JP2918679B2 - Dry media mill - Google Patents

Dry media mill

Info

Publication number
JP2918679B2
JP2918679B2 JP32707090A JP32707090A JP2918679B2 JP 2918679 B2 JP2918679 B2 JP 2918679B2 JP 32707090 A JP32707090 A JP 32707090A JP 32707090 A JP32707090 A JP 32707090A JP 2918679 B2 JP2918679 B2 JP 2918679B2
Authority
JP
Japan
Prior art keywords
container
cylindrical member
mill according
dry
raw material
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
JP32707090A
Other languages
Japanese (ja)
Other versions
JPH04193360A (en
Inventor
克也 水井
良明 安藝
広行 辻本
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.)
HOSOKAWA MIKURON KK
Original Assignee
HOSOKAWA MIKURON KK
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 HOSOKAWA MIKURON KK filed Critical HOSOKAWA MIKURON KK
Priority to JP32707090A priority Critical patent/JP2918679B2/en
Publication of JPH04193360A publication Critical patent/JPH04193360A/en
Application granted granted Critical
Publication of JP2918679B2 publication Critical patent/JP2918679B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は微粉砕を連続的に効率よく行うための乾式媒
体ミルに関するものである。
Description: TECHNICAL FIELD The present invention relates to a dry media mill for continuously and efficiently performing pulverization.

(従来技術) 連続式の乾式媒体ミルとしては、容器内に被粉砕材料
(以下原料という)と共に粉砕ボールを入れ、撹拌羽根
を回転させて撹拌粉砕させるものがあり、微粉砕された
原料は底部よりの導入空気と共に機外に排出され、分級
機および集塵機、又はサイクロン等で捕集されるように
なっていた。
(Conventional technology) As a continuous type dry medium mill, there is a type in which a grinding ball is put into a container together with a material to be ground (hereinafter referred to as a raw material), and a stirring blade is rotated to perform stirring and pulverization. The air was discharged out of the machine together with the introduced air, and was collected by a classifier and a dust collector, or a cyclone.

(発明が解決しようとする課題) 乾式媒体ミルは、一般的には湿式媒体ミルに比べ処理
量、製品粒径の両面で粉砕能力に劣っていた。これは、
一つに粉砕ボールの表面に粉砕された原料微粉末が付着
し、粉砕ボールの衝突時に緩衝材となって粉砕効果を弱
めていることにある。しかも、これら微粉末は粉砕ボー
ル面に強固に付着しているため、搬送空気によっても容
易に剥離させることができなかった。その結果、十分な
粉砕力を付与させることができず、粉砕室内の原料充填
量も次第に増え、新たな原料の供給も抑えられ、粉砕能
力は低下することになる。
(Problems to be Solved by the Invention) Dry media mills are generally inferior to wet media mills in terms of both throughput and product particle size in terms of grinding ability. this is,
One of the reasons is that the pulverized raw material powder adheres to the surface of the pulverized ball and serves as a buffer when the pulverized ball collides, thereby weakening the pulverizing effect. In addition, since these fine powders are firmly adhered to the crushed ball surface, they cannot be easily peeled off by the carrier air. As a result, sufficient pulverizing power cannot be imparted, the amount of raw material charged in the pulverizing chamber gradually increases, supply of new raw material is suppressed, and the pulverizing capacity is reduced.

しかし、乾式媒体ミルには湿式媒体ミルに比べ粉砕ボ
ールの摩耗が少なく、かつ乾燥・解砕工程が不要となる
等の利点もあり、前述の問題を解決することによって利
用範囲を拡大できる。
However, the dry-type media mill has advantages such as less wear of the crushed balls and the elimination of the drying and crushing steps as compared with the wet-type media mill, and the use range can be expanded by solving the above problems.

本発明は、消費動力が少なく、処理能力に優れ、製品
粒径の小さいものまで効率よく製造できる乾湿媒体ミル
を提供するものである。
SUMMARY OF THE INVENTION The present invention provides a dry-wet media mill that consumes less power, has excellent processing capacity, and can efficiently produce products having a small product particle size.

