EP2893078A1 - Fibre sorting system - Google Patents
Fibre sorting systemInfo
- Publication number
- EP2893078A1 EP2893078A1 EP13748013.3A EP13748013A EP2893078A1 EP 2893078 A1 EP2893078 A1 EP 2893078A1 EP 13748013 A EP13748013 A EP 13748013A EP 2893078 A1 EP2893078 A1 EP 2893078A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- rotor blades
- rotor
- rotation
- plane
- jet
- 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
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
- D21D5/18—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force
- D21D5/22—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force in apparatus with a vertical axis
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D99/00—Subject matter not provided for in other groups of this subclass
Definitions
- the invention relates to a device for removing long fibers from a pulp suspension with at least one rotor with rotor blades, in which a jet of pulp suspension is directed to the rotor blades of the rotor, the jet direction with the rotation axis forms an angle of less than 45 °, the rotor blades a have in the direction of rotation facing wing edge and in the spin area of the rotor blades collecting chambers for the thrown off from the rotor blades, longer fibers are arranged.
- the fibers When a new pulp suspension is prepared from wood or when recovered paper is converted to a pulp suspension, the fibers generally have very different lengths. It may then be advantageous to separate the short cellulose fibers from long cellulose fibers, especially to be able to produce paper sheets with different qualities.
- the recovery of a long fiber fraction containing long fibers and, for example, free of mineral contents may also be of interest. Most such arrangements are used, however, to recycle recovered paper fiber raw materials so that they can be used as raw material again for the production of fibrous webs.
- pulp suspension also extends to fibers containing process or wastewater, in which the recovery of the fibers is in the foreground.
- the object of the invention is therefore a low-wear and efficient rotor design.
- this object is achieved in that the area swept by the rotor blades is 3 to 15 times, in particular 5 to 10 times, larger than the total area of all rotor blades in the plane of rotation.
- the object can also be achieved in that over at least 50% of the radial extent of the rotor blades, the distance between the rotor blades 3 to 15 times, in particular 5 to 10 times greater than the width of the rotor blades in the plane of rotation.
- a further enlargement of the rotor blades in the plane of rotation would indeed increase its stability, but also limit the flow rate. This applies in particular to the target peripheral speed of the rotor blades between 10 and 70, preferably between 20 and 40 m / s.
- the wing edge should support the collection, collection and centrifuging of the long fiber fraction into the catchment chambers. Therefore, it is advantageous if the rotor blades have a thickness between 0.2 and 2 mm, preferably between 0.3 and 0.7 mm, transverse to the plane of rotation.
- the rotor blades In order to ensure that the short fibers and fillers of the pulp suspension flow past the rotor blades as easily as possible, it is advantageous if the rotor blades have a flat profile, preferably running with the long side surfaces in the direction of rotation. In addition, it is advantageous if the rotor blades in the rotation plane have a width between 0.5 and 5 mm, preferably between 1 and 3 mm and / or the distance between two adjacent rotor blades in the rotation plane between 5 and 25 mm, preferably between 10 and 15 mm and / or the rotor blades have a length between 5 and 30 mm, preferably between 10 and 20 mm.
- the radial sliding out of the long fibers to the spin along the wing edge can be assisted by the fact that the wing edge extends radially outwardly at least in one, preferably at least the outermost portion with respect to the radial inclined towards the rotational direction, wherein the angle between this inclined portion of the wing edge and the radicals should be between 30 and 70 °, preferably between 55 and 65 °.
- the effect of the rotor blades can be further increased if the leading edges are not sharp, but have a certain rounding, as can be generated, for example, by electropolishing.
- the radii on the blade edge should be greater than 10% of the thickness of the rotor blades transversely to the plane of rotation and / or the roughness R A of Rotor blades lie at least in the region of the wing edge below 1 ⁇ .
- the jet direction of the pulp suspension jet should be approximately parallel to the axis of rotation of the rotor.
- the jet is directed onto the rotor blades via a jet accelerating jet.
