JP2007117825A - Classifier - Google Patents

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JP2007117825A
JP2007117825A JP2005310928A JP2005310928A JP2007117825A JP 2007117825 A JP2007117825 A JP 2007117825A JP 2005310928 A JP2005310928 A JP 2005310928A JP 2005310928 A JP2005310928 A JP 2005310928A JP 2007117825 A JP2007117825 A JP 2007117825A
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classification
raw material
dispersion plate
inner cylinder
gas
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JP4614132B2 (en
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Mitsuru Ikeda
充 池田
Yasuhiro Shigemoto
康弘 繁本
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Ube Machinery Corp Ltd
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Ube Machinery Corp Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a classifier which can resolve a conventional problem of the classifier that an aggregate is classified while it is not fully crushed. <P>SOLUTION: The classifier can control the rotational speed of a dispersing plate and a classification vane, respectively by making a driving machine the dispersing plate and the a classification vane independent, and for example, when a raw material containing much aggregate is classified, only the rotational number of the dispersing plate can be changed while the rotational number of the classification vane is kept constant. Therefore, as the crushing degree of the aggregate can be changed almost without changing the degree of classification (the average particle diameter of a fragment taken out), the efficiency of classification becomes good. Further, in the classifier, a raw-material throwing-in chute is made to pass in an inner cylinder for making the classification vane rotate to be used as a rotational axis and also given a raw-material supplying function. Thus, the classifier is simple in apparatus structure to allow to reduce the apparatus size although the driving machine of the dispersing plate and the classification vane are made to be independent. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明の分級装置は、石炭、石灰石、セメント原料、スラグ、セメントクリンカ、セラミックス、フィラー、化学品等の粉粒体を所定の粒度の粉粒体に効率よく分離する分級装置に関するものである。   The classifying apparatus of the present invention relates to a classifying apparatus that efficiently separates granular materials such as coal, limestone, cement raw material, slag, cement clinker, ceramics, filler, and chemicals into granular materials of a predetermined particle size.

分級装置は、粉粒体を所要の粒度の粉粒体に選別し分離することを目的とするものである。例えば、粉砕機によって粉砕された粉粒体を原料として分級するための乾式分級装置としてサイクロン分離方式等が一般的に多く用いられており、粉粒体を分級装置の分級点以上の大きさの粒径の粉粒体(粗粉)と、それより小さな粒径の粉粒体(細粉)とに選別分離している。なお、分級装置の分級点は、分級装置の種類や構造、運転条件などによって様々に変えることができる。   The classifier is intended to sort and separate powder particles into particles of a required particle size. For example, a cyclone separation method is generally used as a dry classifier for classifying powder particles pulverized by a pulverizer as a raw material, and the particles are larger than the classification point of the classifier. It is separated into a granular material having a particle size (coarse powder) and a granular material having a smaller particle size (fine powder). The classification point of the classifier can be changed variously depending on the type, structure, operating conditions, etc. of the classifier.

前述の分級装置には、多くの型式があり、例えば、特許文献1、特許文献2、又特許文献3に開示されるような構造の分級装置が公知である。   There are many types of the classifiers described above. For example, classifiers having structures as disclosed in Patent Document 1, Patent Document 2, and Patent Document 3 are known.

特開昭63−39666号公報JP 63-39666 A 特開平11−267592号公報Japanese Patent Application Laid-Open No. 11-267592 特開2001−38296公報JP 2001-38296 A

特許文献1に開示される分級装置(セパレータと称することもある)においては、装置下方から分級ガス(空気等)が導入され、該導入されたガスは装置内を上昇する気流となって、案内部材と分級羽根(分級羽根車)を抜けて装置外部に導出されている。
そして、該気流は、装置内を上昇する際に、回転している分級羽根の効果等によって渦を巻くように回転しながら上昇している。
In the classification device disclosed in Patent Document 1 (sometimes referred to as a separator), classification gas (air or the like) is introduced from the lower side of the device, and the introduced gas becomes an air flow that rises inside the device, and is guided. It passes through the member and the classification blade (classification impeller) and is led out of the apparatus.
The airflow rises while rotating so as to wind a vortex due to the effect of the rotating classification blades and the like when rising in the apparatus.

