US2674927A - Disintegrator for fibrous materials - Google Patents

Disintegrator for fibrous materials Download PDF

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US2674927A
US2674927A US208190A US20819051A US2674927A US 2674927 A US2674927 A US 2674927A US 208190 A US208190 A US 208190A US 20819051 A US20819051 A US 20819051A US 2674927 A US2674927 A US 2674927A
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pulp
container
strainer plate
vanes
rotor
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US208190A
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Wicksell Sture Valfrid
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00Methods of beating or refining; Beaters of the Hollander type
    • D21D1/20Methods of refining
    • D21D1/32Hammer mills

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  • the present invention refers to an apparatus for disintegrating and fibrating of fibrous materials such as pulp bundles, paper waste and the like in water.
  • Apparatus of this description socalled. pulp disintegrators, principally consist of a rotor serving for the circulation and the working of the pulp, a pump in the form of a rotating pump wheel, and a strainer plate arranged above the outlet from the pulp container, through which strainer plate the disintegrated pulp is sucked out and strained.
  • the present invention has for its object to increase the disintegrating capacity and the working capacity of such pulp disintegrators, and is principally distinguished by the feature that the rotor, the pump wheel, and the strainer plate are built together to form a rotating unit.
  • the vanes serving for the circulation and the working of the pulp are preferably arranged on the hub portion of'th'e rotor, while thepump wheel has a concentricallyarranged axial inlet around the hub portion, said inlet being covered by an annular strainer plate.
  • FIG. 1 represents a vertical section and Fig. 2 a plan view of the pulp disintegrator.
  • Fig. 3 shows a section through a portion of the strainer plate, representing a special embodiment of the same.
  • the rotor l is arranged at the bottom of a receptacle 2, which is intended to be filled with the material to be disintegrated and with water in a proportion of, for instance, 3.5 to of pulp.
  • a number of vanes 3 arranged in the hub portion of the rotor are arranged in the hub portion of the rotor to bring the pulp into rotation within the container while working at the same time upon the pulp and facilitating the disintegration thereof.
  • the bottom of the container is inclined and consequently brings about a vertical circulation of the pulp, guide plates 4 arranged on the cylindrical wall of the container then efiecting a deflection of the stream of pulp inwardly toward the centre of the container, where the pulp is thus caused to fiow downwardly.
  • a plane disk 5 Extending from the rotor hub is a plane disk 5 forming an attachment for a number of pump wheel vanes 6, which are disposed in an ll surrounding the rotor, said pump housing being secured in a flange 12 on the pulp container, the portion of the pump housing situated between the pump wheel and said flange then forming an annular part of the bottom of the container.
  • the strainer plate 1 is secured with its inner edge in the hub portion of the rotor, and is attached with its outer edge to the wall 8, which at the same time tightens the pump wheel against the pump housing.
  • the bottom portion M of the pump housing is tightened against the rotor shaft [6 by a stuffing box l5, and is formed as an attachment for a bearing housing I! arranged underneath the pump housing, said bearing housing I! having the shaft I6 mounted therein.
  • the rotor shaft It carries at its lower end a belt pulley 18, through which the rotor is connected to a driving motor, not shown in the drawing.
  • the pulp container is mounted on a number of posts 19, the rotor with its associated bearing housing being suspended in the pump housing I! attached to the bottom of the container.
  • the number of revolutions of the rotor is chosen difierently with respect to the nature of the material to be treated. For example, the number of revolutions may vary from 300 up to 800 revolutions per minute.
  • the vanes 3 throw the mixture of Water and pulp over the strainer plate 1, the liberated fibres will be separated to pass through the holes of the strainer plate and to be caught by the vanes 6, 9, the mixture of fibres and water being thus hurled out into the channel H3 in the pump housing, whence it is emptied into a collecting receptacle, or is returned to the pulp container 2 to be subjected to repeated treatment.
  • This outlet opens in front ment of the strainer plate 7 immediately outside the vanes 3, and through the rotary movement of the strainer plate, the latter will powerfully act upon the pulp of fibres in order thus to actuate the disintegration of the fibres in a favourable way.
  • This effect may be further increased by making the strainer plate in the manner shown in Fig. 3.
  • the strainer plate is provided on the upper side thereof with recesses or depressions arranged around the holes 29, the bottom portions of said recesses or depressions forming oblique surface 28 inclined to the walls of the holes.
  • the strainer plate may instead be channeled in a radial direction.
  • the holes themselves may be either cylindrical or conical, and in the latter case they widen to the lower side.
  • the disintegrating and working capacity of the apparatus may be increased further by making the pulp container of a polygonal configuration, for instance with 12 sides, instead of making it round, the material being then also worked upon by the walls of the container during the rotary movement of the pulp.
  • a pulp beater comprising a pulp container, a rotary impeller mounted in said container at the bottom thereof, said bottom having a circular outlet opening coaxially surrounding the impeller, a ring-shaped strainer plate covering said outlet opening and mounted to rotate together with the impeller, and a centrifugal pump wheel mounted coaxially with the impeller below said strainer plate and having an axial inlet registering with said outlet opening.
  • a pulp beater comprising a pulp container, a rotary impeller centrally mounted in said container at the bottom thereof and provided with a central hub portion carrying beating and circulating vanes, a centrifugal pump wheel forming a peripheral portion of the impeller, said peripheral portion having a circular discharge opening, a ring-shaped strainer plate covering said discharge opening and mounted on the peripheral portion of the impeller outside said heating and circulating vanes, and pump wheel vanes provided in said discharge opening below the strainer plate.

