rotor regions need not necessarily be formed by one and the same rotor. In addition, a further rotor region may be located in front of the first rotor region, e.g. one without take-along elements for the fibrous suspension.
the inventive apparatus is expediently designed such that al l the rotor regions are formed by a single, drum-shaped rotor and all the screens by a rotationally symmetrical screen basset. In this connection it should be mentioned that DE-AS 26 11 886 of the applicant discloses an apparatus for sorting, deflaking and re-screening a fibrous suspension which comprises a drum-shaped rotor arranged with its axis horizontal in a housing including a circular-cylindrical screen. One end of the housing is provided with an inlet for the fibrous suspension to be processed, the other end with a rejected material outlet and, inbetween, the housing has an accepted material outlet in the bottom and at the top, next to the rejected material outlet, a diluting water connection. The rotor is provided at its periphery in first and third rotor regions adjacent the inlet and rejected material outlet, respectively, with strip-like take-along elements for the fibrous suspension, these elements extending parallel to the rotor axis, and in a second rotor region arranged between the first and third rotor regions it bears at its periphery a gear-type collar, the teeth of which effect deflaking of the fibrous suspension. In this known apparatus, therefore, all the dirt particles, including those having a heavy specific weight which cause a considerable amount of wear and tear, pass between the rotor and the screen cylinder and the re;ected material leaving the apparatus comprises a relatively large amount of water as a result of the diluting water inlet in the region of the third rotor region.
In a preferred embodiment of the inventive apparatus, a rotor region designed as a fiber washing out region is provided between the sorting region and the rejected material thickening region, this washing out region being surrounded by an annular screen and having associated with it a washing water inlet directed against the rotor. In this region, the usable fibers ''-- 2~
are washed out of the deflaked fibrous suspension and pass through the screen surrounding this rotor region as accepted material and so the rejected material leaving the apparatus is, for the most part, free of fibers.
Since the inventive apparatus is preferably a pressureless sorting apparatus, it is recommended that the rotor be provided at its periphery in the sorting region and the fiber washing out region, respectively, with take-along elements for the fibrous suspension which force the latter against the respective screen. If these take-along elements are designed to have sharp edges they also result in a deflaking effect, and in the fiber washing out region they promote the distribution of the washing water and the washing out of the usable fibers from the rejected material. ' . .
The take-along elements are particularly effective when they are designed as webs or sheets projecting in the manner of vanes from the rotor periphery.
Since the process of deflaking or defibering undissolved conglomerates of fibers essentially takes place between the elevations at the rotor periphery and the edges of the screen apertures and is attributable to an impact and shearing force on the fiber conglomerates, the deflaking effect is essentially dependent on the radial distance of the elevations and webs, respectively, from the respective screen. In preferred embodiments of the inventive apparatus, the radial distance of the webs from the respective screen is approximately 1/2 to approximately 5 mm and preferably 1/2 to approximately 1 mm.
Particularly advantageous embodiments are those in which the webs are adjustable in their height relative to the rotor periphery.
2~2 7~
In order to separate out the dirt particles having a heavy specific weight with the lowest possible energy requirements -the fibrous suspension to be processed flows into the apparatus housing at a certain geodetic water column height, which is, in particular 1 to 4 m WS (= water gage) -, the apparatus inlet for the fibrous suspension to be processed is, in an advantageous embodiment, aligned approximately tangentially and the rotor is drivable in the direction of the inlet flow so that the inlet flow already leads to a rotatory flow of the fibrous suspension between rotor and housing wall. When the take-along elements of the first rotor region and the annular space following the latter between the sorting region and the screen surrounding this sorting region are designed and arranged accordingly, it is possible in accordance with the invention for dirt particles having a heavy specific weight to essenti,ally not come into contact with the take-along elements of the first rotor region and for the fibrous suspension to be able to enter the specified annular space essentially unhindered, additional features which distinguish the inventive apparatus quite appreciably from the known apparatus of a different generic type according to DE-38 20 366-A.
In principle, it would be conceivable to surround the rotor region effecting deflaking with a closed wall, which comprises, for example, pro;ections promoting the deflaking process. In view of the deflaking mechanism described above, preferred embodiments of the inventive apparatus have an annular screen surrounding the deflaking rotor region so that deflaking and sorting can take place in the same region.
Slnce fleece-like fiber collections can form on the feed side of the screens if no special measures are take, and these collections hinder the sorting effect, it is recommended that the take-along elements arranged at the rotor rotate as close as possible to the pertinent screen. An additional measure for preventing clogging of the screen apertures is to associate washing water inlets with the screen of the sorting region for cleaning the screen apertures.
The different screens can have screen apertures of the same size and shape. It is, however, more advantageous for the screen of the sorting region to be provided with finer screen apertures than the screen of the fiber washiny out region so that, on the one hand, an accepted material having as high a quality as possible is first obtained and, on the other hand, all the usable fibers are, as far as possible, passed through the screen in the washing out region. Finally, when it comes to thickening the rejected material, i.e. withdrawing only waxer thérefrom, flner screen apertures can again be used so that, ln a preferred embodiment, the screen of the rejected material thickening region has finer screen apertures than the screen of the washing out region.
The length of time the fibrous suspension to be processed remains in the various regions of the apparatus depends on the quantity supplied per time unit, the amounts of washing water supplied per time unit, the inclination of the webs relative to the rotor axis and the speed of rotation of the rotor. For this reason it is recommended that the webs be constructed so as to be adjustable in their inclination relative to a generatrix of the rotor periphery. S1nce, in the first rotor region, the centrifugal effect achieved is intended to be as great as possible and the fibrous suspension located in this region is displaced anyway by the fresh fibrous suspension flowing in behind it, it is recommended that the webs in the first rotor region extend approximately parallel to the generatrices of the rotor periphery whereas the webs in the rotor regions following this first rotor region can be inclined relative to the generatrices ox the rotor periphery such that they result in a conveying effect in the direction towards the rear housing end.
