JP2006167715A - Apparatus and method for granulating material - Google Patents

Apparatus and method for granulating material Download PDF

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JP2006167715A
JP2006167715A JP2005333712A JP2005333712A JP2006167715A JP 2006167715 A JP2006167715 A JP 2006167715A JP 2005333712 A JP2005333712 A JP 2005333712A JP 2005333712 A JP2005333712 A JP 2005333712A JP 2006167715 A JP2006167715 A JP 2006167715A
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rotating drum
stirring
granulating
drum
rotating
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Tadaaki Shimoe
忠明 下江
Masayuki Kobayashi
正幸 小林
Atsusuke Yamamoto
敦資 山本
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Kitagawa Iron Works Co Ltd
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Kitagawa Iron Works Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To solve such a problem of an agitatedly granulating method that it takes a lot of time to form a granulated material since the granulated material, which is in the middle of growth and has not satisfactory strength, is crushed and it is difficult to make the size or shape of the granulated material uniform in a short time. <P>SOLUTION: This apparatus for granulating a material is provided with: a main body; a rotary drum which is supported by the main body, at one end of which an opening is formed and which has an almost cylindrical shape and is rotated around a rotary shaft; a rotary drum inclining means for changing the angle of inclination of the rotary drum upward from the horizontal position of the rotary shaft of the rotary drum; and an agitating means arranged in the rotary drum for agitating the material. An agitating part for agitating the material and a rolling part for rolling/granulating the material are arranged continuously in one and the same rotary drum. A material outflow preventing means is arranged for preventing the outflow of the material through the opening of the rotary drum when the material is rolled. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、粉体や粘性土、脱水スラッジ等の塊体と、水や溶液または溶融液等の液体などの材料から造粒物を得る造粒装置及びその方法に関するものである。   The present invention relates to a granulating apparatus and method for obtaining a granulated material from a mass such as powder, viscous soil, dehydrated sludge and the like and a material such as water, a solution or a liquid such as a melt.

従来より、材料の造粒方法は、本出願人提案の特開2000−140820号公報のような固定ドラムに攪拌翼を設け、ドラム内の材料を混合、解砕することで造粒を行う攪拌造粒法があり、他の方法として回転ドラム内に材料を投入し、材料をドラム内で転動(転がす)させることで造粒を行う転動造粒法など、種々の方法がおこなわれている。
特開2000−140820号公報
Conventionally, the material granulation method is a stirring method in which a stationary drum is provided with a stirring blade as in Japanese Patent Application Laid-Open No. 2000-140820 proposed by the applicant, and the material in the drum is mixed and pulverized to perform granulation. There is a granulation method. As another method, various methods such as a rolling granulation method in which a material is put in a rotating drum and the material is rolled (rolled) in the drum are used. Yes.
JP 2000-140820 A

前記攪拌造粒方法においては、固定ドラム内に設けた攪拌翼を移動させて材料を解砕し、小さい固まりに分断して、造粒物を形成させる。この方法では、攪拌翼により、材料を均一に混合する点においては適しているが造粒物形成の際には、十分な強度のない成長途中の造粒物が破砕されるため、造粒物の形成に時間がかかり、短時間で造粒物の大きさや形状を一定にそろえることが困難であった。
従って、本発明は材料を造粒するに際し、材料が均一に十分混合され且つ、造粒物の大きさ及び形状が一定に整えられた造粒物を得ることを目的とする。
In the stirring granulation method, the stirring blade provided in the fixed drum is moved to pulverize the material, and it is divided into small chunks to form a granulated product. This method is suitable in terms of uniformly mixing the materials with the stirring blade, but the granulated product is not sufficiently strong during the formation of the granulated product. It took a long time to form the material, and it was difficult to keep the size and shape of the granulated material constant in a short time.
Accordingly, an object of the present invention is to obtain a granulated product in which the material is uniformly mixed sufficiently and the size and shape of the granulated product are adjusted to be uniform when the material is granulated.

前記目的を達成するため、本発明は、本体と、該本体に支承され、一端を開口した略円筒形状となし、回転軸を中心に回転する回転ドラムと、該回転ドラムの回転軸と水平からの傾斜角度を変更する傾胴手段と、前記回転ドラム内に設けられ材料を攪拌する攪拌手段を備え、前記回転ドラムが、材料の攪拌を行なう攪拌部位と、材料を転動させて造粒する転動部位を同一ドラムに連続して設け、材料を転動する際に回転ドラムの開口部から材料の流出を防ぐ材料流出防止手段を備えることを特徴とする材料の造粒装置である。
また、前記回転ドラムの攪拌部位が転動部位よりも下方になるように回転ドラムを傾斜させて材料を攪拌する攪拌工程と、該攪拌工程よりも回転ドラムの傾斜角度を小さくして材料を転動させて造粒する造粒工程と、該造粒工程よりも回転ドラムの傾斜角度を大きくして造粒物の大きさを整える整粒工程を順に実施することを特徴とする材料の造粒方法である。
In order to achieve the above-mentioned object, the present invention has a main body, a substantially cylindrical shape supported by the main body and having one end opened, a rotating drum that rotates about a rotating shaft, and the rotating shaft of the rotating drum from the horizontal. And a stirring means for stirring the material provided in the rotating drum, and the rotating drum rolls the material and granulates the stirring portion. A material granulating apparatus comprising a material outflow prevention means for continuously providing a rolling site on the same drum and preventing the material from flowing out from an opening of the rotating drum when rolling the material.
In addition, the stirring process in which the rotating drum is tilted so that the stirring part of the rotating drum is below the rolling part and the material is stirred, and the tilting angle of the rotating drum is made smaller than that in the stirring process to rotate the material. A granulation step of granulating the material, and a granulation step of adjusting the size of the granulated product by increasing the tilt angle of the rotating drum more than the granulation step Is the method.

