Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0429791B2 - - Google Patents
[go: Go Back, main page]

JPH0429791B2 - - Google Patents

Info

Publication number
JPH0429791B2
JPH0429791B2 JP63278576A JP27857688A JPH0429791B2 JP H0429791 B2 JPH0429791 B2 JP H0429791B2 JP 63278576 A JP63278576 A JP 63278576A JP 27857688 A JP27857688 A JP 27857688A JP H0429791 B2 JPH0429791 B2 JP H0429791B2
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.)
Expired - Lifetime
Application number
JP63278576A
Other languages
Japanese (ja)
Other versions
JPH01266291A (en
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 filed Critical
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)

Description

【発明の詳細な説明】 本発明は繊維質材料特に湿つた又は水を混ぜた
繊維質材料好適にはチツ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。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
ロータを有し、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受に対して傾き
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ヤフトとロータを
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
はロータジヤケツ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
ロータのジヤケツ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に対して両
側でロータの正面に開く或る角度をなす。
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. . The atomization device has a motor-driven rotor with at least two crushing or comminution elements, the surfaces of said elements, preferably surfaces of rotation, in particular frustoconical surfaces, being inclined with respect to or against the rotor bearings. a housing extending substantially perpendicularly, the diameter of which increases in a direction away from the at least one material supply means, and receiving a preferably horizontal rotating shaft and a rotor, the housing being arranged on a corresponding inner wall; at least one material supply means generally radial to the rotor axis or generally tangential to the rotor jacket or housing having opposing crushing or crushing surfaces that are substantially central to said housing, with the crushing or crushing surfaces facing the rotor; extending from the material supply means on both sides onto the inner housing wall on the jacket and correspondingly on an inclined or substantially perpendicularly extending surface, preferably a rotating surface, in particular a frustoconical surface, said frustoconical The diameter of the surface increases with distance from the material supply means, said frustoconical surface forming an angle with respect to the rotor axis that opens out in front of the rotor on both sides.

木材パルプ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イスクをもつ。粉
砕板を有するこのデイスクと同じ向合うデイスク
は回転するか又は不動とする。この既知の例で
は、粉砕ギヤツ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つて傾斜
する。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。この結果高い機械的エネルギーを使用す
れば、主として湿つた又は湿気の多い材料又は水
の混ざつた材料が破砕又は粉砕されるので、粉砕
ギヤツ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ツ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。特に普通のデイスク形微細化装置
においては粉砕ギヤツプを垂直配置とするが困難
である。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。
Most comminution equipment currently used to produce wood pulp mechanically 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. 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. The resulting use of high mechanical energy results in the generation of large amounts of steam in the grinding gap, since primarily wet or humid materials or materials mixed with water are crushed or crushed. Good utilization or recovery of energy and unhindered loading of chips etc. require adequate evacuation of the steam together with the fiber material produced or recovered;
This is difficult to implement due to the large amount of steam generated. In particular, it is difficult to arrange the grinding gap vertically in conventional disk-type atomizers. 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、ロータ又はシヤフトの毎分当
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 stresses, increase material throughput, increase the number of rotations per minute of the rotor or shaft, and improve the problems of steam generation and steam exhaust.