ここで、原料投入口から、分散板の上に供給された粉粒体(以下、原料と称することもある)は、分散板の回転によって分散板から飛び出し、分散板の周囲を流れる上昇気流に乗って搬送される。
そして、分散板から飛び出した原料の中で、径の大きな原料は、重量が重いため上昇気流に乗れず、下方に落下して装置下方から取り出される。
Here, the granular material (hereinafter also referred to as a raw material) supplied from the raw material inlet onto the dispersion plate jumps out of the dispersion plate by the rotation of the dispersion plate, and flows into the rising airflow flowing around the dispersion plate. It is carried on board.
Of the raw materials jumping out of the dispersion plate, the raw material having a large diameter is heavy and does not get on the ascending current but falls downward and is taken out from below the apparatus.

また、一旦、上昇気流に乗って上昇し始めた原料も、気流の回転に影響を受け、回転しながら上昇するため、比較的、粒径の大きな原料は、原料が回転することにより発生する遠心力によって気流の流れから逸脱し、下方に落下して、装置の外部に取り出される。
特許文献1に開示の分級装置は、前述の原理によって、径が大きな原料を装置下方に落下させ、径が小さく重量の小さな原料を選択的に装置上方から取り出すことができ、径の大きな原料と、径の小さな原料を分離して、分級することができる。
In addition, since the raw material once started to rise in the ascending current is also affected by the rotation of the air current and rises while rotating, the raw material having a relatively large particle diameter is generated by the rotation of the raw material. The force deviates from the flow of the air current, falls downward, and is taken out of the apparatus.
According to the principle described above, the classifying device disclosed in Patent Document 1 allows a raw material having a large diameter to fall below the apparatus, and a raw material having a small diameter and a small weight can be selectively taken out from above the apparatus. The raw material having a small diameter can be separated and classified.

また、特許文献2及び特許文献3に開示される分級装置は、前述の分級機構を一部に使用して、特に、粉粒体を粗粉、中粉、細粉の数段階の粒度構成に効率よく分級しうる分級装置に関するものである。 In addition, the classification devices disclosed in Patent Document 2 and Patent Document 3 use the above-described classification mechanism in part, and in particular, the granular material has a particle size configuration of several stages of coarse powder, medium powder, and fine powder. The present invention relates to a classification device that can classify efficiently.

ところで、前述したような従来型の分級装置等においては、分級の度合いを変えるために、分級羽根の回転数を変更することが一般的であり、分級羽根の回転数を上昇させることによって、分級装置内で強い旋回流が生じ、径の大きな原料は分級ガスの気流より逸脱して下方に落下するので、より径の小さな原料を上部から取りだすことができる。 By the way, in the conventional classification device as described above, it is common to change the rotation speed of the classification blade in order to change the degree of classification, and by increasing the rotation speed of the classification blade, classification is performed. A strong swirling flow is generated in the apparatus, and the raw material having a large diameter deviates from the air flow of the classification gas and falls downward, so that the raw material having a smaller diameter can be taken out from the upper part.

ここで、前記特許文献1に開示の分級装置の構造をみると、分散板と分級羽根を一つの駆動軸で駆動しており、分散板と分級羽根の回転数は同一となる。これは、分散板と分級羽根の位置関係に起因しており、分級羽根より装置の下側にある分散板を駆動するために、一つの駆動軸とした方が、装置構造がシンプルでコンパクトであるという技術思想による。その従来例の一例を図2に示す。 Here, looking at the structure of the classification device disclosed in Patent Document 1, the dispersion plate and the classification blade are driven by a single drive shaft, and the rotation speeds of the dispersion plate and the classification blade are the same. This is due to the positional relationship between the dispersion plate and the classification blades. To drive the dispersion plate below the device from the classification blades, it is simpler and more compact to use a single drive shaft. According to the technical idea of being. An example of the conventional example is shown in FIG.

しかし、近年になって、より効率の良い分級が求められてきおり、より分級精度の高い分級装置が求められるようになってきた。
ところが、分散板と分級羽根を一つの駆動軸で回転させる前述した従来型の分級装置を用いた場合に、分級装置内で、凝集物が十分に解砕されないまま分級ガス中に供給されて、その結果、分級精度を悪くする等という問題が生じた。
However, in recent years, more efficient classification has been demanded, and a classification apparatus with higher classification accuracy has been demanded.
However, when the above-described conventional classification device that rotates the dispersion plate and the classification blade with one drive shaft is used, the aggregate is supplied into the classification gas without being sufficiently crushed in the classification device, As a result, problems such as poor classification accuracy occurred.

