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JP6973700B2 - Powder / granular material dispersion supply device and manufacturing method of powder / granular material dispersion - Google Patents
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JP6973700B2 - Powder / granular material dispersion supply device and manufacturing method of powder / granular material dispersion - Google Patents

Powder / granular material dispersion supply device and manufacturing method of powder / granular material dispersion Download PDF

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JP6973700B2
JP6973700B2 JP2017195406A JP2017195406A JP6973700B2 JP 6973700 B2 JP6973700 B2 JP 6973700B2 JP 2017195406 A JP2017195406 A JP 2017195406A JP 2017195406 A JP2017195406 A JP 2017195406A JP 6973700 B2 JP6973700 B2 JP 6973700B2
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powder
granular material
plate
opening
shutter
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JP2019069398A (en
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真樹生 三上
康平 澤田
徳広 内山
愛和 土江
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Meiji Co Ltd
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Meiji Co Ltd
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Description

本発明は粉粒体を対象物の表面に均一に散布供給する装置および同装置を用いた粉粒体分散物の製造方法に関する。 The present invention relates to an apparatus for uniformly spraying and supplying powder or granular material to the surface of an object, and a method for producing a powder or granular material dispersion using the apparatus.

従来から、ホッパーの開口を開閉するシャッターを備えた、粉粒体供給装置があった。 Conventionally, there has been a powder or granular material supply device equipped with a shutter that opens and closes the opening of the hopper.

特開2007−178371号公報Japanese Unexamined Patent Publication No. 2007-178371 特開2014−18195号公報Japanese Unexamined Patent Publication No. 2014-18195 特開2014−105044号公報Japanese Unexamined Patent Publication No. 2014-105044 特開2004−97880号公報Japanese Unexamined Patent Publication No. 2004-97880

しかしながら従来の装置では、粉粒体の落下に偏りやバラツキが生じ、粉粒体を均一に散布供給する点において不十分であった。 However, the conventional apparatus is insufficient in that the powder or granular material falls unevenly or varies, and the powder or granular material is uniformly sprayed and supplied.

本発明は上述の課題に鑑み、粉粒体を対象物の表面に均一に散布供給する装置および粉粒体分散物の製造方法を提供することを目的とする。 In view of the above-mentioned problems, it is an object of the present invention to provide an apparatus for uniformly spraying and supplying powder or granular material to the surface of an object and a method for producing a powder or granular material dispersion.

上記目的を達成するために、本発明の第1の態様に係る粉粒体分散供給装置10は、例えば図1に示すように、 粉粒体11が通過する開口12が形成された粉粒体供給部13と; 開口12を横切って移動するように設けられ、前記移動により開口12を開閉するシャッター板14であって、閉のときに上に供給された所定量の粉粒体11を、開となったときに開口12を通過させるシャッター板14とを備え; 粉粒体供給部13は、開口12に、シャッター板14の移動方向D1と交差する方向D2に配設された邪魔板15を有する。 In order to achieve the above object, the powder or granular material dispersion supply device 10 according to the first aspect of the present invention is, for example, as shown in FIG. 1, a powder or granular material having an opening 12 through which the powder or granular material 11 passes. With the supply unit 13; a shutter plate 14 provided so as to move across the opening 12 and open and close the opening 12 by the movement, and a predetermined amount of powder or granular material 11 supplied above when the opening 12 is closed. A shutter plate 14 that allows the opening 12 to pass through when the shutter plate is opened; the powder or granular material supply unit 13 is provided in the opening 12 as a hindrance plate 15 arranged in the opening 12 in a direction D2 that intersects the moving direction D1 of the shutter plate 14. Has.

このように構成すると、シャッター板の移動方向と交差する方向に配設された邪魔板を有するので、開口を通過して落下する粉粒体を均一に分散散布することができる。 With this configuration, since the baffle plate is arranged in the direction intersecting the moving direction of the shutter plate, the powder or granular material falling through the opening can be uniformly dispersed and sprayed.

また、本発明の第2の態様に係る粉粒体分散供給装置10は、第1の態様の粉粒体分散供給装置において、 邪魔板15は、粉粒体11の流入側の端部151に傾斜152が付けられた構造としてもよい。 Further, in the powder or granular material dispersion and supply device 10 according to the second aspect of the present invention, in the powder or granular material dispersion and supply device of the first aspect, the obstruction plate 15 is attached to the end portion 151 on the inflow side of the powder or granular material 11. It may be a structure with an inclination 152.

流入側の端部とは、邪魔板の上側の辺であり、傾斜をつけることにより、粉粒体の流れがスムーズになる。また、邪魔板の上部に粉粒体が溜まるのを抑えることができる。 The end on the inflow side is the upper side of the baffle plate, and by making an inclination, the flow of the powder or granular material becomes smooth. In addition, it is possible to prevent the powder or granular material from accumulating on the upper part of the baffle plate.

また、本発明の第3の態様に係る粉粒体分散供給装置10は、第1の態様又は第2の態様の粉粒体分散供給装置において、 邪魔板15を、1枚以上有し、前記開口が前記邪魔板で区切られる距離は50mm以下である。 Further, the powder / granular material dispersion / supply device 10 according to the third aspect of the present invention has one or more obstruction plates 15 in the powder / granular material dispersion / supply device according to the first aspect or the second aspect, and is described above. The distance at which the openings are separated by the baffle plate is 50 mm or less.

開口が邪魔板で区切られる距離を50mmより大にすると、分散効果が落ちる。 If the distance at which the openings are separated by the baffle plate is made larger than 50 mm, the dispersion effect is reduced.

また、本発明の第4の態様に係る粉粒体分散供給装置10は、第1の態様乃至第3の態様のいずれか1の粉粒体分散供給装置において、 シャッター板14の開閉を制御する制御装置21を備える。 Further, the powder / granular material dispersion / supply device 10 according to the fourth aspect of the present invention controls the opening / closing of the shutter plate 14 in the powder / granular material dispersion / supply device of any one of the first to the third aspects. A control device 21 is provided.

制御装置を備えるので、装置の操作を自動で行うことができる。 Since it is equipped with a control device, the device can be operated automatically.

また、本発明の第5の態様に係る粉粒体分散供給装置10は、第1の態様乃至第4の態様のいずれか1の粉粒体分散供給装置において、 粉粒体供給部13は、平板状の粉粒体供給板である。 Further, in the powder or granular material dispersion and supply device 10 according to the fifth aspect of the present invention, in the powder or granular material dispersion and supply device of any one of the first to fourth aspects, the powder or granular material supply unit 13 is It is a flat plate-shaped powder or granular material supply plate.