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
形ロータのジヤケツ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
平行な粉砕ギヤツプと前記軸線に対して傾斜した
粉砕ギヤツプを形成し、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直接接合し円錐台
形粉砕面はロータ軸線に向つてほぼ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
つて直ちに、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。本発明による粉砕面は特に有効な
デフアイブレーシヨンを保証し、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
と平行な破砕ギヤツプ内で材料を予備破砕し、前
記粉砕ギヤツプを軸線に対した粉砕ギヤツプへ特
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
によつ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TMP(熱機械的パルプ)と
CTMP(化学的熱機械的パルプ)の生産に適す
る。本発明によれば、好適には前以て水平の粉砕
ギヤツプ内で予備粉砕された径方向に供給される
ギヤツプ等を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ヨンを隣接して傾
斜した、好適には調節自在に傾斜した特に円錐形
の粉砕ギヤツプ内で行うことができる。このギヤ
ツ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 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 approximately 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 inclined to said axis, which are symmetrical with respect to the midplane 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 surface parallel to the axis is in particular directly connected to the frustoconical crushing or comminution surface. The truncated conical grinding surface is inclined towards the rotor axis by an angle of approximately 5 to 45 degrees, in particular by 15 degrees, and said inclined grinding or grinding surface is immediately and particularly uniformly inclined by the optionally merging grinding or grinding surface. , these grinding surfaces make an angle of inclination with respect to the rotor axis that is greater than the angle of the inclined grinding or grinding surfaces, in particular an angle of approximately 90 degrees. The grinding surface according to the invention guarantees a particularly effective differential brake and at the same time facilitates steam extraction, reduced material stress, reduced bearing stress, increased material throughput, increased revolutions per minute and It is possible to pre-crush the material in parallel crushing gaps and to specifically transform said crushing gap into an axial crushing gap to particularly facilitate the crushing operation. 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 TMP (thermo-mechanical pulp).
Suitable for CTMP (chemical thermomechanical pulp) production. According to the invention, the radially fed gear, preferably pre-milled in a horizontal grinding gap, is distributed symmetrically in two directions, resulting in a particularly effective differential break for wood and the like. can be carried out 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ヤ
ツ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。粉砕ギヤツプはパルプの性質の制御に重
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. Grinding gap is important in controlling pulp properties.

粉砕ギヤツプの便利な調節は、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つて行う。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、封止ユニツ
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
中でロータシヤフトを取囲む。もし環状の材料供
給ギヤツ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。この供給ギヤツプはハウジング
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、前記供給ギヤツプは軸
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 having 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ヤツプが装入する空
洞を2つのハウジング正面壁の領域に、ロータの
シヤ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簡単になり、
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ツトによつて2つ
の軸受内に蒸気が侵入しないように封止する。封
止ユニツ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 gears, 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, and which are aligned with the axis. It has crushing or comminution surfaces extending parallel and approximately 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. This makes it easier to vent the steam,
Or vapor exhaust means are made. Due to the generation of steam, 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ヤケ
ツ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ヤフトによつて前記軸
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。この始動モータはステータシヤフトの遊端に
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。従つて始動電流ピークは減少す
る。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3600rpmまでの回転数で運転可能と
なす。
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 generally 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; 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, particularly a DC motor, is provided for starting operations, and the main motor is configured to run at approximately 3000-3600 rpm at full load. 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. 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 3600 rpm.

