JPS5920353Y2 - Peripheral discharge type semi-natural grinding mill - Google Patents

Peripheral discharge type semi-natural grinding mill

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Publication number
JPS5920353Y2
JPS5920353Y2 JP16926382U JP16926382U JPS5920353Y2 JP S5920353 Y2 JPS5920353 Y2 JP S5920353Y2 JP 16926382 U JP16926382 U JP 16926382U JP 16926382 U JP16926382 U JP 16926382U JP S5920353 Y2 JPS5920353 Y2 JP S5920353Y2
Authority
JP
Japan
Prior art keywords
rotating drum
crushed
crushing
mill
shell
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
Application number
JP16926382U
Other languages
Japanese (ja)
Other versions
JPS58108144U (en
Inventor
泰二 大塚
Original Assignee
大塚鉄工株式会社
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 大塚鉄工株式会社 filed Critical 大塚鉄工株式会社
Priority to JP16926382U priority Critical patent/JPS5920353Y2/en
Publication of JPS58108144U publication Critical patent/JPS58108144U/en
Application granted granted Critical
Publication of JPS5920353Y2 publication Critical patent/JPS5920353Y2/en
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 本考案は採掘された大塊の岩石を破砕して得られた砕石
をミル本体内に供給し、該砕石に衝撃、転勤、圧縮等を
付与することによってこれを更に破砕乃至粉砕して所望
粒度の被破砕物乃至細骨材となし、次いで、これらをミ
ル本体の外部に排出するようにした周辺排出型半自生粉
砕ミルに係るものである。
[Detailed description of the invention] The present invention supplies crushed stone obtained by crushing a large block of mined rock into the mill body, and further crushes it by applying impact, displacement, compression, etc. to the crushed stone. The present invention relates to a peripheral discharge type semi-autogenous grinding mill that crushes or grinds the crushed material or fine aggregate to a desired particle size, and then discharges the crushed material to the outside of the mill body.

従来、前記種類の周辺排出型半自生粉砕ミルにおいては
、破砕乃至粉砕のためにミル内に投入された材料はミル
の回転に伴いミルのドラム内周面に取り付けられたレー
ルライナー乃至クラツシングバーの作用を受けて圧縮と
圧縮開放に伴う衝撃並びに転勤等により破砕されるもの
であるが、この場合、ミル本体内で適当な粒径に破砕さ
れた産物はドラム周辺に設けた複数個の排出グレート乃
至スクリーンから排出され且つ軽いスラグ分は微粉化さ
れてミル本体内を通過する空気流によりシェル外に排出
されるようになされている。
Conventionally, in the peripheral discharge type semi-autogenous grinding mill of the above-mentioned type, the material input into the mill for crushing or pulverization is crushed by the action of the rail liner or crushing bar attached to the inner peripheral surface of the drum of the mill as the mill rotates. In this case, the products crushed to an appropriate particle size within the mill body are crushed through a plurality of discharge grates installed around the drum. The light slag discharged from the screen is pulverized and discharged out of the shell by an air flow passing through the mill body.

しかして、前述したような周辺排出型半自生粉砕ミルを
乾式で操業する場合、最適の破砕効率を得るためには投
入原料の量、即ち原料レベルがおのずから定ってくるが
、そのような適量の原料レベルで運転する場合、グレー
ト乃至スクリーン上の原料層が比較的厚くなるために、
既に所定の粒径に破砕されているにもかかわらず原料層
に妨げられて排出されずにミル内に留まってしまう産物
が生じ、この結果として処理能力の低下と過粉砕を招く
原因となる。
However, when operating the peripheral discharge type semi-autogenous grinding mill as described above in a dry manner, the amount of input raw material, that is, the raw material level, is naturally determined in order to obtain the optimal crushing efficiency. When operating at a raw material level of
Although the product has already been crushed to a predetermined particle size, it is obstructed by the raw material layer and remains in the mill without being discharged, resulting in a reduction in processing capacity and over-grinding.

これを回避するために、原料レベルを排出が円滑に行な
われる程度まで下げてしまうと、こんどは破砕作用助勢
用のスチールボールまたは原料大塊の空打ちによってグ
レート乃至スクリーン、デフレクタライナー及びクラツ
シングバー等の寿命を著しく損なう原因となる。
In order to avoid this, the raw material level is lowered to a level that allows smooth discharge, and then the grates, screens, deflector liners, crushing bars, etc. are This will cause a significant decrease in lifespan.

