JPH01266291A - Apparatus for crushing or pulverizing fibrous material - Google Patents

Apparatus for crushing or pulverizing fibrous material

Info

Publication number
JPH01266291A
JPH01266291A JP63278576A JP27857688A JPH01266291A JP H01266291 A JPH01266291 A JP H01266291A JP 63278576 A JP63278576 A JP 63278576A JP 27857688 A JP27857688 A JP 27857688A JP H01266291 A JPH01266291 A JP H01266291A
Authority
JP
Japan
Prior art keywords
crushing
rotor
axis
housing
drum
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
JP63278576A
Other languages
Japanese (ja)
Other versions
JPH0429791B2 (en
Inventor
Emmerich Bernhard
エメリッヒ・ベルンハルト
Johann Lileg
ヨハン・リレグ
Johannes Kappel
ヨハネス・カペル
Dag Bergloff
ダク・ベルクロフ
Bernhard Rebernik
ベルンハルト・レベルニク
Sven-Erik Henriksson
スヴェン‐エリック・ヘンリクソン
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.)
Andritz AG
Original Assignee
Andritz AG
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
Application filed by Andritz AG filed Critical Andritz AG
Publication of JPH01266291A publication Critical patent/JPH01266291A/en
Publication of JPH0429791B2 publication Critical patent/JPH0429791B2/ja
Granted legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/14Disintegrating in mills
    • 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
    • D21D1/22Jordans

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)
  • Disintegrating Or Milling (AREA)
  • Crushing And Pulverization Processes (AREA)
  • Crushing And Grinding (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

PURPOSE: To decrease the stress to a material by installing a crushing and grinding surfaces extending nearly parallel to a rotor axis line and the opposing crushing and grinding surface arranged on the housing, on a rotor jacket between a material feed and the crushing and grinding surface having increasing diameters. CONSTITUTION: A grinding plate 6 of a rotor 2 is arranged along a cylindrical jacket part of a housing 1 to crush chips previously. A grinding plate 7 of the rotor forms 5-45 deg. angle to an axis line of the rotor for defabrication. The grinding plate 9 cooperating with and facing to the grinding plate 7 is installed on a stator ring 8 for regulating the grinding gap so as to be horizontally freely moved. Chips are fed by a material feed 10 in the radial direction, and previously ground at a grinding gap 11. The previously ground chips are symmetrically dispersed in both directions, and the dispersed chips are transferred through a grinding gap 1 to an inner space 13 and discharged with generated steam.

Description

【発明の詳細な説明】 本発明は繊維質材料特に湿った又は水を混ぜた繊維質材
料好適にはチップを破砕又は粉砕するための装置に関し
、詳細に・はドラム形微細化装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for crushing or crushing fibrous materials, particularly wet or aqueous fibrous materials, preferably chips, and in particular to a drum-shaped atomization apparatus. be.

この微細化装置は少なくとも2つの破砕又は粉砕素子を
もつモータ駆動されるロータを存し、前記素子の表面、
好適には回転面、特に円錐台形の面がロータ軸線に対し
て傾き又はそれに対してほぼ直角に延在し、その直径が
少なくとも1つの材料供給手段から離れる方向に増大し
、好適には水平の回転シャフトとロータを受入れるハウ
ジングとをもち、このハウジングが対応する内壁とその
上に配置した向合う破砕又は粉砕面をもちロータ軸線に
対してほぼ径方向の又はロータジャケット又はハウジン
グに対してほぼ接線方向の少なくとも1つの材料供給手
段がほぼ前記ハウジングの中心にあり、破砕又は粉砕面
がロータのジャケット上にそしてそれに対応して傾斜し
た又はほぼ直角に延在する面、好適には回転面特に円錐
台形の面上の内部ハウジング壁上に両側において材料供
給手段から延在し、前記円錐台形の面の直径は材料供給
手段から離れるにつれて増大し、前記円錐台形面はロー
タ軸線と両側でロータの正面に開く成る角度をなす。
The atomization device comprises a motor-driven rotor having at least two crushing or grinding elements, the surface of said elements being
Preferably, the surface of rotation, in particular a frustoconical surface, is inclined to the rotor axis or extends approximately at right angles thereto, the diameter of which increases in the direction away from the at least one material supply means, preferably horizontal a rotating shaft and a housing for receiving the rotor, the housing having a corresponding inner wall and opposing crushing or crushing surfaces disposed thereon substantially radially to the rotor axis or substantially tangential to the rotor jacket or housing; The at least one material feeding means in the direction is approximately centered in said housing and the crushing or comminution surface is a surface, preferably a rotating surface, in particular a conical surface, extending on the jacket of the rotor and correspondingly inclined or approximately at right angles. extending from the material supply means on both sides on the inner housing wall on a trapezoidal surface, the diameter of said frustoconical surface increasing away from the material supply means, said frustoconical surface extending from the rotor axis and in front of the rotor on each side; It forms an angle that opens up.

木材バルブを機械的に生産するのに現在使用される大部
分の微細化装置は一般に水平軸線の回りに回転しかつ粉
砕板を有するディスクをもつ。粉砕板を有するこのディ
スクと同じ向合うディスクは回転するか又は不動とする
。この既知の例では、粉砕ギャップの全体又はその大部
分が垂直に延在するか又は周辺領域で回転軸線に向って
傾斜する。
Most atomization equipment currently used to mechanically produce wood valves generally has a disk that rotates about a horizontal axis and has a grinding plate. This disk and the same opposite disk with the grinding plate may be rotating or stationary. In this known example, the entire grinding gap or a large part thereof extends vertically or is inclined in the peripheral region towards the axis of rotation.

粉砕板の高接触圧力が、粉砕作業に要求されるので、上
記既知の例では過大な応力が材料に、及び何よりも先ず
軸受に加わる。これは微細化装置の最大の許容処理量が
限定されることを意味する。
Since high contact pressures of the grinding plates are required for the grinding operation, excessive stresses are applied in the known example to the material and first of all to the bearings. This means that the maximum allowable throughput of the miniaturization device is limited.

この結果高い機械的エネルギーを使用すれば、主として
湿った又は湿気の多い材料又は水の混ざった材料が破砕
又は粉砕されるので、粉砕ギャップに大量の蒸気が発生
する。エネルギーの良好な利用又は回収及びチップ等の
妨害のない装入を行うためには、゛作られた又は回収さ
れた繊維材料と共に蒸気を適切に排出する必要があるが
、このことは発生する蒸気量が大量であるため実施が困
難である。特に普通のディスク形微細化装置においては
粉砕ギャップを垂直配置とするのが困難である。
As a result of the high mechanical energy used, a large amount of steam is generated in the grinding gap, since mainly wet or humid material or water-admixed material is crushed or crushed. For good utilization or recovery of energy and unhindered charging of chips etc., it is necessary to properly vent the steam together with the fiber material produced or recovered; It is difficult to implement due to the large amount. In particular, it is difficult to achieve a vertical arrangement of the grinding gap in conventional disk-type atomizers.

それは繊維質材料の部分的分離と発生蒸気の強力な逆流
を生じるからである。
This is because it results in partial separation of the fibrous material and a strong backflow of the generated steam.

本発明の目的は、材料の応力を減少させ、材料処理量を
増大させ、ロータ又はシャフトの毎分当たりの回転数を
増大させ、蒸気発生と蒸気排出の問題点を改善すること
にある。
The object of the invention is to reduce material stress, increase material throughput, increase the number of revolutions per minute of the rotor or shaft, and improve the problems of steam generation and steam discharge.