軸線と平行に延在する粉砕ギヤツプに隣接する
円錐台形粉砕ギヤツプの代りに他の回転面をもつ
形状のギヤツプを使用できる。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, gap shapes with other surfaces of rotation 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 particular constantly from the point of contact with the grinding surface extending parallel to the axis to the front of the rotor;
It is necessary to ensure that the target material 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2mmの粉砕
ギヤツプを作るようにする。材料供給は耳軸シヤ
フトの領域内で該装置の一側において行う。この
微細化装置の生産量は、材料供給を片側のみから
そして直ちにシヤフト上へ行つて直接に円錐形粉
砕ギヤツプ内へ入れるため、不満足である。満足
なデフアイブレーシヨンも適切なパルプ生成効果
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。
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. Make a grinding gap of 2mm. Material feeding takes place on one side of the device in the area of the ear 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. Neither a satisfactory differential eyebrasion nor an appropriate pulp production effect 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ーにおいては粉砕素
子はスクリユーコンベヤによつて上部から分離羽
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ヤ
ツプを形成し、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。その平行ギヤツ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つて運ば
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
シヤフトの両側の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ヤツプ
に隣接した円錐形粉砕ギヤツプ等が存在しないこ
とを別にしても、チツプ又は他の湿つた繊維質材
料を処理するのには適していない。
In known microatomizers, the grinding elements are fed from the top by means of a screw conveyor 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 notch 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. Two blowers on either side of the grinding shaft create the necessary air flow. 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、チツ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 An embodiment of the present invention of a drum-shaped refining device for producing wood pulp from chips will now 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つた摺動軸受
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は粉砕ギヤツプ6,7をもち、粉
砕板6をハウジングの円筒形ジヤケツト部に沿つ
て配置してチツプを予備粉砕し、粉砕板7はデフ
アイブレーシヨン用のロータの軸線と或る角度を
なす。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
粉砕ギヤツ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。
1 to 5 show a preferably horizontally divided atomizer housing 1 in which a cylindrical rotor 2
is supported on bearings 3, 4, 5 on both sides, using rolling or sliding bearings, in particular sliding bearings with inclined segments, depending on the diameter, capacity and revolutions per minute. The rotor 2 has grinding gears 6, 7, the grinding plates 6 are arranged along the cylindrical jacket part of the housing to pre-crush the chips, the grinding plates 7 are arranged at an angle with the axis of the rotor for differential braking. to do. To create the grinding plate 7, the angle between the grinding area and the horizontal line is between 5 degrees and 45 degrees, preferably 15 degrees. Opposite grinding plates 9, 9' cooperating with the grinding plate 7 are mounted on the stator ring 8 so as to be horizontally movable for adjusting the grinding 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
向合うリブ17は横ウエブ又は横リブ18によつ
て補強する。ウエブ又はリブ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、この図には横リブ
18は一部のみを示している。定着用突出部19
はハンマーヘツド状断面の対応するロータみぞ2
0内に配置される。
Figures 3 and 4 show enlarged cross-sections of the crushing plate area;
FIG. 3 shows a region parallel to the axis, and FIG. 4 shows a truncated cone region. As shown in FIG. 4, the opposing ribs 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. The internal grinding plate 7 in the truncated conical region is made up of segments 7' (FIG. 4). The dimensions of this particularly practical embodiment are shown in FIG. 5, in which only a portion of the transverse ribs 18 are shown. Fixing protrusion 19
is the corresponding rotor groove 2 with a hammerhead-shaped cross section.
Placed within 0.

チツプは特にコンベヤスクリユーによつて供給
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によつて径方向に送られ
る。チツプは水平粉砕ギヤツプ11内で予備粉砕
し、両方向に対称的に分散させる。木材のデフア
イブレーシヨンは水平線に対して傾いた調節自在
の粉砕ギヤツプ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 fed in particular by means of a conveyor screw, in this embodiment from 1 to 4 chips with openings around the periphery.
The material is fed in the radial direction by the material feeding means 10. The chips are pre-ground in a horizontal grinding gap 11 and distributed symmetrically in both directions. The differential breaking 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.

軸受は封止ユニツト15によつて前記ハウジン
グ内の蒸気に対して密封する。
The bearing is sealed against steam in the housing by means of a sealing unit 15.

シヤフト遊端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, preferably a DC motor, is provided 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
より本発明の微細化装置は3600rpmまでの回転数
で運転できる。
According to this embodiment, which is modified from the conventional atomization apparatus, the atomization apparatus of the present invention can be operated at a rotation speed of up to 3600 rpm.

