EP0275967B1 - Method and apparatus for separating knots - Google Patents
Method and apparatus for separating knots Download PDFInfo
- Publication number
- EP0275967B1 EP0275967B1 EP88100678A EP88100678A EP0275967B1 EP 0275967 B1 EP0275967 B1 EP 0275967B1 EP 88100678 A EP88100678 A EP 88100678A EP 88100678 A EP88100678 A EP 88100678A EP 0275967 B1 EP0275967 B1 EP 0275967B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cylinder
- reject
- pulp
- screen cylinder
- screen
- 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.)
- Revoked
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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
- D21D5/06—Rotary screen-drums
Definitions
- the present invention relates to a method and apparatus for separating knots.
- the method and apparatus are in particular suitable in separating knots from high consistency pulp.
- the apparatus for separating knots and other solids from a fiber suspension or a pulp has a screen cylinder rotating in an outer housing, a shaft for rotating the cylinder, one or more blades positioned inside the cylinder and tangential connections for the pulp inlet and reject outlet and a connection for the accept respectively being attached to the outer housing.
- Such an apparatus is known from GB-A-2 070 456.
- the apparatus described shows in particular the arrangement of a first and a second separation chamber, the second chamber being provided for separating the light fraction discharged from the first chamber with the reject.
- a screen cylinder is also described which is arranged in the first separation chamber and can be rotated.
- a suitable solution for significantly reducing the consumption of energy of the apparatus is not disclosed.
- the fine fibers pass through the holes or slots of the perforated casing and are discharged through the accept outlet in the lower end of the outer casing.
- the coarser material which is not filtered through the holes of the screen casing is carried to the upper end of the screen casing and falls from there to the reject chute.
- SE -A- 316363 Another apparatus according to prior art is introduced in SE -A- 316363 in which there is substantially a slightly conically downwards broadening rotating screen cylinder inside the cylindrical casing. Inside the screen cylinder there are stationary pulsation means arranged to ensure that the openings of the screen cylinder remain open.
- the pulp is tangentially fed to an annular channel situated at the upper end of the outer casing from which channel the pulp flows along the horizontal plate arranged on the outer casing spirally towards the shaft of the screen cylinder.
- In the middle part of the above mentioned plate there is a hole through which the pulp falls down onto the end cover of the rotating screen cylinder, which has radial ribs giving the pulp its initial rotational motion.
- the screen cylinder consists of openings that open to the inside of the cylinder and of connecting pieces which in principle consist of radial arms and parts bent forward to the direction of the pulp flow coming to the cylinder which produce pressure pulses to the pulp to keep the holes of the screen cylinder open.
- the apparatus in accordance with this publication was found to operate especially well in paper machine short circulation and equivalent where it enabled the dampening of the fluctuation of the pressure inconvenient to further processing.
- the latter two devices are characterized in that they reach the consistency range of 4 - 6 %, whereas the device according to the first example functions only in the consistency of up to 1,5 - 2 %. Plugging of the holes on the screen surface limits the operation in all devices. Yet, in stock processing the aim is consistently towards higher consistencies, because it is in every respect more preferable to tend to treat the pulp in different process stages at the same consistency without thickening and dilution. If it is possible to raise the processing consistency, savings can be gained in both device and transportation charges and also considerably in the consumption of energy.
- the object of the present invention is to provide an improved method and apparatus for separating knots which reaches the so called low range of the MC-consistency, ie. medium consistency (6 - 8%) and diminishes significantly of the consumption of energy.
- This object is solved according to the present invention with a method for separating knots and other solids from a fiber suspension or a pulp with a rotating screen cylinder, on the outer surface of which the fiber suspension to be treated is introduced tangentially, from the inside of which accept is discharged and from the outer side of which reject is discharged tangentially, and in which the rotating screen cylinder is maintained clean by subjecting it to positive and/or negative pressure pulses from the inside, wherein the tangential introduction of the fiber suspension and the tangential discharge of the reject take place in the direction of rotation of the screen cylinder.