前述の構成によれば、ひとつの回転ドラムに攪拌部位と転胴部位を設けることで材料を十分に攪拌して、偏りのない状態にし、転胴作用により粒の大きさ形状の均一な造粒物をひとつの回転ドラムを用いて容易に且つ、簡単な構成で得ることができるものである。
又、前述の方法によれば、攪拌工程及び造粒工程で造粒した造粒津物の大きさを攪拌手段を用いた整粒工程で整えることで、均一な大きさの造粒物を容易に得ることが可能となる。
According to the above-mentioned configuration, the material is sufficiently agitated by providing the agitating part and the rolling cylinder part on one rotating drum so that the material is not biased, and the granulation is uniform in size and shape by the rolling action. An object can be obtained easily and with a simple configuration using a single rotating drum.
Moreover, according to the above-mentioned method, it is easy to obtain a granulated product of uniform size by adjusting the size of the granulated tsunami granulated in the agitation step and the granulation step in the sizing step using a stirring means. Can be obtained.

本発明の実施の形態について図を用いて説明する。
図1は、本発明の造粒装置の側面図を示し、図2、図3、図4は、本発明の造粒装置の一部断面図を示している。図5は図3中のX−X矢視図を示す。図1において、本体である台座14とフレーム16が設けられている。略円筒形の回転ドラム1は、フレーム16へ回転ドラム用モータ17を動力源として回転軸を中心に回転自在に設けられている。
フレーム16は、台座14へ回動自在に支持され、台座14とフレーム16との間には傾胴手段としてシリンダ13が設けられ、シリンダ13の伸縮により、フレーム16に設けられる回転ドラム1の傾きが変更できるようになされている。図1に示す様に、図1(a)ではシリンダ13は縮んだ状態であり、回転ドラム1の回転軸は水平から角度Aだけ傾斜している。
図1(b)では、シリンダ13は伸びた状態であり、回転ドラム1は、水平になり角度B=0°の状態になる。この回転ドラム1の傾斜角度はシリンダ13の伸縮長さにより自在に調整できるものである。
Embodiments of the present invention will be described with reference to the drawings.
FIG. 1 shows a side view of the granulating apparatus of the present invention, and FIGS. 2, 3, and 4 show partial sectional views of the granulating apparatus of the present invention. FIG. 5 is a view taken along the line XX in FIG. In FIG. 1, a pedestal 14 and a frame 16 which are main bodies are provided. The substantially cylindrical rotating drum 1 is provided on a frame 16 so as to be rotatable about a rotating shaft using a rotating drum motor 17 as a power source.
The frame 16 is rotatably supported by the pedestal 14, and a cylinder 13 is provided as a tilting cylinder means between the pedestal 14 and the frame 16, and the tilt of the rotary drum 1 provided on the frame 16 is expanded and contracted. Has been made so that it can be changed. As shown in FIG. 1, in FIG. 1A, the cylinder 13 is in a contracted state, and the rotating shaft of the rotating drum 1 is inclined by an angle A from the horizontal.
In FIG. 1B, the cylinder 13 is in an extended state, and the rotary drum 1 is horizontal and has an angle B = 0 °. The inclination angle of the rotary drum 1 can be freely adjusted by the expansion / contraction length of the cylinder 13.

図2、図3、図4において、回転ドラム1の一端側には、材料のドラム内への投入と、造粒物の排出を行う開口部2が備えられている。開口部2の反対側の他端側には、回転ドラム1を閉じる後方壁3が設けられ、後方に送られる材料を後方に蓄えられるようになされている。
回転ドラム1内の後方には、材料の混合、解砕、整粒を行う攪拌手段7が設けられており、後方壁3を貫通して回転自在に設けられる回転軸8が備えられ、回転軸8には軸芯方向と直角へ取り付けられ、解砕刃を有する板形状の攪拌翼9が複数段で設けられている。
回転ドラム1には、攪拌手段7の回転により、材料の混合解砕が行われる攪拌部位4と、攪拌手段7の回転域外で回転ドラム1の回転により材料を転動(材料を転がすこと)させて、造粒物を形成させ、造粒を行う転動部位5が設けられている。
また、図3に示すように回転ドラム1の開口側には、材料を流出防止手段として、角度Cで傾斜をつけて、開口部2へ向けて集束し、回転ドラム1の径が徐々に小さくなるような形状になされ、回転ドラムが略水平状態になっても、材料が開口部2から流出しない様にし、転動部位5での材料の転動を十分に行うようになされている。
2, 3, and 4, one end side of the rotary drum 1 is provided with an opening 2 for feeding material into the drum and discharging the granulated material. A rear wall 3 for closing the rotary drum 1 is provided on the other end side opposite to the opening 2 so that a material fed rearward can be stored rearward.
Agitating means 7 for mixing, crushing, and sizing the material is provided at the rear in the rotary drum 1, and a rotary shaft 8 that is rotatably provided through the rear wall 3 is provided. 8, a plate-shaped stirring blade 9 having a crushing blade is attached in a plurality of stages.
The rotating drum 1 has a stirring portion 4 where the material is mixed and crushed by the rotation of the stirring means 7, and the material rolls (rolls the material) by the rotation of the rotating drum 1 outside the rotation range of the stirring means 7. Thus, a rolling part 5 for forming a granulated material and performing granulation is provided.
Further, as shown in FIG. 3, on the opening side of the rotating drum 1, the material is inclined at an angle C as an outflow prevention means and converged toward the opening 2, and the diameter of the rotating drum 1 is gradually reduced. Even when the rotary drum is in a substantially horizontal state, the material is prevented from flowing out from the opening 2 and the material is sufficiently rolled at the rolling site 5.

