JPH0677864U - Three-way classifier and crushing equipment using the classifier - Google Patents

Three-way classifier and crushing equipment using the classifier

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Publication number
JPH0677864U
JPH0677864U JP5124993U JP5124993U JPH0677864U JP H0677864 U JPH0677864 U JP H0677864U JP 5124993 U JP5124993 U JP 5124993U JP 5124993 U JP5124993 U JP 5124993U JP H0677864 U JPH0677864 U JP H0677864U
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Japan
Prior art keywords
casing
fine powder
medium
raw material
particles
Prior art date
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Pending
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JP5124993U
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Japanese (ja)
Inventor
新悟 向井
哲 富永
暢哉 八田
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石川島播磨重工業株式会社
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Priority to JP5124993U priority Critical patent/JPH0677864U/en
Publication of JPH0677864U publication Critical patent/JPH0677864U/en
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  • Combined Means For Separation Of Solids (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

(57)【要約】 【目的】 原料を大径粒子・中径粒子・微粉に精度よく
しかも効率よく分離することができるようにする。 【構成】 上端に微粉吸引口2を有し下端に中径粒子排
出口3を有するケーシング1と、ケーシング1の上端を
貫通しケーシング1の内部に垂下された原料投入シュー
ト4と、ケーシング1内の上方位置で原料投入シュート
4の外周に設けられ中心側が微粉吸引口2に連通された
回転分級羽根10と、ケーシング1内の下方位置で原料
投入シュート4の下端直下に設けられ下部が逆円錐状に
形成された分散板11と、ケーシング1下端を貫通し上
端が分散板11の下部に沿って拡がる漏斗状に形成され
ケーシング1内に空気を導入する空気導入ダクト12と
を備え、微粉Aは微粉吸引口2から、中径粒子Bは中径
粒子排出口3から、大径粒子Cは空気導入ダクト12か
ら取り出される。
(57) [Summary] [Purpose] To enable the separation of raw materials into large particles, medium particles, and fine powders accurately and efficiently. A casing 1 having a fine powder suction port 2 at an upper end and a medium particle discharge port 3 at a lower end, a raw material charging chute 4 penetrating the upper end of the casing 1 and hanging inside the casing 1, and a casing 1 The rotary classification blade 10 provided on the outer periphery of the raw material feeding chute 4 at a position above the center and communicating with the fine powder suction port 2 on the center side, and the lower portion provided directly below the lower end of the raw material feeding chute 4 at a lower position inside the casing 1 and having a lower portion of the conical The fine powder A is provided with a dispersion plate 11 formed into a shape, and an air introduction duct 12 that penetrates the lower end of the casing 1 and has a funnel shape whose upper end extends along the lower part of the dispersion plate 11 to introduce air into the casing 1. Are taken out from the fine powder suction port 2, medium-sized particles B are taken out from the medium-sized particle discharge port 3, and large-sized particles C are taken out from the air introduction duct 12.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は、粉砕された粉体を、微粉、中径粒子、大径粒子の三種類に分級する 三方向分級機及び該分級機を用いた粉砕設備に関するものである。 The present invention relates to a three-way classifier for classifying pulverized powder into fine powder, medium-sized particles, and large-sized particles, and a crushing equipment using the classifier.

【0002】[0002]

【従来の技術】[Prior art]

セメント製造設備においては、セメント原料を予備粉砕装置と本粉砕装置とに よって二段階に粉砕することが、従来から行われている。 In a cement manufacturing facility, it has been conventionally practiced to pulverize cement raw materials in two stages by a preliminary pulverizing device and a main pulverizing device.