- this object is solved in accordance with the present invention by an apparatus characterized in that the tangential connections are arranged such that the directions of the pulp inlet and the reject outlet are the same as the direction of rotation of the screen cylinder and that the screen cylinder is contoured by means of ridges arranged on the outer surface thereof to increase the speed of motion of and the shear forces acting on the pulp.
- the rise of the applicable range of consistency is achieved by the correct measuring and formulation of the screen profile, and optimizing the rotational speed of the cylinder with respect to the feeding speed of the pulp.
- the consumption of energy of the knotter of the present invention has been measured to have been at most 0,6 kWh/ mass ton.
- the change of the direction of rotation has diminished the wear of the screen cylinder.
- one advantage of an apparatus in accordance with the present invention is facilitation of reject outlet compared to the approach in accordance with the US patent 4,441,999, because in the apparatus according to the present invention the reject is discharged in the direction of the rotation of the screen cylinder.
- This pumping effect together with dilution water led to the reject in the discharge stage significantly facilitates the adjustment of the amount of reject.
- the reject rate can be maintained between 2 to 10 % by using the screen in accordance with the present invention.
- a preferred embodiment of the knotter of the invention is described substantially consisting of a cylindrical outer housing 1, in which there is an inlet connection 2 for the pulp, outlet connection 3 for the accept and outlet connection 4 for the reject, screen cylinder 5, and one or more stationary unrotating blades 6 inside the screen cylinder 5 extending near the surface of the screen cylinder.
- the screen cylinder 5 is attached by members 12 on the shaft 7 which functions e.g. by belt drive (not introduced).
- the space 8 between the screen cylinder 5 and the outer housing 1 is annular and sealed at the ends with radial plates 9 and 10 projecting from the outer housing 1 towards the shaft.
- the above mentioned connections 2 and 4 are tangentially attached to the outer housing 1 of the annular space 8.
- a feed pipe 11 for dilution water is arranged to the reject connection 4, with which, if necessary, the consistency of the reject is lowered in order to facilitate further screening.
- the blades 6 are attached with arms 13 and 14 to a stationary frame 15 which also forms a strut for the shaft 7 through the bearing 16.
- the blades 6 are positioned in the cylinder 5 so that the blade situated near the reject connection 4 is ⁇ 10 - 45° aside from it.
- the other blade is 10 - 45° aside from the input connection 2.
- the above mentioned blades generate the applicable pulse, positive and/or negative, to the cylinder 5.
- the contoured plate 20 consists of openings 21 and of lands 22 between them.
- the plate 20 is plain on the inner surface 23, excluding the openings.
- the outer surface of the plate 20 consists of front surfaces 25 rising at a certain angle from the plane 24 of the plate 20, of the surfaces 26 substantially parallel to the plane 24 of the plate 20, of the end surfaces 27 substantially upright to the plane 24 of the plate 20, and of parts 28 of the plane 24 between the openings 21.
- the screen plate can be considered to consist of a plate which has ridges 29 which consist of the above mentioned parts 25, 26 and 27, and of the plane like parts 28 between them, in which the openings 21 are machined.
- the openings 21 are preferably holes (or slots), the diameter of which can range, depending on the application, at least between 5 - 15 mm. It also appears in Fig. 4 that the ridges 29 can be slightly declined from the axial direction of the plate. From the declination angle of the ridges, the direction of the declination in respect to the direction of rotation, the speed of rotation and the ascending angle of the part 25 of the ridges, the circulation time of the pulp in the knotter can be optimized in relation to the result of the separation.
- the circumferential speed of the cylinder used in the performed tests has been 4 - 10 m/s and for the feed of the pulp 2 m/s in the performed experiments.
- the speed difference between the cylinder and the pulp is 2 - 8 m/s.