In order to remove the rejected material, which is as dry as possible, from the region between rotor and last screening region, a preferred embodiment of the inventive apparatus has the webs of the last rotor region projecting beyond its screen rearwardly into a rejected material chamber formed by the housing so that the rejected material is catapulted from the rotor into this chamber.
Additional features, advantages and details of the invention result from the attached drawings and the following description of a particularly favourable embodiment of the invention apparatus; in the drawings:
Figure 1 is an axial section through the apparatus;
Figure 2 is a section along line 2-2 in Figure l;
Figure 3 is a section along line 3-3 in Figure 1;
Flgure 4 is a section through part of the rotor, namely a section at right angles to the rotor axis, and Figure 5 is a plan view onto part of the rotor periphery.
Figure 1 shows a housing mounted on a frame 10 and designated as a whole as 12. This housing has an outer housing casing l and is closed by an end wall 16 to the left according to Figure 1.
A right-hand end wall 18 has an opening 22 concentric to an axis l t.J J ,~ L1 20-and bears a rejected material box 24 which has at the bottom an exit opening 26 for the rejected material.
The frame 10 also bears a drive motor 28 and a bearing body 30, in which a rotor shaft 32 is rotatably mounted. This is concentric to the apparatus axis 20, bears a belt pulley 34 and is caused to rotate via this, drive belt 36 and a belt pulley 38 of the motor 28, and in a counter-clockwise direction according to Figures 2 and 3. A hollow, circular-cylindrical rotor 40 is attached to the rstor shaft 32. At its ends this rotor is closed by end walls 42 and 44 and it has a casing 46, on which a total of 4 sets of vanes 501, 502, 503 and 504 are attached, these vanes serving to take along, i.e. accelerate in a rotatory manner, the fibrous suspension to be processed. These sets of vanes 501 to 504 are associated with 4 regions I, II, III, IV of the apparatus or rather the rotor 40, namely - according to Figure 1 from left to right - a heavy component separating region I, a sorting and deflaking region II, a washing out region III and a dewatering region IV. In this respect, vanes of the set of vanes 50 of the sorting and deflaking region II
which are adjacent one another in the circumferential direction are offset relative to one another in axial direction due to their axial length, as is apparent from Figure l.
A tangentially oriented inlet pipe 54 for the fibrous suspension to be processed opens into the housing 12 in the heavy component separating region I; in accordance with the invention this inlet pipe is arranged on top of the housing. In the region I the rotor 40 is enclosed only by the outer housing casing 14, into the bottom of whlch a vertically oriented outlet pipe 56 for dirt particles having a heavy specific weight opens. This is followed by a heavy component container 58, to which a diluting water line 60 is connected. Valves closing the heavy component container 58 at the top and bottom are designated 62 and 64, a valve for the dilutlng water line 60 has been designated 66.
Along the regions II, III and IV the housing 12 accommodates a circular-cylindrical screen cylinder 68, the screen apertures of which are finer in the sorting and deflaking region II and in the dewatering region IV than in the washing out region III. As illustrated in Figures l and 3, washing water channels 70 are attached to the outside of the screen cylinder 68, these channels being supplied via a washing water conduit 74 provided with a valve 72. The screen cylinder 68 does not have any screen apertures beneath the washing water channels 70 extending in the direction of the apparatus axis 20 but only spray openings 76 at certain points, according to the invention only rin the sorting and deflaking region II as well as~in the washing out region III, whereas no washing water is supplied to the dewatering region IV.
An accepted material chamber 78 limited by the screen cylinder 68 and the outer housing casing 14 is, according to Figure 1, closed on the right by the end wall 18 and on the left by a circular housing web 80; an accepted material outlet pipe 82 opens into the accepted material chamber 78 from below.
According to the invention, measures are taken to ensure that the rejected material conveyed to the rejected material box 24 cannot conglomerate but leaves the rejected material box at the bottom through its exit openings 26. For this purpose, the vanes 504 of the rotor 40 project somewhat into the rejected material box 24, a guiding wall 86 in the shape of a half shell is associated with the lower region of the rotor 40 in the rejected material box 24 and at the top, adjacent the rotor, a baffle 88 is arranged in the rejected material box and this has - lS -the effect that the rejected material catapulted upwards is, according to Figure 1, reflected towards the bottom right and therefore falls downwards into the exit opening 26 to the right of the guiding wall 86.
The fibrous suspension flowing into the apparatus via the inlet pipe 54 is caught by the vanes 501 attached to the rotor in the heavy component separating region I and catapulted against the outer housing casing 14. The dirt particles in the fibrous suspension having a heavy specific weight slide downwards along the outer housing casing 14 due to the force of gravity; at the lowest point of the housing 12 they pass into the heavy component container 58 via the outlet pipe 56. A thickening of the rejected material in the heavy component container 58 is avoided by a counterwashing via the diluting water line 60.
In the heavy component separating region I the fibrous suspension to be processed is, therefore, freed of dirt particies having a heavy specific weight, such as metal parts and the like, before it enters the annular space between the rotor 40 and the screen cylinder 68.
In the sorting and deflaking region II the fibrous suspension is caught by the vanes 502 and catapulted against the perforated screen cylinder 68, the screen apertures of which allow the accepted material, i.e. the fine fraction formed of usable fibers and water, to pass whereas the dirt is retained in the annular space between rotor and screen cylinder. The accepted material leaves the accepted material chamber 78 via the accepted material outlet pipe 82.
Due to the inventive design of the vanes 502 with sharp edges fibers, i.e. fiber conglomerates, contained in the fibrous 2`~ ,7 suspension are broken up; a sllghtest possible distance between the vanes 502 and the screen cylinder 68 has the same effect, whereby an additional advantage is also obtained: The fibers tend to form a fiber fleece on the inner inflow side of the screen cylinder 68 and this would hinder the flow of the accepted materlal through the screen cylinder. The fact that the vanes 502 rotate at such a slight distance from the screen cylinder 68 prevents the formation of such a fiber fleece or removes any fiber fleece in the process of formation.
