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EP0646199A1 - Trieuse sous pression pour suspensions fibreuses. - Google Patents

Trieuse sous pression pour suspensions fibreuses.

Info

Publication number
EP0646199A1
EP0646199A1 EP92912886A EP92912886A EP0646199A1 EP 0646199 A1 EP0646199 A1 EP 0646199A1 EP 92912886 A EP92912886 A EP 92912886A EP 92912886 A EP92912886 A EP 92912886A EP 0646199 A1 EP0646199 A1 EP 0646199A1
Authority
EP
European Patent Office
Prior art keywords
rotor
sieve
pressure sorter
profile elements
sorter according
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.)
Granted
Application number
EP92912886A
Other languages
German (de)
English (en)
Other versions
EP0646199B1 (fr
Inventor
Wilhelm Hagen Hutzler
Erich Czerwoniak
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Voith Finckh Fiber Systems GmbH and Co KG
Original Assignee
Hermann Finckh Maschinenfabrik GmbH and Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=37429236&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP0646199(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Hermann Finckh Maschinenfabrik GmbH and Co filed Critical Hermann Finckh Maschinenfabrik GmbH and Co
Priority to AT92912886T priority Critical patent/ATE146239T1/de
Publication of EP0646199A1 publication Critical patent/EP0646199A1/fr
Application granted granted Critical
Publication of EP0646199B1 publication Critical patent/EP0646199B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • D21D5/02—Straining or screening the pulp
    • D21D5/023—Stationary screen-drums
    • D21D5/026—Stationary screen-drums with rotating cleaning foils