図5に示すように、本体のフレーム16には、回転ドラム用モータ17と、攪拌手段用モータ10が設けられている。
回転ドラム用のモータ17の回転は、チェーン18を介して、回転ドラム1に接続されたスプロケット19に伝達され、回転ドラム1を回転させる。
攪拌手段用モータ10の回転は、チェーン11を介して攪拌手段7の回転軸8に接続されたスプロケット12に伝達され、攪拌手段7を回転させる。これらの回転の伝達手段は、チェーンに限定するものではなく、ギヤ構造などの他の回転伝達手段を用いても良い。
また、回転ドラム1内にはスクレーパ27が回転ドラム1のない面に沿って設けられ、スクレーパ27は、フレーム16に支持されたシャフト28に固着され、回転ドラム1の回転と同期せずに配設されており、回転ドラム1の内面に残留付着する材料をそぎ落とす。
As shown in FIG. 5, the frame 16 of the main body is provided with a rotary drum motor 17 and a stirring means motor 10.
The rotation of the motor 17 for the rotating drum is transmitted to the sprocket 19 connected to the rotating drum 1 through the chain 18 to rotate the rotating drum 1.
The rotation of the stirring means motor 10 is transmitted to the sprocket 12 connected to the rotating shaft 8 of the stirring means 7 through the chain 11 to rotate the stirring means 7. These rotation transmission means are not limited to chains, and other rotation transmission means such as a gear structure may be used.
Further, a scraper 27 is provided in the rotary drum 1 along a surface without the rotary drum 1, and the scraper 27 is fixed to a shaft 28 supported by the frame 16 and is arranged without being synchronized with the rotation of the rotary drum 1. The material that is provided and remains on the inner surface of the rotary drum 1 is scraped off.

次にこの装置を用いて、造粒物を造る過程を図面を用いて工程別に説明する。
図6には、各々の工程での回転ドラム内の状態を表す状態図を示す。図6(a)で示されるように、材料を回転ドラムに投入し、混合する第1段階である攪拌工程では、傾胴手段であるシリンダ13を縮めて回転ドラム1が傾斜を持たせて配置される。この時、図1(a)で示す回転ドラム1の傾斜角度Aの最適角度は、材料の種類、含水量、比重などの物性条件により変動はあるが、15〜50°までの間で良好な攪拌を行うことができる。この時の回転ドラムの傾きは、後方壁3側を下方に、つまり攪拌部位4側を下方にして傾くので、回転ドラム1内の材料は、攪拌手段7が設けられる回転ドラム1の攪拌部位4側に集められる。
そのため材料を十分に攪拌でき、各材料が偏りなく均一に分布するように混合され、さらには、材料が攪拌翼で細分化されて粉砕されることで、造粒物の核が形成される。
この攪拌工程では、回転ドラム1と攪拌翼9は共に回転速度を高速回転とし、回転方向を正回転(図6(a)中時計回り)とすることで材料の攪拌を十分行うことができ、例えば粘性の高い材料の細分化に適している。
Next, the process of making a granulated product using this apparatus will be described step by step with reference to the drawings.
FIG. 6 is a state diagram showing the state in the rotating drum in each step. As shown in FIG. 6 (a), in the stirring step, which is the first stage in which the material is put into the rotating drum and mixed, the cylinder 13 serving as the tilting cylinder means is shrunk so that the rotating drum 1 is inclined. Is done. At this time, the optimum angle of inclination angle A of the rotating drum 1 shown in FIG. 1 (a) varies depending on physical properties such as the type of material, water content, specific gravity, etc., but is good between 15 and 50 °. Stirring can be performed. The tilt of the rotating drum at this time is tilted with the rear wall 3 side downward, that is, the stirring portion 4 side downward, so that the material in the rotating drum 1 is the stirring portion 4 of the rotating drum 1 provided with the stirring means 7. Collected on the side.
Therefore, the materials can be sufficiently stirred, mixed so that each material is evenly distributed without unevenness, and further, the material is subdivided with a stirring blade and pulverized to form a nucleus of the granulated product.
In this stirring step, both the rotating drum 1 and the stirring blade 9 can rotate the rotation speed at a high speed, and the rotation direction can be positively rotated (clockwise in FIG. 6A) to sufficiently stir the material. For example, it is suitable for subdividing highly viscous materials.

図6(b)は、第2工程である造粒工程を示す図です。この造粒工程では、傾胴手段であるシリンダ13を伸ばして、回転ドラム1の傾斜を小さくする又は水平にするように配置させる。
これにより、回転ドラム1の攪拌部材4側に集められた材料は、回転ドラム1の転動部位1側に移動される。
転動部位1に集められた材料は、回転ドラム1の回転により、回転ドラム1の内周面を転がされ、造粒物の核から大きさを大きくし、且つ形状を球体に整えることが行われる。この造粒工程では、攪拌手段7による攪拌が材料に作用されにくいので、生成過程にある造粒物が破砕されずに粒の成長を妨げられることなく、造粒物を生成させることができる。
FIG. 6B is a diagram showing the granulation process which is the second process. In this granulation step, the cylinder 13 serving as the tilting cylinder means is extended so that the inclination of the rotary drum 1 is reduced or leveled.
As a result, the material collected on the stirring member 4 side of the rotating drum 1 is moved to the rolling part 1 side of the rotating drum 1.
The material collected in the rolling part 1 is rolled on the inner peripheral surface of the rotating drum 1 by the rotation of the rotating drum 1, the size is increased from the core of the granulated material, and the shape can be adjusted to a sphere. Done. In this granulation step, since the stirring by the stirring means 7 is difficult to act on the material, the granulated product in the generation process is not crushed and the granulated product can be generated without hindering the growth of the particles.