As is apparent from Figure 4, the effective height of the vanes may be adjusted or precluded, e.g. by the washers 90 illustrated in Flgure 4. The same applies for the other vanes.
This can influence the intensity of the deflaking operation effected~by the vanes 50 and which is performed between the vane edges and the edges of the screen apertures by impact and shearing effects.
As indicated in Figure 5, the inclination of the vanes relative to the apparatus axis 20 or the generatrix of the rotor 40 may be adjusted. In this way, the fibrous suspension or the dirt can be transported more quickly or more slowly through the annular space between rotor 40 and screen cylinder 68 to the end of the screen cylinder to the right according to Figure 1. In the heavy component separating region I the vanes 501 are preferably axially arranged, i.e. without any angular pitch, since the axial transport of the fibrous suspension in the direct$on of the rejected material box 24 is effected by the fibrous suspension flowing in behind.
The screen cylinder apertures are cleaned, inter alia, by the washing water supplied via the washing water channels 70 and the spray openings 76.
Since the major portion of the individual fibers suspended in the water has passed through the screen cylinder apertures, the rejected material in the washing out region II is supplied with an increased amount of washing water in order to wash the usable fibers still contained in the rejected material off the dirt and then centrifuge them out of the annular space between rotor and screen cylinder by means of the vanes 503. In the inventive apparatus the washing out process is particularly intensive since the jets of water entering the annular space between screen cylinder 68 and rotor 40 strike the rotor casing 46, are then reflected and thereby spray apart. In addition, the washing and diluting water is well distributed by the rotating vanes 503. These vanes 503 are, with respect to their angle, mounted on the rotor in accordance with the desired holding time in the washing out-re~ion III.~
the rejected material remaining in the annular space between rotor 40 and screen cylinder 68 is now freed of the adherent water in the dewatering region IV by means of centrifugation with the aid of the vanes 504. the vanes 504 are, according to the invention, formed of one piece over the entire length of the dewatering region IV.
The dewatered rejected material leaves the apparatus via the exit opening 26 of the rejected material box 24.
If the fibrous suspension or the rejected material are intended to remain a particularly long time in a particular region, despite the f$brous suspension flowing in behind, the vanes in this region are negatively pitched, i.e. such that they act in the sense of a return effect.
APPARATUS FOR SORTING AND DEFLAKING FIBROUS SUSPENSIONS
The invention relates to an apparatus for sorting and deflaking fibrous suspensions and, in particular, a so-called pressureless sorter for heavily soiled fibrous suspensions such as those resulting as rejected material from the most varied sorting systems.
Known open sorting apparatuses, such as, for example, vibratlon sorters often used as the final stage in a multistage sorting system, do not generally lead to a rejected material which is dewatered to any great extent and result, in addition, in relatively high losses of usable fibers remaining in the rejected material. The high costs connected with the storage of the rejected material, above all the requirement of a high dry content of the rejected material, often necessitate the purchase of additional apparatus, such as piston-type presses and worm compressors, to further dewater the re;ected material in a paper mill .
E~nown sorting apparatuses comprising a rotor are, however, subject to considerable wear and tear when processing heavily soiled fibrous suspensions, insofar as an apparatus for separating out dirt particles having a heavy specific weight is not connected to their inlet sides. These dirt particles having a heavy specific weight do have an extremely abrasive effect in these apparatuses between rotor and screen.
The object underlying the invention was therefore to provide a sorting apparatus which is also suitable for processing heavily soiled fibrous suspensions and fulfills the requirement for a r,e~ected material which has a high dry content and is as free of f;ibers as possible.
A sorting apparatus, in which the fiber content of the fibrous suspension to be processed is reduced and which is intended to result in a rejected material having a relatively high dry content, is known from EP-0 235 605~A2. this sorting apparatus has a housing surrounding a rotor with a horizontal axis, the housing having a housing portion on the inlet side with a larger di.ameter and a housing portion on the outlet side with a smaller diameter. In the housing portion on the inlet side the rotor comprises a first rotor region which is designed as an impeller having a relatively large diameter and is intended to effect de!flaking, whereas a second rotor reglon located in the housing portion at the outlet side is designed as a cylinder having a cc,nsiderably smaller diameter and is surrounded by a cylindrical screen, through which the accepted material and the majority of the water pass in order to provide a relatively dry rejected material. A screen plate is located on the side of the impeller opposite the housing portion on the outlet side having a smaller diameter and at a very slight axial distance from the impeller, and is followed by an accepted material chamber provided with an accepted material outlet. If this known apparatus is used for processing fibrous suspensions recovered from mixed waste paper, it is intended to be utilized for the last stage of the sorting process. If it were to form the first stage of the sorting process, the dirt particles, such as sand and metal parts, contained in the fibrous suspension would quickly lead to wear and tear on the impeller, the screen plate, the vanes arranged `~ 2 7 at the periphery of the second rotor region and the cylindrical screen surrounding the second rotor region.
DE-26 11 886-8 of the applicant discloses an apparatus for sorting and deflaking fibrous suspensions, which comprises a housing surrounding a rotor arranged with its axis horizontal, the housing having in a front housing end region an inlet for th,e fibrous suspension to be processed, in a central region at the bottom an accepted material outlet for the sorted fibrous suspension and in a rear housing end region at the bottom a rejected material outlet. The rotor has the form of a hollow, approximately drum-shaped, rotationally symmetrical body and comprises three regions arranged one behind the other in the dLrection of the rotor axis, namely a first rotor region on the inlet side, a central, second rotor region and a third rotor rlgion on the outlet side. Web-like accelerator strips are attached at the rotor periphery in the first and third rotor r,eglons to accelerate the fibrous suspension in the circumferential direction while the second rotor region is provided at the perlphery with ribs extending in axial direction, these ribs being designed such that they develop a deflaking effect together with a screen cylinder encircling the rotor at a slight radial distance. Together with this screen cylinder, the first rotor region effects a dewatering of the fibrous suspension while, at the same time, accepted material is separated out. In other words, the first rotor region is a sorting and dewatering region, the second rotor region brings a,bout, as already mentioned, a deflaking of the fibrous suspenslon, and in the annular space between third rotor region and screen cylinder usable fibers are washed out of the rejected material and sorted, for which purpose a supply of diluting water ls directed from outside in radial direction onto the 2~ F;~U é
screen cylinder. Behind the rotor the rejected material leaves the apparatus housing through the rejected material outlet already mentioned.