このように構成すると、粉粒体供給部は、平板状の粉粒体供給板であるので、シャッター板が、粉粒体供給板に平行に移動する構造とすることができる。また、構造がシンプルである。このように、複雑な器具を使用しないため、粉粒体のロスや目詰まりなどによる汚れが起こりにくく、清掃などのメンテナンスが容易である。 With this configuration, the powder / granular material supply unit is a flat plate-shaped powder / granular material supply plate, so that the shutter plate can be configured to move in parallel with the powder / granular material supply plate. Also, the structure is simple. As described above, since complicated equipment is not used, dirt due to loss of powder or granules or clogging is unlikely to occur, and maintenance such as cleaning is easy.

上記目的を達成するために、本発明の第6の態様に係る粉粒体分散物の製造方法は、例えば図4に示すように、第1の態様乃至第5の態様のいずれか1の粉粒体分散供給装置を用意する工程(ST2)と; 粉粒体11を分散する対象物17を供給する工程(ST6)と; シャッター板14を閉として、シャッター板14上に粉粒体11を供給する工程(ST5)と; シャッター板14を開として、対象物17上に粉粒体11を散布する工程(ST7)とを備える。 In order to achieve the above object, the method for producing a powder or granular material dispersion according to a sixth aspect of the present invention is, for example, as shown in FIG. 4, the powder of any one of the first to fifth aspects. A step of preparing a particle dispersion supply device (ST2) and a step of supplying an object 17 for dispersing the powder or granular material 11 (ST6); the shutter plate 14 is closed and the powder or granular material 11 is placed on the shutter plate 14. A step of supplying (ST5) and a step of spraying the powder or granular material 11 on the object 17 by opening the shutter plate 14 (ST7) are provided.

このように構成すると、粉粒体が均一に分散された粉粒体分散物を製造することができる。 With this configuration, it is possible to produce a powder or granular material dispersion in which the powder or granular material is uniformly dispersed.

本発明によれば、粉粒体を表面に均一に散布供給する装置および粉粒体が表面に均一に散布された粉粒体分散物の製造方法を提供することができる。 According to the present invention, it is possible to provide an apparatus for uniformly spraying and supplying powder or granular material to a surface and a method for producing a powder or granular material dispersion in which powder or granular material is uniformly sprayed on the surface.

粉粒体分散供給装置を説明する斜視図である。It is a perspective view explaining the powder and granular material dispersion supply apparatus. 粉粒体の分散状態を示す平面図である。(A21)は、邪魔板がない場合、(A22)は、邪魔板が1枚の場合、(A23)は、邪魔板が2枚の場合、(A24)は、邪魔板が3枚の場合を示す。It is a top view which shows the dispersed state of the powder or granular material. (A21) is when there is no obstacle plate, (A22) is when there is one obstacle plate, (A23) is when there are two obstacle plates, and (A24) is when there are three obstacle plates. show. シャッタースピードによる、粉粒体の分散状態の違いを示す平面図である。(A31)は、シャッタースピードが遅い場合、(A32)は、シャッタースピードが速い場合を示す。It is a top view which shows the difference of the dispersion state of the powder or granular material by the shutter speed. (A31) indicates a case where the shutter speed is slow, and (A32) indicates a case where the shutter speed is high. 粉粒体分散物の製造方法を示すフローチャートである。It is a flowchart which shows the manufacturing method of the powder or granular material dispersion.

以下、図面を参照して本発明の実施の形態について説明する。なお、各図において互いに同一又は相当する部材には同一あるいは類似の符号を付し、重複した説明は省略する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. In each figure, members that are the same as or correspond to each other are designated by the same or similar reference numerals, and duplicated description will be omitted.

まず、図1の斜視図を参照して、本発明の実施の形態である粉粒体分散供給装置10としての、クッキー粉(粉粒体)の分散供給装置1を説明する。本装置は、砕いて粒状にしたクッキー粉をアイスクリーム上に均一に散布する装置である。 First, the dispersion supply device 1 for cookie powder (powder / granular material) as the powder / granular material dispersion supply device 10 according to the embodiment of the present invention will be described with reference to the perspective view of FIG. This device is a device that evenly sprays crushed and granulated cookie powder onto ice cream.

本装置は、粉粒体11としてのクッキー粉が通過する開口12が形成された粉粒体供給部13としての、粉粒体供給板(スペーサ)が水平に設けられている。粉粒体供給板の下には、その下面に沿って移動するように設けられたシャッター板14が設けられる。シャッター板14は、開口12を横切って移動することにより開口12を開閉するように構成される。このシャッター板14の上には、開口12を閉としているときに所定量の粉粒体11が供給される。粉粒体11は、シャッター板14が移動し、開口12が開となったときに開口12を通過して、開口12の下に置かれた、粉粒体11を分散する対象物17としてのアイスクリームが充填されたカップ上に散布される。すなわち、アイスクリームの表面に散布される。粉粒体11は、重力により開口12を通過する。ここで、所定量は、製品の上面に散布されるその製品が求める適切な量である。典型的には、製品毎に異なる。これは、実験的に特定の対象物17であるアイスクリーム等の製品を作ることにより、事前に定めることができる。粉粒体供給板13は平板状であり、シャッター板14が、がたつくことなく粉粒体供給板13と平行に移動する構造とすることができる。
シャッター板14が開口12を「横切って移動する」とは、シャッター板は図1に示すように直線運動により横切る場合の他に、回転運動により横切る場合も含む。例えば円板状のシャッター板の周縁部の近傍を粉粒体供給板の開口近傍に枢着することにより回動させて開口を開閉する場合である。
この場合、円板状のシャッター板を直径線に沿って二つ割りにして、直径の一端で粉粒体供給板の開口近傍に枢着する。そして二つ割りした円板をそれぞれ反対方向に(鋏のように)回動させて開口を開閉すようにしてもよい。
In this device, a powder or granular material supply plate (spacer) is horizontally provided as a powder or granular material supply unit 13 in which an opening 12 through which the cookie powder as the powder or granular material 11 passes is formed. Below the powder or granular material supply plate, a shutter plate 14 provided so as to move along the lower surface thereof is provided. The shutter plate 14 is configured to open and close the opening 12 by moving across the opening 12. A predetermined amount of powder or granular material 11 is supplied onto the shutter plate 14 when the opening 12 is closed. The powder or granular material 11 is used as an object 17 for dispersing the powder or granular material 11 placed under the opening 12 by passing through the opening 12 when the shutter plate 14 moves and the opening 12 is opened. Sprinkle on a cup filled with ice cream. That is, it is sprayed on the surface of ice cream. The powder or granular material 11 passes through the opening 12 due to gravity. Here, the predetermined amount is an appropriate amount required by the product to be sprayed on the upper surface of the product. Typically, it varies from product to product. This can be determined in advance by experimentally making a product such as ice cream which is a specific object 17. The powder / granular material supply plate 13 has a flat plate shape, and the shutter plate 14 can be configured to move in parallel with the powder / granular material supply plate 13 without rattling.
The phrase "moving across the opening 12" of the shutter plate 14 includes not only the case where the shutter plate crosses by a linear motion as shown in FIG. 1 but also the case where the shutter plate crosses by a rotary motion. For example, there is a case where the vicinity of the peripheral edge of the disk-shaped shutter plate is pivotally attached to the vicinity of the opening of the powder or granular material supply plate to rotate the vicinity of the peripheral portion to open and close the opening.
In this case, the disk-shaped shutter plate is divided into two along the diameter line and pivotally attached to the vicinity of the opening of the powder or granular material supply plate at one end of the diameter. Then, the disc divided into two may be rotated in opposite directions (like scissors) to open and close the opening.