一方、前記周辺排出型半自生粉砕ミルを湿式で操業する
場合は排出グレート乃至スクリーンがドラム外周に設け
であるために言わば遠心脱水機のように水が充分仕事を
しない間に排出されてしまい必要以上に多量の水を補給
しなければ水処理効果が減殺され、スラグ分のミル内へ
の付着や目詰りを起して機能を失なう恐れがある。
On the other hand, when the peripheral discharge type semi-autogenous grinding mill is operated in a wet manner, the discharge grate or screen is installed around the drum outer circumference, so that the water is discharged while it is not doing enough work, like in a centrifugal dehydrator. If a larger amount of water is not replenished, the water treatment effect will be diminished, and there is a risk that slag will adhere to the inside of the mill and cause clogging, resulting in a loss of functionality.

本考案はこれらの欠点を排除することを目的とするもの
であって、その要旨とするところは、採掘された大塊の
岩石を破砕して得られた砕石等の原料をミル本体内に供
給し、該ミル本体の回転によって前記砕石に衝撃、転勤
、圧縮等を付与せしめて所望粒度の産物を得る型式の周
辺排出型半自生粉砕ミルにおいて、前記ミル本体を回転
ドラムとこの回転ドラムの原料投入側に対向する側面に
一体接合したシェルとから形成し、上記の回転ドラムに
破砕に関与するデフレクタライナー、クラツシングバー
等を取り付け、また上記のシェル周面全体に複数個の排
出グレート乃至スクリーンを設け、更に破砕作業中に回
転ドラム内下部に下がら順次層をなして生ずる大塊層、
中塊層、粉層のうちの上層部の破砕産物をシェル内へ移
行させて排出グレート乃至スクリーンから排出させ、ま
た排出できない不完全破砕原料を回転ドラム内に戻すよ
うに、上記のシェルが回転ドラムに向けて広がった截頭
円錐形をなしている点に存するものであり、かくして、
本考案によれば、ミル本体を専ら破砕に関与するドラム
と産物排出に関与するシェルとに区分し上記シェルに被
破砕物乃至細骨材の排出グレート乃至スクリーンを設け
たことによって前記ミル本体内には被破砕物乃至細骨材
がミル回転による遠心力とその嵩比重の大小により外側
から大塊層、中塊層、粉層の順に積層されるために、既
破砕の産物は順次シェル内に移行して早期に取り出され
、従って従来のミルに比較してドラム内での破砕原料レ
ベルを最高の値にすることができると共に供給水の滞留
時間を長く保つことができ、従って、乾式の場合は破砕
原料レベルの過高低による処理能力の低下と過粉砕を防
止し得ると共に排出グレート乃至スクリーン、デフレク
タライナー及びクラツシングバー等の寿命を損なうこと
はなく、加えて、湿式の場合はスラグ分のミル内への付
着や目詰りを起さず機能を失なうことはない等の利点を
有するものである。
The purpose of this invention is to eliminate these drawbacks, and its gist is to supply raw materials such as crushed stone obtained by crushing large blocks of mined rock into the mill body. In a peripheral discharge type semi-autogenous grinding mill of the type in which a product of a desired particle size is obtained by imparting impact, transfer, compression, etc. to the crushed stone by the rotation of the mill body, the mill body is connected to a rotating drum and the raw material for this rotating drum. A shell is integrally joined to the side facing the input side, a deflector liner, a crushing bar, etc. that are involved in crushing are attached to the rotating drum, and a plurality of discharge grates or screens are provided around the entire circumference of the shell. , Furthermore, during the crushing operation, a layer of large lumps is formed in the lower part of the rotating drum, forming successive layers.
The shell rotates so that the crushed products in the upper layer of the middle lump layer and powder layer are transferred into the shell and discharged from the discharge grate or screen, and the incompletely crushed raw materials that cannot be discharged are returned to the rotating drum. It consists in the fact that it has a truncated conical shape that widens towards the drum, and thus,
According to the present invention, the mill body is divided into a drum that is exclusively involved in crushing and a shell that is involved in product discharge, and the shell is provided with a discharge grate or screen for discharging materials to be crushed or fine aggregate. In this case, the materials to be crushed or fine aggregate are layered from the outside in the order of a large lump layer, a medium lump layer, and a powder layer due to the centrifugal force generated by the rotation of the mill and the size of their bulk specific gravity. The raw material level in the drum can be maximized and the residence time of the feed water can be kept longer than in conventional mills, thus allowing for a longer residence time of the feed water. In this case, it is possible to prevent a decrease in processing capacity and over-grinding due to excessively high or low levels of crushed raw materials, and the life of the discharge grate, screen, deflector liner, crushing bar, etc. is not impaired, and in addition, in the case of a wet type, the mill for slag It has the advantage that it does not adhere to the inside or cause clogging and does not lose its function.