When a fibrous suspension recovered from mixed waste paper is sorted and deflaked with this known apparatus, sand, metal particles and the like result in considerable wear and tear on the screen cylinder and on the accelerator and deflaking ribs attached at the rotor periphery. In addition, this known apparatus supplies an undesirably thin rejected material because in the third rotor region the still usable fibers are washed out of the rejected material by diluting water. The aforementioned object cannot, therefore, be accomplished with this known apparatus.
Proceeding on the basis of an apparatus of the generic type, such as that disclosed in DE-26 11 886-8, i.e. an apparatus for sorting and deflaking fibrous suspensions, comprising a housing whlch has in a front housing end region an inlet for the fibrous suspension to be processed, in addition an accepted material outlet for the sorted fibrous suspension as well as a rejected material outlet, and in which a rotor having a horizontal axis is mounted for rotation, this rotor having a plurality of regions disposed one after the other in the direction of the rotor axis and being surrounded by annular chambers having different functions, of these regions a first rotor region on the inlet side and a last rotor region facing the rejected material outlet arranged at a rear housing end region being provided at their periphery with take-along elements for the fibrous suspension, the last rotor region being surrounded by an annular screen, and a deflaking rotor region located upstream of the last rotor region having elevations for effecting deflaking, wherein an additional rotor region surrounded by an 2'at~ v 'I g annular screen is located between said first and said last rotor regions, the object underlying the invention may be accomplished in that the first rotor region is surrounded by an annular housing wall, an outlet for particles of dirt having a heavy specific weight opening into this wall from below, and that the last rotor region is designed as a rejected material thickening region and the additional rotor region is designed as a sorting region. Since, in the inventive apparatus, no screen surrounding the first rotor region has to be provided but rather embodiments are preferred, in which the first rotor region is surrounded by the housing wall which is closed apart from the inlet arranged in the top for the fibrous suspension to be processed and the opening of the outlet for heavy dirt, the dirt particles having a heavy specific weight are, in the inventive apparatus, centrifuged out of the f'ibrous suspension before they can lead to wear and tear on a screen and the rotor parts surrounded by the screen. the fibrous suspension, which is set to rotate quickly by the rotor, catapults the heavy dirt particles against the housing wall where they slide down along this wall and reach the outlet for the dirt particles having a heavy specific weight. Only then is the fibrous suspension deflaked and sorted in the inventive apparatus. It is hereby considered to be a particular advantage for the processes of sorting and thickening not to occur in the same region of the apparatus because in the sorting region, namely, the screen is appropriately acted upon by wash water to clean the screen and wash out usable fibers whereas in the inventive apparatus the rejected material thickening region need not have any wash water supply device.
In an apparatus of a different generic type for sorting and washing out a fibrous suspension as well as thickening the rejected material (DE-28 50 385-~), a rotor having a more or less horizontal axis is surrounded over its entire length by a screen cylinder. At one end of the apparatus housing which also has a more or less horizontal axis and is approximately cylindrical in design, an inlet for the fibrous suspension to be processed is provided. An outlet for the accepted material is located outside the screen cylinder and at the other end of the apparatus housing a reiected material outlet is provided. A
first rotor region on the inlet side is provided with accelerator vanes for the fibrous suspension, a second rotor region with transporting vanes conveying the fibrous suspension in an axial direction and a third rotor region with centrifugal vanes arranged at the rotor periphery. The first rotor region serves to sort the fibrous suspension, the second to wash out the fibrous suspension (by means of wash water outlet openings provided in the rotor casing), and in the third rotor region the rejected material is dewatered. This known apparatus is of a different generic type since it does not relate to a deflaking apparatus. In addition, it does not accomplish the present object since it does not contain any means for removing dirt particles having a heavy specific weight before the fibrous suspension enters an annular space between a rotor and a screen.
A further apparatus of a different generic type (DE-38 20 366-A), in which the fibrous suspension is also not deflaked, relates to an apparatus for sorting cellular material which has an approximately circular-cylindrical housing with a horizontal axis and a rotor arranged concentrically to the housing. The fibrous suspension to be processed is introduced paraxially into the apparatus at one housing end, namely into a chamber formed by the housing wall which is closed around its circumference. A first rotor region designed as a toothed wheel is located in this chamber and followed by a second, circular-cylindrical rotor region which forms, directly behind the toothed wheel, a narrow annular gap with a housing partition wall, the external diameter of the gap being smaller than the external diameter of the toothed wheel. Rib-like vanes extending in axial direction are placed on the second rotor region. A first area of said second rotor region on the inlet side is surrounded by a region of the housing wall designed as a screen so that the fibrous suspension is sorted in this region whereas a second area of the second rotor region remote from the apparatus inlet is surrounded by a closed area of the housing wall into which a rejected material outlet opens from above. In the region of the screen, a diluting water connection leads through the screen. The toothed wheel is intended to be designed such that undesired solid dirt particles are hit by the toothed wheel and catapulted back in a radial direction towards the outside as well as in the direction towards the apparatus inlet in order to prevent the dirt particles from entering the annular gap located behind the toothed wheel. However, DE-38 20 366-A expressly points out that the major portlon of the impurities occurring in the fibrous suspension passes through the apparatus and leaves the apparatus with the re;ected material. In addition, this known apparatus has no rejected material thickening region. To summarize, it can be said that it is inconceivable to process fibrous suspensions recovered from very dirty, mixed waste paper with this known apparatus.