- This acceleration causes a Orientation of the fibers in the flow direction, which supports the detection of long fibers by the rotor blades.
- the speed of the pulp suspension jet when hitting the rotor blades is between 3 and 20 m / s. In this way it is ensured that if possible only the long fibers adhere to the rotor blades, wherein the proportion of removed long fibers can be increased by increasing the peripheral speed of the rotor blades.
- the pulp suspension jet should extend at least predominantly, preferably exclusively only over a radially inner region of the rotor blades.
- a comprehensive use of the rotor blades can be achieved, in particular, if the pulp suspension jet has an annular cross-section enclosing the axis of rotation of the rotor. It is advantageous if the annular pulp suspension jet has a ring thickness between 1 and 5 mm.
- the distance between the nozzle and the rotor blades should be less than 20 mm, preferably less than 10 and in particular less than 5 mm.
- the invention is also suitable for the treatment of pulp suspensions with fabric densities up to 3.5%, preferably up to 3.5%. The invention will be explained in more detail with reference to an exemplary embodiment.
- FIG. 1 shows a schematic cross section through a sorting device
- Figure 2 is a plan view of a rotor 1 with rotor blades 2;
- FIG. 3 shows a detail from FIG. 2 and FIG.
- FIG. 4 shows a partial cross section through a rotor blade 2.
- annular pulp suspension jet 3 is formed in the sorting device for splitting off a long fiber fraction containing predominantly longer fibers from a pulp suspension to produce a paper web via a mold body 10 arranged centrally in a nozzle and directed onto the rotor vanes 2 of a rotor 1.
- the gap between the jet housing 1 1 delimiting the jet 3 on the outside and the molded body 10 is increased. This is possible in the example shown in Figure 1 simply by a displacement of the nozzle housing 1 1 against the flow direction.
- the molded body 10 causes an increase in the flow rate of the pulp suspension and thereby an increased orientation of the fibers in the flow direction, which supports the detection of long fibers by the rotor blades 2. So that alignment of the fibers is not lost too much, is the distance between the exit of the jet 3 from the nozzle and the rotor blades 2 only 5 mm.
- the rotor 1 is driven here by a motor arranged below.
- the jet direction of the pulp suspension jet 3 coincides with the rotor axis 4 of the rotor 1, wherein the speed of the pulp suspension jet 3 when hitting the rotor blades 2 is between 3 and 20 m / s and the peripheral speed of the rotor blades 2 is between 20 and 40 m / s. If the proportion of long fibers separated off via the rotor blades 2 is to be increased, then the peripheral speed of the rotor blades 2 is to be increased for this purpose.
- the centrifuging is not affected by the pulp suspension jet 3, the pulp suspension jet 3 is directed only to the radially inner part of the rotor blades 2, wherein the ring thickness is between 1 and 5 mm and the rotor blades 2 have a length between 10 and 20 mm.
- the rotor with the rotor blades 2 sweeps over a circular area with a diameter between 300 and 1, 500 mm, which ensures sufficient capacity even with an annular pulp suspension jet 3 in connection with the desired flow rate. Since the annular pulp suspension jet 3 is arranged coaxially to the axis of rotation 4, results in an optimal and uniform effect.
- the rotor blades 2 In order to support the trapping of the long fibers when cutting through the pulp suspension jet 3, the rotor blades 2 have an electropolished surface with a roughness R A of less than 1 ⁇ and transversely to the plane of rotation 8 a thickness D between 0.3 and 0.7 mm.
- the rotor blades 2 as shown in Figure 4, a flat, extending in the direction of rotation 5 cross-sectional profile, wherein the radii R in the direction of rotation 5 facing blade edge 6 are greater than 10% of the thickness D of the rotor blades 2.
- the rotor 1 with its rotor blades 2, as shown in Figure 2 are made of a metal sheet.
- the wing edge 6 pointing in the direction of rotation 5 is inclined radially outward with respect to the radials counter to the direction of rotation 5 at an angle 9 between 55 and 65 °. This facilitates the long fibers sliding along the wing edge 6 to the outside.
