JP2015180507A - Mill - Google Patents

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JP2015180507A
JP2015180507A JP2015140385A JP2015140385A JP2015180507A JP 2015180507 A JP2015180507 A JP 2015180507A JP 2015140385 A JP2015140385 A JP 2015140385A JP 2015140385 A JP2015140385 A JP 2015140385A JP 2015180507 A JP2015180507 A JP 2015180507A
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raw material
screen
corrugated
crushing
frame
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JP2015180507A5 (en
JP5973629B2 (en
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加藤 文雄
Fumio Kato
文雄 加藤
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Tsukasa Co Ltd
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Tsukasa Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C13/00Disintegrating by mills having rotary beater elements ; Hammer mills
    • B02C13/26Details
    • B02C13/282Shape or inner surface of mill-housings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C13/00Disintegrating by mills having rotary beater elements ; Hammer mills
    • B02C13/22Disintegrating by mills having rotary beater elements ; Hammer mills with intermeshing pins ; Pin Disk Mills

Abstract

PROBLEM TO BE SOLVED: To provide a mill which makes the particle size of a pulverization material finer and thereby improves the pulverization efficiency.SOLUTION: A wave shape frame 21 includes: a wave shape plate 21a having an arc shape; a screen 21b which is formed at a part of a lower part of the wave shape plate 21a and connected with both end parts of the wave form plate 21a; a cylindrical front frame 21c fixed to a front surface of the wave shape plate 21a; and a cylindrical rear frame 21d fixed to a rear surface of the wave shape plate 21a. The wave shape member 21a has a non-penetration structure where holes are not formed and particulate objects cannot pass. In the wave shape member 21a, a wave, in which trough parts and crest parts are alternately formed in a circumferential direction, is formed regularly. A revolving pulverization material is irregularly reflected by the wave shape member 21a.

Description

本発明は、食品、化学品、医薬品等の粉粒体、例えば、小麦、蕎麦、大豆、小豆、コーヒー豆、コーン、乾麺、米菓、麺端材等を粉砕するミルに関するものである。   The present invention relates to a mill for pulverizing powders, foods, chemicals, pharmaceuticals and the like, for example, wheat, buckwheat, soybeans, red beans, coffee beans, corn, dried noodles, rice crackers, noodle scraps and the like.

従来、特許文献1、2のミルの粉砕室311では、図8に示す通り、固定歯323に対して、回転盤313に固定された回転歯322が回転することにより、中心から外側に移動させながら固定歯322と回転歯323の隙間で原料Gを挟んで粉砕し、粉粒体が平滑な円筒形スクリーン210を通過し外部に排出されていた。   Conventionally, in the mill crushing chamber 311 of Patent Documents 1 and 2, as shown in FIG. 8, the rotating tooth 322 fixed to the rotating disk 313 rotates with respect to the fixed tooth 323, thereby moving the rotating tooth from the center to the outside. However, the raw material G was crushed with a gap between the fixed teeth 322 and the rotating teeth 323, and the granular material passed through the smooth cylindrical screen 210 and was discharged to the outside.

特開2005−66511号公報JP 2005-66511 A 特開2005−66508号公報JP 2005-66508 A

しかしながら、図8に示す通り、従来の普通の単なる平滑な円筒形スクリーン321では、粉砕原料Gがこの回転歯322を備えた回転盤313と一緒に共回りしてしまい、ある程度の規則性を持って外に押し出される程度であったため、粉砕能力が制限され粉砕原料Gの粒度を小さくすることには限界があった。
そこで、本発明は、粉砕能力を高めて、粉砕原料の粒度をより小さくするミルを提供することを課題とする。
However, as shown in FIG. 8, the conventional ordinary simple cylindrical screen 321 has a certain degree of regularity because the pulverized raw material G rotates together with the rotating disk 313 provided with the rotating teeth 322. Therefore, the pulverizing ability is limited, and there is a limit to reducing the particle size of the pulverized raw material G.
Then, this invention makes it a subject to provide the mill which raises a grinding | pulverization capability and makes the particle size of a grinding | pulverization raw material smaller.