上記目的は本文冒頭で述べた型式の破砕又は粉砕装置又
は微細化装置において本発明により達成することができ
る。この本発明装置は材料供給手段と増大する直径の破
砕又は粉砕面の間にドラム形ロータのジャケット上にロ
ータ軸線とほぼ平行に延在する破砕又は粉砕面と、ハウ
ジング上に配置した向合う破砕又は粉砕面を設け、前記
軸線と平行な粉砕ギャップと前記軸線に対して傾斜した
粉砕ギャップを形成し、これらは少なくとも1つの、好
適には2つ以上の材料供給手段の中央平面に対して対称
的に配置し、前記供給手段は好適にはロータ円周上に特
にほぼ径方向又は接線方向に一様に分布させ、軸線と平
行な破砕又は粉砕面は特に円錐台形破砕又は粉砕面によ
って直ちに特に一定に合併状に追従され、円錐台形粉砕
面はロータ軸線に向ってほぼ5乃至45度の角度、特に
15度だけ傾いており、前記傾いた破砕又は粉砕面は任
意に合併する破砕又は粉砕面によって直ちに、特に一定
に追従され、これらの粉砕面はロータ軸線に対して前記
の傾斜した破砕又は粉砕面の角度より大きな傾斜角度、
特にほぼ90度の角度をなす。
The above object can be achieved according to the invention in a crushing or grinding device or a micronization device of the type mentioned at the beginning of the text. The device of the invention comprises a crushing or crushing surface extending substantially parallel to the rotor axis on the jacket of a drum-shaped rotor between the material supply means and a crushing or crushing surface of increasing diameter, and an opposing crushing surface arranged on the housing. or a grinding surface is provided, forming a grinding gap parallel to said axis and a grinding gap oblique to said axis, which are symmetrical with respect to the central plane of at least one, preferably two or more, material supply means. , said feeding means are preferably uniformly distributed over the circumference of the rotor, in particular substantially radially or tangentially, and the crushing or comminution surfaces parallel to the axis are immediately particularly The frustoconical crushing surfaces, which follow a constant merging pattern, are inclined toward the rotor axis by an angle of approximately 5 to 45 degrees, in particular by 15 degrees, said inclined crushing or crushing surfaces being optionally merging crushing or crushing surfaces. These grinding surfaces have an angle of inclination greater than the angle of said inclined grinding or grinding surfaces relative to the rotor axis;
In particular, it forms an angle of approximately 90 degrees.

本発明による粉砕面は特に有効なデファイブレーシゴン
を保証し、同時に蒸気排出、材料応力の減少、軸受応力
の減少、材料処理量の増大、毎分当り回転数の増大を促
進し、軸線と平行な粉砕ギャップ内で材料を予備粉砕し
、前記粉砕ギャップを軸線に対して傾いた粉砕ギャップ
へ特別に変えて粉砕作業を特別に容易にすることができ
る。向合う粉砕面を互いに独立して移動自在の1つ又は
2つのステー°タリング上に配置することによって粉砕
作業は一層容易にな、る。本発明の微細化装置は特にT
MP (熱機械的バルブ)とCTMP (化学灼熱機械
的パルプ)の生産に適する。本発明によれば、好適には
前取て水平の粉砕ギャップ内で予備粉砕された径方向に
供給されるギャップ等を2方向に対称的に分散させ、木
材等の特に有効なデフアイブレーションを隣接して傾斜
した、好適には調節自在に傾斜した特に円錐形の粉砕ギ
ャップ内で行うことができる。このギャップは任意にロ
ータ軸線に対してほぼ直角に延在し、蒸気の排出を更に
促進する。
The grinding surface according to the invention guarantees a particularly effective defibration and at the same time facilitates steam evacuation, reduced material stresses, reduced bearing stresses, increased material throughput, increased revolutions per minute and The material can be pre-comminuted in parallel comminution gaps and the comminution gaps can be specifically transformed into comminution gaps oblique to the axis to make the comminution operation particularly easy. The grinding operation is made easier by arranging the opposing grinding surfaces on one or two stator rings that are movable independently of each other. The micronization device of the present invention is particularly suitable for T
Suitable for producing MP (thermo-mechanical pulp) and CTMP (chemically fired mechanical pulp). According to the present invention, the gap etc. which are supplied in the radial direction of the pre-pulverized material preferably in the pre-horizontal crushing gap are distributed symmetrically in two directions, thereby achieving particularly effective differential isolation of wood and the like. This can take place in an adjacently inclined, preferably adjustable, in particular conical grinding gap. This gap optionally extends approximately perpendicular to the rotor axis to further facilitate steam evacuation.

軸線に対して傾斜又は直角に延在する粉砕キャップを調
節自在とすれば、特に計量を制御することができる。こ
のために例えば向合う破砕又は粉砕面をステータリング
、特に少なくとも2つのステータリングに設ける。これ
らのリングはハウジング内で互いに独立してほぼ水平に
移動自在に配置する。粉砕ギャップはバルブの性質の制
御に重要である。
The metering can be particularly controlled if the grinding cap, which extends obliquely or at right angles to the axis, is adjustable. For this purpose, for example, opposing crushing or grinding surfaces are provided on the stator ring, in particular on at least two stator rings. These rings are arranged to be movable substantially horizontally within the housing, independent of each other. The grinding gap is important in controlling the properties of the valve.

粉砕ギャップの便利な調節は、もし唯1つの移動自在の
ステータリングを設けた場合にはロータをその軸受内で
両側において移動自在に、特に浮動状に支持することに
よって行う。この浮動状に支持するためにロータは好適
には静水圧式摺動軸受中に軸線方向に移動自在に支持し
、封止ユニット特に摺動リングシールが前記摺動軸受と
ロータを受入れるハウジング内部の間の軸受ハウジング
中でロータシャフトを取囲む。もし環状の材料供給ギャ
ップを設ければ材料供給を特に便利に行なうことができ
る。この供給ギャップはハウジング内でロータ外側を囲
む環状スペースに連絡し、特にほぼ接線方向の又はほぼ
径方向の材料供給手段が前記スペースに送入し、前記供
給ギャップは軸線と平行な破砕又は粉砕面間でほぼ該装
置又はそのハウジングの軸と交差する中央平面内に設け
る。
A convenient adjustment of the grinding gap is achieved if only one movable stator ring is provided, by supporting the rotor movably, in particular floatingly, on both sides in its bearings. For this floating support, the rotor is preferably axially movably supported in a hydrostatic sliding bearing, and a sealing unit, in particular a sliding ring seal, is provided between said sliding bearing and the interior of the housing receiving the rotor. encloses the rotor shaft in a bearing housing. Material feeding can be carried out particularly conveniently if an annular material feeding gap is provided. This feed gap communicates in the housing with an annular space surrounding the outside of the rotor, and in particular substantially tangential or substantially radial material feed means feed into said space, said feed gap being a crushing or comminution surface parallel to the axis. approximately in a midplane intersecting the axis of the device or its housing.

本発明の他の実施例では、特に円錐形の又は直角に延在
する破砕又は粉砕ギャップが装入する空洞を2つのハウ
ジング正面壁の領域に、ロータのシャフト軸受に接近し
て設け、軸線と平行な及びほぼ軸線、と直角に延在する
破砕又は粉砕面を備える。粉砕素材は装置特に微細化装
置のハウジングの内部スペースに運ばれ、発生した蒸気
と一緒に排出される。こうして蒸気の排出は而単になり
、又は蒸気排出手段が作られる。蒸気が発生するため、
前記空洞は特別の封止ユニットによって2つの軸受内に
蒸気が侵入しないように封止する。封止ユニットはロー
タとロータ側の軸受ハウジング中の軸受との間に挿入す
る。これらの空洞は好適には粉砕された材料用の排出開
口を底部に備える。
In a further embodiment of the invention, the cavities into which the crushing or crushing gaps, in particular conical or perpendicularly extending, are inserted, are provided in the region of the two front walls of the housing, close to the shaft bearing of the rotor, so that they are aligned with the axis. It comprises a crushing or comminution surface extending parallel and substantially perpendicular to the axis. The ground material is conveyed into the interior space of the housing of the device, in particular the atomization device, and is discharged together with the generated steam. In this way, the evacuation of the steam becomes simple or a means of evacuation of the steam is created. Because steam is generated,
The cavity is sealed against the ingress of steam into the two bearings by means of a special sealing unit. The sealing unit is inserted between the rotor and the bearing in the rotor-side bearing housing. These cavities are preferably provided at the bottom with discharge openings for the ground material.