次に図面により本考案を更に詳細に説明する。Next, the present invention will be explained in more detail with reference to the drawings.

先ず、第1図は従来型式の乾式周辺排出型半自生粉砕ミ
ルを略図的に示すもので、1はミル本体、2はテ゛フレ
クタライナー、3はレール状のクラツシングバー、4,
5は排出グレート乃至スクリーンであり、矢印A方向か
ら給送された砕石はミル本体1内に装入され、該ミル本
体の回転に伴ないテ゛フレクタライナー2とクラツシン
グバー3によって圧縮され、衝撃を加えられ、転勤せし
められて破砕乃至粉砕された後、所望粒度の産物(被破
砕物乃至細骨材)となって排出グレート乃至スフノーン
4,5からミル本体外(矢印B方向)に排出され、軽い
スラグ分は微粉化されてミル本体内を通過する空気流に
より矢印C方向がら外部に排出せしめられる。
First, Fig. 1 schematically shows a conventional dry peripheral discharge type semi-autonomous grinding mill, in which 1 is the mill body, 2 is a deflector liner, 3 is a rail-shaped crushing bar, 4,
Reference numeral 5 designates a discharge grating or screen, in which crushed stone fed from the direction of arrow A is charged into the mill body 1, compressed by the deflector liner 2 and the crushing bar 3 as the mill body rotates, and is subjected to impact. After being transferred and crushed or pulverized, products with the desired particle size (crushed material or fine aggregate) are discharged from the discharge grate or sufnones 4 and 5 to the outside of the mill body (in the direction of arrow B), and a light slag is produced. The fraction is pulverized and discharged to the outside in the direction of arrow C by an air flow passing through the mill body.

更に、第2図乃至第4図は本考案に係る周辺排出型半自
生粉砕ミルを示し、殊に第2図は乾式、第3図及び第4
図は湿式であつ七、ミル本体11を形成するドラム12
(破砕帯域a)の内側には複数個のテ゛フレクタライナ
ー13及びライナー14が、ドラム円周内側には複数個
のレール状のクラツシングバー15が設けであると共に
ミル本体11を形成するシェル16(産物排出帯域b)
には複数個の第1及び第2排出グレート乃至スクリーン
17.18が゛設けてあり、この場合、シェル16は第
2図ではドラム12の側壁19に一体接合せしめられて
おり、更に截頭円錐状に形成されている。
Furthermore, FIGS. 2 to 4 show peripheral discharge type semi-autogenous grinding mills according to the present invention, in particular, FIG. 2 is a dry type, and FIGS.
The figure shows a wet type, and a drum 12 forming the mill body 11.
A plurality of deflector liners 13 and liners 14 are provided inside the crushing zone a, and a plurality of rail-shaped crushing bars 15 are provided inside the drum circumference. Band b)
is provided with a plurality of first and second discharge grates or screens 17, 18, the shell 16 being integrally joined to the side wall 19 of the drum 12 in FIG. It is formed in the shape of

この場合のシェルのテーパー角度は30度前後が好まし
い。
In this case, the taper angle of the shell is preferably around 30 degrees.

第3図及び第4図ではシェル長径がドラム直径に相当し
て前記ドラムの周縁20と一体接合せしめられており、
この場合のシェルのテーパー角度も30度前後が好まし
い。
In FIGS. 3 and 4, the major axis of the shell corresponds to the drum diameter and is integrally joined to the peripheral edge 20 of the drum,
In this case, the taper angle of the shell is also preferably about 30 degrees.

しかして、第2図に示すミルにおいては、矢印、A方向
から供給された砕石等の破砕原料はドラム12内で破砕
乃至粉砕された後、排出グレート乃至スクリーン17.
18から産物乃至細骨材として外部(矢印B方向)に排
出され、微粉化した軽いスラグ分は前記ミル本体内を通
過する空気流により矢印C方向から外部に排出される。
In the mill shown in FIG. 2, crushed raw materials such as crushed stone supplied from the direction of arrow A are crushed or pulverized in the drum 12 and then transferred to the discharge grate or screen 17.
18 as a product or fine aggregate to the outside (in the direction of arrow B), and the pulverized light slag is discharged to the outside in the direction of arrow C by the air flow passing through the mill body.

この場合には篩目の異る第1及び゛第2排出グレート乃
至スクリーン17.18から2種類の粒度の異なる産物
が別々に得られるものである。
In this case, two products with different particle sizes are obtained separately from the first and second discharge grates or screens 17 and 18, which have different mesh sizes.