Definitions

  • the invention relates to a pressure sorter for
  • Fiber suspensions in particular for the preparation of fiber suspensions obtained from waste paper, with a housing in which a stationary one turns into a sieve axis
  • Rejects outlet whereby profile elements are provided on the peripheral surface of the rotor to generate positive and negative pressure surges in the fiber suspension.
  • a first measure which can be found in the prior art, is to design the sieve openings in such a way that they widen in the direction of passage (ie in the direction from the inlet space to the accept material space) (see, for example, US Pat. No. 3,581,903) by the Reduce the risk of clogging of the sieve openings.
  • US Pat. No. 3,581,903 In order to both backwash the screen openings and prevent the formation of a nonwoven fabric on the inlet side of the screen, another became known
  • Pressure sorter (see e.g. US Pat. No. 4,276,159) is equipped with a rotor which, near the screen inlet side, has circumferential cleaning blades with an airfoil-like profile on average perpendicular to the rotor axis for generating positive and negative pressure surges, and its screen is designed in such a way that screen openings widen as a result of the inlet side a "roughened" sieve inlet side results to pass through the
  • Profile elements in the fiber suspension generate such pressure pulses that they interfere in the headbox of a paper machine downstream of the pressure sorter
  • Rotor circumferential direction one row each, with between there are two gaps in the rotor circumferential direction and the lengths of the segments
  • Measured rotor circumferential direction - are dimensioned in such a way and the mentioned offset was chosen such that - seen in the direction of the sieve or rotor axis - the profile element segments of an axial rotor section the gaps between the
  • Circumferential surface of the circular-cylindrical rotor body rises obliquely backwards in the opposite direction of rotation and outwards in the radial direction, by the impact effects of the pressure pulsations generated by the profile element segments
  • Circumferential wall of the rotor body forms two profile elements directly adjoining one another in the rotor circumferential direction, each of which has a vertical first flank lying in a plane of the diameter of the rotor and a second flank that adjoins it and falls against the direction of rotation.
  • Each of these profile elements extends in the direction of the rotor or sieve axis over the entire length of the rotor, so that this also applies to the parallel to the
  • Inlet side (even if the sieve openings are left out) is not smooth, but rather profiled.
  • the purpose of the design of the rotor and the inlet side of the sieve of this known pressure sorter is to continuously expose each area of the sieve to either a positive or a negative pressure pulse, due to the vertical front flanks of the profile elements and the resulting strong acceleration of the fiber suspension in the direction of rotation in Connection with the profiled inlet side of the sieve creates strong turbulence in the inlet area of the pressure sorter
  • the invention had for its object to provide a pressure sorter of the type mentioned which, with relatively fine sieve openings, enables a good sorting result in all fiber suspensions to be processed which occur in practice and which in particular ensures trouble-free continuous operation.
  • the object is achieved in that in each axial section of the rotor circumferential surface acting on the sieve, between two profile elements which follow one another in the rotor circumferential direction, a rotor circumferential surface sector is provided, over which these profile elements protrude in the radial direction and which is part of a surface area parallel to the sieve inlet side and rotationally symmetrical to the sieve axis, whereby - Measured in the circumferential direction of the rotor - the maximum length of each profile element is at least approximately the same size as the minimum length of the opposite direction of rotation
  • the minimum length of the latter is at least about 30% of the maximum length of the profile element lying in front of it in the direction of rotation, and the profile elements are designed and arranged on the rotor circumference in such a way that - viewed in the direction of the sieve axis - the
  • Fiber suspensions to be prepared from waste paper usually contain adhesive particles which are either plastically deformable from the start or plastically deformable at the normal operating temperatures of pressure sorters.
  • adhesive particles which are either plastically deformable from the start or plastically deformable at the normal operating temperatures of pressure sorters.
  • the high positive pressure surges generated in a pressure sorter of the type described in US Pat. No. 4,855,038 lead to none in the absence
  • Non-woven fabric on the inlet side of the screen means that a considerable part of such adhesive particles are pressed through even small screen openings.
  • a pressure sorter according to the invention avoids this disadvantage by producing a weakly formed nonwoven fabric due to the gaps between the profile elements.
  • a strong fiber fleece on the inlet side of the sieve leads to a strong fractionation of the fiber portion of a fiber suspension - long fibers, which in themselves
  • the pressure sorter according to the invention now leads to an optimization of the sorting effect, because a weakly formed non-woven fabric on the inlet side of the sieve allows long, brewable fibers to get into the accepted material to a considerable extent, while tests have shown that such a non-woven fabric
  • the fiber suspension to be processed is fed into the device, the fiber suspension in the inlet space has a flow component aligned parallel to the sieve or rotor axis.
  • the widened gap regions caused by the gaps mentioned also lead to the fact that this axial flow component - in comparison to conventional sorters such as those described in US Pat. No. 4,855,038 and DE-PS
  • the inlet side of the screen of the pressure sorter according to the invention can, however, achieve higher throughputs than with a pressure sorter according to the US patent