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Description

Patented Apr. 13, 1954 UNITED STATES r TNT OFFICE Sweden Application January 27, 1951, Serial No. 208,190
'7 Claims. (Cl. 92--23) The present invention refers to an apparatus for disintegrating and fibrating of fibrous materials such as pulp bundles, paper waste and the like in water. Apparatus of this description, socalled. pulp disintegrators, principally consist of a rotor serving for the circulation and the working of the pulp, a pump in the form of a rotating pump wheel, and a strainer plate arranged above the outlet from the pulp container, through which strainer plate the disintegrated pulp is sucked out and strained.
The present invention has for its object to increase the disintegrating capacity and the working capacity of such pulp disintegrators, and is principally distinguished by the feature that the rotor, the pump wheel, and the strainer plate are built together to form a rotating unit. Here, the vanes serving for the circulation and the working of the pulp are preferably arranged on the hub portion of'th'e rotor, while thepump wheel has a concentricallyarranged axial inlet around the hub portion, said inlet being covered by an annular strainer plate. This constructively simple arrangementof said parts relatively to each other brings the advantage that the strainer plate rotates, merging closely to the vanes, so as to attain, in consequence thereof, a powerfully disintegrating effect on the material.
The invention will be described more closely with reference to the accompanying drawings,
' which illustrate a form of embodiment of a pulp disintegrator constructed in accordance with the invention. Fig. 1 represents a vertical section and Fig. 2 a plan view of the pulp disintegrator. Fig. 3 shows a section through a portion of the strainer plate, representing a special embodiment of the same.
The rotor l is arranged at the bottom of a receptacle 2, which is intended to be filled with the material to be disintegrated and with water in a proportion of, for instance, 3.5 to of pulp. Arranged in the hub portion of the rotor are a number of vanes 3 adapted to bring the pulp into rotation within the container while working at the same time upon the pulp and facilitating the disintegration thereof. The bottom of the container is inclined and consequently brings about a vertical circulation of the pulp, guide plates 4 arranged on the cylindrical wall of the container then efiecting a deflection of the stream of pulp inwardly toward the centre of the container, where the pulp is thus caused to fiow downwardly. Extending from the rotor hub is a plane disk 5 forming an attachment for a number of pump wheel vanes 6, which are disposed in an ll surrounding the rotor, said pump housing being secured in a flange 12 on the pulp container, the portion of the pump housing situated between the pump wheel and said flange then forming an annular part of the bottom of the container. The strainer plate 1 is secured with its inner edge in the hub portion of the rotor, and is attached with its outer edge to the wall 8, which at the same time tightens the pump wheel against the pump housing. The plate,
which may be plane or conical, is also supported by the vanes 6, to which it is preferably also secured. Screwed onto the part of the pump housing I! located on a level with the bottom of the container is a scraper I3 extending over the strainer plate and preventing the fibrous pulp from sticking to the plate.
The bottom portion M of the pump housing is tightened against the rotor shaft [6 by a stuffing box l5, and is formed as an attachment for a bearing housing I! arranged underneath the pump housing, said bearing housing I! having the shaft I6 mounted therein. The rotor shaft It carries at its lower end a belt pulley 18, through which the rotor is connected to a driving motor, not shown in the drawing. The pulp container is mounted on a number of posts 19, the rotor with its associated bearing housing being suspended in the pump housing I! attached to the bottom of the container.