造粒工程での回転ドラム1の傾斜角度は、図1(b)に示すように、水平又は水平に近い位置に配置させることが望ましく、0〜15°迄の間で行われる。
この時、回転ドラム1と攪拌翼9は共に回転速度を前記攪拌工程よりも低速回転となし、又、回転ドラム1の回転方向を正回転(図6(b)中時計回り)とし、攪拌翼9の回転方向を逆回転(図6(b)中反時計回り)とする。
これにより、攪拌手段による材料の攪拌を抑制し、回転ドラム1の回転による材料の転動を行うのに最適となる。
また、この造粒工程の際には、回転ドラム1の傾斜角度を大きくした後すぐに小さくすることをある程度の範囲で繰り返しに行なって、回転ドラム1を揺動させることを行なうと材料を揺することで転動作用をより効果的に加えることを行ない材料の造粒化を短時間で行なうことができる。
As shown in FIG. 1B, the tilt angle of the rotating drum 1 in the granulation step is desirably arranged at a horizontal or near horizontal position, and is performed between 0 and 15 °.
At this time, the rotating drum 1 and the stirring blade 9 are both rotated at a lower speed than that of the stirring step, and the rotating direction of the rotating drum 1 is set to the normal rotation (clockwise in FIG. 6B). 9 is the reverse rotation (counterclockwise in FIG. 6B).
This suppresses the stirring of the material by the stirring means and is optimal for rolling the material by the rotation of the rotary drum 1.
In this granulation step, the material is shaken if the rotation of the rotating drum 1 is repeated within a certain range by repeatedly increasing the inclination angle of the rotating drum 1 and then decreasing the rotation drum 1 within a certain range. Thus, the rolling operation can be applied more effectively and the material can be granulated in a short time.

次に図6(c)には、第3工程である整粒工程を示す。
この整粒工程では、傾胴手段であるシリンダ13を若干縮めさせ、回転ドラム1の傾斜を造粒工程に比べてわずかに大きくするように配置される。
回転ドラム1が若干傾斜することにより、造粒工程で造粒された造粒物の内、大きく成長しすぎた造粒物を回転ドラム1の攪拌部位4へ移動させ、攪拌手段7により解砕させ、所望する粒の大きさに整えることを行う。
Next, FIG.6 (c) shows the sizing process which is a 3rd process.
In this sizing process, the cylinder 13 as the tilting cylinder means is slightly contracted, and the tilt of the rotary drum 1 is arranged to be slightly larger than that in the granulation process.
By slightly tilting the rotating drum 1, the granulated product that has grown too much is moved to the stirring portion 4 of the rotating drum 1 among the granulated products that have been granulated in the granulating step, and pulverized by the stirring means 7. And adjusting to the desired grain size.

造粒工程において、材料の転動により、造粒が良好に行われると、粒の成長が促進される。整粒工程では、回転ドラム1を若干傾斜させて、回転することにより造粒物の転動が行われ、粒の大きい造粒物は、転がりやすいため、傾斜下方側へ移動される。この造粒物の分級作用により、粒の大きい造粒物が回転ドラム1の攪拌部位4側へ送られることになる。
そのため、粒の大きい造粒のみが攪拌部位へ送られ、攪拌手段により、粒の大きさを整えることがおこなわれる。これにより、所望する大きさの造粒物を速やかに造粒することができる。
In the granulation process, if the granulation is performed well by rolling of the material, the growth of the grains is promoted. In the sizing process, the rotating drum 1 is slightly tilted and rotated to rotate the granulated product. Since the granulated product having large grains is easy to roll, the granulated product is moved downwardly. Due to the classification action of the granulated product, the granulated product having large grains is sent to the stirring portion 4 side of the rotary drum 1.
Therefore, only the granulation having large grains is sent to the stirring portion, and the size of the grains is adjusted by the stirring means. Thereby, the granulated material of a desired magnitude | size can be granulated rapidly.

この整粒工程においては、回転ドラム1の傾斜角度は造粒工程よりも傾きを大きくするよう配置され、望ましくは、5〜20°の間の傾斜角度で行われる。この時、回転ドラム1と攪拌翼9は、共に回転方向を正回転(図6(c)中時計回り)とし、又回転ドラム1と攪拌翼9の回転速度を攪拌工程よりも低速にする。
これにより、大きい粒径の造粒物を攪拌することで解砕でき、造粒物の粒径を整えることが可能となり、粒の大きさ、形状が一定に整えられた造粒物を得ることができる。
In this sizing process, the inclination angle of the rotary drum 1 is arranged to be larger than that in the granulation process, and is preferably performed at an inclination angle of 5 to 20 °. At this time, both the rotating drum 1 and the stirring blade 9 are rotated in the forward direction (clockwise in FIG. 6C), and the rotating speed of the rotating drum 1 and the stirring blade 9 is set lower than that of the stirring step.
Thereby, it is possible to disintegrate the granulated product having a large particle size by stirring, to adjust the particle size of the granulated product, and to obtain a granulated product having a uniform grain size and shape. Can do.

前記、実施例では、傾胴手段として、シリンダ13を用いているが、本発明においては、これに限るものではなく、ギヤを用いた構造やジャッキを用いた構造など、回転ドラム1の傾斜を自在に変更できるものであればよい。
又、攪拌手段7は、回転ドラム1に2本設けられた例を示しているが、攪拌手段7は1本でも、又2本以上設けても、攪拌工程において材料が十分に攪拌できればよい。

図12には、スクレーパ27を設けない場合の実施例を示す。粘性の小さな回転ドラム1への付着の少ない材料を造粒する際には、スクレーパ27を設けない簡単な構造になされても良い。
また、本発明において、第一実施例のように回転ドラム1の後方壁3は閉塞させるものに限るものではなく、図12に示すように、回転ドラム1の後方壁3にも開口を設けても同様の効果を得るものである。後方壁3を開口する際には、回転ドラム1の傾斜を垂直又は垂直に近い大きな角度にする必要のない流動性の高い材料を造粒する場合に適する。これにより、回転ドラム1の傾斜手段を小型のものにすることができる。
In the above-described embodiment, the cylinder 13 is used as the tilting cylinder means. However, the present invention is not limited to this, and the tilt of the rotary drum 1 such as a structure using gears or a structure using jacks is used. Anything that can be changed freely is acceptable.
In addition, although two stirring means 7 are provided on the rotating drum 1, the stirring means 7 may be provided with one or two or more stirring means 7 as long as the material can be sufficiently stirred in the stirring step.