開口12は円形に形成され、シャッター板14の移動方向D1と交差する方向D2に向いた邪魔板15が配設される。交差の角度は、本実施の形態では90度である(ここでは、シャッターの移動方向D1に直角(D2の方向)を0度とする)。開口12の直径は、分散する対象物17の大きさによるが、アイスクリームの場合は、典型的には60から90mmであり、例えば76.8mmとするのがよい。邪魔板15は、図1(C1)に示すように、断面の幅Wと高さHが5mmの棒状に形成される。
断面の幅Wと高さHが5mmの場合、垂直方向には、少なくとも約2.5mmの垂直な平面を有する。なお、幅Wと高さHは、粉粒体の粒の大きさや開口12の大きさによる。粉粒体が4mmメッシュ通過品の場合は、幅Wと高さHは2.5〜6mmとするのがよい。幅Wや高さHは、強度を保ち得る範囲で、粉粒体の粒の大きさにより適切に調節するのがよい。粉粒体の粒が大きいほど高さHを高くする。大きい粒が邪魔板を乗り越えるのを抑制するためである。また、粉粒体の粒が小さいほど、又は小さい粒が混じっているほど、幅Wを小さくするとよい。邪魔板の上に粉粒体が溜まるのを抑制するためである。
また、高さHは幅Wより大きくしてもよい。邪魔板15は「板」と言うが、幅Wと同様な高さHのときは、むしろ「棒」と呼ぶのが適切かもしれないが、本明細書では、その場合も邪魔板と呼ぶ。角部は適宜面取りしてもよい。邪魔板ではあるが、棒とみることができるので、数に言及するときは、例えば2枚の他、2本のように呼ぶことがある。
The opening 12 is formed in a circular shape, and an obstruction plate 15 facing the direction D2 intersecting the movement direction D1 of the shutter plate 14 is arranged. The angle of intersection is 90 degrees in the present embodiment (here, the angle perpendicular to the shutter moving direction D1 (direction of D2) is 0 degrees). The diameter of the opening 12 depends on the size of the object 17 to be dispersed, but in the case of ice cream, it is typically 60 to 90 mm, for example 76.8 mm. As shown in FIG. 1 (C1), the baffle plate 15 is formed in a rod shape having a cross-sectional width W and a height H of 5 mm.
When the width W and the height H of the cross section are 5 mm, it has a vertical plane of at least about 2.5 mm in the vertical direction. The width W and the height H depend on the size of the particles of the powder or granular material and the size of the opening 12. When the powder or granular material is a product passing through a 4 mm mesh, the width W and the height H are preferably 2.5 to 6 mm. The width W and the height H should be appropriately adjusted according to the size of the powder or granular material within a range in which the strength can be maintained. The larger the granules, the higher the height H. This is to prevent large grains from getting over the obstacle board. Further, it is preferable that the width W is reduced as the particles of the powder or granular material are smaller or the smaller particles are mixed. This is to prevent the powder or granular material from accumulating on the obstacle plate.
Further, the height H may be larger than the width W. The obstruction plate 15 is referred to as a "plate", but when the height H is the same as the width W, it may be more appropriate to call it a "bar", but in the present specification, it is also referred to as an obstruction plate. The corners may be chamfered as appropriate. Although it is an obstacle board, it can be regarded as a stick, so when referring to a number, it may be called, for example, two or two.

開口12が邪魔板15で区切られる距離(幅)は50mm以下が好ましく、5〜45mmがより好ましく、10〜40mmが更に好ましい。開口12が邪魔板15で区切られる距離(幅)は狭過ぎると分散状態に好ましくない影響を及ぼすことがある。小さな粉粒体は邪魔板15を超えて移動することが困難であるため、分散状態はシューターからシャッター上に落下した際の位置に影響を受ける。開口12が邪魔板15で区切られる距離(幅)が狭過ぎると、対象物表面に粉粒体を均一に分散した状態で供給できないことがある。
ここで、「開口12が邪魔板15で区切られる距離」とは、邪魔板15と開口12の内周との最大の距離(最も外側の邪魔板15から垂直方向に開口12の内周まで測定した距離の最大値、すなわち開口12が円形のときは、その円に邪魔板15と平行に引いた接線と最も外側の邪魔板との間隔)であり、また邪魔板15が2枚以上のときは、隣り合う邪魔板15同士の間隔をいう。
The distance (width) at which the opening 12 is separated by the baffle plate 15 is preferably 50 mm or less, more preferably 5 to 45 mm, still more preferably 10 to 40 mm. If the distance (width) at which the opening 12 is separated by the baffle plate 15 is too narrow, it may adversely affect the dispersed state. Since it is difficult for small powder particles to move beyond the obstruction plate 15, the dispersed state is affected by the position when the powder is dropped from the shooter onto the shutter. If the distance (width) at which the opening 12 is separated by the baffle plate 15 is too narrow, it may not be possible to supply the powder or granular material in a state of being uniformly dispersed on the surface of the object.
Here, the "distance in which the opening 12 is separated by the baffle plate 15" is the maximum distance between the baffle plate 15 and the inner circumference of the opening 12 (measured from the outermost baffle plate 15 to the inner circumference of the opening 12 in the vertical direction). The maximum value of the distance, that is, when the opening 12 is circular, is the distance between the tangent line drawn parallel to the baffle plate 15 and the outermost baffle plate), and when there are two or more baffle plates 15. Refers to the distance between adjacent obstacle plates 15.