The number of revolutions of the rotor is chosen difierently with respect to the nature of the material to be treated. For example, the number of revolutions may vary from 300 up to 800 revolutions per minute. When the vanes 3 throw the mixture of Water and pulp over the strainer plate 1, the liberated fibres will be separated to pass through the holes of the strainer plate and to be caught by the vanes 6, 9, the mixture of fibres and water being thus hurled out into the channel H3 in the pump housing, whence it is emptied into a collecting receptacle, or is returned to the pulp container 2 to be subjected to repeated treatment. Through the arrange This outlet opens in front ment of the strainer plate 7 immediately outside the vanes 3, and through the rotary movement of the strainer plate, the latter will powerfully act upon the pulp of fibres in order thus to actuate the disintegration of the fibres in a favourable way. This effect may be further increased by making the strainer plate in the manner shown in Fig. 3. The strainer plate is provided on the upper side thereof with recesses or depressions arranged around the holes 29, the bottom portions of said recesses or depressions forming oblique surface 28 inclined to the walls of the holes. If desired, the strainer plate may instead be channeled in a radial direction. The holes themselves may be either cylindrical or conical, and in the latter case they widen to the lower side.
On account of the rotary movement of the strainer plate, the latter keeps purer than is the case in known constructions, where the strainer is stationary and a rotating scraper must be used to keep the plate clean. In an arrangement according to the present invention, no scraper is normally required, a scraper being made use of only in cases more or less severe.
The disintegrating and working capacity of the apparatus may be increased further by making the pulp container of a polygonal configuration, for instance with 12 sides, instead of making it round, the material being then also worked upon by the walls of the container during the rotary movement of the pulp.
I claim:
1. A pulp beater comprising a pulp container, a rotary impeller mounted in said container at the bottom thereof, said bottom having a circular outlet opening coaxially surrounding the impeller, a ring-shaped strainer plate covering said outlet opening and mounted to rotate together with the impeller, and a centrifugal pump wheel mounted coaxially with the impeller below said strainer plate and having an axial inlet registering with said outlet opening.
2. A pulp beater as claimed in claim 1, wherein the impeller has a hub portion carrying beating and circulating vanes at the top thereof and vanes of the pump wheel at its peripheral portion beneath the strainer plate.
3. A pulp beater as claimed in claim 1, wherein the strainer plate is supported by the vanes of the pump wheel.
4. A pulp beater comprising a pulp container, a rotary impeller centrally mounted in said container at the bottom thereof and provided with a central hub portion carrying beating and circulating vanes, a centrifugal pump wheel forming a peripheral portion of the impeller, said peripheral portion having a circular discharge opening, a ring-shaped strainer plate covering said discharge opening and mounted on the peripheral portion of the impeller outside said heating and circulating vanes, and pump wheel vanes provided in said discharge opening below the strainer plate.
5. A pulp beater as claimed in claim 4, wherein the impeller is rotatably mounted in a pump housing secured to the bottom of the pulp container and containing an outlet channel communicating with the discharge opening of the impeller.
6. A pulp beater as claimed in claim 4, wherein the impeller and the strainer plate form a central rotary part of the bottom of the pulp container.
7. A pulp beater as claimed in claim 4, wherein the strainer plate is provided on the upper side thereof with recesses or depressions arranged around the holes in the plate.
References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 34,581 Lyman Mar. 4, 1862 2,351,728 Wells June 20, 1944 2,557,174 Cowles June 19, 1951 FOREIGN PATENTS Number Country Date 564,554 Germany Nov. 19, 1932
US208190A 1951-01-27 1951-01-27 Disintegrator for fibrous materials Expired - Lifetime US2674927A (en)