FIG. 12 shows an embodiment in which the scraper 27 is not provided. When granulating a material with little adhesion to the rotating drum 1 having a low viscosity, a simple structure without the scraper 27 may be used.
Further, in the present invention, the rear wall 3 of the rotary drum 1 is not limited to the closed one as in the first embodiment, and an opening is also provided in the rear wall 3 of the rotary drum 1 as shown in FIG. Has the same effect. When opening the rear wall 3, it is suitable for granulating a material with high fluidity that does not require the inclination of the rotary drum 1 to be vertical or a large angle close to vertical. Thereby, the inclination means of the rotating drum 1 can be made small.

次に他の実施例を図に示して説明する。
図7には、第2実施例として攪拌手段7が回転ドラムとは別体とし、回転ドラム1の開口部2より回転ドラム1内に侵入させて備えられた例を示している。
本第2実施例では、攪拌手段7を回転ドラム1内で移動させる移動手段が設けられており、攪拌翼9を備えた回転軸8は、ケース20に設けられ、攪拌手段用モータ10の回転力はシャフト21とケース20の内部に設けられた伝導機構(図示しない)により回転軸8に伝達され、攪拌翼9が回転される。シャフト21には、アーム22の一端が接合され、アーム22の他方端には、移動手段の動力源としてシリンダ23が設けられている。シリンダ23が伸縮することにより、アーム22を回動し、シャフト21が回転される。
Next, another embodiment will be described with reference to the drawings.
FIG. 7 shows an example in which the agitation means 7 is provided separately from the rotating drum and is inserted into the rotating drum 1 from the opening 2 of the rotating drum 1 as a second embodiment.
In the second embodiment, moving means for moving the stirring means 7 in the rotary drum 1 is provided, and the rotating shaft 8 provided with the stirring blades 9 is provided in the case 20 to rotate the stirring means motor 10. The force is transmitted to the rotating shaft 8 by a transmission mechanism (not shown) provided in the shaft 21 and the case 20, and the stirring blade 9 is rotated. One end of an arm 22 is joined to the shaft 21, and a cylinder 23 is provided at the other end of the arm 22 as a power source for moving means. When the cylinder 23 expands and contracts, the arm 22 is rotated and the shaft 21 is rotated.

図8に図7中Y−Y矢視図を示し、攪拌手段の移動した状態を示す。
図8(a)の攪拌工程においては、材料の攪拌を十分に行うため、回転ドラム1内での材料26の分布する位置へ攪拌手段7を配置し、図8(b)の造粒工程においては、材料が攪拌されないようにシリンダ23を伸長して、シャフト21を回転させ、回転ドラム1内での材料26の分布しない位置へ攪拌手段7を回動させる。
これにより、回転ドラム1の攪拌部位4を転動部位5に変更することができ、造粒工程において材料の転がりをより広範囲で行うことが可能となり、材料へ転動作用を十分に行い、短時間で造粒物を得ることができる。さらには、回転ドラム1の小型化が可能となる。
FIG. 8 shows a view taken in the direction of arrows Y-Y in FIG. 7 and shows a state where the stirring means has moved.
In the stirring step of FIG. 8 (a), in order to sufficiently stir the material, the stirring means 7 is disposed at a position where the material 26 is distributed in the rotary drum 1, and in the granulating step of FIG. 8 (b). The cylinder 23 is extended so that the material is not stirred, the shaft 21 is rotated, and the stirring means 7 is rotated to a position where the material 26 is not distributed in the rotary drum 1.
As a result, the stirring portion 4 of the rotating drum 1 can be changed to the rolling portion 5, and the material can be rolled in a wider range in the granulation process, and the material can be used for rolling operation sufficiently, and can be shortened. A granulated product can be obtained in time. Further, the rotating drum 1 can be downsized.

又、本第2実施例には、造粒工程において材料の開口部2からの流出を防ぐ材料流出防止手段6が回転ドラム1と別体に設けられる実施例が示されている。
図7に示すように回転ドラム1の開口部2を塞ぐ蓋部材24が材料流出防止手段6として回転ドラム1とは別体に設けられている。
図示しない蓋部材24の移動手段を備えることで、回転ドラム1の開口部2の開閉を自在となし、回転ドラム1への材料の投入及び造粒後の造粒物の取出しの際には、蓋部材24を開口部2へ密着させて開口部2を閉じ、材料の開口部2からの流出を確実に防ぐことができる。
蓋部材24を用いる他の例としては、蓋部材24を移動させずに固定し、回転ドラム1を傾胴させることで、蓋部材24が開口部2を開閉させる構成とするものがある。回転ドラム1が傾きを大きくした状態で開口部2と当接して閉じる位置に蓋部材24が配設されており、回転ドラム1が傾きを小さくすると、蓋部材24から開口部2から離れ、開口部2が開かれるようになされる。これにより、蓋部材24に移動手段を設けることなく、簡単な構成で材料の開口部2からの流出を防ぐことができる。
Further, in the second embodiment, an embodiment is shown in which material outflow prevention means 6 for preventing outflow of material from the opening 2 in the granulation step is provided separately from the rotary drum 1.
As shown in FIG. 7, a lid member 24 that closes the opening 2 of the rotary drum 1 is provided separately from the rotary drum 1 as the material outflow prevention means 6.
By providing a means for moving the lid member 24 (not shown), the opening 2 of the rotating drum 1 can be freely opened and closed. When the material is put into the rotating drum 1 and the granulated product is taken out after granulation, The lid member 24 is brought into close contact with the opening 2 to close the opening 2, and the outflow of material from the opening 2 can be reliably prevented.
As another example in which the lid member 24 is used, there is a configuration in which the lid member 24 is opened and closed by fixing the lid member 24 without moving and tilting the rotating drum 1. The lid member 24 is disposed at a position where the rotary drum 1 is in contact with the opening 2 and closes in a state where the inclination of the rotary drum 1 is increased. When the rotary drum 1 is reduced in inclination, the lid member 24 is separated from the opening 2 and opened. Part 2 is opened. Thus, the material can be prevented from flowing out from the opening 2 with a simple configuration without providing a moving means in the lid member 24.