上記課題に鑑み、本発明は、粉粒体原料と空気を供給する供給口と、前記粉粒体原料と空気を受け入れる破砕室と、前記破砕室に設けられる破砕歯と、前記破砕歯で粉砕された粉粒体を篩い分けるスクリーンと、を有するミルにおいて、前記破砕歯が回転盤に固定された複数の破砕歯を備え、前記破砕室の周縁に設けられスクリーンを有する円筒形の波型枠が周方向に非透過性の波型の板材を備え、前記粉粒体原料が、前記破砕室の中心部から供給され、前記破砕室の外周部に移動する間に前記破砕歯により粉砕され、前記波型の板材の曲面に沿って移動する際、前記波型の板材で粉砕されて、前記スクリーンから外部に排出されることを特徴とするミルである。   In view of the above problems, the present invention provides a supply port for supplying powder raw material and air, a crushing chamber for receiving the powder raw material and air, a crushing tooth provided in the crushing chamber, and crushing with the crushing tooth A cylindrical corrugated frame having a screen provided with a plurality of crushing teeth, the crushing teeth being fixed to a rotating disk, and provided on the periphery of the crushing chamber. Is provided with a corrugated plate material that is impermeable in the circumferential direction, and the powder material is supplied from the center of the crushing chamber and crushed by the crushing teeth while moving to the outer periphery of the crushing chamber, When moving along the curved surface of the corrugated plate material, the mill is crushed by the corrugated plate material and discharged to the outside from the screen.

前記波型枠が円筒形側面に非透過性の波型の板材を備えたことが好ましい。この場合、板材の一部にスクリーンを設け粉砕原料を通過させる必要がある。   It is preferable that the corrugated frame includes a non-permeable corrugated plate material on a cylindrical side surface. In this case, it is necessary to provide a screen in a part of the plate material and allow the pulverized raw material to pass through.

前記波型枠が円筒形側面に波型のスクリーンを備えたことが好ましい。この場合、波型スクリーンの全部又は一部が波型である。一部に平坦なスクリーンを設けてもよい。   It is preferable that the corrugated frame has a corrugated screen on a cylindrical side surface. In this case, all or part of the corrugated screen is corrugated. A flat screen may be provided in part.

このミルはインライン、非インラインのいずれにも適用できる。インラインの場合には、粉粒体と空気の混合気の空気輸送ライン設備の途中に設置され、粉砕された原料は輸送空気によって輸送される。   This mill can be applied both inline and non-inline. In the case of in-line, the raw material which is installed in the middle of an air transportation line facility of a mixture of powder and air and pulverized is transported by transportation air.

破砕装置は粉粒体を破砕できるものであれば構造は限定されるものではない。例えば、原料供給口と、原料供給口と連通し原料を受け入れ粉砕する粉砕室と、粉砕室を開閉する開閉扉と、該開閉扉の内側に固定される固定盤と、前記粉砕室の内側に配置され回転軸によって回転する回転盤と、該回転盤の表面に固定される複数の第1衝撃片と、該第1衝撃片の隙間に配置され前記固定盤に形成される複数の第2衝撃片とから構成される粉砕部と、を備えたものが好ましい。 The structure of the crushing device is not limited as long as it can crush the granular material. For example, a raw material supply port, a pulverization chamber that communicates with the raw material supply port and receives and pulverizes the raw material, an open / close door that opens and closes the pulverization chamber, a fixed plate fixed inside the open / close door, and an inside of the pulverization chamber A rotating disk disposed and rotated by a rotating shaft, a plurality of first impact pieces fixed to the surface of the rotating disk, and a plurality of second impacts formed in the fixed plate and disposed in a gap between the first impact pieces. What provided the grinding | pulverization part comprised from a piece is preferable.

請求項1記載の発明によれば、波型枠が旋回する粉砕原料を乱反射することにより、粒度を細かくでき、粉砕効果が高くなる。   According to the first aspect of the present invention, the pulverized raw material on which the corrugated frame swirls is irregularly reflected, whereby the particle size can be reduced and the pulverization effect is enhanced.

請求項2記載の発明によれば、粉砕原料の乱反射が確実となるので、粉砕効率が一層高まる。   According to the invention described in claim 2, since the irregular reflection of the pulverized raw material is ensured, the pulverization efficiency is further increased.

請求項3記載の発明によれば、粉砕原料を波型枠で乱反射させながらスクリーンを通過させることができるので、篩い効率が高まる。   According to the invention described in claim 3, since the screen can be passed while the pulverized raw material is diffusely reflected by the corrugated frame, the sieving efficiency is increased.

本発明実施形態のミルの開閉扉が閉じた状態の斜視図である。It is a perspective view in the state where the door of the mill of the embodiment of the present invention was closed. 同ミルの開閉扉が開き波型枠を取り外した状態の外観を示す斜視図である。It is a perspective view which shows the external appearance of the state which the opening-and-closing door of the mill removed the wave formwork. 同粉砕室の開閉扉を閉じた状態の内部構造を示す説明図である。It is explanatory drawing which shows the internal structure of the state which closed the opening / closing door of the crushing chamber. 前記波型枠の斜視図である。It is a perspective view of the corrugated frame. 前記波型枠の変形例の斜視図である。It is a perspective view of the modification of the said waveform frame. 本発明実施形態の動作を示す説明図である。It is explanatory drawing which shows operation | movement of this invention embodiment. 本発明実施形態変形例の動作を示す説明図である。It is explanatory drawing which shows operation | movement of this invention embodiment modification. 従来例の構造と動作を示す説明図である。It is explanatory drawing which shows the structure and operation | movement of a prior art example.