(課題を解決するための手段) 前記問題を調査検討した結果、微粉砕された原料粉末
は素早く機外に排出されることが望ましい。しかし、粉
砕ボールや供給されたままの未粉砕原料から粉砕過程の
原料まで、様々な段階の原料が混在する粉砕室から微粉
末のみを完全に取り出すことは困難である。これは撹拌
羽根によって原料と粉砕ボールとに同じ遠心力が動き、
容器の内壁側に押付けられているためで、導入空気を相
当増やさないと、これらを上方に動かすことも、その中
から微粉末を分離することもできない。しかも、導入空
気を増やし過ぎると、未粉砕の原料や粉砕ボールまでも
排出されたり、微粉中に粗粉が混入して製品精度が低下
するという問題もある。
(Means for Solving the Problems) As a result of investigating and examining the above problems, it is desirable that the finely pulverized raw material powder be quickly discharged out of the machine. However, it is difficult to completely remove only the fine powder from the grinding chamber in which the raw materials of various stages are mixed, from the raw material of the pulverizing balls and the raw material to the raw material in the pulverizing process. This is because the same centrifugal force moves between the raw material and the crushed ball by the stirring blade,
Because they are pressed against the inner wall side of the container, unless the introduced air is considerably increased, they cannot be moved upward or fine powder can be separated therefrom. In addition, when the introduced air is excessively increased, there is also a problem that unmilled raw materials and crushed balls are discharged, or coarse powder is mixed into fine powder, thereby lowering product accuracy.

本発明は、原料と粉砕ボールを共に粉砕室とは別の場
所に移動させてから分離させるものであり、その構成は
容器内において、容器の内面に沿って回転する撹拌羽根
の内側に同心の円筒部材を容器の上面および底面と適当
な隙間を持たせて配設し、円筒部材上方の容器上面に円
筒部材の内径よりも小径の排出口を設け、更に円筒部材
内に原料供給管と空気導入管を配設させたことにあり、
以下にその作用について述べる。
The present invention is to separate the raw material and the crushing ball together after moving them to a different place from the crushing chamber, and the configuration is such that the inside of the container is concentric with the stirring blade rotating along the inner surface of the container. The cylindrical member is disposed with an appropriate gap between the upper and lower surfaces of the container, an outlet having a diameter smaller than the inner diameter of the cylindrical member is provided on the upper surface of the container above the cylindrical member, and a raw material supply pipe and air are further provided in the cylindrical member. Introducing the introduction pipe,
The operation will be described below.