  • Nonwoven has the result that a high percentage of the above-mentioned adhesive particles through the
  • Sieve openings is pressed into the accept area. The same applies due to the high positive pressure surges and the resulting high flow velocities through the screen openings for in the to be processed
  • Fiber suspension contains long-fiber impurities.
  • Embodiment of the pressure sorter according to the invention forms the longitudinal direction of the first flank of each
  • Profile element with the axial direction an acute angle This significantly extends the service life of the sieve; namely, it has been shown that in the known pressure sorter described, the screen is at considerable risk of breakage, for several reasons, which will be discussed in more detail later, but above all for the following
  • Pressure sorters are introduced into the screen along a surface line (a line parallel to the screen axis) because of the axial course of the front edges of the profile elements. Since one because of the flow resistance of the screen openings and the associated pressure drop across the screen
  • the first flanks of the profile elements lying at the front in the direction of rotation are slightly inclined with respect to the direction of the sieve axis, the introduction of the pressure forces which cause the positive pressure surges generated by these first flanks does not take place along one
  • the first flanks of the profile elements could be inclined in any direction with respect to the sieve axis. It would be e.g. conceivable that the inclination is chosen such that the first flanks of the
  • Fiber suspension exert an axial conveying effect in the direction from the second axial end of the inlet space to its first axial end, in order - as is known in the case of pressure sorters - to reclaim the already thickened fiber suspension in the rear part of the inlet space, which is to be reprocessed, and thereby for one
  • Fiber suspension and for an even more extensive separation of usable fibers into the waste material space.
  • the longitudinal direction of the first flank of each profile element is inclined with respect to the axial direction in such a way that the first flanks face the one in the inlet space
  • Fiber suspension exert an axial conveying effect towards the second axial end of the inlet space. It has been shown that the sorting result can be improved even further as a result of this promotional effect, fiber suspension from which has not yet been thickened is intensified
  • Profile elements are inclined with respect to the axial direction, it is advisable to design and arrange the profile elements so that the rear edge of the second flank runs parallel to the sieve axis, namely to narrow the clear cross section of the aforementioned channels or
  • the first flanks of the profile elements at the front are intended to generate positive pressure surges and to drive the fiber suspension in the direction of rotation. Both can best be achieved by designing the profile elements in such a way that their first flank is approximately radial
  • the first flank could also be slightly inclined with respect to the radial direction, namely obliquely inwards (in the direction of the rotor axis) and backwards
  • Fiber suspension located in the profile element is only pushed outwards against the sieve in the radial direction and is not accelerated or is hardly accelerated in the direction of rotation.
  • each profile element can extend in the direction of the rotor axis over the entire length of the rotor circumference encompassed by the sieve; in this case the rotor has only one (in Rotor circumferential direction) row of profile elements and gaps arranged between them. Especially for that
  • Flanks of the profile elements of the second section are set back against the direction of rotation in relation to the first flanks of the profile elements of the first section and the lengths of the profile elements measured in the rotor circumferential direction are dimensioned such that adjacent rotor circumferential surface sectors (gaps) of the two axial rotor sections overlap in the direction of rotation in the axial direction .
  • the rotor of such a pressure sorter according to the invention thus has in particular two axial sections and thus two rows (running in the circumferential direction of the rotor) of
  • Fiber suspension contains impurities and fibers accumulate and clump up these steep first flanks, which, above all, entails the risk that such material accumulations wedge between the radially outer edge of the first flanks and the sieve and thus render the pressure sorter inoperative or even lead to a sieve breakage.
  • a staggered arrangement of the profile elements as described above now has the following effects, especially if the front first flanks are inclined relative to the axial direction in such a way that they have a conveying effect in the direction of the second axial end of the inlet space: Alone that by the delivery pressure in the inlet of the
  • Profile elements of the first axial rotor section slide along these first flanks in the direction of the second axial end of the inlet space; if these accumulations of material come to the edges of the profile elements of the first rotor section facing the second axial end of the inlet space, they become part of them there due to the turbulence that occurs there
  • Fiber suspension is mixed so that the material accumulations at least essentially dissolve before the fiber suspension is gripped by the next first flank of a profile element of the second axial rotor section.
  • This axial derivation of undesirable accumulations of matter is of course intensified when the first flanks of the profile elements are inclined in the manner described. Due to the staggered arrangement of the profile elements described above, the fiber suspension to be sorted is also in those areas of the annular space between the rotor circumference and the sieve
  • the staggered arrangement of the profile elements described above brings about an even better distribution of the pressure forces over the screen, ie those pressure forces which are generated by the positive pressure pulses caused by the profile elements and act on the screen.
  • the overlap in the axial direction is adjacent to one another