また、特許文献1〜3並びに図2に示すような分級装置においては、原料を分散板に投入する際に偏りがちであって、分散板の中央部付近に均等に供給しにくいという問題があり、分散板の中央部付近に原料が均等に供給できないと、分散板から飛び出す原料の分散が均一でなくなり偏る可能性があって、原料の分散が偏ると精度良い分級が出来なくなるという問題が発生する。   Moreover, in the classifiers as shown in Patent Documents 1 to 3 and FIG. 2, there is a problem that the raw material tends to be biased when it is put into the dispersion plate, and it is difficult to supply it uniformly near the center of the dispersion plate. If the raw material cannot be evenly supplied near the center of the dispersion plate, the dispersion of the raw material popping out from the dispersion plate may not be uniform and may be biased. If the dispersion of the raw material is biased, there is a problem that accurate classification cannot be performed. To do.

本発明は、前述した従来の問題に係り、これを解決して、分級、分散効果の高い分級装置を提供することを目的とする。   The present invention relates to the above-described conventional problems, and an object of the present invention is to provide a classifier having high classification and dispersion effects by solving this problem.

上記の目的を達成するため、本発明による分級装置は、
(1) 装置上部に原料投入口と分級ガスの排出口を配し、装置下部に粗粉取出口と分級ガスの導入口を備えて、該原料投入口から垂直下方に延びる原料投入シュートの下端に円盤状の分散板を固設して分級ガスの導入口と排出口との間に配するとともに、該分散板と分級ガスの排出口との間に分級羽根を配設して、該分級ガスを分級羽根を介して該導入口から該排出口まで吹き上げることにより、該分散板上に供給されて分散させた原料を、粗粉と細粉とに分離して、細粉を装置上部に配した分級ガスの排出口より分級ガスとともに取り出すとともに、粗分を装置下部に配した粗粉取出口から取り出す分級装置であって、該分級羽根が連結部材を介して連結された内筒をケーシングに回転自在に軸支して、該内筒に原料投入シュートを挿入するとともに、該内筒の内周部分に該原料投入シュートの外周部分を回転自在に軸支し、該原料投入シュートの上端並びに下端を該内筒より突出させて、上端側の突出部を第一の回転駆動機に連結するとともに、下端側の突出部に開口部を設け、該内筒の上端部近傍を第二の回転駆動機に連結した。
In order to achieve the above object, the classifying device according to the present invention comprises:
(1) The lower end of the raw material input chute, which is provided with a raw material input port and a classification gas discharge port at the upper part of the device, and has a coarse powder outlet and a classification gas inlet at the lower part of the device, and extends vertically downward from the raw material input port. A disc-shaped dispersion plate is fixedly disposed between the introduction port and the discharge port of the classification gas, and a classification blade is disposed between the dispersion plate and the discharge port of the classification gas, and the classification is performed. By blowing up the gas from the inlet to the outlet through a classification blade, the raw material supplied and dispersed on the dispersion plate is separated into coarse powder and fine powder, and the fine powder is placed on the upper part of the apparatus. A classification device that takes out the classified gas from the arranged classification gas discharge port together with the classified gas and also takes out the coarse component from the coarse powder outlet provided in the lower part of the apparatus, and the inner cylinder in which the classification blades are connected via a connecting member is a casing. The material input chute is inserted into the inner cylinder. In addition, the outer peripheral portion of the raw material charging chute is rotatably supported on the inner peripheral portion of the inner cylinder, the upper end and the lower end of the raw material charging chute are protruded from the inner cylinder, and the protruding portion on the upper end side is While being connected to one rotation driving machine, an opening was provided in the projecting part on the lower end side, and the vicinity of the upper end part of the inner cylinder was connected to the second rotation driving machine.

(2) (1)に記載の分級装置において、前記開口部を、原料投入シュート下端部の円周方向に等間隔に設ける構成とした。 (2) In the classification apparatus according to (1), the openings are provided at equal intervals in the circumferential direction of the lower end portion of the raw material charging chute.