(作用) 容器内中心部の円筒部材内に供給された原料は、円筒
部材と容器底面との隙間を通って円筒部材の外側の粉砕
室に送り込まれ、該粉砕室において撹拌羽根と粉砕ボー
ルとにより微粉砕される。また、円筒部材内に送り込ま
れた空気は、一部は原料と共に円筒部材の内部を下降し
容器底面に沿って粉砕室に入り、粉砕室から円筒部材上
方の隙間を通って排出口より機外に抜け、残りの空気は
円筒部材の上方に反転上昇し直接排出口に抜ける。この
二つの空気の流れによって原料および粉砕ボールは、次
のように移動する。つまり、粉砕室の原料および粉砕ボ
ールは、主には円筒部材の回転力と一部の空気によって
押し上げられ、円筒部材上方の隙間より押出される。こ
の際、ある程度微細に粉砕された原料粉末は空気に乗っ
て排出口より機外に排出されるが、遠心力を強く受ける
粉砕ボールと未粉砕の粗粒原料は円筒部材内に落下す
る。次に、円筒部材内では微粉末のない状態で粉砕ボー
ル同士の衝突、あるいは円筒部材の内面に粉砕ボールが
衝突し、粉砕ボール表面に付着した微粉末が剥離し、円
筒部材内より排出口に流れる空気に乗って機外に搬送さ
れる。そして、粉砕ボールと未粉砕の粗粒原料とは円筒
部材の下を通り再度粉砕室に送り込まれるが、この時に
原料供給管からの原料も送り込まれる。
(Operation) The raw material supplied into the cylindrical member at the center of the container is fed into a pulverizing chamber outside the cylindrical member through a gap between the cylindrical member and the bottom surface of the container. Is finely pulverized. In addition, part of the air sent into the cylindrical member descends inside the cylindrical member together with the raw material, enters the pulverizing chamber along the container bottom surface, passes through the gap above the cylindrical member from the pulverizing chamber, and exits from the discharge port through the discharge port. And the remaining air reverses and rises above the cylindrical member and passes directly to the discharge port. The raw material and the crushed balls move as follows by the two air flows. That is, the raw material and the grinding balls in the grinding chamber are mainly pushed up by the rotational force of the cylindrical member and a part of the air, and are extruded from the gap above the cylindrical member. At this time, the raw material powder pulverized to a certain degree is discharged from the discharge port through the discharge port by the air, but the pulverized ball and the unpulverized coarse raw material which are strongly subjected to centrifugal force fall into the cylindrical member. Next, in the cylindrical member, the crushed balls collide with each other in the absence of fine powder, or the crushed ball collides with the inner surface of the cylindrical member, and the fine powder attached to the crushed ball surface is peeled off. It is transported outside the machine on the flowing air. Then, the crushed balls and the uncrushed coarse-grained raw material are sent again into the crushing chamber under the cylindrical member, and at this time, the raw material from the raw material supply pipe is also sent.

このようにして、微粉砕された原料は粉砕室内に長く
留められることなく、速やかに機外に排出され、粉砕ボ
ール表面に付着した微粉末を剥離除去させて粉砕ボール
の粉砕面を更新させる。
In this way, the finely pulverized raw material is discharged out of the apparatus without being kept in the pulverizing chamber for a long time, and the pulverized surface of the pulverized ball is renewed by peeling off the fine powder attached to the surface of the pulverized ball.

(発明の効果) このように、本発明は微粉砕された原料粉末を粉砕室
内に長く留めることなく、速やかに機外に排出させるこ
とができ、原料の過粉砕を抑えて製品粒度の揃ったもの
が得られること。また、動力消費の軽減と粉砕ボールの
摩耗を減少させることができる。更に、粉砕ボール表面
に付着した微粉末を除去させて粉砕面を更新させること
ができ、粉砕効果を維持させて粉砕性能を向上させるこ
とができる。
(Effects of the Invention) As described above, according to the present invention, the finely pulverized raw material powder can be quickly discharged to the outside of the machine without being kept in the pulverizing chamber for a long time. Things can be obtained. Further, power consumption can be reduced and wear of the crushed ball can be reduced. Further, the fine powder attached to the surface of the crushed ball can be removed to renew the crushed surface, and the crushing effect can be maintained and the crushing performance can be improved.

(実施例) 次に、実施例を第1図により説明する。基台1には電
動機2、変速機3よりなる駆動装置4と円筒状の容器5
が固定されてあり、容器5の中心には駆動装置4の回転
軸4aが設けられている。回転軸4aの先端部には傘状の支
持体6が取付られ、該支持体6には複数本の支持桿7が
取付られ、支持桿7の他端は円筒部材8の内側に接合さ
れ、円筒部材8を保持している。円筒部材8の外周部に
は撹拌羽根9を等間隔に複数枚配設して円筒部材8と容
器5との間に粉砕室10を形成させ、円筒部材8の上下端
面と容器5との間には適当な隙間を設けて通路11を形成
させ、原料および粉砕ボールが該円筒部材8の回りを循
環するようにしている。そのため、容器5の内面5aは角
部をなくした曲面で構成させている。
Example Next, an example will be described with reference to FIG. The base 1 has a driving device 4 including an electric motor 2 and a transmission 3 and a cylindrical container 5.
Is fixed, and a rotating shaft 4 a of the driving device 4 is provided at the center of the container 5. An umbrella-shaped support 6 is attached to the tip of the rotating shaft 4a, a plurality of support rods 7 are attached to the support 6, and the other end of the support rod 7 is joined to the inside of the cylindrical member 8, The cylindrical member 8 is held. A plurality of agitating blades 9 are arranged at equal intervals on the outer periphery of the cylindrical member 8 to form a pulverizing chamber 10 between the cylindrical member 8 and the container 5. The passage 11 is formed with an appropriate gap so that the raw material and the crushed balls circulate around the cylindrical member 8. Therefore, the inner surface 5a of the container 5 has a curved surface with no corners.