- the gradient plane 25 of the ridges 29 of the screen plate 20 receives the pulp coming into the cylinder, tending to accelerate its speed.
- the direction of the ridges 29 has the effect that if the ridges 29 on the screen cylinder 5 are backwards inclined, they tend to raise the pulp upwards in the cylinder, thereby the circulation time of the pulp in the knotter becomes longer, the separation takes place more accurately and the amount of reject diminishes while the amount of accept grows.
- the circulation time becomes shorter and the separation is not so accurate.
- the height of the screen cylinder also effects the speed, inclination angles, etc. used.
- the method and apparatus in accordance with the present invention function in the following way.
- the pulp is tangentially fed under pressure into the space between the rotating screen cylinder and the outer housing of the knotter and in the same direction as the rotating motion of the screen.
- the ridges of the screen cylinder subject the infed pulp to circumferential forces for increasing its speed of motion and, due to the shape of the ridges, also shear forces for opening the bonds between the pulp particles, i.e. the fibres.
- the ridges cause a low pressure zone at the outlet end in front of the surface 27 that attracts the loose fibres through openings 21 with the help of the pressure difference between the inlet connections 2 and the accept connections 3.
- the heavier particles carried by the pulp sling towards the surface of the housing 1 when hitting the ridges, whereby they are also subjected to the centrifugal force.
- the lighter particles of the pulp are enriched near the surface of the screen cylinder and are separated from the pulp in the above mentioned way. Due to the contours of the surface of the cylinder, a slight fluidization takes place near the surface of the screen cylinder, helping the separation and on the other hand also diminishing the consumption of energy of the separation and the wear of the screen cylinder.
- the heavy particles separated onto the surface of the outer housing of the knotter circulate down the housing surface along the spiral path and are tangentially discharged from the knotter through the connection 4. The discharge is activated more by feeding, if necessary, dilution water to the reject from the pipe 11.
- the apparatus in accordance with the invention described above has made it possible to diminish the consumption of energy in respect to the prior art by more than 30 % and at the same time it has been possible to increase the consistency of the pulp up to the lower range of the MC-consistency.
- a less wearing screen cylinder and an apparatus better adjustable in its function and in its end products has also been brought about.
- by merely changing the rotational speed of the cylinder it is possible to adjust the apparatus applicable to most different consistencies and different kinds of pulps.
- this method is added by a possibility to produce screen cylinders having varying inclination angles of ridges or openings of variable sizes, one is able to talk about an ultimately optimized knotter.
- a knotter according to the present invention may in reality differ a lot from the form shown above and yet not differ from the inventive idea which is more closely described in the accompanying claims. It is namely quite possible that, in some cases, it is necessary to use ridges with two or more inclination angles or that the speeds of the pulp suspension and the cylinder differ a lot from the example shown above, substantial is, however, only the difference of the speeds which according to the claims is 2-8 m/s.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Paper (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
- Filtration Of Liquid (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Control And Other Processes For Unpacking Of Materials (AREA)
- Ultra Sonic Daignosis Equipment (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
Abstract
Description
- The present invention relates to a method and apparatus for separating knots. The method and apparatus are in particular suitable in separating knots from high consistency pulp.
- In particular, the apparatus for separating knots and other solids from a fiber suspension or a pulp has a screen cylinder rotating in an outer housing, a shaft for rotating the cylinder, one or more blades positioned inside the cylinder and tangential connections for the pulp inlet and reject outlet and a connection for the accept respectively being attached to the outer housing.
- Such an apparatus is known from GB-A-2 070 456. The apparatus described shows in particular the arrangement of a first and a second separation chamber, the second chamber being provided for separating the light fraction discharged from the first chamber with the reject. A screen cylinder is also described which is arranged in the first separation chamber and can be rotated. However, a suitable solution for significantly reducing the consumption of energy of the apparatus is not disclosed.