本発明によれば、分散板と分級羽根の駆動機を別個にすることにより、分散板と分級羽根の回転速度を、それぞれ単独に制御できる。
従って、凝集物が多い原料を分級する場合等においては、分級羽根の回転数を一定に保ったまま、分散板の回転数をのみを変化させることが可能である。
分級羽根の回転数を一定に保ったまま、分散板の回転数を上昇させることができれば、分級の度合い(取り出される細分の平均粒径)をほとんど変えることなく、分散板から飛び出す原料の飛び出し速度を上昇させることができ、勢い良く分散板から飛び出た原料は、分散板の側面にあるケーシングの側壁に強くぶつかり、凝集が解砕されるので、分級の効率が良くなる。
According to the present invention, the rotational speeds of the dispersion plate and the classification blade can be individually controlled by separately providing the driving devices for the dispersion plate and the classification blade.
Therefore, when classifying a raw material having a large amount of aggregates, it is possible to change only the rotational speed of the dispersion plate while keeping the rotational speed of the classification blade constant.
If the rotation speed of the dispersion plate can be increased while keeping the rotation speed of the classification blade constant, the raw material jumping speed that jumps out of the dispersion plate is hardly changed, with almost no change in the degree of classification (average particle size of the extracted subdivision). The raw material jumping out of the dispersion plate vigorously collides with the side wall of the casing on the side surface of the dispersion plate and agglomerates are crushed, so that the classification efficiency is improved.

また、本発明は、分級羽根を回転させるための内筒の中に、原料投入シュートを通して分散板の回転軸として利用するとともに原料供給機能を持たせた。そのため、分散板と分級羽根の駆動機を別個にした分級装置であるにもかかわらず、装置構成が簡単で小型化可能である。 In the present invention, the inner cylinder for rotating the classification blade is used as a rotating shaft of the dispersion plate through the raw material charging chute and has a raw material supply function. Therefore, the apparatus configuration is simple and can be miniaturized despite the classifying apparatus in which the dispersing plate and the classifying blade drive are separately provided.

さらに、分散板に原料を供給する場合に、原料は出来る限り分散板の中央付近に均一に供給することが重要であって、分散板の外周に均一な状態で飛び出させた方が、分級精度が良くなる。本発明により、原料投入シュート下端に形成した開口部を、円周方向に等間隔に設ける構成とすれば、原料投入シュート下端に形成した開口部から分散板の中央付近に原料を均一に供給することができるので、分散板から飛び出す原料の状態を、均一にすることができる。   Furthermore, when supplying the raw material to the dispersion plate, it is important to supply the raw material as uniformly as possible near the center of the dispersion plate. Will be better. According to the present invention, if the opening formed at the lower end of the raw material charging chute is provided at equal intervals in the circumferential direction, the raw material is uniformly supplied from the opening formed at the lower end of the raw material charging chute to the vicinity of the center of the dispersion plate. Therefore, the state of the raw material jumping out from the dispersion plate can be made uniform.

以上説明したように本発明によれば、分級装置を大型化することなく、分散及び分級の機能を個々に最大限発揮でき、分級効率が高まることにより付随する分級ガスの送風機の圧力損失などを低下させることが可能である。 As described above, according to the present invention, without increasing the size of the classifier, the functions of dispersion and classification can be maximized individually, and the classification efficiency is increased, thereby increasing the pressure loss of the accompanying classified gas blower. It can be reduced.

以下、図面に基づき本発明の好ましい実施形態の1例について詳細に説明する。
図1は本実施形態による分級装置の構造を概念的に説明する要部断面図である。
Hereinafter, an example of a preferred embodiment of the present invention will be described in detail with reference to the drawings.
FIG. 1 is a cross-sectional view of an essential part for conceptually explaining the structure of the classification device according to the present embodiment.

まず、最初に、本実施形態における分級装置50の構造を、図1に基づいて説明する。
本実施形態における分級装置50は、図1に示すように、周囲をケーシングで囲まれており、該ケーシングの上側部分は筒状であって、略中央部付近から下側部分は、下側に向かって径が小さくなる逆切頭円錐型に類似する形状となっている。
First, the structure of the classification device 50 in this embodiment will be described with reference to FIG.
As shown in FIG. 1, the classification device 50 in the present embodiment is surrounded by a casing, the upper portion of the casing is cylindrical, and the lower portion extends from the vicinity of the substantially central portion to the lower side. It has a shape similar to a reverse truncated cone shape with a decreasing diameter.