邪魔板15は、図1(C2)(C3)に示すように、前記粉粒体11の流入側の端部151に傾斜152が付けられた構造としてもよい。典型的には、邪魔板15は断面が正方形または縦長の長方形に形成し、その上端面(典型的には水平面)151の長手方向(D2の方向)の両方の角部を面取りする形で傾斜を付ける。傾斜152を付けると粉粒体11の流れがスムーズとなり、端部への粉粒体11の溜まりを抑制することができる。傾斜152の角度θは、粉粒体11の落下を妨げず、かつ強度を保持するような角度とする。好ましくは粉粒体供給板の(水平方向の)平面に対して30〜80度、更に好ましくは40〜60度、最も好ましくは45度である。傾斜152は平面でも曲面でもよい。曲面の場合は、傾斜角度は、例えば傾斜のついている部分(端部151の頂部と邪魔板の側面との間の部分)の中央部の角度で見る。 As shown in FIGS. 1 (C2) and 1 (C3), the baffle plate 15 may have a structure in which an inclined 152 is attached to an end portion 151 on the inflow side of the powder or granular material 11. Typically, the baffle plate 15 is formed into a square or vertically long rectangle in cross section, and is inclined so as to chamfer both corners in the longitudinal direction (direction of D2) of the upper end surface (typically a horizontal plane) 151. Attach. When the inclination 152 is attached, the flow of the powder or granular material 11 becomes smooth, and the accumulation of the powder or granular material 11 at the end can be suppressed. The angle θ of the inclination 152 is set so as not to prevent the powder or granular material 11 from falling and to maintain the strength. It is preferably 30 to 80 degrees, more preferably 40 to 60 degrees, and most preferably 45 degrees with respect to the (horizontal) plane of the powder or granular material supply plate. The inclination 152 may be a flat surface or a curved surface. In the case of a curved surface, the tilt angle is viewed, for example, at the angle of the central portion of the sloped portion (the portion between the top of the end 151 and the side surface of the baffle plate).

傾斜をつけた場合でも、図1(C2)に示すように、溜まる粉粒体11が問題とならない程度の平面部が上側に残ってもよい。平面部があるときは、端部がエッジ状である場合と比較して端部の損傷(エッジの欠け)を抑えることができる。平面部の幅は、邪魔板15の幅Wの1/8以下とするとよい。即ち、邪魔板15の幅Wが、2.5〜6.5mmのとき、0.8mm以下が好ましい。また、平面部を残す代わりに、図1(C3)に示すように、邪魔板15の端部151をまるめてもよい。典型的には、R(アール)を付けてもよい。粉粒体の流れがさらにスムーズになり、先端部に粉粒体が溜まるのを抑制できるだけでなく、先端部の損傷をさらに効果的に抑えることができる。粉粒体の溜まりを抑えるために、R(アール)をつけるときは、R=0.8mm以下とするのが好ましい。丸みをつけるときは、曲率半径がR=0.8mm以下となるようにするとよい。 Even when the slope is provided, as shown in FIG. 1 (C2), a flat surface portion may remain on the upper side to the extent that the accumulated powder or granular material 11 does not matter. When there is a flat surface portion, damage to the end portion (chip of the edge) can be suppressed as compared with the case where the end portion has an edge shape. The width of the flat surface portion may be 1/8 or less of the width W of the baffle plate 15. That is, when the width W of the baffle plate 15 is 2.5 to 6.5 mm, it is preferably 0.8 mm or less. Further, instead of leaving the flat surface portion, as shown in FIG. 1 (C3), the end portion 151 of the baffle plate 15 may be rounded. Typically, R (R) may be added. The flow of the powder or granular material becomes smoother, and not only the accumulation of the powder or granular material at the tip portion can be suppressed, but also the damage to the tip portion can be suppressed more effectively. When adding R (R), it is preferable that R = 0.8 mm or less in order to suppress the accumulation of powder or granular material. When rounding, the radius of curvature should be R = 0.8 mm or less.

邪魔板15のシャッター板14の移動方向D1との交差角度は90度(直交)(D2の方向)が好ましいが、90±10度の範囲の角度であってもよい。
なお、方向D2に対して角度をつけた場合や十文字型とした場合で試みた結果、D2と平行な方向だけの場合が、最も良いことが分かった。角度をつけると、邪魔板の数に関係なくすべての列で分散性が悪くなる傾向があった。特にシューター16が傾斜している場合、シューター16と粉粒体供給部13のなす角度が小さくなるほどその傾向が強く表れた。
The crossing angle of the hindrance plate 15 with the moving direction D1 of the shutter plate 14 is preferably 90 degrees (orthogonal) (direction of D2), but may be an angle in the range of 90 ± 10 degrees.
As a result of trying in the case of making an angle with respect to the direction D2 or in the case of a cross-shaped character, it was found that the case of only the direction parallel to D2 is the best. At an angle, dispersibility tended to be poor in all rows, regardless of the number of baffles. In particular, when the shooter 16 is inclined, the tendency becomes stronger as the angle formed by the shooter 16 and the powder or granular material supply portion 13 becomes smaller.

材質については、粉粒体供給板13は樹脂、シャッター板14はシューター16と共にステンレスとするのが好ましい。特にオーステナイト系のステンレスが好ましい。対汚性に優れているからである。粉粒体供給板を樹脂とすると、ステンレス製のシャッター板14との間での、金属同士の摩耗による異物の発生を抑えることができる。シャッター板14の滑らかな稼働にも資する。粉粒体供給板の樹脂は、超高分子量ポリエチレン樹脂や、フッ素樹脂であるテフロン(登録商標)が好ましい。耐摩耗性に優れるからである。
図1に示すように、シャッター板14は平面でも、停止位置が確実になるよう直角などに曲げたり、シャッター板14上に止め部として突起を設けてもよい。
邪魔板15は、粉粒体供給板と接合部のない一体化した形態が好ましい。このように構成すると、掃除等のメンテナンスが容易となる。
As for the material, it is preferable that the powder / granular material supply plate 13 is made of resin and the shutter plate 14 is made of stainless steel together with the shooter 16. Austenitic stainless steel is particularly preferable. This is because it has excellent stain resistance. When the powder or granular material supply plate is made of resin, it is possible to suppress the generation of foreign matter due to wear between the metals and the shutter plate 14 made of stainless steel. It also contributes to the smooth operation of the shutter plate 14. As the resin of the powder or granular material supply plate, ultra-high molecular weight polyethylene resin or Teflon (registered trademark) which is a fluororesin is preferable. This is because it has excellent wear resistance.
As shown in FIG. 1, the shutter plate 14 may be flat, bent at a right angle or the like so that the stop position is secure, or a protrusion may be provided on the shutter plate 14 as a stop portion.
The obstruction plate 15 is preferably integrated with the powder or granular material supply plate without a joint. With such a configuration, maintenance such as cleaning becomes easy.