【0003】 すなわち、原料ホッパからのセメント原料を、クラッシャ或いはローラミル等 の予備粉砕装置に導いて予備粉砕し、予備粉砕した粉砕物を篩式分級機に導いて 篩分けを行い、篩式分級機で分離された篩上の大径粒子を予備粉砕装置に戻し、 篩式分級機で分離された篩下の微粉・中径粒子を微粉砕性能が優れた横型のボー ルミル等の本粉砕装置に導入して本粉砕を行い、本粉砕装置で本粉砕された粉砕 物を空気式分級機に導いて再度分級し、粉砕の十分でない中径粒子は本粉砕装置 に再投入し、微粉は製品として取り出していた。That is, the cement raw material from the raw material hopper is introduced into a preliminary crushing device such as a crusher or a roller mill for preliminary crushing, and the crushed pulverized product is introduced into a sieve type classifier for sieving, and a sieve type classifier. The large particles on the sieve separated in step 1 are returned to the preliminary crusher, and the fine powder / medium particles under the sieve separated by the sieve classifier are converted to the main crusher such as a horizontal ball mill with excellent fine crushing performance. Introduce the main crushing, then introduce the crushed product crushed by the crusher to the air classifier and classify again. I was taking it out.

【0004】[0004]

【考案が解決しようとする課題】[Problems to be solved by the device]

しかしながら、上述したような従来の粉砕設備では、予備粉砕装置で予備粉砕 した粉砕物を、単に篩式分級機により大径粒子と微粉・中径粒子とに分離するよ うにしているが、篩式分級機では、篩目の磨耗による補修、交換が頻繁に必要で あり、分級能力に機械的な限界があるという問題があった。 However, in the conventional crushing equipment as described above, the crushed material preliminarily crushed by the preliminary crushing device is simply separated into large-sized particles and fine / medium-sized particles by a sieve classifier. The type classifier had a problem that it required frequent repairs and replacements due to abrasion of the sieve mesh, and its classifying capacity had a mechanical limit.

【0005】 また、大径粒子に微粉・中径粒子が多量に付着混合したまま予備粉砕装置に戻 される為に、予備粉砕装置の粉砕効率が低下してしまう問題があり、更に本粉砕 装置に導かれる微粉・中径粒子には、製品となるべき微粉が多量に含まれている ことから、本粉砕装置では微粉を再び粉砕する過粉砕になって、元来微粉砕性能 は優れているが処理能力が小さい本粉砕装置の粉砕効率が著しく低下してしまう といった問題があった。Further, since a large amount of fine powder / medium-sized particles are attached to and mixed with the large-diameter particles and returned to the preliminary crushing device, there is a problem that the pulverization efficiency of the preliminary pulverizing device is lowered. Since the fine powder / medium-sized particles that are guided to contain a large amount of fine powder to be used as a product, this pulverizer re-pulverizes the fine powder again, resulting in excellent fine pulverizing performance. However, there was a problem that the pulverization efficiency of this pulverizer, which has a small processing capacity, is significantly reduced.

【0006】 更に、稼働中の粉砕設備には、設備内輸送機や設備内分級機に制限能力があっ て、予備粉砕された粉砕物中に含まれる小径粒子をも、これら制限能力内で扱わ なければならないことから、処理能力が制限されてしまう問題があった。[0006] Furthermore, the crushing equipment in operation has a restriction capability in the in-equipment transportation machine and the in-equipment classifier, and small particles contained in the pre-crushed pulverized material are also treated within these restriction capabilities. Since it has to be done, there is a problem that the processing capacity is limited.

【0007】 本考案は上述した従来の問題を解決し、従来の篩式分級機より補修、交換の頻 度が少なくてすみ、しかも従来の篩式分級機より分級能力が高く、一台で原料を 大径粒子・中径粒子・微粉に精度よくしかも効率よく分離することができ、分離 した粉体の粒径に応じた後処理を必要とする場合に最適な三方向分級機を提供す ると共に、該分級機を用いた粉砕設備を提供することを目的とするものである。The present invention solves the above-mentioned conventional problems, requires less frequent repair and replacement than conventional sieve classifiers, and has a higher classification capacity than conventional sieve classifiers. It is possible to accurately and efficiently separate large particles, medium particles, and fine powders, and to provide an optimal three-way classifier when post-treatment is required according to the particle size of the separated powder. In addition, the object is to provide a crushing facility using the classifier.