- There are several different further kinds of knot separators already known. An apparatus is described in US -A- 3,947,314 which includes an outer casing, an inner screen casing, of cylindrical configuration, a rotating screw conveyor inside the screen casing and an inlet adjacent the lower end of the screen casing, an accept outlet adjacent the lower end of the outer casing and a reject outlet adjacent the upper end of the screen casing.The whole apparatus is preferably slightly inclined in relation to the vertical. The apparatus functions in the way that the pulp including knots or other fairly large pieces of wood is fed to the lower end of the screen casing to be lifted by the screw conveyor. When the screw conveyor lifts the pulp the fine fibers pass through the holes or slots of the perforated casing and are discharged through the accept outlet in the lower end of the outer casing. The coarser material which is not filtered through the holes of the screen casing is carried to the upper end of the screen casing and falls from there to the reject chute.
- Another apparatus according to prior art is introduced in SE -A- 316363 in which there is substantially a slightly conically downwards broadening rotating screen cylinder inside the cylindrical casing. Inside the screen cylinder there are stationary pulsation means arranged to ensure that the openings of the screen cylinder remain open. The pulp is tangentially fed to an annular channel situated at the upper end of the outer casing from which channel the pulp flows along the horizontal plate arranged on the outer casing spirally towards the shaft of the screen cylinder. In the middle part of the above mentioned plate there is a hole through which the pulp falls down onto the end cover of the rotating screen cylinder, which has radial ribs giving the pulp its initial rotational motion. From the cover the pulp is dashed due to the centrifugal force to the downwards narrowing space between the screen cylinder and the outer casing. The fines pass through the screen cylinder to the accept side. The material left over between the outer casing and the screen cylinder, the reject, is discharged finally to an annular channel in the lower end of the outer casing, from where the reject is discharged to the tangential outlet.
- A third arrangement is described in US -A- 4,441,999 which consists of a cylindrical outer casing and a rotating screen cylinder. Inside the screen cylinder there are one or more stationary non-rotating blades. The pulp is tangentially fed between the screen cylinder and the outer casing, but the opposite to the direction of rotation of the cylinder. The accept is discharged from the inside of the screen cylinder at the end of the cylinder and the reject tangentially, but opposite to the direction of rotation of the cylinder. In accordance with this arrangement, the screen cylinder consists of openings that open to the inside of the cylinder and of connecting pieces which in principle consist of radial arms and parts bent forward to the direction of the pulp flow coming to the cylinder which produce pressure pulses to the pulp to keep the holes of the screen cylinder open. The apparatus in accordance with this publication was found to operate especially well in paper machine short circulation and equivalent where it enabled the dampening of the fluctuation of the pressure inconvenient to further processing.
- The latter two devices are characterized in that they reach the consistency range of 4 - 6 %, whereas the device according to the first example functions only in the consistency of up to 1,5 - 2 %. Plugging of the holes on the screen surface limits the operation in all devices. Yet, in stock processing the aim is consistently towards higher consistencies, because it is in every respect more preferable to tend to treat the pulp in different process stages at the same consistency without thickening and dilution. If it is possible to raise the processing consistency, savings can be gained in both device and transportation charges and also considerably in the consumption of energy.
- The object of the present invention is to provide an improved method and apparatus for separating knots which reaches the so called low range of the MC-consistency, ie. medium consistency (6 - 8%) and diminishes significantly of the consumption of energy.
- This object is solved according to the present invention with a method for separating knots and other solids from a fiber suspension or a pulp with a rotating screen cylinder, on the outer surface of which the fiber suspension to be treated is introduced tangentially, from the inside of which accept is discharged and from the outer side of which reject is discharged tangentially, and in which the rotating screen cylinder is maintained clean by subjecting it to positive and/or negative pressure pulses from the inside, wherein the tangential introduction of the fiber suspension and the tangential discharge of the reject take place in the direction of rotation of the screen cylinder.