次に回転ドラム2の形状の異なる実施例を図9、図10、図11に示して説明する。
図9(a)には、回転ドラム1の攪拌部位4側が下位となるような傾斜を転動部位5へ設けた回転ドラム1形状の実施例を示している。回転ドラム1の転動部位5へ傾斜を設けることで、前述で説明した傾斜したドラムによる分級作用を水平状態での回転ドラム1の内周面でも作用させ、傾動手段による回転ドラム1の傾きを小さくしても、同様の効果を得ることができるものである。
又、図9(b)には、回転ドラム1の攪拌部位4部分においても傾斜を設けた回転ドラム1形状の実施例を示している。これにより、粉体から造粒物を形成するような攪拌作用よりも転動作用を十分に行う必要のある材料の造粒工程において回転ドラム1の攪拌部位でも転動作用を少なからず行うことができる。
Next, examples in which the shape of the rotary drum 2 is different will be described with reference to FIGS.
FIG. 9A shows an embodiment of the shape of the rotating drum 1 in which the rolling portion 5 is provided with an inclination so that the stirring portion 4 side of the rotating drum 1 is in the lower order. By providing an inclination to the rolling part 5 of the rotating drum 1, the classifying action by the inclined drum described above is also applied to the inner peripheral surface of the rotating drum 1 in the horizontal state, and the inclination of the rotating drum 1 by the tilting means is made. Even if it is made smaller, the same effect can be obtained.
FIG. 9B shows an embodiment of the shape of the rotating drum 1 in which an inclination is provided also in the stirring portion 4 portion of the rotating drum 1. Thereby, in the granulation process of a material that needs to be sufficiently used for the rolling operation rather than the stirring action for forming a granulated product from the powder, the rolling operation can be performed not a little at the stirring portion of the rotary drum 1. it can.

図10(a)には、前記図9(a)の実施例における回転ドラム1の傾斜を多段階に設けた回転ドラム形状の実施例を示している。回転ドラム1の傾斜部を複数段設けることで造粒物の分級作用を段階的に複数回行い、造粒物の粒の大きさを整えやすくし、より均一な大きさの造粒物を得ることができるものである。
図10(b)には、図10(a)の実施例において、回転ドラム1の攪拌部位4部分に傾斜を設けた回転ドラム形状の実施例を示している。これにより、前記図10(a)で示す実施例においても、材料の造粒工程での材料の転動作用を十分行うことができる。
FIG. 10A shows an embodiment of a rotating drum shape in which the inclination of the rotating drum 1 in the embodiment of FIG. 9A is provided in multiple stages. By providing a plurality of inclined portions of the rotating drum 1, the granulated product is classified several times step by step, making it easy to adjust the granule size and obtaining a more uniform granulated product. It is something that can be done.
FIG. 10B shows an embodiment of a rotating drum shape in which the stirring portion 4 of the rotating drum 1 is inclined in the embodiment of FIG. Thus, also in the embodiment shown in FIG. 10A, the material can be sufficiently transferred in the granulating step.

図11に示すドラム形状の異なる実施例を説明する。
図11(a)には、前記の図9(b)の実施例とは逆の開口部2側が下位となる傾斜を設けた回転ドラム形状の実施例をしめす。
回転ドラムの傾斜を逆に設けることによっても、前述の造粒物の分級作用が行われ、形動手段による傾斜角度を調整することで同様の作用が得られるものである。
又、図11(b)には、回転ドラム1の形状が中央部に膨らんだ2つの傾斜、つまり開口部2が環を上位となす傾斜Aと、他端側を上位となす傾斜Bを有する実施例が示めされている。本実施例によれば、傾胴手段による回転ドラム1の傾斜角度を調整することにより、1つの回転ドラム内に同時に2種類の傾斜角度を備え、材料の状態に適した転動作用を得られやすくなり、多様な性状の材料に対応でき、容易に造粒することができる。
図11(c)に示す実施例は、回転ドラム1の転胴部位5に前記のような2種類の傾斜角度を備え、且つ、回転ドラム1の攪拌部位4部分を傾斜させずに、攪拌手段7をより有効に作用させて攪拌作用をより多く作用させるものである。これにより、材料の攪拌を十分に行う必要のある材料を十分攪拌できるようになし、材料の均一化された造粒物を得ることができる。
Embodiments having different drum shapes shown in FIG. 11 will be described.
FIG. 11A shows an embodiment of a rotating drum shape in which an opening 2 side opposite to the embodiment of FIG.
By providing the rotating drum with the inclination reversed, the above-mentioned granulated product classification action is performed, and the same action can be obtained by adjusting the inclination angle by the shaping means.
In FIG. 11B, the rotary drum 1 has two slopes in which the shape of the rotary drum 1 swells in the center, that is, the slope A in which the opening 2 has the ring at the upper side and the slope B in which the other end side is at the upper side. Examples are shown. According to the present embodiment, by adjusting the tilt angle of the rotary drum 1 by the tilting means, two types of tilt angles are provided simultaneously in one rotary drum, and a rolling operation suitable for the state of the material can be obtained. It becomes easy to handle materials with various properties and can be easily granulated.
In the embodiment shown in FIG. 11 (c), the rolling drum portion 5 of the rotating drum 1 has the two kinds of inclination angles as described above, and the stirring means 4 is not inclined, and the stirring means 4 is stirred. 7 is made to act more effectively, and the stirring action is made to act more. Thereby, it is possible to sufficiently stir a material that needs to be sufficiently stirred, and a granulated material having a uniform material can be obtained.