実際上、もしドラム形ロータを摺動軸受に支持すれば特
に好適である。このロータはそのジャケット上にほぼ軸
線と平行に延在する破砕又は粉砕面と両側に隣接した破
砕又は粉砕面を備え、後者の粉砕面は材料供給手段から
離れるにつれて増大する直径をもち、更にロータ軸線に
対してほぼ直角に延在する破砕又は粉砕面を備える。前
記ロータはそれに固定した回転シャフトによって前記軸
受に支持する。特別の始動モータ、特に直流モータは始
動操作用に設け、主モータは全負荷において約3000
乃至3600rpmで運転するように構成する。
In practice, it is particularly advantageous if the drum-shaped rotor is supported on sliding bearings. The rotor has on its jacket a crushing or crushing surface extending substantially parallel to the axis and adjacent crushing or crushing surfaces on both sides, the latter crushing surfaces having a diameter increasing away from the material supply means, and It has a crushing or grinding surface extending substantially perpendicular to the axis. The rotor is supported on the bearing by a rotating shaft fixed thereto. A special starting motor, especially a DC motor, is provided for starting operations, and the main motor has a power rating of approximately 3000 at full load.
It is configured to operate at a speed of 3,600 rpm to 3,600 rpm.

この始動モータはステータシャフトの遊端に設ける。そ
れは主モータが破砕又は粉砕面特に微細化装置の運転に
要する出力よりもかなり低い出力を必要とする。従って
始動電流ピークは減少する。
This starting motor is provided at the free end of the stator shaft. It requires a considerably lower power than that required by the main motor to operate the crushing or comminution surface, especially the atomization device. The starting current peak is therefore reduced.

本発明による微細化装置等の実施例は大形のこの種装置
を360Orpmまでの回転数で運転可能となす。
Embodiments of the micronization device according to the present invention allow large-sized devices of this type to be operated at rotational speeds up to 360 rpm.

軸線と平行に延在する粉砕ギャップに隣接する円錐台形
粉砕ギャップの代わりに他の回転面をもつ形状のギャッ
プを使用できる。例えば回転放物面、回転双曲面等の形
状を使用できるが、これらの面の直径は特に一定に、軸
線と平行に延在する粉砕面との接合点からロータ正面ま
で増大して、目的とする材料を確実に通過せしめる必要
がある。
Instead of a truncated conical grinding gap adjacent to the grinding gap extending parallel to the axis, gaps of other rotational surface shapes can be used. For example, shapes such as paraboloids of revolution, hyperboloids of revolution, etc. can be used, the diameter of these surfaces increasing in a particularly constant manner from the point of contact with the grinding surface extending parallel to the axis to the front of the rotor to achieve the objective. It is necessary to ensure that the material that will be used passes through.

既知の微細化装置では、円錐形耳軸がその周辺に可変長
さの破砕棒を備え、ハウジングの円錐形内部スペース内
に配置され、前記ハウジングの内壁が対応する向合う棒
を備えて1乃至21TII!lの粉砕ギャップを作るよ
うにする。材料供給は耳軸シャフトの領域内で該装置の
一例において行う。この微細化装置の生産量は、材料供
給を片側のみからそして直ちにシャフト上へ行って直接
に円錐形粉砕ギャップ内へ入れるため、不満足である。
In the known atomization device, a conical ear shaft is provided with a crushing rod of variable length around its periphery and is arranged in a conical internal space of a housing, the inner wall of said housing being provided with corresponding opposing rods. 21TII! A grinding gap of l is created. Material feeding takes place in one example of the device in the region of the auricular shaft. The output of this atomization device is unsatisfactory because the material feed is from one side only and immediately onto the shaft and directly into the conical grinding gap.

満足なデフアイブレーションも適切なバルブ生成効果も
得られない。この装置は既知の円錐形微細化装置と同じ
寸法で使用される。
Neither satisfactory differential isolation nor appropriate valve generation effects can be obtained. This device is used with the same dimensions as known conical refiners.

既知のマイクロアトマイザ−においては粉砕素材はスク
リューコンベヤによって1部から分離羽根車の軸線と平
行に延在するホランダーの中心へ供給される。ホランダ
ーは前記軸線と平行なギャップを形成し、ハウジングが
前記羽根車を受入れ、この羽根車はその内壁に小さな切
欠きをもつ。その平行ギャップ内で粉砕される粉砕素材
は外側から内側へ粉砕域から空気流によって運ばれ、そ
の過程で前記分離羽根車を通過する。分離された粗粒の
粉砕物質は粉砕域へ戻される。粉砕シャフトの両側の2
つの送風車が必要な空気流を作る。この既知装置は軸線
と平行な粉砕ギャップに隣接した円錐形粉砕ギャップ等
が存在しないことを別にしても、チップ又は他の湿った
繊維質材料を処理するのには適していない。
In known microatomizers, the ground material is fed by means of a screw conveyor from one part to the center of a hollander extending parallel to the axis of the separating impeller. The hollander forms a gap parallel to the axis and a housing receives the impeller, which has a small cutout in its inner wall. The ground material that is ground in the parallel gap is carried by an air stream from the grinding zone from the outside to the inside and passes through the separating impeller in the process. The separated coarse grinding material is returned to the grinding zone. 2 on both sides of the grinding shaft
Two blowers create the necessary airflow. Apart from the absence of a conical grinding gap or the like adjacent to the grinding gap parallel to the axis, this known device is not suitable for processing chips or other wet fibrous materials.

以下、チップから木材パルプを生産するドラム形微細化
装置の本発明の実施例を図につき詳述する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In the following, embodiments of the present invention of a drum-shaped refining device for producing wood pulp from chips will be described in detail with reference to the drawings.

第1〜5図は好適には水平分割される微細化装置ハウジ
ング1を示し、この中で円筒形ロータ2の両側を軸受3
,4.5上に支持し、転がり又は摺動軸受、特に傾斜セ
グメントをもった摺動軸受を直径、容量及び毎分当りの
回転数に応じて使用する。ロータ2は粉砕ギャップ6.
7をもち、粉砕板6をハウジングの円筒形ジャケット部
に沿って配置してチップを予備粉砕し、粉砕板7はデフ
アイブレーション用のロータの軸線と成る角度をなす。
1 to 5 show a micronizer housing 1, preferably horizontally split, in which a cylindrical rotor 2 is mounted on both sides by bearings 3.
, 4.5 and use rolling or sliding bearings, in particular sliding bearings with inclined segments, depending on the diameter, capacity and revolutions per minute. The rotor 2 has a crushing gap 6.
7, and a grinding plate 6 is placed along the cylindrical jacket of the housing to pre-crush the chips, the grinding plate 7 being angled with the axis of the defibration rotor.

粉砕板7を作るため粉砕域と水平線のなす傾斜は5度乃
至45度間の角度、好適には15度とする。粉砕板7と
協働する向合う粉砕板9,9′は粉砕ギャップ調節のた
め水平移動自在にステータリング8上に設ける。
To create the grinding plate 7, the angle between the grinding zone and the horizontal line is between 5 degrees and 45 degrees, preferably 15 degrees. Opposite crushing plates 9, 9' cooperating with crushing plate 7 are mounted on stator ring 8 so as to be horizontally movable for adjusting the crushing gap.