また、ケーシングの上部は、分級ガス(本実施形態では空気)や原料(粉粒体)が、不必要に漏れださないように天板により封止されているが、内筒65が軸受によって回転自在な状態でケーシングの天板に軸支されて、天板を貫通し、ケーシング内に挿入されているとともに、分級ガスとともに細粉を取り出すための排出口63が設けられている。   The upper part of the casing is sealed with a top plate so that classification gas (air in this embodiment) and raw materials (powder particles) do not leak unnecessarily, but the inner cylinder 65 is supported by a bearing. It is pivotally supported on the top plate of the casing in a rotatable state, passes through the top plate, is inserted into the casing, and is provided with a discharge port 63 for taking out fine powder together with the classification gas.

ここで、内筒65は、その下端部を円盤状の連結部材56の中心部分に固設して、該連結部材56の外周縁部に、複数枚の分級羽根を配している。
分級羽根52は、その各々の下端が連結部材56の外周縁に取り付けられて、内筒65を中心においた円を描くようにして円周方向に等間隔に配されている。
なお、分級羽根52は、その上端がケーシング上部に配した天板と近接して、環状通路Sから流れてきた分級ガスが、分級羽根を通過して排出口63に流れていくようにするために、排出口63により天板に開けられた開口を、連結部材と分級羽根52の列で下側から囲むよう配置されている
従って、本実施形態においては、複数枚の分級羽根52において隣り合う2枚の分級羽根の周方向の間に、運転中、分級ガスと細粉が通過することができる隙間を有しているとともに、原料が分級羽根52をショートパスして排出口63に到達しないような構造としている。
Here, the lower end of the inner cylinder 65 is fixed to the central portion of the disk-shaped connecting member 56, and a plurality of classification blades are arranged on the outer peripheral edge of the connecting member 56.
The classification blades 52 are attached to the outer peripheral edge of the connecting member 56 at their lower ends, and are equally spaced in the circumferential direction so as to draw a circle centered on the inner cylinder 65.
The classification blade 52 is arranged so that the upper end of the classification blade 52 is close to the top plate arranged on the upper part of the casing so that the classification gas flowing from the annular passage S flows to the discharge port 63 through the classification blade. Further, the openings opened in the top plate by the discharge port 63 are arranged so as to surround from the lower side with the row of the connecting members and the classification blades 52. Therefore, in the present embodiment, the plurality of classification blades 52 are adjacent to each other. Between the circumferential directions of the two classification blades, there is a gap through which the classification gas and fine powder can pass during operation, and the raw material does not pass through the classification blades 52 and does not reach the discharge port 63. It has a structure like this.

また、内筒65の管内には、原料投入シュート58が、軸受により回転自在に軸支された状態で貫通しており、原料投入シュート58の上端及び下端が、内筒65から突出した状態となっている。そして、原料投入シュート58の上端部には、原料投入口59が形成されており、また、原料投入シュート58の下端部には、円盤状の分散板が水平な状態で固設されている。   Further, a raw material charging chute 58 passes through the pipe of the inner cylinder 65 while being rotatably supported by a bearing, and the upper end and the lower end of the raw material charging chute 58 protrude from the inner cylinder 65. It has become. A raw material charging port 59 is formed at the upper end of the raw material charging chute 58, and a disc-shaped dispersion plate is fixed to the lower end of the raw material charging chute 58 in a horizontal state.

ここで、分散板53の外周側で一定の距離が離れた位置にケーシングの一部が側壁として形成されている。詳細を後述するが、分散板53の外周部分と該側壁部分の間に形成された環状通路Sを、分級ガスが吹き上げる構成となっており、また、分散板から遠心力によって飛び出した原料の一部が側壁に衝突するよう構成されている。
本実施形態においては、前述の構成により、分散板53から環状通路Sに放出された原料及び前述の側壁に衝突した原料は、環状通路Sを吹き上げられる分級ガスにより粗粉とそれより小さな粉に分離させられる。従って、本実施形態においては、該分散板53、側壁、及び、環状通路Sにより一つの分級部を構成する。
Here, a part of the casing is formed as a side wall at a position away from the outer peripheral side of the dispersion plate 53 by a certain distance. As will be described in detail later, classification gas blows up an annular passage S formed between the outer peripheral portion of the dispersion plate 53 and the side wall portion, and one of the raw materials jumped out of the dispersion plate by centrifugal force. The part is configured to collide with the side wall.
In the present embodiment, the raw material released from the dispersion plate 53 into the annular passage S and the raw material that collided with the side wall are converted into coarse powder and smaller powder by the classification gas blown up in the annular passage S in the present embodiment. Be separated. Therefore, in this embodiment, one classifying part is constituted by the dispersion plate 53, the side wall, and the annular passage S.