本発明実施形態のインライン型のミル1は、ラインに原料を投入するときに、原料の粉砕・解砕の機能を持たせたものである。図1〜図4の通り、粉粒体輸送ラインの初段に設置されるもので、上部に原料投入口2を備える。原料投入口2の下には安全上、ベルトコンベア3が設置されており、原料投入口2から投入された原料はベルトコンベア3で、ベルトコンベア3の下方に位置するカッター部4に運ばれ、カッター部4である程度の大きさに切断され解砕された原料は、ホッパ5に排出され、スクリューフィーダ6に供給されるようになっている。   The in-line mill 1 according to the embodiment of the present invention has a function of pulverizing / disintegrating raw materials when the raw materials are put into a line. As shown in FIGS. 1 to 4, it is installed in the first stage of the granular material transport line, and is provided with a raw material inlet 2 at the top. For safety, a belt conveyor 3 is installed under the raw material input port 2, and the raw material input from the raw material input port 2 is conveyed by the belt conveyor 3 to the cutter unit 4 located below the belt conveyor 3, The raw material cut and crushed to a certain size by the cutter unit 4 is discharged to the hopper 5 and supplied to the screw feeder 6.

このスクリューフィーダ6の出口にはサイレンサを兼ねる空気取入装置7が設けられている。供給口8と排出口9を備えた本体ケーシング10の内部に粉砕室11が形成されている(図3参照)。この粉砕室11の開閉に用いられる開閉扉12が本体ケーシング10に連結されている。供給口8は開閉扉12の中央部分に形成されている。空気取入装置7は粉砕室11からの騒音を防音するものである。本体ケーシング10は方形であって、高さや幅と比較して厚みが薄く形成されている。   An air intake device 7 also serving as a silencer is provided at the outlet of the screw feeder 6. A crushing chamber 11 is formed in a main body casing 10 having a supply port 8 and a discharge port 9 (see FIG. 3). An opening / closing door 12 used for opening / closing the grinding chamber 11 is connected to the main casing 10. The supply port 8 is formed in the central portion of the open / close door 12. The air intake device 7 prevents noise from the crushing chamber 11. The main body casing 10 has a rectangular shape and is formed with a smaller thickness than the height and width.

その他、本体ケーシング10は、開閉扉12を開閉するロック装置25、フックを引っ掛けて吊り上げるための吊上部26、開閉扉12を回動させるヒンジ部27と、を備えている(図2参照)。   In addition, the main body casing 10 includes a lock device 25 that opens and closes the opening / closing door 12, a hanging portion 26 for hooking and lifting the hook, and a hinge portion 27 for rotating the opening / closing door 12 (see FIG. 2).

図2及び図3に示すように、粉砕室11には閉じられた開閉扉12と平行に回転盤13が備えられ、回転盤13の中心にある回転軸14に蓋15が取り付けられている。回転軸14は本体ケーシング10の高さ方向および幅方向の中央部に配置され、先端部が粉砕室11に突出し、基端部は後方に配置されたものである。回転軸14に取り付けられた回転盤13が、回転軸14とベルト14aで連結した駆動モータ19(図1、図3参照)によって高速回転する構造であり、開閉扉12の供給口8から、カッター部4で切断された粉砕原料が、スクリューフィーダ6によって、図1の矢印Aに示す通り、図3の矢印Dに示す通り、粉砕室11の中央部分の領域16に定量的に供給される。   As shown in FIGS. 2 and 3, the crushing chamber 11 is provided with a rotating disk 13 parallel to the closed door 12, and a lid 15 is attached to a rotating shaft 14 at the center of the rotating disk 13. The rotating shaft 14 is disposed at the center in the height direction and the width direction of the main body casing 10, the distal end portion projects into the crushing chamber 11, and the proximal end portion is disposed rearward. A rotating disk 13 attached to the rotating shaft 14 is structured to rotate at a high speed by a drive motor 19 (see FIGS. 1 and 3) connected to the rotating shaft 14 by a belt 14a. The pulverized raw material cut by the section 4 is quantitatively supplied by the screw feeder 6 to the region 16 in the central portion of the pulverization chamber 11 as shown by the arrow A in FIG.

ラインにおける粉砕室11は、駆動モータ19によって高速回転する回転盤13によって、吸い込み風量を発生し、送風機と同じような役目をするので、スムーズな空気の流れとともに、原料粉粒体が供給口8から領域16に供給される。つまり回転盤13は風力増幅装置として働く。   The crushing chamber 11 in the line generates a suction air volume by a rotating disk 13 that is rotated at high speed by a drive motor 19 and functions in the same manner as a blower. To region 16. That is, the turntable 13 functions as a wind power amplifying device.