第3.4図は粉砕板領域の拡大横断面を示し、第3図は
軸線と平行な領域を、第4図は円錐台領域を示す。第4
図に示すように、外部粉砕板9の向合うリング17は横
ウェブ又は横リブ18によって補強する。ウェブ又はリ
ブ18は繊維材料を保持するために備え、粉砕域内の滞
在時間を増すことができる。円錐台領域の内部粉砕板7
はセグメント7′から作る(第4図)。特に実用的な上
記実施例の寸法は第5図に示すが、この図には横リプ1
8は一部のみを示している。
3.4 shows an enlarged cross section of the grinding plate area, FIG. 3 the area parallel to the axis and FIG. 4 the truncated conical area. Fourth
As shown, the opposing rings 17 of the external grinding plate 9 are reinforced by transverse webs or ribs 18. Webs or ribs 18 may be provided to retain the fibrous material and increase residence time within the grinding zone. Internal crushing plate 7 in the truncated cone area
is made from segment 7' (Fig. 4). The dimensions of the particularly practical embodiment described above are shown in FIG.
8 shows only a part.

チップは特にコンベヤスクリューによって供給し、この
実施例では周囲に開口をもつ1個乃至4個の材料送り手
段10によって径方向に送られる。
The chips are fed in particular by a conveyor screw, which in this example is radially fed by one to four material feed means 10 with peripheral openings.

チップは水平粉砕ギャップ11内で予備破砕し、両方向
に対称的に分散させる。木材のデフアイブレーションは
水平線に対して傾いた調節自在の粉砕ギャップ12内で
行う。次に粉砕素材は微細化装置のハウジング1の内部
スペース13へ運ばれて、発生蒸気と共に排出される。
The chips are pre-crushed in the horizontal grinding gap 11 and distributed symmetrically in both directions. The defibration of the wood takes place in an adjustable grinding gap 12 tilted to the horizontal. The ground material is then conveyed to the internal space 13 of the housing 1 of the atomizer and discharged together with the generated steam.

軸線は封止ユニット15によって前記ハウジング内の蒸
気に対して密封する。
The axis is sealed against steam in the housing by means of a sealing unit 15.

シャフト遊端16において、モータ、好適には主モータ
より出力が相当小さい直流モータを設けて始動電流ピー
クを減少させる。
At the free end of the shaft 16, a motor is provided, preferably a DC motor with considerably less power than the main motor, to reduce starting current peaks.

従来の微細化装置に比して変更された本実施例により本
発明の微細化装置は3600 rpmまでの回転数で運
転できる。
Due to this embodiment, which is modified compared to conventional atomizers, the atomizer of the present invention can be operated at rotational speeds up to 3600 rpm.

本発明は垂直のロータシャフトをもつ微細化装置にを利
に適用できる。木材以外の繊維材料を簡単に粉砕でき、
水その他の液体を成る条件下で予備破砕した材料に加え
る。
The present invention can be advantageously applied to a micronization device having a vertical rotor shaft. Can easily crush fiber materials other than wood,
Adding water or other liquid to the pre-crushed material under the following conditions:

本発明によれば、既知の微細化装置に比して材料の応力
がかなり減少し、軸受に加わる応力が減少し、軸受の使
用寿命が長(なる。この結果、材料処理量が増大する。
According to the present invention, material stresses are significantly reduced compared to known micronization devices, the stress on the bearing is reduced, and the service life of the bearing is extended (resulting in increased material throughput).

第6〜8図の実施例は特に供給材料の種類、ロータの特
殊な支持及び変更されたステータ調節において前述の実
施例とは異なる。対応する部品には第1〜5図と同じ数
字を付している。
The embodiment of FIGS. 6-8 differs from the previous embodiments, inter alia in the type of feed material, the special support of the rotor and the modified stator adjustment. Corresponding parts are labeled with the same numbers as in FIGS. 1-5.

この実施例では、材料供給はロータ102に対してほぼ
接線方向に2つの場所で110′において環状スペース
110#内へ行い、次いでここから材料は粉砕板へ運ば
れる。ロータ102のシャフト端116′、従ってロー
タ102自体はこの場合浮動状に支持される。そのよう
に支持するため、静水圧式摺動軸受203.204を軸
受201.202中に設ける。これらの軸受も封止ユニ
ッl−115’によって微細化装置のハウジング101
内で蒸気に対して密封する。
In this embodiment, the material feed takes place approximately tangentially to the rotor 102 at two locations 110' into the annular space 110#, from where it is then conveyed to the grinding plate. The shaft end 116' of the rotor 102, and thus the rotor 102 itself, is in this case supported in a floating manner. For such support, hydrostatic sliding bearings 203, 204 are provided in bearings 201, 202. These bearings are also connected to the housing 101 of the miniaturization device by the sealing unit l-115'.
sealed against steam inside.

二重矢印205はロータの前述の支持手段によって可能
にされるロータの移動又は浮動状のロータ支持を示す。
The double arrow 205 indicates the movement of the rotor or the floating rotor support made possible by the aforementioned support means for the rotor.

この場合唯1つのステークが調節できれば十分であり、
同様に両ステータ1,1′の、従ってこれらに取付けた
粉砕板206.207の調節がこの場合可能である。こ
れらの粉砕板は円錐台形の部品206.207に加えて
、ロータ軸線との間に部品208.209よりも大きな
角度、即ちほぼ90度の角度をなす部品210.211
をもつ。部品210.211と協働する追加の粉砕板2
12.213は部品210.211と同様にロータ軸線
に対して急勾配をなし、ロータ102に連結された特別
なリング214.215によって支持される。
In this case it is sufficient that only one stake can be adjusted,
Adjustment of the two stators 1, 1' and thus of the grinding plates 206, 207 attached to them is likewise possible in this case. These grinding plates, in addition to truncated conical parts 206, 207, have parts 210, 211 which form a larger angle with the rotor axis than parts 208, 209, i.e. approximately 90 degrees.
have. Additional grinding plate 2 cooperating with parts 210.211
12.213, like the part 210.211, has a steep slope to the rotor axis and is supported by a special ring 214.215 connected to the rotor 102.

ステータ1,1′の、従って粉砕板206.207゜2
10、211の調節、及び円筒形粉砕板の調節も部品3
〜5によって第1〜5図に示すものと同様にして行うが
、この場合は調節手段7〜9によって一様に移動させら
れる彎曲フープ218によって反対方向に同時に行われ
る。浮動状に支持したロータのために、唯1つのステー
タの調節を同様に行うことができる。そのとき第二のス
テータはハウジング内に固定支持される。粉砕ギャップ
の調節移動はロータの軸線方向の自由移動性(浮動支持
)によって可能にされる。
of the stator 1, 1' and hence the crushing plate 206.207°2
10, 211 and the adjustment of the cylindrical crushing plate are also part 3.
1 to 5, but in this case simultaneously in opposite directions by the curved hoop 218, which is moved uniformly by the adjustment means 7 to 9. Due to the floating rotor, adjustment of only one stator can be carried out as well. The second stator is then fixedly supported within the housing. An adjustable movement of the grinding gap is made possible by the axial freedom of movement (floating support) of the rotor.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は第2図のA−8面上でとった軸線方向断面図; 第2図は本発明装置の正面図; 第3図は第1図のC−D面上の拡大断面図:第4図は第
1図のE−F面上の拡大断面図:第5図は第4図と同様
の、他の実施例の拡大断面図; 第6図、第7図、第8図は夫々粉砕ギャップと浮動状ロ
ータ支持の他の実施例を示す、縦断図、正面図及び側面
図である。。 ■・・・ハウジング    2・・・円筒形ロータ3.
4.5・・・軸受   6,7・・・粉砕板8・・・ス
テータリング 9.9′・・・外部粉砕板 10・・・材料送り手段   11・・・水平粉砕ギャ
ップ12・・・傾いた粉砕ギャップ 15・・・封止ユニット   17・・・向合うリブ1
8・・・横リプ      101・・・ハウジング1
02・・・ロータ     110#・・・環状スペー
ス115′・・・封止ユニット201.202・・・軸
受203、204・・・摺動軸受 206、207.210.211・・・粉砕板218・
・・彎曲フープ
Fig. 1 is an axial sectional view taken on plane A-8 in Fig. 2; Fig. 2 is a front view of the device of the present invention; Fig. 3 is an enlarged sectional view taken on plane CD in Fig. 1: Fig. 4 is an enlarged sectional view on the E-F plane of Fig. 1; Fig. 5 is an enlarged sectional view of another embodiment similar to Fig. 4; Figs. 6, 7, and 8 are Figures 2A and 2B are longitudinal, front and side views, respectively, of alternative embodiments of grinding gaps and floating rotor support; . ■...Housing 2...Cylindrical rotor 3.
4.5...Bearing 6,7...Crushing plate 8...Stator ring 9.9'...External grinding plate 10...Material feeding means 11...Horizontal grinding gap 12...Inclination Grinding gap 15... Sealing unit 17... Opposing rib 1
8...Horizontal reply 101...Housing 1
02...Rotor 110#...Annular space 115'...Sealing unit 201.202...Bearings 203, 204...Sliding bearings 206, 207.210.211...Crushing plate 218...
・Curved hoop