本発明は垂直のロータシヤフトをもつ微細化装
置に有利に適用できる。木材以外の繊維材料を簡
単に粉砕でき、水その他の液体を或る条件下で予
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. Fibrous materials other than wood can be easily crushed and water or other liquids can be added to the pre-crushed material under certain 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くなる。この結果、材
料処理量が増大する。
According to the invention, the material stress is significantly reduced compared to known atomization devices, the stress on the bearing is reduced, and the service life of the bearing is increased. This results 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のシヤ
フト端116′、従つてロータ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20
1,202中に設ける。これらの軸受も封止ユニ
ツト115′によつて微細化装置のハウジング1
01内で蒸気に対して密封する。二重矢印205
はロータの前述の支持手段によつて可能にされる
ロータの移動又は浮動状のロータ支持を示す。こ
の場合唯1つのステータが調節できれば十分であ
り、同様に両ステータ1,1′の、従つてこれら
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分
206,207に加えて、ロータ軸線との間に部
分208,209よりも大きな角度、即ちほぼ90
度の角度をなす部分210,211をもつ。部分
210,211と協働する追加の粉砕板212,
213は部分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によつて支持され
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 the material is then conveyed to the grinding plate. The shaft end 116' of the rotor 102 Therefore, the rotor 102 itself is supported in a floating manner in this case.To support it in this way, hydrostatic sliding bearings 203 and 204 are mounted on the bearing 20.
1,202. These bearings are also connected to the housing 1 of the micronization device by means of a sealing unit 115'.
01 and sealed against steam. double arrow 205
shows the movement of the rotor or the floating rotor support made possible by the above-mentioned support means for the rotor. In this case it is sufficient that only one stator can be adjusted; it is likewise possible in this case to adjust both stators 1, 1' and thus also the grinding plates 206, 207 attached to them. These grinding plates, in addition to the frustoconical sections 206, 207, form a larger angle with the rotor axis than the sections 208, 209, i.e. approximately 90
It has portions 210 and 211 forming angles of degrees. an additional grinding plate 212 cooperating with parts 210, 211;
213, like sections 210, 211, is steeply inclined to the rotor axis and is supported by special rings 214, 215 connected to rotor 102.

ステータ1,1′の、従つて粉砕板206,2
07,210,211の調節、及び円筒形粉砕板
の調節も部品3〜5によつて第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によつて一様に移動させられる彎曲フープ21
8によつ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
ヤツプの調節移動ロータの軸線方向の自由移動性
(浮動支持)によつて可能にされる。
of the stator 1, 1' and hence of the crushing plate 206, 2
07, 210, 211 and the cylindrical crushing plate are also carried out in the same manner as shown in FIGS.
Curved hoop 21 moved uniformly by 9
8 simultaneously in opposite directions. 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. Adjustment movement of the grinding gap is made possible by the free axial movement of the rotor (floating support).