カッター部4は、図1の矢印B、Cに示す通り原料投入口2から投入された原料をある程度の大きさに切断するものである。例えば、乾麺、乾燥海藻、パン、麺端材、固化した食品粉粒塊等を、鋭利な刃でカットしてある程度の大きさに揃えるものである。大豆や煎餅のかけら等、粉砕対象物の種類によっては、カッター部4で必ずしも切断される必要はないので、カッター部4は省略が可能である。   The cutter part 4 cuts the raw material input from the raw material input port 2 to a certain size as shown by arrows B and C in FIG. For example, dry noodles, dry seaweed, bread, noodle scraps, solidified food powder lump, etc. are cut with a sharp blade to have a certain size. Depending on the type of the object to be crushed, such as a piece of soybean or rice cracker, the cutter unit 4 does not necessarily need to be cut, so the cutter unit 4 can be omitted.

図3、図6に示すように、回転盤13の表面部13aには複数の衝撃ピン22が固着され、粉砕室11の開閉扉12の内側(粉砕室側)側面に固定された固定盤18には、その衝撃ピン22に噛み合うように形成された複数の櫛歯形状の衝撃片23を円環状に配置されている。この衝撃片23は、3つの輪状歯23a〜23cが、同心円状に固着されたものである。本具体例では衝撃片23の輪状歯を3周列としたが、用途に応じて適宜数の周列の配置が可能である。   As shown in FIGS. 3 and 6, a plurality of impact pins 22 are fixed to the surface portion 13 a of the rotating disc 13, and the stationary platen 18 is fixed to the inside (grinding chamber side) side surface of the open / close door 12 of the crushing chamber 11. A plurality of comb-shaped impact pieces 23 formed so as to mesh with the impact pins 22 are arranged in an annular shape. The impact piece 23 is formed by concentrically fixing three annular teeth 23a to 23c. In this specific example, the ring-shaped teeth of the impact piece 23 are arranged in three rows, but an appropriate number of rows can be arranged depending on the application.

衝撃ピン22および衝撃片23により原料の粉砕が行われる空間を粉砕部17とすると、衝撃片23の輪状歯を3周列とする本具体例の構成では、粉砕部17は3つの輪状歯23a〜23cにより4つの空間に区切られる。すなわち、領域16から輪状歯23aまでの粉砕部17aと、輪状歯23aから輪状歯23bまでの粉砕部17bと、輪状歯23bから輪状歯23cまでの粉砕部17cと、輪状歯23cから波型枠21までの粉砕部17dと、の4つの空間である。   When the space where the raw material is crushed by the impact pin 22 and the impact piece 23 is defined as the pulverization unit 17, in the configuration of this specific example in which the ring-shaped teeth of the impact piece 23 are arranged in three circumferential rows, the pulverization unit 17 has three ring-shaped teeth 23a. It is divided into four spaces by ˜23c. That is, the grinding part 17a from the region 16 to the annular tooth 23a, the grinding part 17b from the annular tooth 23a to the annular tooth 23b, the grinding part 17c from the annular tooth 23b to the annular tooth 23c, and the corrugated frame from the annular tooth 23c. These are four spaces of up to 21 grinding parts 17d.

領域16から供給された原料は、粉砕部17aで粉砕され、粉砕室11内の遠心力によって輪状歯23aの間隙20aを通過して粉砕部17bに移動する。同様にして、原料は、粉砕部17bでも粉砕され、輪状歯23bの間隙20bを通過して粉砕部17cに移動し、さらに粉砕部17cで粉砕され、輪状歯23cの間隙20cを通過して粉砕部17dに到達する。   The raw material supplied from the region 16 is pulverized by the pulverization unit 17a, and moves to the pulverization unit 17b through the gap 20a of the annular teeth 23a by the centrifugal force in the pulverization chamber 11. Similarly, the raw material is pulverized also in the pulverizing part 17b, moved to the pulverizing part 17c through the gap 20b of the annular teeth 23b, further pulverized in the pulverizing part 17c, and pulverized through the gap 20c of the annular teeth 23c. The part 17d is reached.