容器5の底部には原料を外周部に導くための傘状体12
を設けるほか、傘状体12の下部には空気または不活性ガ
スを導入するための吹込口13を設け、ブロア41または不
活性ガス源29に接続させている。また、容器5の上部に
は容器5と同心で円筒部材8よりも小径の排出口14を設
け、分級機31に接続させている。排出口14の入口部には
調節可能な内筒15を取り付け、この下端が容器5の上端
内面5aよりも幾分下方に突き出るように配設している。
At the bottom of the container 5, an umbrella 12 for guiding the raw material to the outer periphery is provided.
In addition to the above, a blow port 13 for introducing air or an inert gas is provided below the umbrella-shaped body 12, and is connected to the blower 41 or the inert gas source 29. In addition, a discharge port 14 which is concentric with the container 5 and has a smaller diameter than the cylindrical member 8 is provided at the upper part of the container 5 and is connected to a classifier 31. An adjustable inner cylinder 15 is attached to the inlet of the discharge port 14, and is arranged so that its lower end protrudes slightly below the upper inner surface 5 a of the container 5.

排出口14には原料供給管16と空気導入管18よりなる二
重管を中心部を貫通させて配設し、該管の端部が前記支
持体6上部に位置するように配設される。外側の空気導
入管18にはブロア39が接続され、内側の原料供給管16に
はスクリュー式の供給管27を側面部に接続させるほか、
該原料供給管16を上方に延長させて分級機31に連通さ
せ、分級選別後の粗粉を容器5内に返すための循環路17
を形成させている。
A double pipe composed of a raw material supply pipe 16 and an air introduction pipe 18 is disposed at the discharge port 14 so as to penetrate the central part thereof, and is disposed such that an end of the pipe is located above the support 6. . A blower 39 is connected to the outer air introduction pipe 18, and a screw type supply pipe 27 is connected to the side of the inner raw material supply pipe 16,
The raw material supply pipe 16 is extended upward to communicate with a classifier 31, and a circulation path 17 for returning the coarse powder after classification and sorting into the container 5.
Is formed.

分級機31は上部で支持させた分級羽根車32を配置した
分級室33と、分級羽根車32内を通過し排出される微粉排
出口34と、分級室33の下方に設けられた下方小径の傾斜
面を有する円錐環状部35と、該円錐環状部35の下方の機
胴外周部に設けられた二次空気導入口36とによって構成
されている。該分級機31で分級選別された粗粉は前記循
環路17を経て容器5内に戻し、微粉排出口34より排出さ
れた微粉はバグフイルタ37で捕集させる。なお、バグフ
イルタ37にはブロア38が接続される。
The classifier 31 has a classifying chamber 33 in which a classifying impeller 32 supported at an upper portion is disposed, a fine powder discharge port 34 that is discharged through the inside of the classifying impeller 32, and a lower small diameter provided below the classifying chamber 33. It comprises a conical annular portion 35 having an inclined surface, and a secondary air inlet 36 provided on the outer peripheral portion of the machine body below the conical annular portion 35. The coarse powder classified and sorted by the classifier 31 is returned into the container 5 through the circulation path 17, and the fine powder discharged from the fine powder discharge port 34 is collected by a bag filter 37. Note that a blower 38 is connected to the bag filter 37.