Claims (1)

【特許請求の範囲】 1、少なくとも2つの回転面をもつモータ駆動されるロ
ータを備え、前記回転面は少なくとも1つの材料供給手
段から離れるにつれて直径が大きくなる破砕又は粉砕素
子をもち、更にロータを受入れるハウジングを備え、前
記ハウジングは対応する内壁とその上に設けた向合う破
砕又は粉砕面とをもち、少なくとも1つの材料供給手段
を前記ハウジングのほぼ中心に配置し、前記破砕又は粉
砕面がロータのジャケット上でかつハウジング内壁上で
傾斜面上の材料供給手段から離れた両側へ延在し、その
直径が前記材料供給手段から離れるにつれて増大し、前
記材料供給手段がロータ正面に開くロータの軸線と或る
角度をなしている如き繊維質材料の破砕又は粉砕装置に
おいて、ロータ軸線とほぼ平行に延在する破砕又は粉砕
面とハウジング上の対応する向合う破砕又は粉砕面が材
料供給手段と直径が増大する破砕又は粉砕面の間でドラ
ム形ロータジャケット上に設けられ、軸線と平行に延在
しかつ軸線に対して傾斜した粉砕ギャップを形成する破
砕又は粉砕面とそれに向合う破砕又は粉砕面とが少なく
とも1つの材料供給手段の中央平面に対して対称的に配
置され、軸線に向って傾斜した破砕又は粉砕面が軸線と
平行な破砕又は粉砕面に直接に追従しかつそれと合併す
ることを特徴とする繊維質材料の破砕又は粉砕装置。 2、破砕又は粉砕面がロータ軸線とほぼ5乃至45度の
角度をなすことを特徴とする、請求項1記載の装置。 3、傾斜した破砕又は粉砕面がロータ軸線に対して或る
傾斜角度をもって破砕又は粉砕面によって直接に追従さ
れ、前記角度は前記傾斜した破砕面の角度より大きいこ
とを特徴とする、請求項1記載の装置。 4、前記傾斜角度はほぼ90度とすることを特徴とする
請求項3記載の装置。 5、軸線に向って傾斜した粉砕ギャップは調節自在とし
、そのために向合う破砕又は粉砕面はハウジング内でほ
ぼ水平に移動自在の少なくとも1つのステータリング上
に設けたことを特徴とする、請求項1記載の装置。 6、少なくとも2つの移動自在のステータリングを設け
たことを特徴とする、請求項5記載の装置。 7、ステータリングをお互いに独立して移動自在とする
ことを特徴とする、請求項6記載の装置。 8、ロータの両側を軸受内に移動自在に支持することを
特徴とする、請求項5記載の装置。 9、ロータを静水圧式摺動軸受中に軸線方向に移動自在
に浮動状に支持し、封止ユニットが前記摺動軸受とロー
タを受入れるハウジング内部との間で軸受ハウジング内
のロータシャフトを囲むことを特徴とする、請求項8記
載の装置。 10、環状の材料供給ギャップがハウジング内でロータ
外側を囲む環状スペースに連結し、前記スペース内に供
給材料を送入し、前記環状材料供給ギャップはほぼ該装
置の、又はそのハウジングの軸線と交差する中央平面内
に軸線と平行に延在する破砕又は粉砕面間において設け
ることを特徴とする、請求項1記載の装置。 11、軸線と平行な及び軸線に対して傾斜した破砕又は
粉砕面をもつロータの両側に設けたシャフト軸受の近く
の2つのハウジング正面壁の領域に空洞を設け、前記破
砕又は粉砕ギャップは前記空洞内へ送入し、前記空洞は
特別の封止ユニットによって2つの軸受に対して蒸気密
封状に封止され、前記封止ユニットはロータとこのロー
タ側面の軸受との間で軸線ハウジング内に挿入されかつ
粉砕された材料の排出開口を有することを特徴とする、
請求項1記載の装置。 12、ドラム形ロータをそのジャケット上に設け、破砕
又は粉砕面がその軸線とほぼ平行に両側に隣接して延在
し、破砕又は粉砕面の直径が材料供給手段から離れるに
つれて増大し、前記ロータがロータに固定した回転シャ
フトによって摺動軸受中に支持され、特別の始動モータ
を始動操作用に設け、主モータは全負荷において約30
00乃至3600rpmで作動するように構成したこと
を特徴とする、請求項1記載の装置。 13、モータ駆動されるロータをもち、このロータは少
なくとも2つの破砕又は粉砕素子を備えた円錐台形の面
と少なくとも1つの材料供給手段から離れるにつれて増
大する直径とをもち、前記ロータは水平回転シャフトと
ハウジングを有し、このハウジングは対応する内壁とそ
の上に配置した向合う破砕又は粉砕面をもち、前記ハウ
ジングはロータを受入れ、ロータ軸線に対してほぼ径方
向に向いた少なくとも1つの材料供給手段を前記ハウジ
ングのほぼ中心に配置し、破砕又は粉砕面がロータのジ
ャケット上に延在し、従ってハウジング内壁上に延在し
て傾斜面上の材料供給手段から離れて両側へ至り、前記
傾斜面の直径は材料供給手段から離れるにつれて増大し
、前記傾斜面とロータの正面に開いて両側でロータ軸線
は成る角度をなしている如き、湿った繊維質材料の破砕
又は粉砕用のドラム形微細化装置において、ドラム形ロ
ータのジャケット上でロータ軸線とほぼ平行に延在する
破砕又は粉砕面とハウジング上の対応する向合った破砕
又は粉砕面を材料供給手段と直径が増大する破砕又は粉
砕面の間に設け、前記軸線と平行な及び前記軸線に対し
て傾斜した粉砕ギャップを形成する破砕又は粉砕面と向
合う破砕又は粉砕面は少なくとも1つのほぼ径方向の材
料供給手段の中央平面に対して対称的に配置され、前記
軸線と平行な破砕又は粉砕面は前記軸線に向って傾斜し
た破砕又は粉砕面によって直ちに合併状に追従されるこ
とを特徴とするドラム形微細化装置。 14、破砕又は粉砕面はロータ軸線とほぼ5乃至45度
の角度をなすことを特徴とする、請求項13記載のドラ
ム形微細化装置。 15、前記破砕面の傾斜角度より大きな傾斜角をもつ傾
斜した破砕又は粉砕面はロータ軸線に対して傾斜した破
砕又は粉砕面によって直ちに合併状に追従されることを
特徴とする、請求項13記載のドラム形微細化装置。 16、拡大した角度はほぼ90度とすることを特徴とす
る、請求項15記載のドラム形微細化装置。 17、軸線に向って傾いた粉砕ギャップを調節自在とし
、そのために向合う破砕又は粉砕面はハウジング内でほ
ぼ水平に移動自在の少なくとも1つのステータリング上
に設けたことを特徴とする、請求項13記載のドラム形
微細化装置。 18、少なくとも2つの移動自在のステータリングを設
けたことを特徴とする、請求項17記載のドラム形微細
化装置。 19、ステータリングは互いに独立して移動自在とする
ことを特徴とする、請求項18記載のドラム形微細化装
置。 20、唯1つの移動自在のステータリングを設けた場合
、ロータをその軸受内に両側で移動自在に支持すること
を特徴とする、請求項17記載のドラム形微細化装置。 21、ロータは静水圧式摺動軸受内に軸線方向に移動自
在に浮動状に支持され、封止ユニットが前記摺動軸受と
ロータを受け入れるハウジング内部の間で軸受ハウジン
グ内においてロータシャフトを囲むことを特徴とする、
請求項20記載のドラム形微細化装置。 22、環状の材料供給ギャップをハウジング内でロータ
外側を囲む環状スペースに連結し、このスペース内にほ
ぼ径方向の材料供給手段が送入し、前記供給ギャップは
ほぼ該微細化装置の又はそのハウジングの軸線と交差す
る中央平面内に軸線と平行な破砕又は粉砕面の間におい
て設けたことを特徴とする、請求項13記載のドラム形
微細化装置。 23、破砕又は粉砕ギャップから送入する空洞がシャフ
ト軸受の近くでハウジングの2つの正面壁領域に設けら
れ、前記シャフト軸受は軸線と平行な破砕又は粉砕面を
もつロータの両側に備え、前記空洞は特別の封止ユニッ
トによって2つの軸受に対して蒸気密封状に封止され、
前記封止ユニットはロータ側で軸受ハウジング内にロー
タと軸受の間に設けかつ粉砕された材料用の排出開口を
有することを特徴とする、請求項13記載のドラム形微
細化装置。 24、ドラム形ロータが軸線とほぼ平行に延在する破砕
又は粉砕面と両側に隣接した材料供給手段から離れるに
つれて直径が増大する破砕又は粉砕面をもつジャケット
上に設けられ、前記ロータはロータに固定した回転シャ
フトによって摺動軸受内に支持され、特別の始動モータ
を始動操作のために備え、主モータは全負荷においてほ
ぼ3000乃至3600rpmで作動するように構成し
たことを特徴とする、請求項13記載のドラム形微細化
装置。 25、モータ駆動されるロータをもち、このロータは少
なくとも1つの材料供給手段から離れるにつれて直径が
増大する破砕又は粉砕素子を有する少なくとも2つの回
転面をもち、更に水平回転シャフトとロータを受入れる
ハウジングとを有し、前記ハウジングは対応する内壁と
、その上に設けた向合う破砕又は粉砕面をもち、少なく
とも1つの材料供給手段はロータジャケット又はハウジ
ング外殻に対してほぼ接線方向に延在し、ほぼ前記ハウ
ジングの中心に設けられ、破砕又は粉砕素子はロータの
ジャケット上で及びこれに対応するハウジングの内壁上
で材料供給手段から離れるにつれて直径が増大する傾斜
面上で材料供給手段から離れるように両側へ延在し、全
傾斜面はロータ正面に開く両側でロータ軸線と或る角度
をなす如き、繊維質材料又は水と混ざった繊維質材料の
破砕又は粉砕用ドラム形微細化装置において、ほぼロー
タ軸線と平行に延在する破砕又は粉砕面は材料供給手段
とドラム形ロータのジャケット上の直径が増大する破砕
又は粉砕面との間に延在し、対応する向合う破砕又は粉
砕面がハウジング上に設けられ、軸線と平行な及び軸線
に対して傾斜した粉砕ギャップを形成する破砕又は粉砕
面とこれに向合う破砕又は粉砕面が少なくとも1つのほ
ぼ接線方向の材料供給手段の中央平面に対して対称的に
配置され、軸線と平行な破砕又は粉砕面が軸線に対して
傾斜した破砕又は粉砕面によって直ちに合併状に追従さ
れることを特徴とする、ドラム形微細化装置。 26、破砕又は粉砕面はロータ軸線と約5乃至45度の
角度をなすことを特徴とする、請求項25記載のドラム
形微細化装置。 27、傾斜した破砕又は粉砕面はロータ軸線に対して或
る傾斜角度をもつ破砕又は粉砕面によって直ちに合併状
に追従され、前記傾斜角度は前述の傾斜した破砕面の傾
斜角度より大きいことを特徴とする、請求項25記載の
ドラム形微細化装置。 28、前記角度はほぼ90度とすることを特徴とする、
請求項27記載のドラム形微細化装置。 29、軸線に向って傾いた粉砕ギャップを調節自在とし
、そのために向合う破砕又は粉砕面がハウジング内をほ
ぼ水平に移動自在の少なくとも1つのステータリング上
に設けられることを特徴とする、請求項25記載のドラ
ム形微細化装置。 30、少なくとも2つの移動自在のステータリングを設
けたことを特徴とする、請求項29記載のドラム形微細
化装置。 31、ステータリングは互いに独立して移動自在とする
ことを特徴とする、請求項30記載のドラム形微細化装
置。 32、唯1つのステータリングを設けた場合ロータを両
側でその軸受内に移動自在に支持することを特徴とする
、請求項29記載のドラム形微細化装置。 33、ロータが摺動軸受内に軸線方向に移動自在に浮動
状に支持され、主として摺動リングシールの形をなす封
止ユニットが前記摺動軸受とロータを受入れるハウジン
グの内部との間で軸受ハウジングのロータシャフトを囲
むことを特徴とする、請求項32記載のドラム形微細化
装置。 34、環状の材料供給ギャップがハウジング内のロータ
外側を取囲む環状スペースに連結され、前記スペース内
へほぼ接線方向の材料供給手段が送入し、前記ギャップ
は軸線と平行な破砕又は粉砕面間においてほぼドラム形
微細化装置又はそのハウジングの軸と交差する中央平面
内に設けられることを特徴とする、請求項25記載のド
ラム形微細化装置。 35、破砕又は粉砕ギャップが送入する空洞をシャフト
軸受の近くでハウジングの2つの正面壁の領域に設け、
前記シャフト軸受は軸線と平行なそして軸線に対して傾
いた破砕又は粉砕面をもつロータの両側に設け、前記空
洞は特別の封止ユニットによって2つの軸受に対して蒸
気密封状に封止され、前記封止ユニットはロータとロー
タ側のロータハウジング中の軸受の間に挿入されかつ粉
砕された材料のための排出開口を有することを特徴とす
る、請求項25記載のドラム形微細化装置。 36、ドラム形ロータがそのジャケット上に破砕又は粉
砕面を有し、前記粉砕面はほぼその軸線と平行に、そし
て材料供給手段から離れるにつれて直径が増大する破砕
又は粉砕面に隣接した両側に延在し、前記ロータは摺動
軸受内にそれに固定された回転シャフトによって支持さ
れ、特別の始動モータを始動操作のために備え、主モー
タは全負荷において3000乃至3600rpmで作動
するように構成したことを特徴とする、請求項25記載
のドラム形微細化装置。
Claims: 1. A motor-driven rotor having at least two rotating surfaces, said rotating surface having a crushing or comminution element whose diameter increases away from at least one material supply means; a receiving housing, the housing having a corresponding inner wall and an opposing crushing or crushing surface disposed thereon, the at least one material supply means being disposed approximately centrally in the housing, and the crushing or crushing surface being disposed on the rotor. an axis of the rotor extending on the jacket of the rotor and on the inner wall of the housing on both sides away from the material supply means on the inclined surface, the diameter of which increases as it moves away from said material supply means, and where said material supply means opens in front of the rotor; In such apparatus for crushing or crushing fibrous materials, a crushing or crushing surface extending substantially parallel to the rotor axis and a corresponding opposing crushing or crushing surface on the housing are at an angle with the material supply means. a crushing or crushing surface provided on the drum-shaped rotor jacket between increasing crushing or crushing surfaces and forming a crushing gap extending parallel to the axis and inclined to the axis; are arranged symmetrically with respect to the central plane of the at least one material supply means, such that the crushing or comminution surface inclined towards the axis directly follows and merges with the crushing or comminution surface parallel to the axis; A device for crushing or crushing fibrous materials. 