本具体例では間隙20a〜20cは同一の間隔としているが、これらの間隔を変え、間隙20aを一番大きくして、間隙20b、20cと徐々に間隔を小さくする構成を採用しても好適である。このとき、原料が一番内側の輪状歯23aの間隙20aを通り抜けるくらいの大きさまで粉砕されると、原料は粉砕室11内の遠心力によって粉砕部17aから粉砕部17bに移動し、ここで二番目の輪状歯23bの間隙20bを通り抜けるくらいの大きさまで粉砕されると、原料は粉砕部17bから粉砕部17cに移動し、ここで三番目の輪状歯23cの間隙20cを通り抜けるくらいの大きさまで粉砕されると、原料は粉砕部17cから粉砕部17dに到達することになる。   In this specific example, the gaps 20a to 20c are set to the same interval, but it is also preferable to adopt a configuration in which these intervals are changed, the gap 20a is made the largest, and the gaps 20b and 20c are gradually reduced. is there. At this time, when the raw material is pulverized to such a size that it passes through the gap 20a of the innermost ring-shaped tooth 23a, the raw material moves from the pulverizing portion 17a to the pulverizing portion 17b by the centrifugal force in the pulverizing chamber 11, and When the raw material is pulverized to a size enough to pass through the gap 20b of the third annular tooth 23b, the raw material moves from the pulverizing part 17b to the pulverizing part 17c, where it is pulverized to a size enough to pass through the gap 20c of the third annular tooth 23c. Then, the raw material reaches the crushing part 17d from the crushing part 17c.

図4に示す通り、波型枠21は、下部の一部領域を切り欠いた略円筒状の概形を持ち回転軸14を中心として位置する波型板材21aと、波型板材21aの下部の一部領域に形成され波形板材21aの両端部に連結されたスクリーン21bと、波型板材21aの前面に固定された環状の前枠21cと、波型板材aの後面に固定された環状の後枠21dと、を備えたものである。前枠21cと後枠21dの主面は平行である。スクリーン21bは、円弧状に曲げられ、波型板材21aとともに略円筒状の概形を構成する形状であり、この円弧の中心軸は、波型板材21a、前枠21cおよび後枠21dの中心軸と同軸である。波型部材21aの材質は金属が好ましいが、セラミック、プラスチック等の他の材質でもよい。波型部材21aは孔が形成されていなく、粉粒体が通過できない非透過型の構造である。波型部材21aは、円周方向に谷部と山部とが交互に形成された波が規則的に形成されたものである。これにより、旋回する粉砕原料Pが乱反射されるように構成されている。スクリーン21bは設定粒径以下の粉粒体が透過する篩網、又は金属シートに孔がパンチングで形成されたパンチング・メタルシートを備えたものである。なお、波型部材21aの波は不規則的に形成されたものでもよい。   As shown in FIG. 4, the corrugated frame 21 includes a corrugated plate member 21 a having a substantially cylindrical shape with a part of a lower region cut out and positioned around the rotation shaft 14, and a lower portion of the corrugated plate member 21 a. A screen 21b formed in a partial region and connected to both ends of the corrugated plate 21a, an annular front frame 21c fixed to the front of the corrugated plate 21a, and an annular rear fixed to the rear surface of the corrugated plate a And a frame 21d. The main surfaces of the front frame 21c and the rear frame 21d are parallel. The screen 21b is bent in an arc shape and forms a substantially cylindrical shape together with the corrugated plate material 21a. The central axis of the arc is the central axis of the corrugated plate material 21a, the front frame 21c, and the rear frame 21d. And coaxial. The corrugated member 21a is preferably made of metal, but may be made of other materials such as ceramic and plastic. The corrugated member 21a has a non-transmissive structure in which no holes are formed and the granular material cannot pass through. The corrugated member 21a is formed by regularly forming waves in which valleys and peaks are alternately formed in the circumferential direction. Thereby, it is comprised so that the turning grinding | pulverization raw material P may be irregularly reflected. The screen 21b is provided with a sieve mesh through which a granular material having a set particle size or less permeates, or a punched metal sheet in which holes are formed in a metal sheet by punching. The wave of the corrugated member 21a may be irregularly formed.

図5に示される、波型枠21の変形例の波型枠121は、略円筒状の概形で波型のスクリーン121bと、スクリーン121bの前面に固定される前枠121cと、スクリーン121bの後面に固定された環状の後枠121dと、前枠121cと後枠121cとを連結し固定する連結部材121e、を備えたものである。スクリーン121bの強度が十分である場合には、連結部材121eがなくてもよい。   A corrugated frame 121 of a modification of the corrugated frame 21 shown in FIG. 5 has a substantially cylindrical and corrugated screen 121b, a front frame 121c fixed to the front surface of the screen 121b, and a screen 121b. An annular rear frame 121d fixed to the rear surface, and a connecting member 121e for connecting and fixing the front frame 121c and the rear frame 121c are provided. When the strength of the screen 121b is sufficient, the connecting member 121e may not be provided.