It is obvious that the different rotor regions need not necessarily be formed by one and the same rotor. In addition, a further rotor region may be located in front of the first rotor region, e.g. one without take-along elements for the fibrous suspension.
the inventive apparatus is expediently designed such that al l the rotor regions are formed by a single, drum-shaped rotor and all the screens by a rotationally symmetrical screen basset. In this connection it should be mentioned that DE-AS 26 11 886 of the applicant discloses an apparatus for sorting, deflaking and re-screening a fibrous suspension which comprises a drum-shaped rotor arranged with its axis horizontal in a housing including a circular-cylindrical screen. One end of the housing is provided with an inlet for the fibrous suspension to be processed, the other end with a rejected material outlet and, inbetween, the housing has an accepted material outlet in the bottom and at the top, next to the rejected material outlet, a diluting water connection. The rotor is provided at its periphery in first and third rotor regions adjacent the inlet and rejected material outlet, respectively, with strip-like take-along elements for the fibrous suspension, these elements extending parallel to the rotor axis, and in a second rotor region arranged between the first and third rotor regions it bears at its periphery a gear-type collar, the teeth of which effect deflaking of the fibrous suspension. In this known apparatus, therefore, all the dirt particles, including those having a heavy specific weight which cause a considerable amount of wear and tear, pass between the rotor and the screen cylinder and the re;ected material leaving the apparatus comprises a relatively large amount of water as a result of the diluting water inlet in the region of the third rotor region.
In a preferred embodiment of the inventive apparatus, a rotor region designed as a fiber washing out region is provided between the sorting region and the rejected material thickening region, this washing out region being surrounded by an annular screen and having associated with it a washing water inlet directed against the rotor. In this region, the usable fibers ''-- 2~
are washed out of the deflaked fibrous suspension and pass through the screen surrounding this rotor region as accepted material and so the rejected material leaving the apparatus is, for the most part, free of fibers.
Since the inventive apparatus is preferably a pressureless sorting apparatus, it is recommended that the rotor be provided at its periphery in the sorting region and the fiber washing out region, respectively, with take-along elements for the fibrous suspension which force the latter against the respective screen. If these take-along elements are designed to have sharp edges they also result in a deflaking effect, and in the fiber washing out region they promote the distribution of the washing water and the washing out of the usable fibers from the rejected material. ' . .
The take-along elements are particularly effective when they are designed as webs or sheets projecting in the manner of vanes from the rotor periphery.
Since the process of deflaking or defibering undissolved conglomerates of fibers essentially takes place between the elevations at the rotor periphery and the edges of the screen apertures and is attributable to an impact and shearing force on the fiber conglomerates, the deflaking effect is essentially dependent on the radial distance of the elevations and webs, respectively, from the respective screen. In preferred embodiments of the inventive apparatus, the radial distance of the webs from the respective screen is approximately 1/2 to approximately 5 mm and preferably 1/2 to approximately 1 mm.
Particularly advantageous embodiments are those in which the webs are adjustable in their height relative to the rotor periphery.
2~2 7~
In order to separate out the dirt particles having a heavy specific weight with the lowest possible energy requirements -the fibrous suspension to be processed flows into the apparatus housing at a certain geodetic water column height, which is, in particular 1 to 4 m WS (= water gage) -, the apparatus inlet for the fibrous suspension to be processed is, in an advantageous embodiment, aligned approximately tangentially and the rotor is drivable in the direction of the inlet flow so that the inlet flow already leads to a rotatory flow of the fibrous suspension between rotor and housing wall. When the take-along elements of the first rotor region and the annular space following the latter between the sorting region and the screen surrounding this sorting region are designed and arranged accordingly, it is possible in accordance with the invention for dirt particles having a heavy specific weight to essenti,ally not come into contact with the take-along elements of the first rotor region and for the fibrous suspension to be able to enter the specified annular space essentially unhindered, additional features which distinguish the inventive apparatus quite appreciably from the known apparatus of a different generic type according to DE-38 20 366-A.
In principle, it would be conceivable to surround the rotor region effecting deflaking with a closed wall, which comprises, for example, pro;ections promoting the deflaking process. In view of the deflaking mechanism described above, preferred embodiments of the inventive apparatus have an annular screen surrounding the deflaking rotor region so that deflaking and sorting can take place in the same region.
Slnce fleece-like fiber collections can form on the feed side of the screens if no special measures are take, and these collections hinder the sorting effect, it is recommended that the take-along elements arranged at the rotor rotate as close as possible to the pertinent screen. An additional measure for preventing clogging of the screen apertures is to associate washing water inlets with the screen of the sorting region for cleaning the screen apertures.
The different screens can have screen apertures of the same size and shape. It is, however, more advantageous for the screen of the sorting region to be provided with finer screen apertures than the screen of the fiber washiny out region so that, on the one hand, an accepted material having as high a quality as possible is first obtained and, on the other hand, all the usable fibers are, as far as possible, passed through the screen in the washing out region. Finally, when it comes to thickening the rejected material, i.e. withdrawing only waxer thérefrom, flner screen apertures can again be used so that, ln a preferred embodiment, the screen of the rejected material thickening region has finer screen apertures than the screen of the washing out region.
The length of time the fibrous suspension to be processed remains in the various regions of the apparatus depends on the quantity supplied per time unit, the amounts of washing water supplied per time unit, the inclination of the webs relative to the rotor axis and the speed of rotation of the rotor. For this reason it is recommended that the webs be constructed so as to be adjustable in their inclination relative to a generatrix of the rotor periphery. S1nce, in the first rotor region, the centrifugal effect achieved is intended to be as great as possible and the fibrous suspension located in this region is displaced anyway by the fresh fibrous suspension flowing in behind it, it is recommended that the webs in the first rotor region extend approximately parallel to the generatrices of the rotor periphery whereas the webs in the rotor regions following this first rotor region can be inclined relative to the generatrices ox the rotor periphery such that they result in a conveying effect in the direction towards the rear housing end.
In order to remove the rejected material, which is as dry as possible, from the region between rotor and last screening region, a preferred embodiment of the inventive apparatus has the webs of the last rotor region projecting beyond its screen rearwardly into a rejected material chamber formed by the housing so that the rejected material is catapulted from the rotor into this chamber.