【0008】[0008]

【課題を解決するための手段】[Means for Solving the Problems]

本考案の請求項1に記載の考案は、上部に微粉吸引口を有し下部に中径粒子排 出口を有するケーシングと、該ケーシングの上端を貫通し該ケーシングの内部に 垂下された原料投入シュートと、前記ケーシング内の上方位置で前記原料投入シ ュートの外周に設けられ中心側が前記微粉吸引口に連通された回転分級羽根と、 前記ケーシング内の下方位置で前記原料投入シュートの下端直下に設けられ下部 が逆錐形状に形成された分散板と、前記ケーシング下端を貫通し上端が前記分散 板の下部に沿って拡がる漏斗状に形成され前記ケーシング内に空気を導入すると 共に前記漏斗状部上方で大径粒子と中径粒子を分離し大径粒子を排出する空気導 入ダクトとを備えたことを特徴とする三方向分級機に係るものであり、本考案の 請求項2に記載の考案は、前述した三方向分級機を、予備粉砕装置と本粉砕装置 との間に設け、前記予備粉砕機により粗粉砕された予備粉砕物を前記三方向分級 機の原料投入シュートに導き得るよう構成すると共に、前記三方向分級機の中径 粒子排出口より排出された中径粒子を前記本粉砕装置に導き且つ前記三方向分級 機の空気導入ダクトより排出された大径粒子を前記予備粉砕装置に戻し得るよう 構成し、更に前記三方向分級機の微粉吸引口には微粉を吸引して回収する微粉捕 集装置を接続したことを特徴とする三方向分級機を用いた粉砕設備に係るもので ある。 The invention according to claim 1 of the present invention is a casing having a fine powder suction port in the upper part and a medium diameter particle discharge port in the lower part, and a raw material charging chute penetrating the upper end of the casing and hanging inside the casing. A rotary classifying blade provided on the outer periphery of the raw material feeding short at an upper position in the casing and having a center side communicating with the fine powder suction port; and a lower position directly below the lower end of the raw material feeding chute at a lower position in the casing. The lower part of the dispersion plate is formed in the shape of an inverted pyramid, and the upper end is formed into a funnel shape that penetrates the lower end of the casing and expands along the lower part of the dispersion plate. According to claim 2 of the present invention, there is provided a three-way classifier, comprising: an air introduction duct for separating large particles and medium particles and discharging large particles. The idea is to install the above-mentioned three-way classifier between the preliminary crushing device and the main crushing device so that the preliminary crushed material roughly crushed by the preliminary crusher can be guided to the raw material chute of the three-way classifier. In addition to the above, the medium-sized particles discharged from the medium-sized particle discharge port of the three-way classifier are guided to the main pulverizer, and the large-sized particles discharged from the air introduction duct of the three-way classifier are pre-milled. A pulverizing equipment using a three-way classifier characterized in that a fine powder collecting device for sucking and collecting fine powder is connected to the fine powder suction port of the three-way classifier. It is a thing.

【0009】[0009]

【作用】[Action]

従って本考案の請求項1に記載の三方向分級機では、空気導入ダクトからケー シング内に空気を導入すると共に、微粉吸引口からケーシング内の空気を吸引し て回転分級羽根を回転しながら、原料を原料投入シュートからケーシング内に投 入すると、原料は分散板上に落下して分散板の周りに分散し、小径粒子の微粉と 中径粒子とは、分散板の下部周囲から吹き上げる空気により上昇し、微粉は回転 分級羽根の間を通って微粉吸引口からケーシングの外部に吸引され、中径粒子は 回転分級羽根に飛ばされ、ケーシングの内周を落下して中径粒子排出口からケー シングの外部に排出され、大径粒子は分散板の下部周囲から吹き上げる空気では 上昇せずに空気導入ダクト内に落下してケーシングの外部に排出される。 Therefore, in the three-way classifier according to claim 1 of the present invention, while introducing air into the casing from the air introduction duct and sucking air in the casing from the fine powder suction port to rotate the rotary classifying blade, When the raw material is thrown into the casing from the raw material chute, the raw material falls on the dispersion plate and is dispersed around the dispersion plate, and the fine powder of small particles and the medium particles are blown by the air blown from around the lower part of the dispersion plate. Ascends, the fine powder passes between the rotary classification blades and is sucked from the fine powder suction port to the outside of the casing, and the medium-sized particles are blown to the rotary classification blade and fall on the inner circumference of the casing to be discharged from the medium-sized particle discharge port. The large particles are discharged to the outside of the singing, and the large particles do not rise by the air blown from around the lower part of the dispersion plate, but fall into the air introduction duct and are discharged to the outside of the casing.