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

第1図は第2図のA−B面上でとつた軸線方向
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図は夫々粉砕ギヤツ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。 1……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……水平粉砕ギヤツプ、12
……傾いた粉砕ギヤツプ、15……封止ユニツ
ト、17……向合うリブ、18……横リブ、10
1……ハウジング、102……ロータ、110″
……環状スペース、115′……封止ユニツト、
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-B 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; Figure 4 is the first
An enlarged sectional view on the E-F plane of the figure; FIG. 5 is an enlarged sectional view of another embodiment similar to FIG. 4; FIGS. 6 and 7
8 are a longitudinal sectional view, a front view, and a side view, respectively, showing other embodiments of the grinding gap and floating rotor support. 1...Housing, 2...Cylindrical rotor, 3,
4, 5...Bearing, 6,7...Crushing plate, 8...Stator ring, 9,9'...External crushing plate, 10...
Material feeding means, 11...Horizontal crushing gap, 12
... Inclined crushing gap, 15 ... Sealing unit, 17 ... Opposing ribs, 18 ... Lateral ribs, 10
1...Housing, 102...Rotor, 110''
... annular space, 115' ... sealing unit,
201, 202... bearing, 203, 204... sliding bearing, 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き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
砕面がロータのジヤケツト上とハウジング内壁上
で材料供給手段から離れた傾斜面の両側へ延在
し、前記傾斜面は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、かつロータ軸線に対し
てロータ正面に開く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き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
ドラム形ロータジヤケツト上に設けられ、軸線と
平行に延在しかつ軸線に対応して傾斜した粉砕ギ
ヤツプを形成する破砕又は粉砕面とそれに向き合
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
に向かつ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接合していることを特徴
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1項記載の
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つて破砕又は粉砕面に直接接
合し、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 軸線に向かつて傾斜した破砕ギヤツプは調節
自在とし、そのために向き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特許請求の範囲第6項記
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、封止ユニツトが前記摺
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ヤフトを囲むこと
を特許とする請求項8記載の装置。 10 環状の材料供給ギヤツ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り込み、前記環状材料供
給ギヤツプはほぼ該装置の、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ヤフ
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ヤツプは前記空
洞内へ送り込み、前記空洞は特別の封止ユニツト
によつて2つの軸受に対して蒸気密封状に封止さ
れ、前記封止ユニツトはロータとこのロータ側面
の軸受との間で軸受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ヤケツト上に設
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ヤフトによつて摺動軸
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3000乃至
3600rpmで作動するように構成したこと特徴とす
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
ータは水平回転シヤ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
向き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半径
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
面がロータのジヤケツト上に延在し、従つてハウ
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
は両側でロータの正面に開いてロータ軸線に対し
て或る角度をなしている如き、湿つた繊維質材料
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ヤケツト上でロータ軸線
とは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き合つ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
傾斜した粉砕ギヤツプを形成する破砕又は粉砕面
と向き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
は前記軸線に向かつて傾斜した破砕又は粉砕面に
直接接合してい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直接接合しているこ
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 軸線に向かつて傾いた粉砕ギヤツプを調節
自在とし、そのために向き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、封止ユニツトが前
記摺動軸受とロータを受入れるハウジング内部の
間で軸受ハウジング内においてロータシヤフトを
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 環状の材料供給ギヤツ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に材料供給手段が送り込
み、前記供給ギヤツ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 破砕又は粉砕ギヤツプから送り込む空洞が
シヤフト軸受の近くでハウジングの2つの正面領
域に設けられ、前記シヤ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ツトによつて2つの軸受に
対して蒸気密封状に封止され、前記封止ユニツト
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
面をもつジヤケツト上に設けられ、前記ロータは
ロータに固定した回転シヤフトによつて摺動軸受
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
ヤ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
た向き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ヤケツト又はハウジ
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
子はロータのジヤケツ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、全傾斜面は両側で
ロータ軸線に対してロータ正面に開く或る角度を
なす如き、繊維質材料又は水と混ざつた繊維質材
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ヤケツ
ト上の直径が増大する破砕又は粉砕面との間に延
在し、対応する向き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
て傾斜した粉砕ギヤツプを形成する破砕又は粉砕
面とこれに向き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
直接接合してい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
して或る角度をもつ破砕又は粉砕面に直接接合し
ており、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 軸線に向かつて傾いた粉砕ギヤツプを調節
自在とし、そのための向き合う破砕又は粉砕面が
モータ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ツ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
ングのロータシヤ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 環状の材料供給ギヤツプからハウジング内
のロータ外側を取り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
段が送り込み、前記ギヤツ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
はそのハウジングに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 破砕又は粉砕ギヤツプが送り込む空洞をシ
ヤ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、前記シヤ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ツ
トによつて2つの軸受に対して蒸気密封に封止さ
れ、前記封止ユニツ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ヤケツト上にほぼ
その軸線と平行に延在する破砕又は粉砕面と、そ
の両側で材料供給手段から離れるにつれて直径が
増大する隣接した破砕又は粉砕面を有し、前記ロ
ータは摺動軸受内にそれに固定された回転シヤフ