図1に示す本実施の形態では、粉粒体供給板13には、開口12が複数個形成されている。量産に適するようにするためである。各開口12の上方には、シャッター板14上に粉粒体11を供給する筒状のシューター(配管)16が配置される。シューター16の上部には、秤量装置(不図示)が設けられる。秤量装置は、所定量の粉粒体11をシューター16に供給する。粉粒体は、シューター16をある程度の時間をかけて落下し、閉状態にあるシャッター板14上に均一に分散する。 In the present embodiment shown in FIG. 1, a plurality of openings 12 are formed in the powder or granular material supply plate 13. This is to make it suitable for mass production. Above each opening 12, a tubular shooter (pipe) 16 for supplying the powder or granular material 11 is arranged on the shutter plate 14. A weighing device (not shown) is provided on the upper portion of the shooter 16. The weighing device supplies a predetermined amount of powder or granular material 11 to the shooter 16. The powder or granular material drops the shooter 16 over a certain period of time and is uniformly dispersed on the closed shutter plate 14.

秤量装置で秤量された粉粒体11は、シューター16を通して落下し、閉じたシャッター板14上に一旦留め置かれる。秤量装置は、粉粒体を収容するホッパーと、ホッパーに収容された粉粒体の所定容量または所定重量を秤量する計量部と、計量した粉粒体を本発明の粉粒体供給装置または次の段階へ送るシューターとを備え、更に、必要に応じてホッパーから計量部へ移送する移送部と、移送を制御する制御部とを備え、秤量の精度を高めることができる。秤量装置における計量の方法および計量部としては、例えば、特開昭60−66120、実登2578684号、特開平6−263103、特開2001−124619など公知の装置を使うことができ、間欠的に駆動し計量した粉粒体を次の段階へ送る装置、または計重器と計重器からの信号を基にして開閉する開閉機構を備えることにより、粉粒体を計量する。 The powder or granular material 11 weighed by the weighing device falls through the shooter 16 and is temporarily held on the closed shutter plate 14. The weighing device includes a hopper for accommodating the powder or granular material, a measuring unit for weighing a predetermined volume or a predetermined weight of the powder or granular material contained in the hopper, and the powder or granular material to be weighed by the powder or granular material supply device of the present invention or the following. It is equipped with a shooter for sending to the stage of, and further, a transfer unit for transferring from the hopper to the measuring unit and a control unit for controlling the transfer, so that the accuracy of weighing can be improved. As the weighing method and measuring unit in the weighing device, known devices such as JP-A No. 60-66120, JP-A-2578684, JP-A-6-263103, and JP-A-2001-124619 can be used intermittently. The powder or granular material is weighed by providing a device for sending the driven and weighed powder or granular material to the next stage, or an opening / closing mechanism that opens and closes based on the weight measuring device and the signal from the weight measuring device.

粉粒体11を、シューター16から対象物17上に直接供給する構成では、シューター16をある程度の時間をかけて落下するのを待たなければならないので、生産性が低くなりがちである。そこで一旦シャッター板に載せる構成にすれば、シャッター板14が閉の状態で、所定の粉粒体11をシャッター板14の上に供給している間に、粉粒体11の散布が終わった対象物17を次の対象物17に置き換えることができる。このようにして生産性を高くすることができる。 In the configuration in which the powder or granular material 11 is directly supplied from the shooter 16 onto the object 17, it is necessary to wait for the shooter 16 to fall for a certain period of time, so that the productivity tends to be low. Therefore, once the device is mounted on the shutter plate, the object in which the powder or granular material 11 has been sprayed while the predetermined powder or granular material 11 is being supplied onto the shutter plate 14 with the shutter plate 14 closed. The object 17 can be replaced with the next object 17. In this way, productivity can be increased.

図2を参照して、邪魔板の間隔(邪魔板が2枚以上のとき)、又は邪魔板と開口の内周との距離による分散性のテスト結果を説明する。開口の直径は76.8mmとした。粉粒体としては、砕いて4mmメッシュを通したクッキー粉(粉粒体)を用いた。左側に邪魔板の配置状態を示す。右側に、分散状態を示す。なお写真の黒い部分が粉粒体である。図中の矢印はシャッター板を開にする際の移動の向きを示す。 With reference to FIG. 2, the dispersibility test result by the distance between the baffle plates (when there are two or more baffle plates) or the distance between the baffle plates and the inner circumference of the opening will be described. The diameter of the opening was 76.8 mm. As the powder or granular material, cookie powder (powder or granular material) that was crushed and passed through a 4 mm mesh was used. The arrangement state of the baffle plate is shown on the left side. The distributed state is shown on the right side. The black part in the photo is the powder or granular material. The arrows in the figure indicate the direction of movement when the shutter plate is opened.

図2の(A21)に示すように、開口に邪魔板が設けられていない粉粒体供給板では、シャッター板上に均一に分散したはずの粉粒体はシャッターを開にする際の移動により、対象物上で移動側に偏ってしまう。 As shown in FIG. 2 (A21), in the powder / granular material supply plate having no obstruction plate in the opening, the powder / granular material that should be uniformly dispersed on the shutter plate is moved when the shutter is opened. , It will be biased to the moving side on the object.