【0010】 また、本考案の請求項2に記載の三方向分級機を用いた粉砕設備では、予備粉 砕装置にて粗粉砕された予備粉砕物が三方向分級機の原料投入シュートに導かれ 、三方向分級機内で微粉、中径粒子、大径粒子に分級され、三方向分級機の中径 粒子排出口より排出された中径粒子が本粉砕装置に導かれて微粉砕され、三方向 分級機の空気導入ダクト下部より排出された大径粒子は前記予備粉砕装置に戻さ れ、三方向分級機の微粉吸引口より排出された微粉は微粉捕集装置により回収さ れる。Further, in the crushing equipment using the three-way classifier according to claim 2 of the present invention, the preliminary crushed material roughly crushed by the preliminary crushing device is guided to the raw material chute of the three-way classifier. In the three-way classifier, fine particles, medium-sized particles, and large-sized particles are classified, and the medium-sized particles discharged from the medium-direction particle discharge port of the three-way classifier are guided to the crusher and finely crushed in three directions. The large-diameter particles discharged from the lower part of the air introduction duct of the classifier are returned to the preliminary crushing device, and the fine powder discharged from the fine powder suction port of the three-way classifier is collected by the fine powder collecting device.

【0011】[0011]

【実施例】【Example】

以下、本考案の実施例を図に基づいて説明する。 An embodiment of the present invention will be described below with reference to the drawings.

【0012】 図1は本考案の三方向分級機の一実施例の縦断面図であって、ケーシング1は 上部が円筒状で下部は縮径する漏斗状に作られており、ケーシング1の上端には 側方に延びる微粉吸引口2が設けてあって、この微粉吸引口2は、図示しない微 粉捕集機および吸引ファンに接続されていて、ケーシング1内の空気を吸引する ようになっている。またケーシング1の下端には、下部側方に延びる中径粒子排 出口3が設けてあって、図示しない中径粒子捕集機に接続されている。FIG. 1 is a vertical cross-sectional view of an embodiment of a three-way classifier of the present invention. The casing 1 is formed in a funnel shape with a cylindrical upper portion and a reduced diameter lower portion. A fine powder suction port 2 extending laterally is provided on the side, and the fine powder suction port 2 is connected to a fine powder collector and a suction fan (not shown) so as to suck the air in the casing 1. ing. Further, the lower end of the casing 1 is provided with a medium diameter particle discharge outlet 3 extending laterally downward and connected to a medium diameter particle collector (not shown).

【0013】 ケーシング1の上端中心を貫通して、筒状の原料投入シュート4がケーシング 1の内部に垂下しており、原料投入シュート4の下端は円筒状のままか、或いは 内面に絞り板又は誘導板5が取り付けられていても良い。また原料投入シュート 4の下端外面には、上方に向かって拡径する逆円錐形の整流板6が取り付けられ ている。A cylindrical raw material charging chute 4 is penetrating the center of the upper end of the casing 1 and hangs down inside the casing 1. The lower end of the raw material charging chute 4 remains cylindrical, or a diaphragm plate or The guide plate 5 may be attached. Further, on the outer surface of the lower end of the raw material charging chute 4, an inverted conical straightening plate 6 whose diameter is expanded upward is attached.

【0014】 原料投入シュート4の整流板6が取り付けられている箇所の上部外周には、中 空回転軸7が配設してあって、この中空回転軸7は軸受8によりケーシング1に 回転自在に支持され、上端の伝導プーリ9を介して図示しないモータで回転され るようになっている。そして中空回転軸7の下端には多数の回転分級羽根10が 放射状或いは放射方向に対して所要の角度で取り付けられていて、この回転分級 羽根10は、整流板6直上のケーシング1内上方位置にあって、中心側は微粉吸 引口2に連通している。A hollow rotary shaft 7 is disposed on the outer periphery of the upper portion of the raw material charging chute 4 where the flow straightening plate 6 is attached, and the hollow rotary shaft 7 is rotatable by the bearing 8 in the casing 1. And is rotated by a motor (not shown) via a transmission pulley 9 at the upper end. A large number of rotary classifying blades 10 are attached to the lower end of the hollow rotary shaft 7 radially or at a required angle with respect to the radial direction. The rotary classifying blades 10 are located above the straightening plate 6 in the casing 1. The center side communicates with the fine powder suction port 2.