- Furthermore, this object is solved in accordance with the present invention by an apparatus characterized in that the tangential connections are arranged such that the directions of the pulp inlet and the reject outlet are the same as the direction of rotation of the screen cylinder and that the screen cylinder is contoured by means of ridges arranged on the outer surface thereof to increase the speed of motion of and the shear forces acting on the pulp.
- The rise of the applicable range of consistency is achieved by the correct measuring and formulation of the screen profile, and optimizing the rotational speed of the cylinder with respect to the feeding speed of the pulp. In addition to that it has been possible to diminish the consumption of energy of the knotter itself essentially compared to the apparatus of the US publication 4,441,999. This is mainly due to changing the direction of rotation of the screen cylinder to a direction parallel to the direction of the pulp feed. According to the performed tests the consumption of energy of the knotter of the present invention has been measured to have been at most 0,6 kWh/ mass ton. Furthermore the change of the direction of rotation has diminished the wear of the screen cylinder.
- Additionally, one advantage of an apparatus in accordance with the present invention is facilitation of reject outlet compared to the approach in accordance with the US patent 4,441,999, because in the apparatus according to the present invention the reject is discharged in the direction of the rotation of the screen cylinder. This pumping effect together with dilution water led to the reject in the discharge stage significantly facilitates the adjustment of the amount of reject. Thus even with higher consistencies the reject rate can be maintained between 2 to 10 % by using the screen in accordance with the present invention.
- Further advantageous features of the present invention are disclosed in the dependent claims.
- The method and apparatus according to the present invention are further described with reference to the accompanying drawings, in which
- Fig. 1
- is a partly sectional side view of the apparatus according to the invention,
- Fig. 2
- is a partly sectional top view of an apparatus according to Fig. 1,
- Fig. 3
- is a straightened sectional side view of the screen profile according to a preferred embodiment, and
- Fig. 4
- is an over view of the screen according to Fig. 3
- In Fig. 1 and 2 of the drawings a preferred embodiment of the knotter of the invention is described substantially consisting of a cylindrical
outer housing 1, in which there is aninlet connection 2 for the pulp,outlet connection 3 for the accept and outlet connection 4 for the reject,screen cylinder 5, and one or more stationaryunrotating blades 6 inside thescreen cylinder 5 extending near the surface of the screen cylinder. Thescreen cylinder 5 is attached bymembers 12 on theshaft 7 which functions e.g. by belt drive (not introduced). Thespace 8 between thescreen cylinder 5 and theouter housing 1 is annular and sealed at the ends withradial plates outer housing 1 towards the shaft. The above mentionedconnections 2 and 4 are tangentially attached to theouter housing 1 of theannular space 8. In addition afeed pipe 11 for dilution water is arranged to the reject connection 4, with which, if necessary, the consistency of the reject is lowered in order to facilitate further screening. - The
blades 6 are attached witharms stationary frame 15 which also forms a strut for theshaft 7 through thebearing 16. Theblades 6 are positioned in thecylinder 5 so that the blade situated near the reject connection 4 is ± 10 - 45° aside from it. Correspondingly, the other blade is 10 - 45° aside from theinput connection 2. Thus the above mentioned blades generate the applicable pulse, positive and/or negative, to thecylinder 5. - In Fig. 3 and 4 there is described an opened screen in accordance with one preferred embodiment. The
contoured plate 20 consists ofopenings 21 and of lands 22 between them. Theplate 20 is plain on the inner surface 23, excluding the openings. The outer surface of theplate 20 consists offront surfaces 25 rising at a certain angle from theplane 24 of theplate 20, of thesurfaces 26 substantially parallel to theplane 24 of theplate 20, of theend surfaces 27 substantially upright to theplane 24 of theplate 20, and ofparts 28 of theplane 24 between theopenings 21. On the other hand, the screen plate can be considered to consist of a plate which hasridges 29 which consist of the above mentionedparts parts 28 between them, in which theopenings 21 are machined. - As shown in Fig. 4, the