図2の(A22)は、開口に邪魔板を1枚設けた場合である。開口は直径が76.8mmの円形であり、邪魔板は円の直径に沿って設けられている。このとき邪魔板15と開口12の内周の邪魔板15から直角方向に最も遠い点までの距離(邪魔板と開口の内周との最大の距離)を35.6mmとした。粉粒体であるクッキー粉は、ほぼ均一に対象物としての紙カップ上に分散できた。(A23)は邪魔板を2枚設けた場合である。2枚の邪魔板間の距離を19.5mm、邪魔板と開口の内周との最大の距離を24.7mmとした。このとき、1枚よりも、均一度は高くなった。(A24)は、邪魔板が3枚の場合である。3枚の邪魔板間の距離を13.3mm、邪魔板と開口の内周との最大の距離を19.4mmとした。邪魔板が2枚の場合がベストであるが、1枚から3枚のいずれでも、邪魔板無しの場合と比較して、均一度は大きく改善された。3枚以上にしても改善度はあまり変わらないと推測される。邪魔板と開口の内周との最大の距離で言えば、あるいは邪魔板を2枚以上有するときの邪魔板同士の間隔で言えば、これらを所定値より小さくしても改善度はあまり変わらないと推測される。 FIG. 2 (A22) shows a case where one baffle plate is provided in the opening. The opening is a circle with a diameter of 76.8 mm, and the baffle plate is provided along the diameter of the circle. At this time, the distance from the obstruction plate 15 on the inner circumference of the obstruction plate 15 and the opening 12 to the farthest point in the perpendicular direction (maximum distance between the obstruction plate and the inner circumference of the opening) was set to 35.6 mm. The cookie powder, which is a granular material, could be dispersed almost uniformly on a paper cup as an object. (A23) is a case where two obstacle plates are provided. The distance between the two baffle plates was 19.5 mm, and the maximum distance between the baffle plates and the inner circumference of the opening was 24.7 mm. At this time, the uniformity was higher than that of one sheet. (A24) is a case where there are three obstacle plates. The distance between the three baffle plates was 13.3 mm, and the maximum distance between the baffle plates and the inner circumference of the opening was 19.4 mm. The case of two baffle plates is the best, but the uniformity is greatly improved in any of the cases of 1 to 3 as compared with the case of no baffle plate. It is estimated that the degree of improvement does not change much even if there are three or more. In terms of the maximum distance between the baffle plate and the inner circumference of the opening, or in terms of the distance between the baffle plates when having two or more baffle plates, the degree of improvement does not change much even if these are made smaller than the predetermined values. It is presumed.

図3にシャッター板を開にするスピードによる、均一度の違いを示す。この例では、邪魔板とシャッター板の移動方向D1との交差角度は90度、数は2本、幅Wは5mmとした。(A31)はシャッタースピード(シャッターの移動速度又は動作速度とも言う)が遅い場合であり、(A32)は、(A31)よりも速い場合である。対象物としては、紙カップを用いた。遅い場合、速い場合の各々につき、紙カップを置いた。 FIG. 3 shows the difference in uniformity depending on the speed at which the shutter plate is opened. In this example, the crossing angle between the baffle plate and the moving direction D1 of the shutter plate is 90 degrees, the number is two, and the width W is 5 mm. (A31) is a case where the shutter speed (also referred to as a shutter moving speed or an operating speed) is slow, and (A32) is a case where it is faster than (A31). A paper cup was used as the object. A paper cup was placed for each of the slow and fast cases.

このテストの結果、シャッター板14の開の移動速度は速い方がよいことが分かった。また、開口12のシャッター移動方向D1の長さが100mmのとき、30mm/秒以上とするとよく、好ましくは、80〜300mm/秒とする。また、シャッター板14が開方向に移動するとき、シャッター板14に振動を加えてもよい。 As a result of this test, it was found that the faster the shutter plate 14 is opened, the better. Further, when the length of the shutter moving direction D1 of the opening 12 is 100 mm, it is preferably 30 mm / sec or more, preferably 80 to 300 mm / sec. Further, when the shutter plate 14 moves in the opening direction, vibration may be applied to the shutter plate 14.

制御装置21は、シャッター板14の開閉、粉粒体11を散布する対象物17と粉粒体11を散布された対象物17との置き換えのタイミング保存部を備える。特に秤量装置からシューター16を通って粉粒体11がシャッター板14に到達する時間は重要である。この時間は、粉粒体11の材質、粒度分布によって変わるものであり、事前の試行により具体的な時間を特定するとよい。保存されたタイミングに従って、粉粒体分散物の製造方法を遂行する。すなわち、秤量装置で粉粒体が解放されたときからシャッター板に一時保留された後、シャッター板を開とするまでの適切な時間間隔を求める。その時間間隔を保存し、適切なタイミングでシャッター板を開閉するようにする。例えば、クッキー粉を4mmメッシュを通した場合、粉粒体の粒度は均一ではなく、より小径の粒子を含む。小径の粒子は、シューターを落下するのに、大径の粒子よりも時間がかかるので、試行の上それを考慮して、粉粒体の粒度に応じてシャッター板の開のタイミングを定める。なお、秤量装置で粉粒体が解放されたときからシャッター板を開とするまでの時間間隔は、対象物の入れ換えに要する時間で決まる場合もある。 The control device 21 includes an opening / closing unit for opening and closing the shutter plate 14, and a timing storage unit for replacing the object 17 on which the powder or granular material 11 is sprayed with the object 17 on which the powder or granular material 11 is sprayed. In particular, the time for the powder or granular material 11 to reach the shutter plate 14 from the weighing device through the shooter 16 is important. This time varies depending on the material and particle size distribution of the powder or granular material 11, and it is preferable to specify a specific time by a prior trial. The method for producing a powder or granular material dispersion is carried out according to the stored timing. That is, an appropriate time interval is obtained from the time when the powder or granular material is released by the weighing device to the time when the powder or granular material is temporarily held on the shutter plate and then the shutter plate is opened. Save the time interval and open and close the shutter plate at an appropriate timing. For example, when the cookie powder is passed through a 4 mm mesh, the particle size of the powder is not uniform and contains particles having a smaller diameter. Small-diameter particles take longer to drop the shooter than large-diameter particles, so the timing of opening the shutter plate is determined according to the particle size of the powder or granular material in consideration of this after trial. The time interval from when the powder or granular material is released by the weighing device to when the shutter plate is opened may be determined by the time required for replacing the object.