【0015】 ケーシング1内下方位置の原料投入シュート4下端直下には、下部が逆円錐状 になっている分散板11が設けられており、またケーシング1の下端中心を貫通 して、筒状の空気導入ダクト12がケーシング1の内部に突設されている。空気 導入ダクト12の上端は、前述した分散板11下部の逆円錐状の形状に沿って拡 がる漏斗状に形成されており、この漏斗状部12’の上端と分散板11下部の逆 円錐状の部分との間には誘導羽根13が設けられていて、分散板11を支持する ようにされている。なお、誘導羽根13の代わりに、単なるサポート材を設けた 構造であってもよい。この空気導入ダクト12には、下端から空気14が吸引さ れるようになっていて、この空気14は分散板11の下部外周を通ってケーシン グ1内に吹き込まれるようになっている。Directly below the lower end of the raw material charging chute 4 inside the casing 1 is provided a dispersion plate 11 whose lower part has an inverted conical shape, and which penetrates the center of the lower end of the casing 1 to form a cylindrical shape. An air introduction duct 12 is provided so as to project inside the casing 1. The upper end of the air introduction duct 12 is formed in a funnel shape that expands along the above-mentioned inverted conical shape of the lower part of the dispersion plate 11, and the upper end of this funnel-shaped part 12 ′ and the inverted conical part of the lower part of the dispersion plate 11. A guide vane 13 is provided between the portion and the plate-shaped portion so as to support the dispersion plate 11. Note that, instead of the guide vanes 13, a simple support material may be provided. Air 14 is sucked into the air introduction duct 12 from the lower end, and the air 14 is blown into the casing 1 through the outer periphery of the lower portion of the dispersion plate 11.

【0016】 図1に示した実施例において、分散板11の上部は緩やかな円錐状になってい て、円錐の頂点が原料投入シュート4の中心軸線の延長上に位置した形状になっ ているが、分散板11の上部は仮想線で示すように水平の平面15になっていて もよく、或いは図2に示すように分散板11の上部は水平な所要の大きさの円板 17になっていて、該円板17の中心下部に設けた回転軸16を、分散板11内 に設けたモータ18或いはケーシング1外に設けたモータによって回転させるよ うになっていてもよい。In the embodiment shown in FIG. 1, the upper part of the dispersion plate 11 has a gentle conical shape, and the apex of the conical shape is located on the extension of the central axis of the raw material charging chute 4. The upper part of the dispersion plate 11 may be a horizontal plane 15 as shown by an imaginary line, or, as shown in FIG. 2, the upper part of the dispersion plate 11 is a horizontal disk 17 of a required size. The rotating shaft 16 provided at the lower center of the disc 17 may be rotated by a motor 18 provided inside the dispersion plate 11 or a motor provided outside the casing 1.

【0017】 次に、図1の装置の作用を説明する。Next, the operation of the apparatus shown in FIG. 1 will be described.

【0018】 空気導入ダクト12の下端から空気14を吹き込み、微粉吸引口2を外部の図 示しない吸引ファンで吸引し、中空回転軸7上端の伝導プーリ9を図示しないモ ータを介して回転し、回転分級羽根10を回転させた状態にする。空気導入ダク ト12から吹き込まれた空気14は分散板11下部の逆円錐状の形状に沿って拡 がりながら誘導羽根13またはサポート材の間を通ってケーシング1の内部上方 に拡散する上昇気流となった後、回転している回転分級羽根10の間を通って回 転分級羽根10の中心側に達し、微粉吸引口2から外部に吸引されるようになる 。Air 14 is blown from the lower end of the air introduction duct 12, the fine powder suction port 2 is sucked by an external suction fan (not shown), and the transmission pulley 9 at the upper end of the hollow rotary shaft 7 is rotated via a motor (not shown). Then, the rotary classification blade 10 is rotated. The air 14 blown from the air introduction duct 12 spreads along the inverted conical shape of the lower part of the dispersion plate 11 and passes between the guide vanes 13 or the support materials to diffuse upwardly into the casing 1. After that, it reaches the center side of the rotating classification blade 10 through the space between the rotating classification blades 10 and is sucked to the outside from the fine powder suction port 2.