本発明の造粒装置の側面図Side view of the granulating apparatus of the present invention 攪拌工程時の回転ドラムの一部断面図Partial sectional view of the rotating drum during the stirring process 造粒工程時の回転ドラムの一部断面図Partial sectional view of rotating drum during granulation process 整粒工程時の回転ドラムの一部断面図Partial sectional view of rotating drum during sizing process 図3のX−X矢視図XX arrow view of FIG. 各工程時の回転ドラムの断面図Cross section of rotating drum at each process 第二実施例の回転ドラムの一部断面図Partial sectional view of the rotating drum of the second embodiment 第二実施例での各工程時の回転ドラムの一部断面図Partial sectional view of the rotating drum at the time of each step in the second embodiment 他の実施例での回転ドラムの一部断面図Partial sectional view of a rotating drum in another embodiment 他の実施例での回転ドラムの一部断面図Partial sectional view of a rotating drum in another embodiment 他の実施例での回転ドラムの一部断面図Partial sectional view of a rotating drum in another embodiment 他の実施例での回転ドラムの一部断面図Partial sectional view of a rotating drum in another embodiment

符号の説明Explanation of symbols

1 回転ドラム
2 開口部
4 攪拌部位
5 転動部位
6 材料流出防止手段
7 攪拌手段
9 攪拌翼
13 シリンダ(傾胴手段)
24 蓋部材
27 スクレーパ
DESCRIPTION OF SYMBOLS 1 Rotating drum 2 Opening 4 Stirring part 5 Rolling part 6 Material outflow prevention means 7 Stirring means 9 Stirring blade 13 Cylinder (tilting body means)
24 Lid member 27 Scraper

Claims (11)

本体と、該本体に支承され、一端を開口した略円筒形状となし、回転軸を中心に回転する回転ドラムと、該回転ドラムの回転軸と水平からの傾斜角度を変更する傾胴手段と、前記回転ドラム内に設けられ材料を攪拌する攪拌手段を備え、前記回転ドラムが、材料の攪拌を行なう攪拌部位と、材料を転動させて造粒する転動部位を同一ドラムに連続して設け、材料を転動する際に回転ドラムの開口部から材料の流出を防ぐ材料流出防止手段を備えることを特徴とする材料の造粒装置。 A main body, a substantially cylindrical shape supported by the main body and having one end opened, a rotating drum that rotates around a rotating shaft, and a tilting drum means that changes an angle of inclination of the rotating drum with respect to the rotating shaft; Stirring means provided in the rotating drum for stirring the material is provided, and the rotating drum has a stirring portion for stirring the material and a rolling portion for rolling and granulating the material continuously provided on the same drum. A material granulating apparatus comprising material outflow prevention means for preventing outflow of material from the opening of the rotating drum when rolling the material. 前記材料流出防止手段が、回転ドラムの開口側を開口に向けてドラム径を徐々に小さくするドラム形状とすることを特徴とする請求項1記載の材料の造粒装置。 2. The material granulation apparatus according to claim 1, wherein the material outflow prevention means has a drum shape in which the diameter of the drum is gradually reduced with the opening side of the rotating drum facing the opening. 前記材料流出防止手段が、回転ドラムと別体に設けられ、回転ドラムの開口を塞ぐ蓋部材を備えることを特徴とする請求項1記載の材料の造粒装置。 2. The material granulating apparatus according to claim 1, wherein the material outflow prevention means includes a lid member that is provided separately from the rotating drum and closes the opening of the rotating drum. 前記蓋部材が、回転ドラムの傾斜角度を変更することで回転ドラムの開口を開閉することを特徴とする請求項3記載の材料の造粒装置。 4. The material granulating apparatus according to claim 3, wherein the lid member opens and closes the opening of the rotating drum by changing an inclination angle of the rotating drum. 材料を転動する際に、前記攪拌手段を回転ドラム内で材料の攪拌を行なわない位置へ移動させる移動手段を備えることを特徴とする請求項1から4に記載の材料の造粒装置。 5. The material granulating apparatus according to claim 1, further comprising moving means for moving the stirring means to a position where the material is not stirred in the rotary drum when rolling the material. 前記回転ドラムとは別体に回転ドラムの内周に沿って設けられ、材料を掻き落とすスクレイパーを備えることを特徴とする請求項1から5に記載の材料の造粒装置。 6. The material granulating apparatus according to claim 1, further comprising a scraper that is provided along the inner periphery of the rotating drum separately from the rotating drum and scrapes off the material. 一端を開口し、一端側に材料を転動させて造粒する転動部位と他端側に材料の攪拌を行なう攪拌部位を連続して備え、回転軸を中心に回転する回転ドラムと、該回転ドラムの傾斜角度を変更する傾胴手段と、前記回転ドラム内に設けられ材料を攪拌する攪拌手段を備える材料の造粒装置を用い、前記回転ドラムの攪拌部位が転動部位よりも下方になるように回転ドラムを傾斜させて材料を攪拌する攪拌工程と、該攪拌工程よりも回転ドラムの傾斜角度を小さくして材料を転動させて造粒する造粒工程と、該造粒工程よりも回転ドラムの傾斜角度を大きくして造粒物の大きさを整える整粒工程を順に実施することを特徴とする材料の造粒方法。 One end is opened, a rolling part for rolling and granulating the material on one end side, and a stirring part for stirring the material on the other end side are provided continuously, and a rotating drum that rotates about a rotating shaft, Using a material granulating apparatus comprising a tilting drum means for changing the tilt angle of the rotating drum and a stirring means provided in the rotating drum for stirring the material, the stirring part of the rotating drum is located below the rolling part. An agitation step of inclining the rotating drum so as to stir the material, a granulation step of granulating the material by rolling the material at a smaller inclination angle of the rotating drum than the agitation step, and the granulation step A granulation method of a material characterized by sequentially performing a granulating step for adjusting the size of the granulated material by increasing the inclination angle of the rotating drum. 前記攪拌工程が、回転ドラムの回転軸と水平軸との傾斜角度を15°〜50°になして実施され、前記造粒工程が、回転ドラムの回転軸と水平軸との傾斜角度を0°〜15°になして実施され、前記整粒工程が、回転ドラムの回転軸と水平軸との傾斜角度を5°〜20°になして実施されることを特徴とする請求項7記載の材料の造粒方法。 The stirring step is performed with an inclination angle between the rotation axis of the rotating drum and the horizontal axis of 15 ° to 50 °, and the granulation step sets the inclination angle between the rotation axis of the rotating drum and the horizontal axis to 0 °. The material according to claim 7, wherein the material is sized at ˜15 °, and the sizing step is performed at an inclination angle between the rotating shaft of the rotating drum and the horizontal axis of 5 ° -20 °. Granulation method. 前記攪拌工程が、回転ドラムの回転速度を造粒工程より高速で回転させて実施され、前記整粒工程が、回転ドラムの回転速度を造粒工程より低速で回転させて実施されることを特徴とする請求項7又は8記載の材料の造粒方法。 The stirring step is performed by rotating the rotating drum at a higher speed than the granulating step, and the granulating step is performed by rotating the rotating drum at a lower speed than the granulating step. A method for granulating the material according to claim 7 or 8. 前記造粒工程が、攪拌手段の回転方向を攪拌工程と逆方向で回転させて実施され、前記整粒工程が、攪拌手段の回転方向を攪拌工程と同方向で回転させて実施されることを特徴とする請求項7から9記載の材料の造粒方法。 The granulation step is performed by rotating the stirring unit in the direction opposite to the stirring step, and the granulating step is performed by rotating the stirring unit in the same direction as the stirring step. 10. A method for granulating a material according to claim 7-9. 前記造粒工程が、回転ドラムの傾斜角度を連続的に変化させて回転ドラムを揺動させて実施されることを特徴とする請求項7から10記載の材料の造粒方法。