実機にてクッキー粉砕品によりテストを実施した。
開口の直径は前述のように、76.8mmとした。
テスト原料は、クッキー粉砕品であり、4mmメッシュを通した粉粒体である。4mmのメッシュを通したクッキー粉(粉粒体)の粒度分布は、1mmのメッシュを通るような小さい粒度のものが40%程度であった。
邪魔板15の本数は1本、2本、3本、幅Wは3mmと5mmとした。
結果;
図2に、邪魔板15の幅W5mm、本数1本、2本、3本の場合の分散状態を示す。シャッタースピードは前記の速い場合である。
シャッター板は、矢印の方向に動作する。
(A21)は、邪魔板の無い場合。
(A22)は、邪魔板が1本の場合。邪魔板と開口12円周の邪魔板から直角方向に最も遠い点までの距離は35.6mmであった。
(A23)は、邪魔板が2本の場合。邪魔板間の距離は19.5mm、邪魔板と開口12円周の邪魔板から直角方向に最も遠い点までの距離は24.7mmであった。
(A24)は、邪魔板が3本の場合。邪魔板間の距離は13.3mm、邪魔板と開口12円周の邪魔板から直角方向に最も遠い点までの距離は19.4mmであった。
A test was conducted using a cookie crushed product on an actual machine.
The diameter of the opening was 76.8 mm as described above.
The test raw material is a cookie crushed product, which is a powder or granular material passed through a 4 mm mesh. The particle size distribution of the cookie powder (powder and granular material) that passed through the 4 mm mesh was about 40% with a small particle size that passed through the 1 mm mesh.
The number of baffle plates 15 was 1, 2, 3, and the widths W were 3 mm and 5 mm.
result;
FIG. 2 shows a dispersed state in the case where the width W5 mm of the baffle plate 15 and the number of the baffle plates 15 are 1, 2, and 3. The shutter speed is the above-mentioned fast case.
The shutter plate moves in the direction of the arrow.
(A21) is when there is no obstacle plate.
(A22) is the case where there is only one obstacle plate. The distance from the baffle plate and the baffle plate around the opening 12 to the farthest point in the right angle direction was 35.6 mm.
(A23) is the case where there are two obstacle plates. The distance between the baffle plates was 19.5 mm, and the distance between the baffle plate and the baffle plate having an opening of 12 circumferences to the farthest point in the perpendicular direction was 24.7 mm.
(A24) is when there are three obstacle plates. The distance between the baffle plates was 13.3 mm, and the distance between the baffle plate and the baffle plate having an opening of 12 circumferences to the farthest point in the perpendicular direction was 19.4 mm.

同じく、実機にてクッキー粉砕品、4mmメッシュを通した粉粒体で、シャッタースピードを変えて2通りテストした。
図3に、シャッタースピードが遅い場合と、それよりも速い場合の分散状態を示す。
邪魔板15の幅W5mm、角度0度(D2の方向)、本数2本の場合の分散状態である。
(A31)は、シャッタースピードが遅い場合である。
(A32)は、シャッタースピードが速い場合である。
Similarly, in the actual machine, a cookie crushed product and a powder or granular material passed through a 4 mm mesh were tested in two ways at different shutter speeds.
FIG. 3 shows a dispersed state when the shutter speed is slow and when the shutter speed is faster than that.
This is a dispersed state when the width of the baffle plate 15 is W5 mm, the angle is 0 degrees (direction of D2), and the number of the baffle plates 15 is two.
(A31) is a case where the shutter speed is slow.
(A32) is a case where the shutter speed is high.

以上の実施例1、2のテストから以下の知見を得た;
邪魔板15の数は1本よりも、2本の方が若干分散性は良かった。
邪魔板15の幅Wは3mmと5mmで大きな違いは無かった。したがって強度を考えると5mmの方が良いと考えられる。
シャッターの動作スピードについては、動作速度を速くした方が全体的な分散性が良くなる傾向がある事が確認出来た。
The following findings were obtained from the above tests of Examples 1 and 2;
The number of baffle plates 15 was slightly better for two than for one.
The width W of the baffle plate 15 was 3 mm and 5 mm, and there was no big difference. Therefore, considering the strength, 5 mm is considered to be better.
Regarding the operating speed of the shutter, it was confirmed that the higher the operating speed, the better the overall dispersibility.

以上の通り、邪魔板15を設けることにより、粉粒体11の落下位置が対象物17上で分散され、万遍なく均一に散布供給することができることが分かった。 As described above, it was found that by providing the baffle plate 15, the falling position of the powder or granular material 11 is dispersed on the object 17, and the powder or granular material 11 can be evenly and uniformly sprayed and supplied.

図4のフローチャートを参照して、実施の形態である粉粒体分散物の製造方法を説明する。先ず、以上説明した粉粒体分散供給装置10を用意する(ST2)。
粉粒体11を用意する(ST3)。秤量された粉粒体11を受けるために、シャッター板14を閉とする(ST4)。粉粒体分散供給装置10には、秤量装置に粉粒体11を供給する(ST3)。閉状態のシャッター板14の上に秤量した所定量の粉粒体11を供給する(ST5)。シャッター板14の下方に、粉粒体11を分散する対象物17を置く(ST6)。対象物17の載置(ST6)は開口12がシャッター板で閉となっているときであればよく、粉粒体11の供給(ST5)と同時進行であってもよい。次に、シャッター板14を開として、対象物17上に粉粒体11を散布する(ST7)。粉粒体11を分散し終わった対象物(粉粒体分散物としての製品)を粉粒体分散供給装置10から送り出す(ST8)。製品の製造が未完了の場合は、シャッター板閉の工程(ST4)に戻る。製品の製造が完了したときは、製造プロセスがエンドとなる(ST10)。
The method for producing the powder or granular material dispersion according to the embodiment will be described with reference to the flowchart of FIG. First, the powder / granular material dispersion supply device 10 described above is prepared (ST2).
Prepare the powder or granular material 11 (ST3). The shutter plate 14 is closed to receive the weighed powder or granular material 11 (ST4). In the powder / granular material dispersion supply device 10, the powder / granular material 11 is supplied to the weighing device (ST3). A predetermined amount of powder or granular material 11 weighed is supplied onto the shutter plate 14 in the closed state (ST5). An object 17 for dispersing the powder or granular material 11 is placed below the shutter plate 14 (ST6). The placement of the object 17 (ST6) may be performed when the opening 12 is closed by the shutter plate, and may be simultaneously performed with the supply of the powder or granular material 11 (ST5). Next, the shutter plate 14 is opened and the powder or granular material 11 is sprayed on the object 17 (ST7). The object (product as a powder or granular material dispersion) in which the powder or granular material 11 has been dispersed is sent out from the powder or granular material dispersion supply device 10 (ST8). If the production of the product is not completed, the process returns to the shutter plate closing step (ST4). When the production of the product is completed, the manufacturing process ends (ST10).

具体的には、例えばココアパウダーやクッキーなどの粉粒体を冷菓などの食品の表面に万遍なく均一に散布供給する。 Specifically, for example, powders such as cocoa powder and cookies are evenly and evenly distributed and supplied to the surface of foods such as frozen desserts.