第3図に示すミルにおいては、矢印A方向から水と一緒
に供給された砕石等の破砕原料はドラム12内で破砕乃
至粉砕された後、微粉化せしめられたスラグ分は水と共
に第1排出グレート乃至スクリーン17より排出され且
つ他の破砕物乃至細骨材は第2排出グレート乃至スクリ
ーン18より排出される(矢印B方向)。
In the mill shown in Fig. 3, crushed raw materials such as crushed stones supplied together with water from the direction of arrow A are crushed or pulverized in the drum 12, and then the pulverized slag is discharged together with water into the first discharge chamber. The aggregate is discharged from the grate or screen 17, and the other crushed material or fine aggregate is discharged from the second discharge grate or screen 18 (in the direction of arrow B).

次に、第3図に略図的に示されているミルの具体例を第
4図について説明すると、ミル本体11はこれと同一軸
線上にある一対のトラニオン21.22により支持され
ており、この場合、これらトラニオンは、図示していな
いがそれぞれ基礎上に取付けられたベアリングにて軸承
され、一方のトラニオン21には矢印A方向から破砕原
料23を水と一緒に供給し、他方のトラニオン22は適
宜駆動伝達機構に接続して回転可能となすことによって
前記ミル本体が回転駆動せしめられるものであり、この
回転駆動に伴ない砕石等の破砕原料23はデフレクタラ
イナー13、ライナー14及びクラツシングバー15の
協働作用による衝撃、転勤、圧縮等が付与されて破砕乃
至粉砕せしめられ、ミル回転にて生成する遠心力と被破
砕物の嵩比重の大小により図示のようにドラム12(破
砕帯域a)からシェル16(産物排出帯域b)に亘って
大塊層24、中塊層25、粉層26の順に積層される。
Next, a specific example of the mill schematically shown in FIG. 3 will be explained with reference to FIG. In this case, these trunnions are each supported by a bearing mounted on the foundation (not shown), and one trunnion 21 is supplied with crushed raw material 23 along with water from the direction of arrow A, and the other trunnion 22 is supplied with water. The mill main body is rotationally driven by being connected to an appropriate drive transmission mechanism so as to be rotatable, and as the mill body is rotated, the crushed raw material 23 such as crushed stone is moved by the cooperation of the deflector liner 13, liner 14, and crushing bar 15. The shells are crushed or pulverized by applying impact, transfer, compression, etc. due to the action, and the shells are separated from the drum 12 (crushing zone a) as shown in the figure due to the centrifugal force generated by the rotation of the mill and the bulk specific gravity of the material to be crushed. 16 (product discharge zone b), a large lump layer 24, a medium lump layer 25, and a powder layer 26 are stacked in this order.

即ち、破砕帯域aには大塊層24が存在し、産物排出帯
域すには中塊層25及び゛粉層26か゛第2及び第1排
出グレート乃至スクリーン18及び17にそれぞれ対応
して位置するように積層されるために中塊層25の砕石
乃至細骨材は第2排出グレート乃至スクリーン18から
水にて洗滌されて、また粉層26の微粉化されたスラグ
分は第1排出グレート乃至スクリーン17から水と共に
外部に排出される。
That is, in the crushing zone a, there is a large lump layer 24, and in the product discharge zone, a medium lump layer 25 and a powder layer 26 are located corresponding to the second and first discharge grates to the screens 18 and 17, respectively. In order to be layered in this manner, the crushed stone or fine aggregate in the medium lump layer 25 is washed with water from the second discharge grate or the screen 18, and the pulverized slag in the powder layer 26 is washed away from the first discharge grate or the screen 18. The water is discharged from the screen 17 to the outside together with water.

なお、叙上の実施例では湿式の場合について説明したも
ので、所定サイズの産物(細骨材)は1種類しか得られ
ないが、乾式の場合は微粉化されたスラグ分はミル本体
11内を通過する空気流にてトラニオン22から排出さ
れるために第1及び第2排出グレート乃至スクリーン1
7,18の篩目を異ならしめれば2種類の産物(細骨材
)を得ることができるものであり、また岩石乃至砕石よ
りコンクリート用細骨材を得る代りに転炉、高炉等にて
生ずるスラグを材料としても同様の目的を遠戚すること
ができ、更には他の用途に使用されるべき砂の製造にも
適用することができるものである。
In addition, in the above-mentioned example, explanation was given for the case of a wet type, and only one type of product (fine aggregate) of a predetermined size can be obtained, but in the case of a dry type, the pulverized slag is stored in the mill body 11. first and second exhaust grate or screen 1 for exhaust from the trunnion 22 with the airflow passing through the
Two types of products (fine aggregate) can be obtained by using different sieve sizes for sieves 7 and 18, and instead of obtaining fine aggregate for concrete from rock or crushed stone, it can be obtained by using a converter, blast furnace, etc. The same purpose can be achieved by using the resulting slag as a material, and it can also be applied to the production of sand to be used for other purposes.