- the width of the rotor blades 2 in the plane of rotation 8 is between 1 and 3 mm and the distance between two adjacent rotor blades 2 in the plane of rotation 8 between 10 and 15 mm.
- the area swept by the rotor blades 2 is 5 to 10 times greater than the total area of all the rotor blades 2 in the plane of rotation 8.
- the distance between adjacent rotor blades 2 5 to 10 times larger than the width of these rotor blades 2 in the plane of rotation. 8
- a plurality of sorting devices according to the invention can also use a common axis of rotation 4 and thus also a common drive.
- the sorting devices can be operated in series or in parallel.
- the structure of the rotor 1 of several segments may be advantageous.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Paper (AREA)
- Nonwoven Fabrics (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE201210215964 DE102012215964A1 (en) | 2012-09-10 | 2012-09-10 | fiber screening |
PCT/EP2013/066563 WO2014037178A1 (en) | 2012-09-10 | 2013-08-07 | Fibre sorting system |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2893078A1 true EP2893078A1 (en) | 2015-07-15 |
EP2893078B1 EP2893078B1 (en) | 2016-12-14 |
Family
ID=48979735
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP13748013.3A Not-in-force EP2893078B1 (en) | 2012-09-10 | 2013-08-07 | Fibre sorting system |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP2893078B1 (en) |
CN (1) | CN104619912B (en) |
DE (1) | DE102012215964A1 (en) |
WO (1) | WO2014037178A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102018127914A1 (en) * | 2018-11-08 | 2020-05-14 | Voith Patent Gmbh | Rotor for a heating unit |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE339165B (en) | 1969-04-22 | 1971-09-27 | Calor & Sjoegren Ab | |
US4427541A (en) * | 1982-04-28 | 1984-01-24 | Wisconsin Alumni Research Foundation | Method and apparatus for spray fractionation of particles in liquid suspension |
SE444962B (en) * | 1985-07-08 | 1986-05-20 | Kamyr Ab | DEVICE FOR SEPARATION OF NON-REQUIRED PARTICLES IN A FIBER MASS |
EP0262124B1 (en) * | 1986-04-11 | 1990-08-29 | Beloit Corporation | Rotating separator |
CN1040254A (en) * | 1988-08-08 | 1990-03-07 | 高信光 | Divergent-centrifugal impeller and rotating machinery thereof |
US5104522A (en) * | 1990-05-09 | 1992-04-14 | Wisconsin Alumni Research Foundation | Spray fractionation disks and method of using the same |
AU1313001A (en) | 1999-10-20 | 2001-04-30 | Auckland Uniservices Limited | A method of fibre separation |
CA2545313C (en) * | 2003-11-14 | 2010-08-10 | Akzo Nobel N.V. | Separation apparatus |
CN102119248A (en) | 2008-08-11 | 2011-07-06 | 沃依特专利有限责任公司 | Arrangement for fractionating a suspension of fibrous material |
DE102011076518A1 (en) | 2011-05-26 | 2012-11-29 | Voith Patent Gmbh | fiber screening |
-
2012
- 2012-09-10 DE DE201210215964 patent/DE102012215964A1/en not_active Withdrawn
-
2013
- 2013-08-07 EP EP13748013.3A patent/EP2893078B1/en not_active Not-in-force
- 2013-08-07 CN CN201380046886.7A patent/CN104619912B/en not_active Expired - Fee Related
- 2013-08-07 WO PCT/EP2013/066563 patent/WO2014037178A1/en active Application Filing
Non-Patent Citations (1)
Title |
---|
See references of WO2014037178A1 * |
Also Published As
Publication number | Publication date |
---|---|
CN104619912A (en) | 2015-05-13 |
DE102012215964A1 (en) | 2014-03-13 |
CN104619912B (en) | 2017-06-09 |
WO2014037178A1 (en) | 2014-03-13 |
EP2893078B1 (en) | 2016-12-14 |
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