  • the profile elements of different axial rotor sections could be designed identically. However, it is advisable to adjust the different consistency of the fiber suspension to be sorted in the different axial areas of the annular space between the rotor circumference and the sieve by a different design
  • Profile elements in the first axial rotor circumferential surface section — measured in the rotor circumferential direction — are to be dimensioned shorter than in the second rotor circumferential surface section.
  • the height of the first flanks of the profile elements measured in the radial direction in the first axial rotor circumferential surface section can be dimensioned smaller than in the second for the same purpose
  • Fiber suspension in the direction of rotation up to
  • the peripheral speed of the rotor can be accelerated because the profile elements then generate maximum positive pressure pulses and particularly strong turbulence.
  • the invention now remedies this by proposing to use a three-phase motor as the motor for driving the rotor. which is preceded by a frequency converter that is controllable with regard to its output frequency.
  • Pressure sorters can therefore be varied simply by changing the setting of the frequency converter and thus the frequency of the feed current for the three-phase motor, and thus adapted to the desired sorting method or sorting result.
  • this pressure difference can, according to the invention, be as
  • Control variable can be used for the frequency converter; in a preferred embodiment of the invention
  • Pressure sorter is the frequency converter by one
  • Measuring device for measuring the pressure difference between
  • the invention proposes some particularly advantageous embodiments of the rotor of the pressure sorter according to the invention, above all with regard to the rational production of a pressure sorter according to the invention and to the fact that wear of the profile elements, especially in the area of their front first flanks, cannot be avoided.
  • the rotor has a circular-cylindrical and hollow rotor body, the peripheral surface of which Forms rotor circumferential surface sectors and in which the first flanks of the profile elements of strips fastened on the circumferential surface of the rotor body and the second flanks of the profile elements of an arc in the side view
  • the strips and sheets could e.g. by screws on the rotor body or on the
  • Strips are attached, but are preferred.
  • a plastic e.g. It can be a hardenable casting resin, but it is more advantageous if an in-situ foamed plastic is used, since this allows these cavities to be filled in easily and completely in such a way that liquid cannot penetrate into these cavities.
  • Profile elements are formed by a metal strip, which e.g. is inserted into the all-plastic body, because then in the event of wear, only this metal strip normally has to
  • an embodiment of the pressure sorter according to the invention should be used, in which the inlet side of the sieve has a turbulence-generating profile.
  • Fig. 1 is a partially sectioned side view of the
  • the sectional view being a section in a vertical diameter plane of the rotor or sieve
  • Figure 2 is a section along the line 2-2 in Fig. 1.
  • Fig. 1; Fig. 4 is an end view of the rotor, according to Fig. 1 seen from the left, including the sieve shown in an axial section, and
  • the actual pressure sorter 10 shown in FIG. 1 with a housing 14 standing on supports 12 also includes a motor 18 standing on a frame 16, which is a three-phase or three-phase AC motor, which is operated by means of a pulley 20 and V-belt 22 drives a belt pulley 24 which is mounted on a rotor shaft 26 which is rotatably mounted in the frame 16 and the housing 14
  • the housing 14 consists essentially of a left end wall 28 according to FIG. 1, a circular cylindrical housing jacket 30 arranged concentrically to the rotor shaft 26 and a housing cover 32 which are connected to one another in a pressure-tight manner.
  • Rotor shaft 26 carries a rotor designated as a whole as 36, which can be driven about axis 34 with the aid of rotor shaft 26 and is surrounded by a circular cylindrical sieve 38 which is concentric with axis 34 and which is attached to two
  • Housing elements 40 and 42 is attached and is held by these housing rings.
  • the axial length (in the direction of the axis 34) of the rotor 36 is equal to the axial length of the effective area of the screen 38 between the
  • the axial length of the rotor 36 should be selected to be larger or smaller than the axial length of the sieve 38.
  • Inlet connection 46 provided, through which - as indicated by the arrow F - the to be processed or sorted
  • Fiber suspension is conveyed into the pressure sorter, by means of a pump, not shown. Approximately in the middle above the sieve 38 is on the housing jacket 30
  • Outlet connector 48 attached through which the so-called
  • Pressure sorter leaves.
  • the accepted substance is the part of the fiber suspension that has passed the sieve 38.
  • a second outlet connection 50 is finally fastened to the left end of the housing shell 30 according to FIG. 1, through which the so-called reject material - as indicated by the arrow R in FIG. 2 - leaves the pressure sorter; at the
  • the inlet connection 46 will be arranged such that the fiber suspension to be sorted is approximately tangential into the housing 14
  • outlet connection 48 could of course also be arranged at the bottom of the housing jacket 30, insofar as the installation of the pressure sorter 10 permits the removal of the accepted substance downwards.
  • the fiber suspension to be processed which is fed into the pressure sorter 10 via an inlet connection 46, first enters an inlet space 52 and then enters an annular space between the circumference of the rotor 36 and the sieve 38, which will be referred to below as the inlet space 54, namely the fiber suspension to be sorted via a first axial end 54a of this inlet space
  • the reject passes through and thus reaches the accept material space 58.
  • the reject leaves the inlet space 54 at its second end 54b and thus arrives in the reject space 56, from which the reject leaves the pressure sorter via the second outlet connection 50.
  • the axis 34 runs at least approximately horizontally, but in principle it would also be conceivable to set up the pressure sorter in such a way that its axis 34