2. Apparatus according to claim 1, characterized in that the crushing or grinding surface makes an angle of approximately 5 to 45 degrees with the rotor axis. 3.Claim 1, characterized in that the inclined crushing or crushing surface is directly followed by the crushing or crushing surface with an angle of inclination relative to the rotor axis, said angle being greater than the angle of said inclined crushing surface. The device described. 4. The device of claim 3, wherein the tilt angle is approximately 90 degrees. 5.Claim 5, characterized in that the grinding gap inclined towards the axis is adjustable, for which purpose the opposing grinding or grinding surfaces are arranged on at least one stator ring which is movable substantially horizontally in the housing. 1. The device according to 1. 6. Device according to claim 5, characterized in that it is provided with at least two movable stator rings. 7. Device according to claim 6, characterized in that the stator rings are movable independently of each other. 8. Device according to claim 5, characterized in that the rotor is movably supported on both sides in bearings. 9. The rotor is supported in a hydrostatic sliding bearing in a floating manner so as to be freely movable in the axial direction, and a sealing unit surrounds the rotor shaft in the bearing housing between the sliding bearing and the inside of the housing that receives the rotor. 9. Device according to claim 8, characterized in that: 10. An annular material feed gap is connected in the housing to an annular space surrounding the outside of the rotor, and feeds the feed material into said space, said annular material feed gap substantially intersecting the axis of said device or its housing. 2. The device according to claim 1, characterized in that it is provided between crushing or comminution surfaces extending parallel to the axis in a central plane. 11. A cavity is provided in the region of the two housing front walls near the shaft bearings on both sides of the rotor with crushing or crushing surfaces parallel to and inclined to the axis, the crushing or crushing gap being defined by the cavity. the cavity is sealed in a steam-tight manner against the two bearings by a special sealing unit, said sealing unit being inserted into the axis housing between the rotor and the bearing on the side of this rotor. characterized in that it has a discharge opening for the crushed material,
The device according to claim 1. 12. A drum-shaped rotor is provided on its jacket, the crushing or crushing surfaces extending substantially parallel to its axis and adjacent on both sides, the diameter of the crushing or crushing surface increasing away from the material supply means, said rotor is supported in sliding bearings by a rotating shaft fixed to the rotor, and a special starting motor is provided for starting operation, the main motor having a power of approx.
The device according to claim 1, characterized in that it is configured to operate between 00 and 3600 rpm. 13. having a motor-driven rotor having a frustoconical surface with at least two crushing or comminution elements and a diameter increasing away from the at least one material supply means, said rotor having a horizontal rotating shaft; and a housing having a corresponding inner wall and opposing crushing or comminution surfaces disposed thereon, the housing receiving a rotor and at least one material supply oriented generally radially relative to the rotor axis. means are arranged approximately in the center of said housing, with a crushing or comminution surface extending over the jacket of the rotor and thus on the inner wall of the housing to both sides away from the material supply means on the ramp; A drum-shaped fine mill for crushing or grinding wet fibrous materials, the diameter of the surface increasing away from the material supply means and forming an angle with said inclined surface and the rotor axis opening in front of the rotor on both sides. In a crushing device, a crushing or crushing surface extending substantially parallel to the rotor axis on the jacket of a drum-shaped rotor and a corresponding opposing crushing or crushing surface on the housing are connected to a material supply means and a crushing or crushing surface of increasing diameter. a crushing or crushing surface provided between and facing a crushing or crushing surface forming a crushing gap parallel to said axis and oblique to said axis relative to the central plane of at least one substantially radial material supply means; A drum-shaped atomization device, characterized in that the crushing or crushing surface parallel to the axis is immediately followed in a merging manner by the crushing or crushing surface inclined towards the axis. 14. A drum-shaped atomization device according to claim 13, characterized in that the crushing or grinding surface forms an angle of approximately 5 to 45 degrees with the rotor axis. 15. An inclined crushing or crushing surface having an inclination angle greater than the inclination angle of the crushing surface is immediately followed in a merging manner by a crushing or crushing surface inclined with respect to the rotor axis. drum-shaped atomization device. 16. The drum-shaped atomization device according to claim 15, characterized in that the enlarged angle is approximately 90 degrees. 17. Claim 17, characterized in that the grinding gap inclined towards the axis is adjustable, for which purpose the opposing grinding or grinding surfaces are provided on at least one stator ring which is movable approximately horizontally in the housing. 14. The drum-shaped atomization device according to 13. 18. Drum-shaped atomization device according to claim 17, characterized in that it is provided with at least two movable stator rings. 19. The drum-shaped atomization device according to claim 18, characterized in that the stator rings are movable independently of each other. 20. Drum-shaped atomization device according to claim 17, characterized in that, if only one movable stator ring is provided, the rotor is movably supported on both sides in its bearings. 21. The rotor is axially movably supported in a floating manner within a hydrostatic sliding bearing, and a sealing unit surrounds the rotor shaft within the bearing housing between the sliding bearing and the interior of the housing receiving the rotor. Characterized by