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

第1図は従来の周辺排出型半自生粉砕ミルを示す略図的
断面図、第2図及び第3図は本考案のそれぞれ異なった
周辺排出型半自生粉砕ミルを示す略図的断面図、第4図
は第3図の具体例を示す軸方向半部断面正面図である。 なお、図示された主要部と符号との対応関係は下記の通
りである。 11・・・・・・ミル本体、12・・・・・・ドラム、
16・・・・・・シェル、17.18・・・・・・第1
及び第2排出グレート乃至スクリーン、19・・・・・
・ドラム側壁、20・・・・・・ドラム周縁、23・・
・・・・破砕原料、24・・・・・・大塊層、25・・
・・・・中塊層、26・・・・・・粉層。
FIG. 1 is a schematic sectional view showing a conventional peripheral discharge type semi-autogenous grinding mill, FIGS. 2 and 3 are schematic sectional views showing different peripheral discharge type semi-autogenous grinding mills of the present invention, and FIG. The figure is an axial half-sectional front view showing the specific example of FIG. 3. Note that the correspondence relationship between the main parts shown and the symbols is as follows. 11... Mill body, 12... Drum,
16...Shell, 17.18...1st
and second discharge grate or screen, 19...
・Drum side wall, 20...Drum periphery, 23...
...Crushed raw material, 24...Large lump layer, 25...
...Medium lump layer, 26...Powder layer.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 採掘された大塊の岩石を破砕して得られた砕石等の原料
をミル本体内に供給し、該ミル本体の回転によって前記
砕石に衝撃、転勤、圧縮等を付与せしめて所望粒度の産
物を得る型式の周辺排出型半自生粉砕ミルにおいて、前
記ミル本体を回転ドラムと、この回転ドラムの原料投入
側に対向する側面に一体接合したシェルとから形威し、
上記の回転ドラムに破砕に関与するテ゛フレクタライナ
ー、クラツシングバー等を取り付け、また上記のシェル
周面全体に複数個の排出グレート乃至スクリーンを設け
、更に破砕作業中に回転ドラム内下部に下から順次層を
なして生ずる大塊層、中塊層、粉層のうちの上層部の破
砕産物をシェル内へ移行させて排出グレート乃至スクリ
ーンから排出させ、また排出できない不完全破砕原料を
回転ドラム内に戻すように、上記のシェルが回転ドラム
に向けて広がった截頭円錐形をなしていることを特徴と
する周辺排出型半自生粉砕ミル。
Raw materials such as crushed stone obtained by crushing a large block of mined rock are fed into the mill body, and the rotation of the mill body applies impact, transfer, compression, etc. to the crushed stone to produce a product with a desired particle size. In the peripheral discharge type semi-autogenous grinding mill of the type obtained, the mill body is formed of a rotating drum and a shell integrally joined to the side surface of the rotating drum opposite to the raw material input side,
A deflector liner, crushing bar, etc. that are involved in crushing are attached to the above rotating drum, and multiple discharge grates or screens are provided around the entire circumference of the above shell, and layers are sequentially applied from the bottom inside the rotating drum during the crushing operation. The crushed products in the upper layers of the large lump layer, medium lump layer, and powder layer that are generated are transferred into the shell and discharged from the discharge grate or screen, and the incompletely crushed raw materials that cannot be discharged are returned to the rotating drum. A peripheral discharge type semi-autonomous grinding mill characterized in that the above-mentioned shell has a truncated conical shape that widens toward the rotating drum.
JP16926382U 1982-11-10 1982-11-10 Peripheral discharge type semi-natural grinding mill Expired JPS5920353Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16926382U JPS5920353Y2 (en) 1982-11-10 1982-11-10 Peripheral discharge type semi-natural grinding mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16926382U JPS5920353Y2 (en) 1982-11-10 1982-11-10 Peripheral discharge type semi-natural grinding mill

Publications (2)

Publication Number Publication Date
JPS58108144U JPS58108144U (en) 1983-07-23
JPS5920353Y2 true JPS5920353Y2 (en) 1984-06-13

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP16926382U Expired JPS5920353Y2 (en) 1982-11-10 1982-11-10 Peripheral discharge type semi-natural grinding mill

Country Status (1)

Country Link
JP (1) JPS5920353Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101827655B (en) * 2007-10-18 2012-11-21 泰加工业有限公司 Composite steel claded mill liner

Also Published As

Publication number Publication date
JPS58108144U (en) 1983-07-23

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