openings 21 are preferably holes (or slots), the diameter of which can range, depending on the application, at least between 5 - 15 mm. It also appears in Fig. 4 that theridges 29 can be slightly declined from the axial direction of the plate. From the declination angle of the ridges, the direction of the declination in respect to the direction of rotation, the speed of rotation and the ascending angle of thepart 25 of the ridges, the circulation time of the pulp in the knotter can be optimized in relation to the result of the separation. The circumferential speed of the cylinder used in the performed tests has been 4 - 10 m/s and for the feed of the pulp 2 m/s in the performed experiments. In that case the speed difference between the cylinder and the pulp is 2 - 8 m/s. Thegradient plane 25 of theridges 29 of thescreen plate 20 receives the pulp coming into the cylinder, tending to accelerate its speed. The direction of theridges 29 has the effect that if theridges 29 on thescreen cylinder 5 are backwards inclined, they tend to raise the pulp upwards in the cylinder, thereby the circulation time of the pulp in the knotter becomes longer, the separation takes place more accurately and the amount of reject diminishes while the amount of accept grows. - If the ridges are forwards inclined the circulation time becomes shorter and the separation is not so accurate. In addition to the above mentioned factors the height of the screen cylinder also effects the speed, inclination angles, etc. used.
- The method and apparatus in accordance with the present invention function in the following way. The pulp is tangentially fed under pressure into the space between the rotating screen cylinder and the outer housing of the knotter and in the same direction as the rotating motion of the screen. The ridges of the screen cylinder subject the infed pulp to circumferential forces for increasing its speed of motion and, due to the shape of the ridges, also shear forces for opening the bonds between the pulp particles, i.e. the fibres. The ridges cause a low pressure zone at the outlet end in front of the
surface 27 that attracts the loose fibres throughopenings 21 with the help of the pressure difference between theinlet connections 2 and the acceptconnections 3. The heavier particles carried by the pulp sling towards the surface of thehousing 1 when hitting the ridges, whereby they are also subjected to the centrifugal force. In that case the lighter particles of the pulp are enriched near the surface of the screen cylinder and are separated from the pulp in the above mentioned way. Due to the contours of the surface of the cylinder, a slight fluidization takes place near the surface of the screen cylinder, helping the separation and on the other hand also diminishing the consumption of energy of the separation and the wear of the screen cylinder. The heavy particles separated onto the surface of the outer housing of the knotter circulate down the housing surface along the spiral path and are tangentially discharged from the knotter through the connection 4. The discharge is activated more by feeding, if necessary, dilution water to the reject from thepipe 11. - As already mentioned above, the apparatus in accordance with the invention described above has made it possible to diminish the consumption of energy in respect to the prior art by more than 30 % and at the same time it has been possible to increase the consistency of the pulp up to the lower range of the MC-consistency. As a by product a less wearing screen cylinder and an apparatus better adjustable in its function and in its end products has also been brought about. For example, by merely changing the rotational speed of the cylinder, it is possible to adjust the apparatus applicable to most different consistencies and different kinds of pulps. When this method is added by a possibility to produce screen cylinders having varying inclination angles of ridges or openings of variable sizes, one is able to talk about an ultimately optimized knotter.
- It should be borne in mind that in the above only one preferred embodiment of the apparatus in accordance with the present invention has been described. A knotter according to the present invention may in reality differ a lot from the form shown above and yet not differ from the inventive idea which is more closely described in the accompanying claims. It is namely quite possible that, in some cases, it is necessary to use ridges with two or more inclination angles or that the speeds of the pulp suspension and the cylinder differ a lot from the example shown above, substantial is, however, only the difference of the speeds which according to the claims is 2-8 m/s.
- The reference numerals introduced in the claims are solely provided for reasons of clarity and do not limit the scope of the claims.