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2954174A (en) * 1957-06-19 1960-09-27 Bolton John W & Sons Inc Batch pulper
US2956753A (en) * 1958-12-12 1960-10-18 Georgia Kaolin Co Clay mixer and blunger
US2973153A (en) * 1958-05-16 1961-02-28 Improved Machinery Inc Pulper
US3154255A (en) * 1961-03-01 1964-10-27 Amberley Co Method of reclaiming cellulsoe fibers from thermoplastic coated cellulosic webs
US3380669A (en) * 1966-04-11 1968-04-30 Black Clawson Co Plural defibering zones in a pulping apparatus
US3565350A (en) * 1968-05-20 1971-02-23 Wascon Systems Inc Comminuting apparatus
US3774853A (en) * 1972-01-26 1973-11-27 Black Clawson Fibreclaim Inc Pulping apparatus for waste material
US3814334A (en) * 1971-07-26 1974-06-04 F Funk Colloid mill
CN104372706A (en) * 2013-08-12 2015-02-25 苏州维艾普新材料股份有限公司 Glass wool pulping device with guide spirals inside

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US34581A (en) * 1862-03-04 Azel stores lyman
DE564554C (en) * 1929-05-18 1932-11-19 Anton D J Kuhn Aufloese-Hollaender
US2351728A (en) * 1942-08-08 1944-06-20 Wells Harold Donald Continuous beater and pulp selector
US2557174A (en) * 1949-01-26 1951-06-19 Cowles Co Apparatus for pulping paper stock

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US34581A (en) * 1862-03-04 Azel stores lyman
DE564554C (en) * 1929-05-18 1932-11-19 Anton D J Kuhn Aufloese-Hollaender
US2351728A (en) * 1942-08-08 1944-06-20 Wells Harold Donald Continuous beater and pulp selector
US2557174A (en) * 1949-01-26 1951-06-19 Cowles Co Apparatus for pulping paper stock

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2954174A (en) * 1957-06-19 1960-09-27 Bolton John W & Sons Inc Batch pulper
US2973153A (en) * 1958-05-16 1961-02-28 Improved Machinery Inc Pulper
US2956753A (en) * 1958-12-12 1960-10-18 Georgia Kaolin Co Clay mixer and blunger
US3154255A (en) * 1961-03-01 1964-10-27 Amberley Co Method of reclaiming cellulsoe fibers from thermoplastic coated cellulosic webs
US3380669A (en) * 1966-04-11 1968-04-30 Black Clawson Co Plural defibering zones in a pulping apparatus
US3565350A (en) * 1968-05-20 1971-02-23 Wascon Systems Inc Comminuting apparatus
US3814334A (en) * 1971-07-26 1974-06-04 F Funk Colloid mill
US3774853A (en) * 1972-01-26 1973-11-27 Black Clawson Fibreclaim Inc Pulping apparatus for waste material
CN104372706A (en) * 2013-08-12 2015-02-25 苏州维艾普新材料股份有限公司 Glass wool pulping device with guide spirals inside

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