次に、本実施形態においては、分散板53の位置を境にして、それより下方のケーシングは、下側に向かって縮径して、所謂、逆向きの切頭円錐形状に類似する形状となっており、その下端に粗粉取出口55を設けている。
前述したように装置内で分級ガスの気流に乗れなかった原料は、下側のケーシングに落下して、粗分取出口55に集まるように滑り落ちていく構造となっている。
Next, in the present embodiment, with the position of the dispersion plate 53 as a boundary, the casing below it is reduced in diameter toward the lower side, and has a shape similar to a so-called reverse truncated cone shape. The coarse powder outlet 55 is provided at the lower end.
As described above, the raw material that has not been able to get on the classification gas flow in the apparatus falls into the lower casing and slides down so as to gather at the coarse separation outlet 55.

また、分散板53の底面には、下側に向かって縮径する逆円錐形状の下部コーン57が配されており、下部コーン57のすぐ下方で、分級ガスが吹き上がる環状通路Sの下方に、ガス導入口61からのガス通路が先端を上方に開口した状態で設けられており、前述した下部コーン57の下端が、ガス通路先端の開口に入った状態で配されている。
従って、下部コーン57の作用によりガス導入口61から分級装置50内に吹き出される分級ガスを環状通路Sの周方向に均等に流すことができる。
そのため、一度、分級されて、粗粉としてケーシングを滑り落ちていく原料を分級ガスで、再度、下側から吹き上げるといった無駄を減らすことが出来る。
In addition, an inverted conical lower cone 57 whose diameter is reduced toward the lower side is disposed on the bottom surface of the dispersion plate 53. Just below the lower cone 57, below the annular passage S where the classification gas blows up. The gas passage from the gas inlet 61 is provided with the tip opened upward, and the lower end of the lower cone 57 described above is disposed in the state where the gas passage tip is opened.
Therefore, the classification gas blown out from the gas inlet 61 into the classification device 50 by the action of the lower cone 57 can be made to flow evenly in the circumferential direction of the annular passage S.
For this reason, it is possible to reduce waste that the raw material that has been classified once and slides down the casing as coarse powder is again blown from the lower side with the classification gas.

また、分散板53に固設された原料投入シュート58の内筒65より上側に突出した部分と、天板上に固設された第1の電動機68とベルトを介して連結されているので、電動機68の回転により分散板53を回転させることができる。   In addition, since the raw material charging chute 58 fixed to the dispersion plate 53 is connected to the portion protruding above the inner cylinder 65 and the first electric motor 68 fixed to the top plate via a belt, The dispersion plate 53 can be rotated by the rotation of the electric motor 68.

また、分級羽根52を支持する内筒65は、天板上に設けられた第2の電動機69とベルトを介して介して連結されているので、電動機69の回転により分級羽根52を回転させることができる。 Further, since the inner cylinder 65 that supports the classification blade 52 is connected to the second electric motor 69 provided on the top plate via a belt, the classification blade 52 is rotated by the rotation of the electric motor 69. Can do.

次に、図1に基づいて、上記のように構成された分級装置50の作動について説明する。
まず、原料投入口59より投入された原料(以下、粉粒体と称することもある)が原料投入シュート58を通り、分散板53上の中央部付近に落下し、原料投入シュート58の下端に形成された開口部54から分散板53上に供給される。
ここで、本実施形態においては、原料投入シュート下端に形成した略正方形上の開口部54を、円周方向に等間隔に4個設ける構成として、分散板上に均一な状態で原料を供給した。しかし、本発明に適応できる開口部54の構成は前述の実施形態による構成に限らず、開口部54は、長方形や半円形状などであっても良く、本発明による技術思想を逸脱しない範囲で変更することが可能である。
Next, the operation of the classifier 50 configured as described above will be described with reference to FIG.
First, a raw material (hereinafter also referred to as a powder) introduced from the raw material input port 59 passes through the raw material input chute 58 and falls to the vicinity of the central portion on the dispersion plate 53, and reaches the lower end of the raw material input chute 58. It is supplied onto the dispersion plate 53 from the formed opening 54.
Here, in this embodiment, the raw material is supplied in a uniform state on the dispersion plate as a configuration in which four substantially square openings 54 formed at the lower end of the raw material charging chute are provided at equal intervals in the circumferential direction. . However, the configuration of the opening 54 that can be applied to the present invention is not limited to the configuration according to the above-described embodiment, and the opening 54 may be a rectangle or a semicircular shape, and does not depart from the technical idea of the present invention. It is possible to change.