以上説明したミル1の使用について説明する。ミル1はロック装置25を用いて開閉扉12を閉めて使用する。このとき波型枠21をセットして開閉扉12を閉めておく。なお、開閉扉12は粉砕室11をメインテナンスする際に使用するものである。まず、粉砕したい材料を原料投入口2に投入する。ここではカッター部4を設けているため、粉砕室11に供給するには若干大きな塊の原料であっても構わない。原料投入口2から投入された原料は、ベルトコンベア3によりカッター部4に運ばれ、カッター部4である程度の大きさに解砕され、ホッパ5、スクリューフィーダ6を経て領域16に供給される。以下、領域16に供給された原料を粉砕原料Pとする。   The use of the mill 1 described above will be described. The mill 1 is used by closing the door 12 using a lock device 25. At this time, the corrugated frame 21 is set and the door 12 is closed. The open / close door 12 is used when the grinding chamber 11 is maintained. First, the material to be crushed is charged into the raw material inlet 2. Since the cutter unit 4 is provided here, a slightly larger lump material may be supplied to the crushing chamber 11. The raw material input from the raw material input port 2 is conveyed to the cutter unit 4 by the belt conveyor 3, crushed to a certain size by the cutter unit 4, and supplied to the region 16 through the hopper 5 and the screw feeder 6. Hereinafter, the raw material supplied to the region 16 is referred to as a pulverized raw material P.

図6に示す通り、領域16に供給された粉砕原料Pは、空気の流れと共に粉砕部17に拡散され、衝撃ピン22および衝撃片23からの衝撃を受けて細かく砕かれ、一番外側の輪状歯23cの間隙20cを抜け、粉砕室11の外周部周面に取り付けられた波型枠21のスクリーン21bを通過して所望の粒度に整粒され、図3の矢印Eに示す通り、微粉(製品)として排出口9から排出されるのである。   As shown in FIG. 6, the pulverized raw material P supplied to the region 16 is diffused into the pulverization unit 17 together with the air flow, and is finely crushed by the impact from the impact pin 22 and the impact piece 23, and is the outermost ring shape. After passing through the gaps 20c of the teeth 23c, passing through the screen 21b of the corrugated frame 21 attached to the outer peripheral surface of the grinding chamber 11, the particles are sized to a desired particle size, and as shown by arrow E in FIG. Product) is discharged from the discharge port 9.

本実施形態のミル1では、波型枠を使用することにより、従来の平滑な円筒形スクリーンを用いる場合と比較してスクリーンの目開きを同じとしても、明らかに粒度が細かなものを得ることができる。すなわち粉砕結果物の物性の向上を得て、粉砕効率を高めることができるものである。   In the mill 1 of the present embodiment, by using the corrugated frame, it is possible to obtain a finer particle size even when the screen opening is the same as in the case of using a conventional smooth cylindrical screen. Can do. That is, the physical properties of the pulverized product can be improved and the pulverization efficiency can be increased.

この効果は、図6に示す通り、波型枠21の波型板材21aを波状とすることで、従来のように粉砕原料Gが衝撃ピン322と共回りせず、粉砕原料Pの流れが波型板材21aにより不規則に乱れるという特有の現象が生じることによると考えられる。この特有の現象が上記効果に貢献する過程の詳細なメカニズムは詳らかではないが、発明者は次のように推察している。すなわち、平滑な円筒形スクリーンを用いる場合は粉砕室が渦巻き様のほぼ規則正しい流れの中で粉砕が行われるのに比べ(図8の粉砕原料Gを参照)、本実施形態のミル1では、波型板材21aにより乱流が生起して粉砕原料Pの移動方向がランダムになるので、粉砕原料Pが波型枠21に衝突する際に粉砕され、また、粉砕原料P同士が衝突して粉砕され、さらに、粉砕原料Pが衝撃ピン22又は衝撃片23cに衝突することになる。これにより、平滑な円筒形スクリーンの場合よりも、粉砕原料Pの粒度が一層細かくなり、粉化が一層促進される。なお、スクリーン21bも目開きを適宜変更することで、所望の粒度の粉粒体が得られる。たとえば、目開きを細かくすれば細かくなるまで粉砕されたものが得られる。本実施形態のミル1は、平滑な円筒形スクリーンを用いる場合と比べ、このスクリーンの目開きを同じとしても、一層粒度の細かな粉砕物が得られるものである。また、波型板材21aは孔が形成されておらず、粉砕原料Pが通過しないシート材質であるので、粉砕原料の乱反射が確実となるので、粉砕効率が一層高まる。   As shown in FIG. 6, this effect is obtained by making the corrugated plate 21 a of the corrugated frame 21 corrugated so that the pulverized raw material G does not co-rotate with the impact pin 322 and the flow of the pulverized raw material P is waved. This is thought to be due to the occurrence of a unique phenomenon of irregularity caused by the template 21a. The detailed mechanism of the process by which this unique phenomenon contributes to the above effect is not clear, but the inventor presumes as follows. That is, in the case where a smooth cylindrical screen is used, the pulverization chamber is pulverized in a substantially regular flow (see the pulverized raw material G in FIG. 8). Since the turbulent flow is generated by the template material 21a and the moving direction of the pulverized raw material P becomes random, the pulverized raw material P is pulverized when it collides with the corrugated frame 21, and the pulverized raw materials P collide with each other to be pulverized. Furthermore, the pulverized raw material P collides with the impact pin 22 or the impact piece 23c. Thereby, the particle size of the grinding | pulverization raw material P becomes finer than the case of a smooth cylindrical screen, and powdering is accelerated | stimulated further. In addition, the screen 21b can change the opening as appropriate to obtain a granular material having a desired particle size. For example, if the opening is made finer, a finely pulverized product can be obtained. The mill 1 of the present embodiment is capable of obtaining a pulverized product with a finer particle size even when the screen has the same mesh size as compared with the case of using a smooth cylindrical screen. Further, since the corrugated plate material 21a is not formed with a hole and is a sheet material through which the pulverized raw material P does not pass, irregular reflection of the pulverized raw material is ensured, and the pulverization efficiency is further increased.