トによつて支持され、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 with at least two rotating surfaces, said rotating surfaces having crushing or comminution elements whose diameter increases away from at least one material supply means and further receiving the rotor. a 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 a jacket of the rotor. extending on both sides of an inclined surface remote from the material supply means on the upper and inner walls of the housing, said inclined surface increasing in diameter away from said material supply means and opening in front of the rotor with respect to the rotor axis; In such an angular crushing or crushing device for fibrous materials, a crushing or crushing surface extending approximately parallel to the rotor axis and a corresponding opposing crushing or crushing surface on the housing are connected to the material supply means and the crushing device increases in diameter. or at least one crushing or crushing surface and an opposing crushing or crushing surface provided on the drum-shaped rotor jacket between the crushing surfaces and forming a crushing gap extending parallel to the axis and inclined correspondingly to the axis; Crushing of fibrous material, characterized in that the crushing or crushing surface, which is arranged symmetrically with respect to the central plane of the material supply means and is inclined towards the axis, is directly joined to the crushing or crushing surface parallel to the axis. or crushing equipment. 2 The crushing or crushing surface is approximately 5 to 45 degrees from the rotor axis.
2. A device according to claim 1, characterized in that it forms an angle of .degree. 3. The inclined crushing or crushing surface directly joins the crushing or crushing surface at an angle of inclination relative to the rotor axis, said angle being greater than the angle of said inclined crushing surface. equipment. 4. The device of claim 3, wherein the angle of inclination is approximately 90 degrees. 5. The crushing gear according to claim 1, characterized in that the crushing gear inclined towards the axis is adjustable, for which purpose the facing crushing or crushing surfaces are provided on at least one stator ring which is movable substantially horizontally within the housing. Device. 6. Device according to claim 5, characterized in that it is provided with at least two movable stator rings. 7. The device according to claim 6, characterized in that the stator rings are movable independently of each other. 8. The apparatus of claim 5, wherein the rotor is movably supported in bearings on both sides. 9 The rotor is supported in a floating manner in a hydrostatic sliding bearing so as to be freely movable in the axial direction, and the sealing unit surrounds the rotor shaft in the bearing housing between the sliding bearing and the inside of the housing that receives the rotor. The device according to claim 8, which is patented. 10. An annular material feed gap connects 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 in a midplane intersecting the axis of the device or of its housing. 2. Device according to claim 1, characterized in that it is provided between crushing or comminution surfaces extending parallel to the axis within the device. 11. A cavity is provided in the region of the two front walls of the housing near the shaft bearings on both sides of the rotor with crushing or crushing surfaces parallel to and inclined to the axis, said crushing or crushing gap being located within said cavity. the cavity is sealed in a steam-tight manner to the two bearings by means of a special sealing unit, said sealing unit being inserted into the bearing housing between the rotor and the bearing on the side of this rotor. 2. The device according to claim 1, further comprising a discharge opening for the ground material. 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 with distance from the material supply means, said rotor It is supported in sliding bearings by a rotating shaft fixed to the rotor, and a special starting motor is provided for starting operations, with the main motor having a
2. The apparatus of claim 1, wherein the apparatus is configured to operate at 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; a housing having a corresponding inner wall and opposing crushing or comminution surfaces disposed thereon, the housing receiving a rotor and having at least one material supply means oriented generally radially relative to the rotor axis; arranged approximately in the center of said housing, with a crushing or crushing 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 inclined surface; A drum for crushing or grinding wet fibrous materials, the diameter of which increases away from the material supply means, said inclined surfaces being open on both sides in front of the rotor and forming an angle to the rotor axis. In a shape refining 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 surface of increasing diameter. or between the crushing surfaces, the crushing or crushing surfaces facing the crushing or crushing surfaces forming a crushing gap parallel to said axis and oblique to said axis are in the central plane of at least one substantially radial material supply means; A drum-shaped atomization device, characterized in that a crushing or crushing surface parallel to the axis is directly joined to a crushing or crushing surface inclined toward the axis. 14 The crushing or crushing surface is approximately 5 to
14. The drum-shaped atomization device according to claim 13, characterized in that it forms an angle of 45 degrees. 15. The drum-shaped fine grinder according to claim 13, wherein the inclined crushing or crushing surface having an inclination angle larger than the inclination angle of the crushing surface is directly joined to the crushing or crushing surface inclined with respect to the rotor axis. conversion device. 16. The drum-shaped atomization device according to claim 15, wherein the enlarged angle is approximately 90 degrees. 17. The grinding gear according to claim 13, characterized in that the grinding gear inclined towards the axis is adjustable, for which purpose the facing grinding or grinding surfaces are provided on at least one stator ring which is movable substantially horizontally within the housing. Drum-shaped micronization device. 18. A 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, wherein 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. The drum-shaped atomization device according to claim 20. 