  • first pressure transmitter 62 and a second pressure transmitter 64 which are arranged in the inlet connection 46 or in the first outlet connection 48, but could also be arranged in the inlet chamber 52 or in the accept material chamber 58. They are on lines 66 and 68 in which
  • Display devices 70 and 72 are arranged, connected to the inputs of a difference former 74, which at its
  • Output delivers a control signal proportional to the pressure difference, which is connected via a line 76 to the control input of a frequency converter 78.
  • This is fed from a current source, not shown, with a 3-phase alternating current or three-phase current of frequency f 1 and supplies a three-phase current of frequency f 2 for driving three-phase motor 18, frequency f 2 being a function of the control signal generated by difference generator 74.
  • the rotor 36 is driven at a speed which is a function of this control signal and thus the pressure difference between the inlet space 54 and the accept material space 58.
  • Indicators 70 and 72 could also have potentiometers or others in lines 66 and 68
  • Adjustment elements can be provided with which the signals supplied by pressure transmitters 62 and 64 can be changed in order to be able to influence the dependence of the control signal on line 76 on the pressure difference mentioned. 3 to 5, the invention
  • a hub 80 fixedly connected to the rotor shaft 26 carries a closed, hollow circular cylindrical rotor body 82 with a circular cylindrical rotor jacket 84.
  • This has a first axial end 84a at the first axial end 54a of the inlet space 54 and a second axial end 84b at the second axial end 54b of the Inlet space and carries two sets of profile elements, namely a first set, which is formed by profile elements 86a, 86b, 86c and 86d, and a second set, formed by profile elements 88a, 88b, 88c and 88d.
  • the first set of profile elements forms a first row of profile elements and gaps 86a ', 86b', 86c 'and 86d' extending in the rotor circumferential direction or direction of rotation U of the rotor, and this row defines a first axial rotor section 90 which defines the inlet space 52 faces;
  • the second set of profile elements 88a-88d forms a second, likewise row of profile elements and interposed gaps 88a ', 88b', 88c 'and 88d', and this second row defines a second axial rotor section 92 which corresponds to the
  • Rejects room 56 is adjacent.
  • all profile elements are of equal height (measured in the direction of the axis 34), but depending on the desired sorting result and / or depending on the type of fiber suspension to be sorted, it could be expedient to increase or decrease the height of the first row choose as the height of the second row. It may also be useful to provide the rotor with more than two such rows.
  • each profile element has a front lying in the direction of rotation U. End face or first flank I, which is perpendicular to
  • the first edges I run along
  • running flow component of the fiber suspension in the Inlet space 54 is reinforced in the direction from the first axial end 54a of the inlet space to the second axial end 54b thereof.
  • each of the particularly advantageous embodiment extends
  • the smallest length L 1 'of the gaps 86a' - 86d 'of the first row is also 45 ° and is therefore equal to the greatest length L 1 of
  • the second row is 53 ° in this embodiment; since, according to the invention, the number of profile elements of the second row is equal to the number of profile elements of the first row, the minimum length L 2 'of the gaps 88a' - 88d 'of the second row results in a lower value of 37 ° here. As can also be seen in FIG. 5, these are
  • Profile elements 88a-88d of the second row and thus their gaps are offset relative to the profile elements of the first row or their gaps in the opposite direction of rotation U, the size of the offset being matched to the lengths of the profile elements or the gaps such that they are in axial relation to one another
  • Direction of rotation U or in the rotor circumferential direction overlap to such an extent that they form a continuous channel in the axial direction, which extends from one axial end 84a of the rotor shell 84 to its other axial end 84b.
  • the inside width L 3 of this channel is 25 °, the inside width being understood as the width which the observer sees in the direction of the axis 34 when the rotor is viewed from the front.
  • the lengths of the profile elements of the first row are therefore approximately equal to the lengths of the gaps of the first row, the lengths of the profile elements of the second row are greater than the lengths of the profile elements of the first row, and the length of the gaps of the second row are smaller than the lengths of the
  • Profile elements 88a-88d of the second row are also transported in the axial direction and reach the
  • the lengths L 1 and L 2 lie in a range between approximately 200 mm and approximately 450 mm.
  • Circumferential speeds of the rotor are expediently between approximately 10 m / s and approximately 40 m / s, with generally the best sorting results
  • Circumferential speeds of about 15 to about 30 m / s can be achieved.
  • the sieve openings 38a of the sieve 38 are bores, their diameter is expediently approximately 1 mm to approximately 3.5 mm if the rotor has a
  • Peripheral speed of about 10 to about 15 m / s is operated. Smaller holes can be used at higher peripheral speeds; expediently one also operates a pressure sorter according to the invention
  • slot-shaped sieve openings with a width of approx. 0.1 mm to approx. 0.35 mm are recommended for this case.
  • Profile elements 86a-86d and 88a-88d of the preferred embodiment shown Each of these profile elements - apart from the rotor shell 84 - consists of a strip 100 forming the first flank I, a bent sheet 102 forming the second flank II and two side walls 104, reference being made to FIG. 3 to indicate that in FIG this figure because of the oblique course of the first flanks I and thus the strips 100 the latter were not cut perpendicular to their longitudinal extension, but obliquely thereto.
  • Cavities 106 of the profile elements should be liquid-tight or with a filler such as e.g. one
  • Foam plastic must be filled in to avoid imbalance in the rotor. The same applies to the