Claims (11)
- A method for separating knots and other solids from a fiber suspension or a pulp with a rotating screen cylinder, on the outer surface of which the fiber suspension to be treated is introduced tangentially, from the inside of which accept is discharged and from the outer side of which reject is discharged tangentially, and in which the rotating screen cylinder is maintained clean by subjecting it to positive and/or negative pressure pulses from the inside,
characterized in that
the tangential introduction of the fiber suspension and the tangential discharge of the reject take place in the direction of rotation of the screen cylinder. - The method according to claim 1, characterized in that the discharge of the reject is facilitated by spraying water into the reject outlet duct with which the consistency of the reject is diluted at the same time.
- An apparatus for separating knots and other solids from a fiber suspension or a pulp, the apparatus having a screen cylinder (5) rotating in an outer housing (1), a shaft (7) for rotating said cylinder, one or more blades (6) positioned inside the cylinder (5) and tangential connections (2, 4) for the pulp inlet and reject outlet and a connection (3) for the accept respectively being attached to the outer housing (1), characterized in that the tangential connections (2, 4) are arranged such that the directions of the pulp inlet and the reject outlet are the same as the direction of rotation of the screen cylinder and that the screen cylinder (5) is contoured by means of ridges (29) arranged on the outer surface (24) thereof to increase the speed of motion of and the shear forces acting on the pulp.
- The apparatus according to claim 3, characterized in that the ridges (29) consist of front surfaces (25) rising declined from the outer surface (24) of the cylinder (5) and of the end surfaces (27) substantially upright to the outer surface (24) of the cylinder (5).
- The apparatus according to claim 3 or 4, characterized in that the ridges are declined in respect to the shaft (7) of the cylinder (5).
- The apparatus according to claim 5, characterized in that the declination angle of the ridges is between -45° - +45°.
- The apparatus according to claim 3, characterized in that the openings on the cylinder are either holes or slots.
- The apparatus according to claim 3, characterized in that the difference between the circumferential speed of the cylinder and the feeding speed of the fibre suspension is 2 - 8 m/s.
- The apparatus according to claim 3, characterized in that one of the blades (6) generating a positive or negative pressure pulse is situated ±10 - 45° aside from the reject connection (4).
- The apparatus according to claim 3, characterized in that one of the blades (6) generating a positive or negative pressure pulse is situated ±10 - 45° aside from the pulp inlet connection (2).
- The apparatus according to claim 3, characterized in that the connection (3) for the accept is tangential.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT88100678T ATE69472T1 (en) | 1987-01-19 | 1988-01-19 | METHOD AND DEVICE FOR DISENGAGING KNOTS. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI870190 | 1987-01-19 | ||
FI870190A FI76139C (en) | 1987-01-19 | 1987-01-19 | Twigs separation method and apparatus |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0275967A2 EP0275967A2 (en) | 1988-07-27 |
EP0275967A3 EP0275967A3 (en) | 1989-02-08 |
EP0275967B1 true EP0275967B1 (en) | 1991-11-13 |
Family
ID=8523793
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP88100678A Revoked EP0275967B1 (en) | 1987-01-19 | 1988-01-19 | Method and apparatus for separating knots |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0275967B1 (en) |