上記波型枠21の変形例である波型枠121によれば、粉砕原料を波型のスクリーン121bで乱反射させながらスクリーン121bを通過させることができるので、同様の効果を奏する上、篩い効率が高まる。図5に示すこの波型枠121と、図4に示す波型枠21との粉砕過程は、概ね同様の動作であるが、相違点としては、波型枠21では波型枠21の下部にあるスクリーン21bのみから粉砕原料Pが通過することに比べ(図6参照)、波型枠121では、スクリーン121bが粉砕原料Pを乱反射することもあれば、粉砕原料を通過させることもある点である(図7参照)。スクリーン121bが波型となっているので、粉砕原料の旋回方向に対して斜めになる。粉砕原料Pがスクリーン121bの当たる場所によってランダムに反射され、また一方、粉砕原料Pが通過しやすい領域と、通過し難い領域が形成される。スクリーン121bは全周に波形の山と谷とが設けられているが、一部が平坦なスクリーン、例えば、図4のスクリーン21bと同様な部材を設けたものであってもよい。   According to the corrugated frame 121 which is a modified example of the corrugated frame 21, the ground material can be passed through the screen 121b while being irregularly reflected by the corrugated screen 121b. Rise. The crushing process of the corrugated frame 121 shown in FIG. 5 and the corrugated frame 21 shown in FIG. 4 is substantially the same operation, but the difference is that the corrugated frame 21 has a lower part of the corrugated frame 21. Compared with the case where the pulverized raw material P passes only from a certain screen 21b (see FIG. 6), in the corrugated frame 121, the screen 121b may diffusely reflect the pulverized raw material P or may pass the pulverized raw material. Yes (see FIG. 7). Since the screen 121b has a wave shape, the screen 121b is inclined with respect to the turning direction of the pulverized raw material. The pulverized raw material P is randomly reflected by the location where the screen 121b hits. On the other hand, an area where the pulverized raw material P easily passes and an area where the pulverized raw material P hardly passes are formed. The screen 121b is provided with corrugated peaks and valleys on the entire circumference, but a screen having a partially flat surface, for example, a member similar to the screen 21b of FIG. 4 may be provided.

上述の通り、輪状歯23a〜23cの間隙20a〜20cを、内側を大きな間隔にして外側に向かって徐々に小さな間隔とすれば、段階的な粉砕を経ることにより、着実で効率的な粉砕を図ることができる。   As described above, if the gaps 20a to 20c of the ring-shaped teeth 23a to 23c are set to a large interval on the inner side and gradually decreased toward the outer side, a steady and efficient pulverization can be achieved through the stepwise pulverization. Can be planned.

尚、本発明は、上述の実施の形態に限定されるものではなく、本発明の技術的思想を逸脱しない範囲において、様々な改変等を加えることが出来るものであり、それらの改変、均等物等も本発明の技術的範囲に含まれることとなる。例えば、波型枠21a等の波の頻度、配置等は適宜変更され得る。   The present invention is not limited to the above-described embodiment, and various modifications can be made without departing from the technical idea of the present invention. Etc. are also included in the technical scope of the present invention. For example, the frequency and arrangement of waves of the wave form frame 21a and the like can be changed as appropriate.

本発明のミルは、小麦粉、蕎麦粉等の穀物等の製粉・粉砕等に利用される。   The mill of the present invention is used for milling and pulverizing grains such as wheat flour and oat flour.