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

Trieuse sous pression pour la préparation de suspensions fibreuses obtenues à partir de vieux papiers de récupération, qui comprend un tamis (38) entourant un rotor (38), une chambre d'alimentation (54) située entre la circonférence du rotor et le tamis, ainsi qu'une chambre de pâte acceptée (58) située à l'extérieur du tamis. La trieuse comprend également des éléments profilés (86a - 86d) placés sur la surface circonférentielle du rotor, afin de produire des coups de bélier positifs et négatifs. Afin d'obtenir de bons résultats au niveau du tri et d'arriver à ce que le tamis dure plus longtemps, un secteur de surface circonférentielle du rotor se trouve dans chacune des sections axiales de la surface circonférentielle du rotor qui agit sur le tamis, entre deux éléments profilés placés à la suite, dans le sens circonférentiel du rotor. Ledit secteur fait partie d'une surface d'enveloppe parallèle au côté d'alimentation du tamis. La longueur de chaque élément profilé, mesurée dans le sens circonférentiel du rotor, est au moins à peu près la même que celle du secteur de surface circonférentielle du rotor, qui suit. La longueur de ce dernier secteur représente cependant au moins environ 30 % de la longueur de l'élément profilé se trouvant devant. Les éléments profilés sont conçus et disposés sur la circonférence du rotor de manière que, vus dans le sens de l'axe du tamis, les secteurs de surface circonférentielle du rotor forment des canaux transversaux entre les éléments profilés le long de la zone du rotor entourée par le tamis.
EP92912886A 1992-06-20 1992-06-20 Trieuse sous pression pour suspensions fibreuses Expired - Lifetime EP0646199B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT92912886T ATE146239T1 (de) 1992-06-20 1992-06-20 Drucksortierer für fasersuspensionen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/EP1992/001393 WO1994000634A1 (fr) 1992-06-20 1992-06-20 Trieuse sous pression pour suspensions fibreuses

Publications (2)

Publication Number Publication Date
EP0646199A1 true EP0646199A1 (fr) 1995-04-05
EP0646199B1 EP0646199B1 (fr) 1996-12-11