JP (2) | JPH0696834B2 (en) |
AT (1) | ATE69472T1 (en) |
CA (1) | CA1329333C (en) |
DE (2) | DE275967T1 (en) |
FI (1) | FI76139C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4308225C1 (en) * | 1993-03-16 | 1994-11-24 | Escher Wyss Gmbh | Process for sorting fiber suspension and screening device for carrying it out |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE515589C2 (en) * | 1999-03-10 | 2001-09-03 | Valmet Fibertech Ab | Screening device for separating fiber suspensions, and stator for use in the screening device |
US6254729B1 (en) | 1999-03-22 | 2001-07-03 | Voith Sulzer Paper Technology North America, Inc. | Pulper with extraction plate assembly having removable inserts and method of manufacturing same |
JP4909693B2 (en) * | 2006-07-24 | 2012-04-04 | 相川鉄工株式会社 | Screen device |
FI20095769A (en) * | 2009-07-07 | 2011-01-08 | Andritz Oy | Apparatus for handling a fiber suspension |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH182068A (en) * | 1935-03-21 | 1936-01-31 | Miag Muehlenbau & Ind Ag | Classifier for fiber-containing goods, in particular for paper making materials. |
SE315479B (en) * | 1963-10-21 | 1969-09-29 | Knutsilplatar Malm N Ab | |
US3363759A (en) * | 1964-04-29 | 1968-01-16 | Bird Machine Co | Screening apparatus with rotary pulsing member |
DE1905832U (en) * | 1964-09-16 | 1964-12-03 | Hermann Finckh G M B H | SECURE FOR PAPER FABRIC SUSPENSIONS. |
SE316363B (en) | 1966-12-01 | 1969-10-20 | Karlstad Mekaniska Ab | |
SE374148B (en) * | 1972-08-31 | 1975-02-24 | S E E Ahlfors | |
US3947314A (en) | 1974-04-29 | 1976-03-30 | The Black Clawson Company | Method of treating paper fibers in a stationary screen |
US4017387A (en) * | 1975-08-11 | 1977-04-12 | The Black Clawson Company | Screening apparatus |
SE427124B (en) * | 1980-01-28 | 1983-03-07 | Celleco Ab | DEVICE FOR FILING OF FIBER PASS PENSIONS |
SE426958B (en) * | 1980-02-25 | 1983-02-21 | Celleco Ab | SEPARATOR FOR DIVISION OF AN INCOMING MIXTURE OF CELLULOSA SUSPENSION OR SIMILAR AND GROUND HEAVY PARTICLES |
WO1986003688A1 (en) * | 1984-12-25 | 1986-07-03 | Mitsubishi Jukogyo Kabushiki Kaisha | Pressure slit screen |
JPS61207689A (en) * | 1985-03-12 | 1986-09-16 | 三菱重工業株式会社 | Screening apparatus |
JPS61207069A (en) * | 1985-03-12 | 1986-09-13 | Nec Corp | Semiconductor device |
JPS61207690A (en) * | 1985-03-12 | 1986-09-16 | 三菱重工業株式会社 | Screening apparatus |
-
1987
- 1987-01-19 FI FI870190A patent/FI76139C/en not_active IP Right Cessation
-
1988
- 1988-01-18 CA CA000556763A patent/CA1329333C/en not_active Expired - Fee Related
- 1988-01-19 DE DE198888100678T patent/DE275967T1/en active Pending
- 1988-01-19 EP EP88100678A patent/EP0275967B1/en not_active Revoked
- 1988-01-19 DE DE8888100678T patent/DE3866116D1/en not_active Revoked
- 1988-01-19 AT AT88100678T patent/ATE69472T1/en not_active IP Right Cessation
- 1988-01-19 JP JP63007648A patent/JPH0696834B2/en not_active Expired - Fee Related
-
1991
- 1991-07-31 JP JP3191588A patent/JPH0533280A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4308225C1 (en) * | 1993-03-16 | 1994-11-24 | Escher Wyss Gmbh | Process for sorting fiber suspension and screening device for carrying it out |
Also Published As
Publication number | Publication date |
---|---|
JPH0533280A (en) | 1993-02-09 |
FI76139B (en) | 1988-05-31 |
FI870190A0 (en) | 1987-01-19 |
DE3866116D1 (en) | 1991-12-19 |
JPS63249792A (en) | 1988-10-17 |
FI76139C (en) | 1988-09-09 |
ATE69472T1 (en) | 1991-11-15 |
DE275967T1 (en) | 1989-06-01 |
EP0275967A2 (en) | 1988-07-27 |
JPH0696834B2 (en) | 1994-11-30 |
EP0275967A3 (en) | 1989-02-08 |
CA1329333C (en) | 1994-05-10 |
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