Additional features, advantages and details of the invention result from the attached drawings and the following description of a particularly favourable embodiment of the invention apparatus; in the drawings:
Figure 1 is an axial section through the apparatus;
Figure 2 is a section along line 2-2 in Figure l;
Figure 3 is a section along line 3-3 in Figure 1;
Flgure 4 is a section through part of the rotor, namely a section at right angles to the rotor axis, and Figure 5 is a plan view onto part of the rotor periphery.
Figure 1 shows a housing mounted on a frame 10 and designated as a whole as 12. This housing has an outer housing casing l and is closed by an end wall 16 to the left according to Figure 1.
A right-hand end wall 18 has an opening 22 concentric to an axis l t.J J ,~ L1 20-and bears a rejected material box 24 which has at the bottom an exit opening 26 for the rejected material.
The frame 10 also bears a drive motor 28 and a bearing body 30, in which a rotor shaft 32 is rotatably mounted. This is concentric to the apparatus axis 20, bears a belt pulley 34 and is caused to rotate via this, drive belt 36 and a belt pulley 38 of the motor 28, and in a counter-clockwise direction according to Figures 2 and 3. A hollow, circular-cylindrical rotor 40 is attached to the rstor shaft 32. At its ends this rotor is closed by end walls 42 and 44 and it has a casing 46, on which a total of 4 sets of vanes 501, 502, 503 and 504 are attached, these vanes serving to take along, i.e. accelerate in a rotatory manner, the fibrous suspension to be processed. These sets of vanes 501 to 504 are associated with 4 regions I, II, III, IV of the apparatus or rather the rotor 40, namely - according to Figure 1 from left to right - a heavy component separating region I, a sorting and deflaking region II, a washing out region III and a dewatering region IV. In this respect, vanes of the set of vanes 50 of the sorting and deflaking region II
which are adjacent one another in the circumferential direction are offset relative to one another in axial direction due to their axial length, as is apparent from Figure l.
A tangentially oriented inlet pipe 54 for the fibrous suspension to be processed opens into the housing 12 in the heavy component separating region I; in accordance with the invention this inlet pipe is arranged on top of the housing. In the region I the rotor 40 is enclosed only by the outer housing casing 14, into the bottom of whlch a vertically oriented outlet pipe 56 for dirt particles having a heavy specific weight opens. This is followed by a heavy component container 58, to which a diluting water line 60 is connected. Valves closing the heavy component container 58 at the top and bottom are designated 62 and 64, a valve for the dilutlng water line 60 has been designated 66.
Along the regions II, III and IV the housing 12 accommodates a circular-cylindrical screen cylinder 68, the screen apertures of which are finer in the sorting and deflaking region II and in the dewatering region IV than in the washing out region III. As illustrated in Figures l and 3, washing water channels 70 are attached to the outside of the screen cylinder 68, these channels being supplied via a washing water conduit 74 provided with a valve 72. The screen cylinder 68 does not have any screen apertures beneath the washing water channels 70 extending in the direction of the apparatus axis 20 but only spray openings 76 at certain points, according to the invention only rin the sorting and deflaking region II as well as~in the washing out region III, whereas no washing water is supplied to the dewatering region IV.
An accepted material chamber 78 limited by the screen cylinder 68 and the outer housing casing 14 is, according to Figure 1, closed on the right by the end wall 18 and on the left by a circular housing web 80; an accepted material outlet pipe 82 opens into the accepted material chamber 78 from below.
According to the invention, measures are taken to ensure that the rejected material conveyed to the rejected material box 24 cannot conglomerate but leaves the rejected material box at the bottom through its exit openings 26. For this purpose, the vanes 504 of the rotor 40 project somewhat into the rejected material box 24, a guiding wall 86 in the shape of a half shell is associated with the lower region of the rotor 40 in the rejected material box 24 and at the top, adjacent the rotor, a baffle 88 is arranged in the rejected material box and this has - lS -the effect that the rejected material catapulted upwards is, according to Figure 1, reflected towards the bottom right and therefore falls downwards into the exit opening 26 to the right of the guiding wall 86.
The fibrous suspension flowing into the apparatus via the inlet pipe 54 is caught by the vanes 501 attached to the rotor in the heavy component separating region I and catapulted against the outer housing casing 14. The dirt particles in the fibrous suspension having a heavy specific weight slide downwards along the outer housing casing 14 due to the force of gravity; at the lowest point of the housing 12 they pass into the heavy component container 58 via the outlet pipe 56. A thickening of the rejected material in the heavy component container 58 is avoided by a counterwashing via the diluting water line 60.
In the heavy component separating region I the fibrous suspension to be processed is, therefore, freed of dirt particies having a heavy specific weight, such as metal parts and the like, before it enters the annular space between the rotor 40 and the screen cylinder 68.
In the sorting and deflaking region II the fibrous suspension is caught by the vanes 502 and catapulted against the perforated screen cylinder 68, the screen apertures of which allow the accepted material, i.e. the fine fraction formed of usable fibers and water, to pass whereas the dirt is retained in the annular space between rotor and screen cylinder. The accepted material leaves the accepted material chamber 78 via the accepted material outlet pipe 82.
Due to the inventive design of the vanes 502 with sharp edges fibers, i.e. fiber conglomerates, contained in the fibrous 2`~ ,7 suspension are broken up; a sllghtest possible distance between the vanes 502 and the screen cylinder 68 has the same effect, whereby an additional advantage is also obtained: The fibers tend to form a fiber fleece on the inner inflow side of the screen cylinder 68 and this would hinder the flow of the accepted materlal through the screen cylinder. The fact that the vanes 502 rotate at such a slight distance from the screen cylinder 68 prevents the formation of such a fiber fleece or removes any fiber fleece in the process of formation.
As is apparent from Figure 4, the effective height of the vanes may be adjusted or precluded, e.g. by the washers 90 illustrated in Flgure 4. The same applies for the other vanes.