A drum-shaped atomization device according to claim 20. 22. An annular material feed gap is connected in the housing to an annular space surrounding the outside of the rotor, into which a substantially radial material feed means is fed, said feed gap being substantially connected to the atomization device or its housing; 14. The drum-shaped atomization device according to claim 13, characterized in that it is provided between crushing or crushing surfaces parallel to the axis in a central plane intersecting the axis of the drum. 23. Cavities feeding from the crushing or crushing gap are provided in the two front wall regions of the housing near the shaft bearings, said shaft bearings being provided on both sides of the rotor with crushing or crushing surfaces parallel to the axis, said cavities is vapor-tightly sealed to the two bearings by a special sealing unit,
14. Drum-shaped atomization device according to claim 13, characterized in that the sealing unit is arranged on the rotor side in the bearing housing between the rotor and the bearing and has a discharge opening for the pulverized material. 24. A drum-shaped rotor is provided on the jacket with a crushing or crushing surface extending substantially parallel to the axis and a crushing or crushing surface increasing in diameter away from the material supply means adjacent on both sides, said rotor having a crushing or crushing surface extending substantially parallel to the axis; Claim 1, characterized in that it is supported in a sliding bearing by a fixed rotary shaft and is provided with a special starting motor for starting operations, the main motor being arranged to operate at approximately 3000-3600 rpm at full load. 14. The drum-shaped atomization device according to 13. 25, a motor-driven rotor having at least two rotating surfaces having crushing or comminution elements increasing in diameter away from the at least one material supply means, further comprising a horizontal rotating shaft and a housing receiving the rotor; the housing has a corresponding inner wall and opposing crushing or comminution surfaces provided thereon, the at least one material supply means extending generally tangentially to the rotor jacket or housing shell; provided substantially centrally in said housing, such that the crushing or comminution element moves away from the material supply means on an inclined surface increasing in diameter away from the material supply means on the jacket of the rotor and on a corresponding inner wall of the housing; In a drum-shaped atomization device for crushing or grinding fibrous materials or fibrous materials mixed with water, which extends on both sides and whose fully inclined surface forms an angle with the rotor axis on both sides opening in front of the rotor, approximately A crushing or crushing surface extending parallel to the rotor axis extends between the material supply means and a crushing or crushing surface of increasing diameter on the jacket of the drum-shaped rotor, and a corresponding opposing crushing or crushing surface extends on the housing. at least one crushing or crushing surface provided above and forming a crushing gap parallel to and oblique to the axis and an opposing crushing or crushing surface oriented approximately tangentially to the central plane of the material supply means; drum-shaped atomization device, characterized in that a crushing or grinding surface parallel to the axis is immediately followed in a merging manner by a crushing or grinding surface oblique to the axis. 26. A drum-shaped atomization device according to claim 25, characterized in that the crushing or grinding surface forms an angle of about 5 to 45 degrees with the rotor axis. 27. The inclined crushing or crushing surface is immediately followed in a merging manner by a crushing or crushing surface having an angle of inclination with respect to the rotor axis, said inclination angle being greater than the inclination angle of said inclined crushing surface. The drum-shaped atomization device according to claim 25. 28. The angle is approximately 90 degrees,
A drum-shaped atomization device according to claim 27. 29. Claim 29, characterized in that the grinding gap inclined towards the axis is adjustable, for which purpose the opposing grinding or grinding surfaces are provided on at least one stator ring which is movable substantially horizontally in the housing. 25. The drum-shaped atomization device according to 25. 30. Drum-shaped atomization device according to claim 29, characterized in that it is provided with at least two movable stator rings. 31. The drum-shaped atomization device according to claim 30, characterized in that the stator rings are movable independently of each other. 32. Drum-shaped atomization device according to claim 29, characterized in that when only one stator ring is provided, the rotor is movably supported on both sides in its bearings. 33. A rotor is supported in a floating manner for axial movement in a sliding bearing, and a sealing unit mainly in the form of a sliding ring seal is mounted between the sliding bearing and the interior of the housing receiving the rotor. 33. A drum-shaped atomization device according to claim 32, characterized in that the housing surrounds the rotor shaft. 34. An annular material feed gap is connected to an annular space surrounding the outside of the rotor in the housing, into which a substantially tangential material feed means feeds, said gap being connected between crushing or comminution surfaces parallel to the axis. 26. A drum-shaped atomizer according to claim 25, characterized in that the drum-shaped atomizer is located approximately in a central plane intersecting the axis of the drum-type atomizer or its housing. 35. providing a cavity in the area of the two front walls of the housing near the shaft bearing, into which the crushing or crushing gap feeds;
said shaft bearings are provided on both sides of the rotor with crushing or crushing surfaces parallel to and inclined to the axis, said cavity being sealed vapor-tightly to the two bearings by a special sealing unit; 26. Drum-shaped atomization device according to claim 25, characterized in that the sealing unit is inserted between the rotor and the bearing in the rotor housing on the rotor side and has a discharge opening for the pulverized material. 36. A drum-shaped rotor having a crushing or crushing surface on its jacket, said crushing surface extending substantially parallel to its axis and on both sides adjacent to the crushing or crushing surface increasing in diameter away from the material supply means. said rotor is supported by a rotating shaft fixed thereto in a sliding bearing, and is equipped with a special starting motor for starting operations, the main motor being configured to operate at 3000-3600 rpm at full load. 26. A drum-shaped atomization device according to claim 25, characterized in that:
JP63278576A 1987-11-05 1988-11-05 Apparatus for crushing or pulverizing fibrous material Granted JPH01266291A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AT2924/87 1987-11-05
AT0292487A AT389533B (en) 1987-11-05 1987-11-05 DEVICE, ESPECIALLY REFINER, FOR CRUSHING OR FOR GRINDING FIBER MATERIAL