容器5の外周上方部には空気噴出口19を設け、ブロア
40を接続して円筒部材8上部の隙間11に向けて空気を噴
出させるようにしている。
An air outlet 19 is provided in the upper part of the outer periphery of the container 5, and a blower
40 is connected to blow air toward the gap 11 above the cylindrical member 8.

また、容器5の外周囲にはジャケット20を設け、加熱
または冷媒の供給源30が接続されている。
A jacket 20 is provided around the outer periphery of the container 5, and a heating or coolant supply source 30 is connected to the jacket 20.

(別の実施例) 第2図および第3図は他の実施例であり、容器5の底
部に多孔板21を取り付け、その下方に空気室22を設け、
ブロア41を接続して円筒部材8内底部において流動作用
を付与させるようにしている。また、円筒部材8の内壁
および空気導入管16の外側にはピン状の撹拌部材23の複
数本を交互に重ね合わせて配設し、円筒部材8内部で撹
拌と解砕の両作用を付加させるようにしている。
(Another Embodiment) Figs. 2 and 3 show another embodiment, in which a perforated plate 21 is attached to the bottom of the container 5, and an air chamber 22 is provided below the perforated plate.
The blower 41 is connected so that a fluidizing action is provided at the inner bottom portion of the cylindrical member 8. Further, a plurality of pin-shaped stirring members 23 are alternately arranged on the inner wall of the cylindrical member 8 and the outside of the air introduction pipe 16 so as to add both the stirring and the crushing action inside the cylindrical member 8. Like that.

支持桿7の形状は、断面が円形、楕円形、角、平形、
菱形の何れであってもよいが、図示のように平板を撹拌
羽根9の回転方向側あるいは反回転方向側に傾斜させて
原料および粉砕ボールに対する撹拌効果を高めるように
してもよい。
The shape of the support rod 7 is circular, elliptical, square, flat,
Any of rhombic shapes may be used, but the flat plate may be inclined in the rotation direction side or the counter rotation direction side of the stirring blade 9 as shown in the figure to enhance the stirring effect on the raw material and the grinding balls.

排出口14周壁に多数の小片24を取付け、第3図に示す
ように、容器5内における施回気流eに対して小片24を
反回転方向に傾斜させてスリット状の隙間25を形成さ
せ、該隙間25を空気流fに乗せて原料粉砕品を通過さ
せ、他方、粉砕ボールPは通過させないで円筒部材8内
に落とし込むように構成させている。
A large number of small pieces 24 are attached to the peripheral wall of the discharge port 14, and as shown in FIG. 3, the small pieces 24 are inclined in the anti-rotation direction with respect to the circulating air flow e in the container 5 to form slit-shaped gaps 25. The gap 25 is placed on the air flow f to allow the pulverized raw material to pass therethrough, while the pulverized ball P is dropped into the cylindrical member 8 without passing through.

分級機31からの粗粉はロータリーバブル26を介して供
給機27のホッパ28に返すようにしている。また、撹拌羽
根9の形状は種々の設計変更が可能であり、例えば第4
図にその一例を示すが、(A)のように平板9aを回転方
向の後方側に傾斜させたり、(B)のように円筒部材8
の軸方向に対して平板9aの下方を回転後方に傾けて取り
付けたり、(C)のように多数のピン9cや小片部材で構
成させたり、(D)のように撹拌羽根9d部分を円筒部材
8と一体成形させたものであってもよい。
The coarse powder from the classifier 31 is returned to the hopper 28 of the feeder 27 via the rotary bubble 26. Further, the shape of the stirring blade 9 can be variously changed in design.
One example is shown in the figure. The flat plate 9a is inclined rearward in the rotation direction as shown in FIG.
The lower part of the flat plate 9a is rotated and tilted rearward with respect to the axial direction, or it is composed of a large number of pins 9c and small piece members as shown in (C), or the stirring blade 9d is formed as a cylindrical member as shown in (D). 8 may be integrally formed.