22 An annular material supply gap is connected in the housing to an annular space surrounding the outside of the rotor, into which space the material supply means feeds generally radially, said supply gap being substantially aligned with the axis of the atomization device or of 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 intersecting central planes. 23 Cavities feeding from the crushing or crushing gear are provided in the two front areas 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 being provided with special seals. sealed in a steam-tight manner to the two bearings by a sealing unit, said sealing unit being arranged in the bearing housing on the rotor side between the rotor and the bearing and having a discharge opening for the pulverized material; The drum-shaped atomization device according to claim 13, characterized in that: 24. A drum-shaped rotor is provided on a jacket having a crushing or crushing surface extending substantially parallel to the axis and a crushing or crushing surface whose diameter increases as it moves away from the material supply means adjacent on both sides, said rotor being fixed to the rotor. 2. A special starting motor is provided for the starting operation, the main motor being arranged to operate at approximately 3000 to 3600 rpm at full load. 14. The drum-shaped atomization device according to 13. 25 having a motor-driven rotor having at least two rotating surfaces with 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; have,
The housing has a corresponding inner wall and opposing crushing or crushing surfaces provided thereon, the housing having at least one
The two material supply means extend approximately tangentially to the rotor jacket or housing shell and are provided approximately in the center of said housing, and the crushing or comminution elements are located on the rotor jacket and on the corresponding inner wall of the housing. The fibers extend on both sides away from the material supply means on inclined surfaces whose diameter increases as they move away from the material supply means, and the entire inclined surface forms an angle on both sides with respect to the rotor axis, opening in front of the rotor. In a drum-shaped refining device for crushing or grinding of fibrous materials or fibrous materials mixed with water, the crushing or grinding surface extending approximately parallel to the rotor axis has a diameter on the jacket of the material supply means and the drum-shaped rotor. a crushing or crushing surface extending between the increasing crushing or crushing surfaces and corresponding opposing crushing or crushing surfaces provided on the housing forming a crushing gap parallel to and inclined to the axis; the crushing or crushing surface facing the at least one substantially tangential material feeding means is arranged symmetrically with respect to the central plane of the material supply means, and the crushing or crushing surface parallel to the axis is directly connected to the crushing or crushing surface oblique to the axis. A drum-shaped micronization device characterized by being joined. 26 The crushing or crushing surface is approximately 5 to 45 mm away from the rotor axis.
26. The drum-shaped atomization device according to claim 25, characterized in that the drum-shaped atomization device forms an angle of .degree. 27. A claim characterized in that the inclined crushing or crushing surface is directly connected to a crushing or crushing surface having an angle with respect to the rotor axis, and said inclination angle is greater than the inclination angle of said inclined crushing surface. Section 25
The described drum-shaped atomization device. 28. The drum-shaped atomization device of claim 27, wherein said angle is approximately 90 degrees. 29. The grinding gear according to claim 25, characterized in that the grinding gear tilted towards the axis is adjustable and the opposing grinding or grinding surfaces therefor are provided on at least one stator ring which is movable substantially horizontally in the motor. Drum type micronization device. 30. A 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 in a sliding bearing for axial movement, and a sealing unit, mainly in the form of a sliding ring seal, is provided between the sliding bearing and the interior of the housing receiving the rotor in the bearing housing. 33. A drum-shaped atomization device according to claim 32, characterized in that it surrounds a rotor shaft of. 34 An annular material feed gap 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 having a substantially drum-shaped shape between the crushing or comminution surfaces parallel to the axis. 26. A drum-shaped atomization device according to claim 25, characterized in that it is provided in a central plane intersecting the axis of the atomization device or its housing. 35 Cavities into which the crushing or crushing gear feeds are provided in the area of the two front walls of the housing near the shaft bearings, said shaft bearings having crushing or crushing surfaces parallel to and inclined to the axis on both sides of the rotor. and the cavity is sealed steam-tightly to the two bearings by a special sealing unit, said sealing unit being inserted between the rotor and the bearing in the rotor housing on the rotor side and crushed. 26. Drum-shaped atomization device according to claim 25, characterized in that it has a discharge opening for the material. 36. A drum-shaped rotor having on its jacket a crushing or crushing surface extending generally parallel to its axis and adjacent crushing or crushing surfaces on each side thereof increasing in diameter away from the material supply means, said rotor comprising: It is supported by a rotating shaft fixed to it in a sliding bearing and is equipped with a special starting motor for starting operations, the main motor having a
26. The drum-shaped atomization device according to claim 25, characterized in that it is configured to operate at a speed of 3,600 rpm to 3,600 rpm.
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 atomization equipment