This can influence the intensity of the deflaking operation effected~by the vanes 50 and which is performed between the vane edges and the edges of the screen apertures by impact and shearing effects.
As indicated in Figure 5, the inclination of the vanes relative to the apparatus axis 20 or the generatrix of the rotor 40 may be adjusted. In this way, the fibrous suspension or the dirt can be transported more quickly or more slowly through the annular space between rotor 40 and screen cylinder 68 to the end of the screen cylinder to the right according to Figure 1. In the heavy component separating region I the vanes 501 are preferably axially arranged, i.e. without any angular pitch, since the axial transport of the fibrous suspension in the direct$on of the rejected material box 24 is effected by the fibrous suspension flowing in behind.
The screen cylinder apertures are cleaned, inter alia, by the washing water supplied via the washing water channels 70 and the spray openings 76.
Since the major portion of the individual fibers suspended in the water has passed through the screen cylinder apertures, the rejected material in the washing out region II is supplied with an increased amount of washing water in order to wash the usable fibers still contained in the rejected material off the dirt and then centrifuge them out of the annular space between rotor and screen cylinder by means of the vanes 503. In the inventive apparatus the washing out process is particularly intensive since the jets of water entering the annular space between screen cylinder 68 and rotor 40 strike the rotor casing 46, are then reflected and thereby spray apart. In addition, the washing and diluting water is well distributed by the rotating vanes 503. These vanes 503 are, with respect to their angle, mounted on the rotor in accordance with the desired holding time in the washing out-re~ion III.~
the rejected material remaining in the annular space between rotor 40 and screen cylinder 68 is now freed of the adherent water in the dewatering region IV by means of centrifugation with the aid of the vanes 504. the vanes 504 are, according to the invention, formed of one piece over the entire length of the dewatering region IV.
The dewatered rejected material leaves the apparatus via the exit opening 26 of the rejected material box 24.
If the fibrous suspension or the rejected material are intended to remain a particularly long time in a particular region, despite the f$brous suspension flowing in behind, the vanes in this region are negatively pitched, i.e. such that they act in the sense of a return effect.
Claims (21)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. An apparatus for sorting and deflaking fibrous suspensions, comprising a housing having in a front housing end region an inlet for the fibrous suspension to be processed, in addition an accepted material outlet for the sorted fibrous suspension as well as a rejected material outlet, and a rotor having a horizontal axis being mounted for rotation in said housing, said rotor having a plurality of regions disposed one after the other in the direction of the rotor axis and being surrounded by annular chambers having different functions, of said regions a first rotor region on the inlet side and a last rotor region facing said rejected material outlet arranged at a rear housing end region being provided at their periphery with take-along elements for said fibrous suspension, said last rotor region being surrounded by an annular screen and a deflaking rotor region located upstream of said last rotor region having elevations for effecting deflaking, wherein an additional rotor region surrounded by an annular screen is located between said first and said last rotor regions, characterized in that said first rotor region (I) is surrounded by an annular housing wall (14), an outlet (56) for particles of dirt having a heavy specific weight opening into said wall from below, and that said last rotor region (IV) is designed as a rejected material thickening region and said additional rotor region (II) is designed as a sorting region.
2. Apparatus as defined in claim 1, characterized in that said housing wall (14) surrounding said first rotor region (I) is closed except for said inlet (54) and said opening of said heavy dirt outlet (56).
3. Apparatus as defined in claim 1 or 2, characterized in that a rotor region designed as a fiber washing out region (III) is provided between said sorting region (II) and said rejected material thickening region (IV), said washing out region being surround by an annular screen (68) and having associated with it a washing water inlet (76) directed against said rotor (40).
4. Apparatus as defined in one or more of the preceding claims, characterized in that said rotor (40) is provided in said sorting region (II) at its periphery with take-along elements (502) for said fibrous suspension.
5. Apparatus as defined in claim 3, characterized in that said rotor (40) is provided in said fiber washing out region (III) at its periphery with take-along elements (503) for said fibrous suspension.
6. Apparatus as defined in one or more of the preceding claims, characterized in that in at least one of said rotor regions (I, II, III, IV) said take-along elements (501, 502, 503, 504) are designed as webs projecting like vanes from said rotor periphery.
7. Apparatus as defined in one or more of the preceding claims, characterized in that the elevations (502) effecting deflaking are also designed as webs projecting like vanes from said rotor periphery.
8. Apparatus as defined in one or more of the preceding claims, characterized in that the radial distance of said webs (502, 503, 504) from said respective screen (68) is approximately 1/2 to 5 mm.
9. Apparatus as defined in claim 8, characterized in that said radial distance of said webs (502, 503, 504) from said respective screen (68) is approximately 1/2 to 1 mm.
10. Apparatus as defined in one or more of the preceding claims, characterized in that said housing inlet (54) for said fibrous suspension to be processed is aligned approximately tangentially and said rotor (40) is adapted for rotary drive in the direction of the inlet flow, and that said take-along elements (501) of said first rotor region (I) as well as the annular space following the latter between said sorting region (II) and said screen (68) surrounding said region are arranged and designed such that dirt particles having a heavy specific weight do not essentially come into contact with said take-along elements (501) of said first rotor region (I) and that said fibrous suspension can enter said annular space essentially unhindered.
11. Apparatus as defined in one or more of the preceding claims, characterized in that said deflaking rotor region (II) is surrounded by an annular screen (68).
12. Apparatus as defined in claim 11, characterized in that said deflaking region (II) also forms said sorting region.
13. Apparatus as defined in one or more of the preceding claims, characterized in that washing water inlets (76) are associated with said screen (68) of said sorting region (II).
14. Apparatus as defined in one or more of the preceding claims, characterized in that said screen (68) of said sorting region (II) has finer screen apertures than said screen of said fiber washing out region (III).
15. Apparatus as defined in one or more of the preceding claims, characterized in that said screen (68) of said rejected material thickening region (IV) has finer screen apertures than said screen of said fiber washing out region (III).
16. Apparatus as defined in one or more of the preceding claims, characterized in that the height of said webs (501, 502, 503, 504) relative to said rotor periphery is adjustable.