Family

ID=37429236

Family Applications (1)

Application Number Title Priority Date Filing Date
EP92912886A Expired - Lifetime EP0646199B1 (fr) 1992-06-20 1992-06-20 Trieuse sous pression pour suspensions fibreuses

Country Status (8)

Country Link
US (1) US5601192A (fr)
EP (1) EP0646199B1 (fr)
JP (1) JP3542594B2 (fr)
AU (1) AU2018492A (fr)
CA (1) CA2138371C (fr)
DE (1) DE59207688D1 (fr)
FI (1) FI110011B (fr)
WO (1) WO1994000634A1 (fr)

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EP0646199B1 (fr) * 1992-06-20 1996-12-11 Hermann Finckh Maschinenfabrik GmbH & Co. Trieuse sous pression pour suspensions fibreuses
US5566833A (en) * 1995-01-25 1996-10-22 Hermannfinckh Maschinenfabrik Gmbh & Co. Pressure sorter for fiber suspensions as well as a process for the preparation of fiber suspensions
WO1996023930A1 (fr) * 1995-02-03 1996-08-08 Hermann Finckh Maschinenfabrik Gmbh & Co. Trieuse sous pression de suspensions de fibres et crible pour ces trieuses sous pression
US5954956A (en) * 1997-07-22 1999-09-21 J&L Fiber Services Modular screen cylinder and a method for its manufacture
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US6348130B1 (en) * 1998-03-11 2002-02-19 Thermo Black Clawson Inc. Variable pressure screening
US6138838A (en) * 1998-05-29 2000-10-31 J&L Fiber Services, Inc. Screen media and a screening passage therefore
US6324490B1 (en) 1999-01-25 2001-11-27 J&L Fiber Services, Inc. Monitoring system and method for a fiber processing apparatus
AT408773B (de) * 2000-02-03 2002-03-25 Andritz Ag Maschf Sieb und verfahren zur herstellung eines derartigen siebes
AT408770B (de) * 2000-02-03 2002-03-25 Andritz Ag Maschf Sortierer zur reinigung einer faserstoffsuspension
ES2226787T3 (es) * 2000-02-19 2005-04-01 Voith Paper Patent Gmbh Criba para suspensiones de fibras, asi como procedimiento para su fabricacion.
AT408997B (de) * 2000-04-03 2002-04-25 Andritz Ag Maschf Sortierer für die papier-erzeugung und flügel für sortierer
ITVI20010039A1 (it) * 2001-02-15 2002-08-16 Comer Spa Filtro rotante per sospensioni fibrose
JP4931096B2 (ja) * 2001-07-03 2012-05-16 臼井国際産業株式会社 温度感応型流体式ファン・カップリング装置
DE10304621B4 (de) * 2003-02-05 2005-04-28 Voith Paper Patent Gmbh Verfahren zur Bestimmung von rheologischen Eigenschaften einer Faserstoffsuspension
JP4577065B2 (ja) * 2005-03-31 2010-11-10 王子製紙株式会社 スクリーン装置およびこれを用いた再生パルプの製造方法
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US10865520B2 (en) 2017-09-18 2020-12-15 International Paper Company Method and apparatus for controlling a fiber fractionation system
DE202022104529U1 (de) 2022-08-09 2023-11-16 Vogelsang Gmbh & Co. Kg Separator zum Separieren eines Mediums

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Also Published As

Publication number Publication date
EP0646199B1 (fr) 1996-12-11
FI110011B (fi) 2002-11-15
CA2138371A1 (fr) 1994-01-06
DE59207688D1 (de) 1997-01-23
US5601192A (en) 1997-02-11
FI945949A0 (fi) 1994-12-19
JPH07508077A (ja) 1995-09-07
JP3542594B2 (ja) 2004-07-14
WO1994000634A1 (fr) 1994-01-06
AU2018492A (en) 1994-01-24
CA2138371C (fr) 1999-12-07
FI945949A7 (fi) 1994-12-19

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