原料が供給された際に、分散板53は第1電動機68によって回転しているため、供給した原料も分散板53の回転に従働されて回転を始める。そのため、原料に回転による遠心力が発生して、原料は分散板53の外周方向へ移動し、やがて、分散板53から環状通路Sの方向へ飛び出して行く。   Since the dispersion plate 53 is rotated by the first electric motor 68 when the raw material is supplied, the supplied raw material is also driven by the rotation of the dispersion plate 53 and starts rotating. Therefore, centrifugal force is generated in the raw material, and the raw material moves toward the outer periphery of the dispersion plate 53, and eventually jumps out from the dispersion plate 53 toward the annular passage S.

分散板53から飛び出した原料は、分級ガス吹き上げている分散板53とケーシング側壁部分の間の環状通路Sに達し、環状通路Sに放り出されるか、または、該側壁に衝突し、環状通路Sに放り出される。この時、環状通路Sには、ガス導入口61より吹き出された分級ガスが、下部コーン57とケーシングの間を通って、下方から周囲均等流となって吹き上げられており、大きな粒径以外の原料は、上方に吹き上げられるが、大きな粒径の原料(粗粉)は吹き上げられず、そのまま落下する。
落下した大きな粒径の原料は、環状通路Sから落下して、ケーシングを滑り落ちながら、下端の粗粉取出口55より取り出される。
The raw material that has jumped out from the dispersion plate 53 reaches the annular passage S between the dispersion plate 53 and the casing side wall portion where the classification gas is blown up, and is thrown out into the annular passage S or collides with the side wall to enter the annular passage S. Thrown out. At this time, the classified gas blown from the gas introduction port 61 is blown up into the annular passage S through the space between the lower cone 57 and the casing as a uniform flow from the lower side. The raw material is blown upward, but the raw material having a large particle size (coarse powder) is not blown up and falls as it is.
The dropped raw material having a large particle diameter falls from the annular passage S and is taken out from the coarse powder outlet 55 at the lower end while sliding down the casing.

なお、凝集物が多い原料を分級する場合、或いは分級後、取り出された細粉の中に凝集物が多いなどの場合は、分級羽根52の回転数を一定に保ったまま、分散板53の回転数をのみを上昇させる。分散板53の回転数を上昇させることによって、分散板53から飛び出す原料の飛び出し速度を上昇させることができ、勢い良く分散板53から飛び出た原料は、分散板53の側面にあるケーシングの側壁に強くぶつかり、凝集が解砕されるので、分級の効率が良くなる。 In addition, when classifying a raw material with a lot of aggregates, or when there are a lot of aggregates in the fine powder taken out after classification, the rotational speed of the classification blade 52 is kept constant and the dispersion plate 53 Only increase the number of revolutions. By raising the rotation speed of the dispersion plate 53, the jumping speed of the raw material jumping out from the dispersion plate 53 can be increased, and the raw material jumping out from the dispersion plate 53 vigorously hits the side wall of the casing on the side surface of the dispersion plate 53. Since it collides strongly and agglomeration is crushed, the classification efficiency is improved.

また、ガス導入口61から装置内に吹き出された分級ガスが下部コーン57で整流され、環状通路Sの全体に分級ガスを均等に吹き上げることができるので、どの場所でも比較的均一な分級が行われる。   Further, since the classified gas blown into the apparatus from the gas inlet 61 is rectified by the lower cone 57 and the classified gas can be evenly blown up to the entire annular passage S, relatively uniform classification can be performed at any place. Is called.

また、一旦、分級ガスにより吹き上げられた原料は、気流の回転に影響を受け、回転しながら上昇するため、比較的、粒径の大きな原料は、原料が回転することにより発生する遠心力によって気流の流れから逸脱し、下方に落下して、装置の外部に取り出される。
そして、小さな粒径の粉原料(細粉)のみ回転している分級羽根52向の隙間を通り抜けて、分級ガスに同伴されて排出口63より取り出される。
In addition, since the raw material once blown up by the classification gas is affected by the rotation of the air flow and rises while rotating, the raw material having a relatively large particle size is flown by the centrifugal force generated by the rotation of the raw material. Deviates from the flow of the flow, falls downward and is taken out of the apparatus.
Then, only the powder raw material (fine powder) having a small particle diameter passes through the gap toward the classifying blade 52 and is taken out from the discharge port 63 along with the classification gas.