17. Apparatus as defined in one or more of the preceding claims, characterized in that the inclination of said webs (501, 502, 503, 504) relative to a generatrix of said rotor periphery is adjustable.
18. Apparatus as defined in one or more of the preceding claims, characterized in that said webs (501) in said first rotor region (I) extend approximately parallel to said generatrices of said rotor periphery.
19. Apparatus as defined in one or more of the preceding claims, characterized in that said webs (502, 503, 504) in said rotor regions (II, III, IV) following said first rotor region (I) are inclined relative to said generatrices of said rotor periphery such that they result in a conveying effect in the direction towards said rear housing end (24).
20. Apparatus as defined in one or more of the preceding claims, characterized in that said webs (504) of said last rotor region (IV) project beyond its screen (68) rearwardly into a rejected material chamber (24) formed by said housing (12).
21. Apparatus as defined in one or more of the preceding claims, characterized in that said inlet (54) is arranged at the top in said housing wall (14) surrounding said first rotor region (I).
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP3904960.4 | 1989-02-18 | ||
| DE3904960A DE3904960A1 (en) | 1989-02-18 | 1989-02-18 | DEVICE FOR SORTING AND DEBELING FIBER SUSPENSIONS |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2027564A1 true CA2027564A1 (en) | 1990-08-19 |
Family
ID=6374382
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002027564A Abandoned CA2027564A1 (en) | 1989-02-18 | 1990-02-07 | Appliance for sorting and deflaking fibre suspensions |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP0427802B1 (en) |
| CA (1) | CA2027564A1 (en) |
| DE (2) | DE3904960A1 (en) |
| WO (1) | WO1990009480A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5096127A (en) * | 1990-08-22 | 1992-03-17 | Ingersoll-Rand Company | Apparatus for pressurized screening of a fibrous material liquid suspension |
| DE102018122808A1 (en) * | 2018-09-18 | 2020-03-19 | Voith Patent Gmbh | Control method of a cleaning device with heavy part separator |
| CN110479740B (en) * | 2019-08-26 | 2021-12-28 | 西藏瑞华资本管理有限公司 | Sanitary towel fiber separation equipment adopting guiding, collecting and scraping principle |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3437204A (en) * | 1965-12-27 | 1969-04-08 | Bird Machine Co | Screening apparatus |
| CA889156A (en) * | 1969-09-19 | 1971-12-28 | Cowan Ben | Screen impeller |
| DE2611886C3 (en) * | 1976-03-20 | 1981-09-03 | Hermann Finckh, Maschinenfabrik GmbH & Co, 7417 Pfullingen | Device for sorting and deflaking of fiber suspensions |
| DE2850385C2 (en) * | 1978-11-21 | 1981-02-05 | J.M. Voith Gmbh, 7920 Heidenheim | Device for separating impurities from pulp suspensions |
| ES2015545B3 (en) * | 1986-02-18 | 1990-09-01 | Voith Gmbh J M | CLASSIFIER DEVICE FOR FIBER SUSPENSIONS |
| SE458036C (en) * | 1987-07-03 | 1990-05-03 | Kamyr Ab | DEVICE FOR DIVISION OF A SUSPENSION OF FIBER-containing CELLULOSAMASSA |
-
1989
- 1989-02-18 DE DE3904960A patent/DE3904960A1/en not_active Withdrawn
-
1990
- 1990-02-07 EP EP90903349A patent/EP0427802B1/en not_active Expired - Lifetime
- 1990-02-07 DE DE9090903349T patent/DE59002193D1/en not_active Expired - Fee Related
- 1990-02-07 WO PCT/EP1990/000199 patent/WO1990009480A1/en active IP Right Grant
- 1990-02-07 CA CA002027564A patent/CA2027564A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| DE3904960A1 (en) | 1990-08-23 |
| WO1990009480A1 (en) | 1990-08-23 |
| EP0427802B1 (en) | 1993-08-04 |
| EP0427802A1 (en) | 1991-05-22 |
| DE59002193D1 (en) | 1993-09-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5358637A (en) | Apparatus for sorting and deflaking fibrous suspensions | |
| US4356085A (en) | Rotary screening machine for pulp suspensions | |
| US4167438A (en) | Method and apparatus for preparing and cleaning fibrous material | |
| US3939065A (en) | Screening device | |
| US3912622A (en) | Screening machine with lights removal | |
| US4107033A (en) | Apparatus for cleaning fibrous suspensions of low stock consistency | |
| US4140629A (en) | Conical screen separator | |
| US3865243A (en) | Pressure strainer device | |
| US6613191B2 (en) | Pressurized screen and process for removing contaminants from a fibrous paper suspension containing contaminants | |
| US4396161A (en) | Disk refiner | |
| US4634521A (en) | Screening apparatus with light reject removal | |
| CA1064428A (en) | Stationary cylindrical screen for liquid suspensions including a heavy impurities trap and dilution means | |
| CA1309978C (en) | Sorting apparatus for fiber suspensions | |
| GB1566468A (en) | Apparatus for screening paper fibre stock | |
| US5143220A (en) | Apparatus for screening to remove knots from a fluid borne slurry of fibers and knots | |
| CA2027564A1 (en) | Appliance for sorting and deflaking fibre suspensions | |
| US4346007A (en) | Method at screening apparatus for cleaning the apertures in a screen plate and device for carrying out the method | |
| FI109038B (en) | Process for treating fiber pulp mixture and strainer | |
| US4420117A (en) | Waste paper disintegrating, sorting and fiber recovery apparatus | |
| US6131742A (en) | Device for separating contaminants from fibre pulp suspensions | |
| AT408771B (en) | SORTER FOR CLEANING A FIBER SUSPENSION | |
| EP1124003B1 (en) | Screen for purification of fibrous pulp | |
| GB2109260A (en) | Sorting fibre suspensions | |
| JPH0140155B2 (en) | ||
| CA1335191C (en) | Screening method and apparatus for light reject removal |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FZDE | Dead |