11. The method for granulating a material according to claim 7, wherein the granulating step is performed by continuously changing the tilt angle of the rotating drum and swinging the rotating drum.

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008284501A (en) * 2007-05-18 2008-11-27 Noritake Co Ltd Granulation method, zirconia granulated powder and zirconia porous body
JP2009078232A (en) * 2007-09-26 2009-04-16 Omnibus:Kk Coating device
JP2014030858A (en) * 2012-08-01 2014-02-20 Yamashita Works:Kk Polishing device

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JPS59222218A (en) * 1983-06-01 1984-12-13 Nippon Steel Corp Granulating method of sintered material
JPH0270729U (en) * 1988-11-14 1990-05-29
JPH0619822U (en) * 1992-08-07 1994-03-15 新東工業株式会社 Rolling stirring granulator
JPH06315619A (en) * 1993-05-04 1994-11-15 Koyo Kikai Sangyo Kk Granulator
JPH07136485A (en) * 1993-11-19 1995-05-30 Sintokogio Ltd Particulate material kneading apparatus
JPH07144248A (en) * 1993-11-25 1995-06-06 Sintokogio Ltd Method for kneading molding sand by kneading device
JPH07246354A (en) * 1994-03-11 1995-09-26 Freunt Ind Co Ltd Granulation coating device and granulation coating method using the same
JPH07257958A (en) * 1994-03-17 1995-10-09 Ngk Insulators Ltd Granulating method of raw material for ceramics
JPH11286555A (en) * 1998-04-02 1999-10-19 Dainippon Ink & Chem Inc Production of granular colorant and production apparatus therefor
JP2001187115A (en) * 1999-12-28 2001-07-10 Freunt Ind Co Ltd Method and apparatus for powder and granule material treatment

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Publication number Priority date Publication date Assignee Title
JPS59222218A (en) * 1983-06-01 1984-12-13 Nippon Steel Corp Granulating method of sintered material
JPH0270729U (en) * 1988-11-14 1990-05-29
JPH0619822U (en) * 1992-08-07 1994-03-15 新東工業株式会社 Rolling stirring granulator
JPH06315619A (en) * 1993-05-04 1994-11-15 Koyo Kikai Sangyo Kk Granulator
JPH07136485A (en) * 1993-11-19 1995-05-30 Sintokogio Ltd Particulate material kneading apparatus
JPH07144248A (en) * 1993-11-25 1995-06-06 Sintokogio Ltd Method for kneading molding sand by kneading device
JPH07246354A (en) * 1994-03-11 1995-09-26 Freunt Ind Co Ltd Granulation coating device and granulation coating method using the same
JPH07257958A (en) * 1994-03-17 1995-10-09 Ngk Insulators Ltd Granulating method of raw material for ceramics
JPH11286555A (en) * 1998-04-02 1999-10-19 Dainippon Ink & Chem Inc Production of granular colorant and production apparatus therefor
JP2001187115A (en) * 1999-12-28 2001-07-10 Freunt Ind Co Ltd Method and apparatus for powder and granule material treatment

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008284501A (en) * 2007-05-18 2008-11-27 Noritake Co Ltd Granulation method, zirconia granulated powder and zirconia porous body
JP2009078232A (en) * 2007-09-26 2009-04-16 Omnibus:Kk Coating device
JP2014030858A (en) * 2012-08-01 2014-02-20 Yamashita Works:Kk Polishing device

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