なお、以上の実施形態では分散板53と分級羽根52の駆動原動機は、第1電動機68、及び第2電動機69とした場合を示したが、該原動機は2台の油圧モータ等であっても良い。   In the above embodiment, the driving motors of the dispersion plate 53 and the classification blade 52 are the first motor 68 and the second motor 69. However, the driving motor may be two hydraulic motors or the like. good.

本実施形態に係る分級装置構造を説明するための要部断面図である。It is principal part sectional drawing for demonstrating the classification apparatus structure which concerns on this embodiment. 従来の分級装置構造を説明するための要部断面図である。It is principal part sectional drawing for demonstrating the conventional classification apparatus structure.

符号の説明Explanation of symbols

50 分級装置
52 分級羽根
53 分散板
55 粗粉取出口
56 連結部材
57 下部コーン
58 原料投入シュート
59 原料投入口
61 ガス導入口
63 排出口
65 内筒
68 電動機
69 電動機
50 classifier 52 classifying blade 53 dispersion plate 55 coarse powder outlet 56 connecting member 57 lower cone 58 raw material input chute 59 raw material input port 61 gas inlet 63 discharge port 65 inner cylinder 68 electric motor 69 electric motor

Claims (2)

装置上部に原料投入口と分級ガスの排出口を配し、装置下部に粗粉取出口と分級ガスの導入口を備えて、該原料投入口から垂直下方に延びる原料投入シュートの下端に円盤状の分散板を固設して分級ガスの導入口と排出口との間に配するとともに、該分散板と分級ガスの排出口との間に分級羽根を配設して、
該分級ガスを分級羽根を介して該導入口から該排出口まで吹き上げることにより、該分散板上に供給されて分散させた原料を、粗粉と細粉とに分離して、細粉を装置上部に配した分級ガスの排出口より分級ガスとともに取り出すとともに、粗分を装置下部に配した粗粉取出口から取り出す分級装置であって、
該分級羽根が連結部材を介して連結された内筒を装置ケーシングに回転自在に軸支して、該内筒に原料投入シュートを挿入するとともに、該内筒の内周部分に該原料投入シュートの外周部分を回転自在に軸支し、該原料投入シュートの上端並びに下端を該内筒より突出させて、上端側の突出部を第一の回転駆動機に連結するとともに、下端側の突出部に開口部を設け、該内筒の上端部近傍を第二の回転駆動機に連結した分級装置。
A raw material inlet and a classification gas outlet are arranged at the upper part of the device, a coarse powder outlet and a classification gas inlet are provided at the lower part of the device, and a disk-like shape is formed at the lower end of the raw material input chute extending vertically downward from the raw material input port. The dispersion plate is fixed and disposed between the classification gas introduction port and the discharge port, and the classification blade is disposed between the dispersion plate and the classification gas discharge port,
By blowing up the classification gas from the inlet to the outlet through a classification blade, the raw material supplied and dispersed on the dispersion plate is separated into coarse powder and fine powder, and a fine powder is obtained. A classification device that takes out the classification gas from the classification gas discharge port disposed in the upper portion together with the classification gas, and extracts the coarse portion from the coarse powder outlet disposed in the lower portion of the apparatus,
An inner cylinder to which the classifying blades are connected via a connecting member is rotatably supported on an apparatus casing, and a raw material charging chute is inserted into the inner cylinder, and the raw material charging chute is inserted into an inner peripheral portion of the inner cylinder. The outer peripheral portion of the raw material is rotatably supported, the upper end and the lower end of the raw material charging chute are protruded from the inner cylinder, the upper end side protruding portion is connected to the first rotary drive unit, and the lower end side protruding portion A classifying device in which an opening is provided in the inner cylinder and the vicinity of the upper end of the inner cylinder is connected to a second rotary driving machine.
前記開口部を、原料投入シュート下端部の円周方向に等間隔に設けた請求項1記載の分級装置。   The classification device according to claim 1, wherein the openings are provided at equal intervals in a circumferential direction of a lower end portion of the raw material charging chute.
JP2005310928A 2005-10-26 2005-10-26 Classification device Expired - Fee Related JP4614132B2 (en)

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