また、撹拌羽根9と円筒部材8との間には隙間があっ
てもよく、両部材間にスペーサを取り付けたり、あるい
は長さの異なる別々の支持桿7により別個に保持させて
もよい。
In addition, a gap may be provided between the stirring blade 9 and the cylindrical member 8, and a spacer may be attached between both members, or may be separately held by separate support rods 7 having different lengths.

なお、特許請求の範囲の項に図面との対照を便利にす
るために符号を記すが、該記入により本発明は添付図面
の構造に限定されるものではない。
In the claims, reference numerals are provided for convenience of comparison with the drawings, but the present invention is not limited to the structure of the accompanying drawings by the entry.

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

第1図は本実施例の要部断面図、第2図は別の実施例の
要部断面図、第3図は第2図I−I部分の拡大断面視
図、第4図は撹拌羽根9についての実施例である。 図において、5……容器、5a……内面、8……円筒部
材、9……撹拌羽根、11……隙間、12……傘状体、13…
…吹込口、14……排出口、15……内筒、16……原料供給
管、17……循環路、18……空気導入管、19……空気噴出
口、20……ジャケット、22……空気室、23……撹拌部
材、24……小片、25……スリット状の隙間、31……分級
機である。
1 is a cross-sectional view of a main part of this embodiment, FIG. 2 is a cross-sectional view of a main part of another embodiment, FIG. 3 is an enlarged cross-sectional view of a portion II in FIG. 2, and FIG. Example 9 is an example. In the figure, 5 ... container, 5a ... inner surface, 8 ... cylindrical member, 9 ... stirring blade, 11 ... gap, 12 ... umbrella, 13 ...
... Inlet, 14 ... Outlet, 15 ... Inner cylinder, 16 ... Raw material supply pipe, 17 ... Circulation path, 18 ... Air introduction pipe, 19 ... Air outlet, 20 ... Jacket, 22 ... ... air chamber, 23 ... stirring member, 24 ... small piece, 25 ... slit-shaped gap, 31 ... classifier.