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2015115A Division JPH02237654A (en) 1987-11-05 1990-01-26 Crushing grinding element for drum type fine grinder

Publications (2)

Publication Number Publication Date
JPH01266291A true JPH01266291A (en) 1989-10-24
JPH0429791B2 JPH0429791B2 (en) 1992-05-19

Family

ID=3542452

Family Applications (2)

Application Number Title Priority Date Filing Date
JP63278576A Granted JPH01266291A (en) 1987-11-05 1988-11-05 Apparatus for crushing or pulverizing fibrous material
JP2015115A Pending JPH02237654A (en) 1987-11-05 1990-01-26 Crushing grinding element for drum type fine grinder

Family Applications After (1)

Application Number Title Priority Date Filing Date
JP2015115A Pending JPH02237654A (en) 1987-11-05 1990-01-26 Crushing grinding element for drum type fine grinder

Country Status (7)

Country Link
JP (2) JPH01266291A (en)
AT (1) AT389533B (en)
CA (1) CA1317499C (en)
DE (1) DE3837757A1 (en)
FI (1) FI90259C (en)
NO (1) NO173455C (en)
SE (2) SE503362C2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01250485A (en) * 1987-11-05 1989-10-05 Mas Fab Andritz Ag Apparatus for crushing or grinding fibrous material
JPH05508454A (en) * 1991-04-12 1993-11-25 ニルソン、ハリー Beating equipment for fiber suspension
JP2009078242A (en) * 2007-09-27 2009-04-16 Sakura Seisakusho:Kk Uniaxial attrition mill

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106334597B (en) * 2015-07-14 2023-08-01 四川雄健实业有限公司 Powerful impact powder loosening machine
DE102017109080B4 (en) * 2017-04-27 2019-03-14 Günter Betz Apparatus for dewatering, defibrating and conveying waste paper, wood pulp or wood chips
CN112252120A (en) * 2020-11-03 2021-01-22 哈工(辽宁)交通科技有限公司 High-efficient fine separation integrated equipment of old and useless bituminous paving material

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01250485A (en) * 1987-11-05 1989-10-05 Mas Fab Andritz Ag Apparatus for crushing or grinding fibrous material

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3960332A (en) * 1974-10-23 1976-06-01 The Black Clawson Company Defibering apparatus for paper making stock

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01250485A (en) * 1987-11-05 1989-10-05 Mas Fab Andritz Ag Apparatus for crushing or grinding fibrous material

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01250485A (en) * 1987-11-05 1989-10-05 Mas Fab Andritz Ag Apparatus for crushing or grinding fibrous material
JPH0429792B2 (en) * 1987-11-05 1992-05-19
JPH05508454A (en) * 1991-04-12 1993-11-25 ニルソン、ハリー Beating equipment for fiber suspension
JP2009078242A (en) * 2007-09-27 2009-04-16 Sakura Seisakusho:Kk Uniaxial attrition mill

Also Published As

Publication number Publication date
JPH0429791B2 (en) 1992-05-19
FI885093A0 (en) 1988-11-04
FI90259C (en) 1994-01-10
CA1317499C (en) 1993-05-11
NO884922L (en) 1989-05-08
SE9000613D0 (en) 1990-02-21
SE9000613L (en) 1990-02-21
NO884922D0 (en) 1988-11-04
NO173455B (en) 1993-09-06
FI90259B (en) 1993-09-30
NO173455C (en) 1993-12-15
FI885093A (en) 1989-05-06
DE3837757A1 (en) 1989-05-18
SE8803990D0 (en) 1988-11-03
ATA292487A (en) 1989-05-15
SE503362C2 (en) 1996-06-03
SE8803990L (en) 1989-05-06
DE3837757C2 (en) 1993-07-01
JPH02237654A (en) 1990-09-20
AT389533B (en) 1989-12-27

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