1・・・ミル
2・・・原料投入口
3・・・ベルトコンベア
4・・・カッター部
5・・・ホッパ
6・・・スクリューフィーダ
7・・・空気取入装置
8・・・供給口
9・・・排出口
10・・・本体ケーシング
11・・・粉砕室
12・・・開閉扉
13・・・回転盤
13a・・・表面部
14・・・回転軸
・・・ベルト14a
15・・・蓋
16・・・領域
17・・・粉砕部
18・・・固定盤
19・・・駆動モータ
22・・・衝撃ピン
23・・・衝撃片
23a〜23c・・・輪状歯
20a〜20c・・・間隙
21・・・波型枠
25・・・ロック装置
26・・・吊上部
27・・・ヒンジ部
21a・・・波型板材
21b・・・スクリーン
21c・・・前枠
21d・・・後枠
121・・・波型枠
121b・・・スクリーン
121c・・・前枠
121d・・・後枠
121e・・・連結部材
P・・・粉砕原料
DESCRIPTION OF SYMBOLS 1 ... Mill 2 ... Raw material inlet 3 ... Belt conveyor 4 ... Cutter part 5 ... Hopper 6 ... Screw feeder 7 ... Air intake device 8 ... Supply port 9 ... Exhaust port 10 ... Main body casing 11 ... Crushing chamber 12 ... Open / close door 13 ... Rotary disc 13a ... Surface 14 ... Rotating shaft ... Belt 14a
DESCRIPTION OF SYMBOLS 15 ... Lid 16 ... Area | region 17 ... Grinding part 18 ... Fixed disk 19 ... Drive motor 22 ... Impact pin 23 ... Impact piece 23a-23c ... Ring-shaped tooth 20a- 20c ... Gap 21 ... Corrugated frame 25 ... Locking device 26 ... Suspension upper part 27 ... Hinge part 21a ... Corrugated plate material 21b ... Screen 21c ... Front frame 21d ..Rear frame 121 ... Wavy frame 121b ... Screen 121c ... Front frame 121d ... Rear frame 121e ... Connecting member P ... Grinding raw material

Claims (1)

粉粒体原料と空気を供給する供給口と、前記粉粒体原料と空気を受け入れる破砕室と、前記破砕室に設けられる破砕歯と、前記破砕歯で粉砕された粉粒体を篩い分けるスクリーンと、を有するミルにおいて、
前記破砕歯が回転盤に固定された複数の破砕歯を備え、
前記破砕室の周縁に設けられスクリーンを有する円筒形の波型枠が周方向に非透過性の波型の板材を備え、
前記粉粒体原料が、前記破砕室の中心部から供給され、前記破砕室の外周部に移動する間に前記破砕歯により粉砕され、前記波型の板材の曲面に沿って移動する際、前記波型の板材で粉砕されて、前記スクリーンから外部に排出されることを特徴とするミル。
A supply port for supplying powder raw material and air, a crushing chamber for receiving the powder raw material and air, a crushing tooth provided in the crushing chamber, and a screen for sieving the powder crushed by the crushing tooth And in a mill having
The crushing teeth comprise a plurality of crushing teeth fixed to a rotating disk,
A cylindrical corrugated frame provided at the periphery of the crushing chamber and having a screen comprises a corrugated plate material that is impermeable in the circumferential direction,
When the granular material is supplied from the center of the crushing chamber and is crushed by the crushing teeth while moving to the outer periphery of the crushing chamber, and moves along the curved surface of the corrugated plate, A mill characterized in that it is pulverized with a corrugated plate and discharged from the screen to the outside.
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1636033A (en) * 1926-03-10 1927-07-19 Minerva A Brotherton Centrifugal impact pulverizer
US2651470A (en) * 1949-05-26 1953-09-08 Safety Car Heating & Lighting Method for milling wheat
JP2005066508A (en) * 2003-08-26 2005-03-17 Tsukasa Kogyo Kk Mill
JP2005169246A (en) * 2003-12-11 2005-06-30 National Institute Of Advanced Industrial & Technology Method of crushing composite material and apparatus therefor
JP2006136870A (en) * 2004-10-14 2006-06-01 Hosokawa Funtai Gijutsu Kenkyusho:Kk Grinder and powder production method using the grinder

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1636033A (en) * 1926-03-10 1927-07-19 Minerva A Brotherton Centrifugal impact pulverizer
US2651470A (en) * 1949-05-26 1953-09-08 Safety Car Heating & Lighting Method for milling wheat
JP2005066508A (en) * 2003-08-26 2005-03-17 Tsukasa Kogyo Kk Mill
JP2005169246A (en) * 2003-12-11 2005-06-30 National Institute Of Advanced Industrial & Technology Method of crushing composite material and apparatus therefor
JP2006136870A (en) * 2004-10-14 2006-06-01 Hosokawa Funtai Gijutsu Kenkyusho:Kk Grinder and powder production method using the grinder

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