開口12は、円形に限らず、対象物17の形状に合わせて矩形にしてもよいし、模様状としてもよい。 The opening 12 is not limited to a circular shape, but may be rectangular or patterned according to the shape of the object 17.

粉粒体11の材質は問わないが、例えば、食品の上表面に散布するものとしては、クッキーなどの焼菓子、チョコチップ、ナッツ、果物のドライ品やそれらの粉砕物、およびココアパウダー、粉糖、抹茶などの粉体が挙げられる。
粉粒体11の粒度は、1〜8mmのメッシュ(篩)を通過したものが好ましく、2〜6mmのメッシュを通過したものが更に好ましく、4mmのメッシュを通過したものが最も好ましい。
粉粒体11を散布する対象物17は特に限定しないが、食品、例えば、アイスクリーム類などの冷菓、チョコレート、ムースやプリン等の高水分デザート、ケーキなどの焼菓子などが挙げられる。
食品は必ずしも容器に入っている必要はない。容器には、予め食品が充填されていても、供給した粉粒体11の上に食品を充填してもよい。
広範囲の粒度分布をもつ粉粒体であっても、均一に散布供給することができる。
粉粒体供給部13は平板状の粉粒体供給板の場合で説明したが、これに限らず邪魔板15を設けることができれば、枠のようになっていてもよい。例えば、シューター等粉粒体を供給するための管の下端部を兼用してもよい。
The material of the powder or granular material 11 is not limited, but for example, baked goods such as cookies, chocolate chips, nuts, dried fruits and their crushed products, and cocoa powder and powder can be sprayed on the upper surface of food. Examples include powders such as sugar and matcha.
The particle size of the powder or granular material 11 is preferably those that have passed through a mesh (sieve) of 1 to 8 mm, more preferably those that have passed through a mesh of 2 to 6 mm, and most preferably those that have passed through a mesh of 4 mm.
The object 17 to which the powder and granules 11 are sprayed is not particularly limited, and examples thereof include foods such as frozen desserts such as ice cream, high-moisture desserts such as chocolate, mousse and pudding, and baked confectionery such as cakes.
Food does not necessarily have to be in a container. The container may be pre-filled with food, or the food may be filled on the supplied powder or granular material 11.
Even powder particles having a wide particle size distribution can be uniformly sprayed and supplied.
The powder / granular material supply unit 13 has been described in the case of a flat plate-shaped powder / granular material supply plate, but the present invention is not limited to this, and the powder / granular material supply unit 13 may be like a frame as long as the baffle plate 15 can be provided. For example, the lower end of a tube for supplying powder or granular material such as a shooter may also be used.

10 粉粒体分散供給装置
11 粉粒体
12 開口
13 粉粒体供給部
14 シャッター板
15 邪魔板
16 シューター
17 対象物
21 制御装置
151 流入側の端部
152 傾斜
D1 シャッター板の移動方向
D2 シャッター板の移動方向と交差する方向
H 邪魔板の高さ
W 邪魔板の幅
θ 邪魔板の傾斜の角度
10 Powder / granular material dispersion supply device 11 Powder / granular material 12 Opening 13 Powder / granular material supply unit 14 Shutter plate 15 Obstruction plate 16 Shooter 17 Object 21 Control device 151 Inflow side end 152 Inclined D1 Shutter plate movement direction D2 Shutter plate Direction of intersection with the direction of movement H Height of the baffle plate W Width of the baffle plate θ Angle of inclination of the baffle plate

Claims (6)

粉粒体が通過する開口が形成された粉粒体供給部と;
前記開口の前記粉粒体の流出側の端面に沿って前記開口を横切るように移動するように設けられ、前記移動により前記開口を開閉するシャッター板であって、閉のときに上に供給された所定量の粉粒体を、開となったときに前記開口を通過させるシャッター板とを備え;
前記粉粒体供給部は、前記開口に、前記シャッター板の移動方向と交差する方向に配設された邪魔板を有する;
粉粒体分散供給装置。
With the powder or granular material supply part where the opening through which the powder or granular material passes is formed;
Along said end face of the outlet side of the powder or granular material of the opening is provided so as to move so that traverse the opening, a shutter plate for opening and closing the opening by the movement, up to the time of closing It is provided with a shutter plate that allows a predetermined amount of the supplied powder or granular material to pass through the opening when it is opened;
The powder or granular material supply unit has a baffle plate arranged in the opening in a direction intersecting the moving direction of the shutter plate;
Granule dispersion supply device.
前記邪魔板は、前記粉粒体の流入側の端部に傾斜が付けられた、
請求項1に記載の粉粒体分散供給装置。
The baffle plate has an inclined end on the inflow side of the powder or granular material.
The powder or granular material dispersion supply device according to claim 1.
前記邪魔板を、1枚以上有し、前記開口が前記邪魔板で区切られる距離は50mm以下である、
請求項1又は請求項2に記載の粉粒体分散供給装置。
It has one or more baffle plates, and the distance at which the openings are separated by the baffle plates is 50 mm or less.
The powder or granular material dispersion supply device according to claim 1 or 2.
前記シャッター板の開閉を制御する制御装置を備える、
請求項1乃至請求項3のいずれか1項に記載の粉粒体分散供給装置。
A control device for controlling the opening and closing of the shutter plate is provided.
The powder or granular material dispersion supply device according to any one of claims 1 to 3.
前記粉粒体供給部は、平板状の粉粒体供給板である、
請求項1乃至請求項4のいずれか1項に記載の粉粒体分散供給装置。
The powder or granular material supply unit is a flat plate-shaped powder or granular material supply plate.
The powder or granular material dispersion supply device according to any one of claims 1 to 4.
請求項1乃至請求項5のいずれか1項に記載の粉粒体分散供給装置を用意する工程と;
前記粉粒体を分散する対象物を供給する工程と;
前記シャッター板を閉として、前記シャッター上に前記粉粒体を供給する工程と;
前記シャッター板を開として、前記対象物上に前記粉粒体を散布する工程とを備える;
粉粒体分散物の製造方法。
The step of preparing the powder or granular material dispersion supply device according to any one of claims 1 to 5.
The step of supplying the object for dispersing the powder or granular material;
With the step of closing the shutter plate and supplying the powder or granular material onto the shutter;
The shutter plate is opened, and the step of spraying the powder or granular material on the object is provided;
A method for producing a powder or granular material dispersion.
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