Publications (2)

Publication Number Publication Date
JPH01266291A JPH01266291A (en) 1989-10-24
JPH0429791B2 true 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 atomization equipment

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 atomization equipment

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)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT390456B (en) * 1987-11-05 1990-05-10 Andritz Ag Maschf REFINER FOR CRUSHING OR FOR GRINDING FIBER MATERIAL, PREFERABLY CHIPS
SE468601B (en) * 1991-04-12 1993-02-15 Harry Nilsson FIBER SUSPENSION MALAWARE
JP5623000B2 (en) * 2007-09-27 2014-11-12 株式会社櫻製作所 Uniaxial grinder
CN106334597B (en) * 2015-07-14 2023-08-01 四川雄健实业有限公司 Powerful impact loose powder 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
AT527474B1 (en) * 2024-07-16 2025-03-15 Andritz Ag Maschf DEVICE FOR TREATING A FIBRE MATERIAL

Family Cites Families (2)

* 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
AT390456B (en) * 1987-11-05 1990-05-10 Andritz Ag Maschf REFINER FOR CRUSHING OR FOR GRINDING FIBER MATERIAL, PREFERABLY CHIPS

Also Published As

Publication number Publication date
FI90259C (en) 1994-01-10
SE503362C2 (en) 1996-06-03
NO884922D0 (en) 1988-11-04
NO173455B (en) 1993-09-06
DE3837757C2 (en) 1993-07-01
SE9000613D0 (en) 1990-02-21
JPH01266291A (en) 1989-10-24
NO884922L (en) 1989-05-08
CA1317499C (en) 1993-05-11
JPH02237654A (en) 1990-09-20
SE8803990L (en) 1989-05-06
NO173455C (en) 1993-12-15
FI885093A0 (en) 1988-11-04
SE8803990D0 (en) 1988-11-03
FI90259B (en) 1993-09-30
FI885093A7 (en) 1989-05-06
ATA292487A (en) 1989-05-15
SE9000613L (en) 1990-02-21
AT389533B (en) 1989-12-27
DE3837757A1 (en) 1989-05-18

Similar Documents

Publication Publication Date Title
KR100384704B1 (en) Fine grinding device
US4754935A (en) Method and apparatus for refining fibrous material
US5335865A (en) Two-stage variable intensity refiner
US4401280A (en) Disc-type pulp refining apparatus
JPH0429792B2 (en)
JPH0429791B2 (en)
IL131174A (en) Dynamic classifier with hollow shaft drive motor
FI72891B (en) TALLRIKSKROSS.
US5127591A (en) Apparatus for crushing or grinding of fibrous material, in particular drum refiner
WO1989000455A1 (en) Gyratory crusher
US5145121A (en) Apparatus for crushing or grinding of fibrous material, in particular drum refiner
EP0168398A1 (en) Method and apparatus for manufacturing fiber pulp
JPS6229554B2 (en)
KR19990008275A (en) Disc refiners with conical ribbon feeders
US5228629A (en) Grinding element for drum refiner
US7648090B2 (en) Disc housing
RU2143322C1 (en) Cone crusher
SU785404A1 (en) Disc mill
JPH039799Y2 (en)
AU618545B2 (en) Gyratory crusher
CN210994582U (en) Ball mill lining assembly, ball mill rotary drum and ball mill
SU957953A1 (en) Self-disintegration dynamic mill
SU1583504A1 (en) Device for milling cellulose-containing material
AT394586B (en) Drum refiner for the comminution or refining of fibrous material
SU1364361A1 (en) Medium running mill