Claims (11)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】容器内に粉砕ボールを入れ撹拌羽根を回転
させる形式の粉砕機であって、撹拌羽根9の内側に同心
の円筒部材8を容器5の上面および底面に適当な隙間11
を持たせて配設し、円筒部材8上方の容器5上面に円筒
部材8の内径よりも小径の排出口14を設け、円筒部材8
内に原料供給管16と空気導入管18とを配設させたことを
特徴とする乾式媒体ミル。
1. A crusher of the type in which crushing balls are put into a container and a stirring blade is rotated, and a concentric cylindrical member 8 is provided inside a stirring blade 9 with an appropriate gap 11 on the upper and lower surfaces of the container 5.
A discharge port 14 having a diameter smaller than the inner diameter of the cylindrical member 8 is provided on the upper surface of the container 5 above the cylindrical member 8.
A dry medium mill characterized in that a raw material supply pipe 16 and an air introduction pipe 18 are provided therein.
【請求項2】撹拌羽根9を円筒部材8の外周部に取り付
けた請求項1記載の乾式媒体ミル。
2. The dry medium mill according to claim 1, wherein the stirring blades 9 are attached to an outer peripheral portion of the cylindrical member 8.
【請求項3】円筒部材8の内面および空気導入管18の外
周部に複数の撹拌部材23を取り付けた請求項1記載の乾
式媒体ミル。
3. The dry-type medium mill according to claim 1, wherein a plurality of agitating members are mounted on an inner surface of the cylindrical member and an outer peripheral portion of the air introducing pipe.
【請求項4】原料供給管16と空気導入管18を二重管で構
成し、該二重管を排出口14の中心部に上方より貫通させ
て配設した請求項1記載の乾式媒体ミル。
4. The dry medium mill according to claim 1, wherein the raw material supply pipe 16 and the air introduction pipe 18 are constituted by double pipes, and the double pipe is disposed so as to penetrate from the upper portion to the center of the discharge port 14 from above. .
【請求項5】排出口14の入口部に容器5の内面5aよりも
下方に突出させて円筒15を具備した請求項1記載の乾式
媒体ミル。
5. The dry-type medium mill according to claim 1, further comprising a cylinder 15 protruding below the inner surface 5a of the container 5 at an inlet of the discharge port 14.
【請求項6】排出口14の入口部周壁に多数の小片24を撹
拌羽根9の反回転方向に傾斜させて配設してスリット状
の隙間25を形成させた請求項1記載の乾式媒体ミル。
6. A dry medium mill according to claim 1, wherein a number of small pieces are arranged on the peripheral wall of the inlet of the discharge port so as to be inclined in the counter-rotating direction of the stirring blade to form slit-shaped gaps. .
【請求項7】原料供給管16の他端上方側を延長して分級
機31に接続し、分級機31内の回収粗粉を容器5内に送り
込むための循環路17を形成させた請求項1記載の乾式媒
体ミル。
7. A circulation path 17 for feeding the recovered coarse powder in the classifier 31 into the container 5 by extending the upper end of the other end of the raw material supply pipe 16 and connecting to the classifier 31. 2. A dry media mill according to claim 1.
【請求項8】容器5底部に多孔板21を取り付け、その下
方にブロア41を接続させて空気室22を設けた請求項1記
載の乾式媒体ミル。
8. The dry media mill according to claim 1, wherein a perforated plate 21 is attached to the bottom of the container 5 and a blower 41 is connected below the perforated plate 21 to provide an air chamber 22.
【請求項9】容器5底部の中心部に空気または不活性ガ
スの吹込口13を有する傘状体12を配設した請求項1記載
の乾式媒体ミル。
9. A dry media mill according to claim 1, wherein an umbrella-shaped body having an air or inert gas inlet is disposed at the center of the bottom of the container.
【請求項10】容器5の外周部上方に円筒部材8の上方
側の隙間11に向けて開口させた空気噴出口19を配設した
請求項1記載の乾式媒体ミル。
10. The dry medium mill according to claim 1, further comprising an air outlet opening above the outer peripheral portion of the container toward the gap above the cylindrical member.
【請求項11】容器5の外周部に加熱または冷却用のジ
ャケット20を配設した請求項1記載の乾式媒体ミル。
11. The dry medium mill according to claim 1, wherein a jacket 20 for heating or cooling is provided on an outer peripheral portion of the container 5.
JP32707090A 1990-11-27 1990-11-27 Dry media mill Expired - Lifetime JP2918679B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32707090A JP2918679B2 (en) 1990-11-27 1990-11-27 Dry media mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32707090A JP2918679B2 (en) 1990-11-27 1990-11-27 Dry media mill

Publications (2)

Publication Number Publication Date
JPH04193360A JPH04193360A (en) 1992-07-13
JP2918679B2 true JP2918679B2 (en) 1999-07-12

Family

ID=18194957

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32707090A Expired - Lifetime JP2918679B2 (en) 1990-11-27 1990-11-27 Dry media mill

Country Status (1)

Country Link
JP (1) JP2918679B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101431045B1 (en) * 2008-08-25 2014-08-21 호소가와미크론 가부시키가이샤 Medium-agitating powder processing device

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4447321C2 (en) * 1994-12-31 1999-07-22 Omya Gmbh Agitator mill for wet comminution, with separator to retain grinding beads
US5577675A (en) * 1995-01-25 1996-11-26 Mitsui Mining Co., Ltd. Agitating pulverizer
JP5921172B2 (en) 2011-12-09 2016-05-24 アシザワ・ファインテック株式会社 Horizontal dry crusher

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101431045B1 (en) * 2008-08-25 2014-08-21 호소가와미크론 가부시키가이샤 Medium-agitating powder processing device

Also Published As

Publication number Publication date
JPH04193360A (en) 1992-07-13

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