【0019】 この状態で原料投入シュート4の上端から原料を所定量ずつ矢印19で示すよ うに供給すると、原料は原料投入シュート4内を通って分散板11の上部中心に 落下する。分散板11の上部が、図1に示すように緩やかな円錐状になっている 場合には、分散板11の上部中心に落下した原料は、緩やかな円錐に沿って分散 板11の周囲に均等に分散されて落下し、分散板11の上部が水平の平面15に なっている場合には、分散板11の上部中心に落下した原料は平面15の中心に 次第に円錐状に堆積した後、安息角以上に堆積すると次第に崩れ落ちて分散板1 1の周囲に均等に分散されて落下する。また図2に示すように回転する円板17 が取り付けられている場合には、原料は円板17の中心に落下し、円板17の回 転により周囲に飛ばされて分散板11の周囲から均等に分散されて落下する。In this state, when a predetermined amount of the raw material is supplied from the upper end of the raw material charging chute 4 as shown by an arrow 19, the raw material passes through the raw material charging chute 4 and falls to the center of the upper portion of the dispersion plate 11. When the upper part of the dispersion plate 11 has a gentle conical shape as shown in FIG. 1, the raw material dropped to the center of the upper part of the dispersion plate 11 is evenly distributed around the dispersion plate 11 along the gentle cone. When the upper part of the dispersion plate 11 is a horizontal flat surface 15, the raw material that has fallen to the center of the upper part of the dispersion plate 11 gradually accumulates in a conical shape at the center of the flat surface 15 and then rests. If it accumulates on the corners or more, it gradually collapses and is evenly dispersed around the dispersion plate 11 and falls. When the rotating disc 17 is attached as shown in FIG. 2, the raw material falls to the center of the disc 17 and is blown to the periphery by the rotation of the disc 17 from the periphery of the dispersion plate 11. It is evenly distributed and falls.

【0020】 分散板11の周囲から均等に分散されて落下する原料中の微粉および中径粒子 は、分散板11下部の逆円錐状の形状に沿って拡がりながら、誘導羽根13また はサポート材の間を通ってケーシング1の内部上方に拡散する上昇気流によって 吹上げられる。そして微粉Aは回転している回転分級羽根10の間を通って回転 分級羽根10の中心側に達し、微粉吸引口2から外部に吸引される。また中径粒 子Bは回転している回転分級羽根10に弾かれて微粉Aから分離され、ケーシン グ1の内周面に沿って落下した後、中径粒子排出口3から取り出される。The fine powder and medium-sized particles in the raw material, which are evenly dispersed and fall from the periphery of the dispersion plate 11, spread along the shape of an inverted cone at the bottom of the dispersion plate 11, and are dispersed in the guide blade 13 or the support material. It is blown up by the ascending air current that diffuses upward in the casing 1 through the gap. Then, the fine powder A passes between the rotating rotary classification blades 10, reaches the center side of the rotary classification blades 10, and is sucked to the outside from the fine powder suction port 2. The medium-sized particles B are repelled by the rotating rotary classification blade 10 to be separated from the fine powder A, fall along the inner peripheral surface of the casing 1, and then are taken out from the medium-sized particle discharge port 3.

【0021】 一方、分散板11の周囲から均等に分散されて落下する原料中の大径粒子Cは 、分散板11下部の逆円錐状の形状に沿ってケーシング1の内部上方に拡散する 上昇気流に吹上げられることなく空気導入ダクト12上端の漏斗状部12’に落 下し、ケーシング1内に吹き込まれる空気14の上昇流に逆らって空気導入ダク ト12の下端から外部に排出される。On the other hand, the large-diameter particles C in the raw material that are evenly dispersed and fall from the periphery of the dispersion plate 11 are diffused upward in the casing 1 along the shape of an inverted cone below the dispersion plate 11. Without being blown up, the air drops to the funnel-shaped portion 12 ′ at the upper end of the air introduction duct 12, and is discharged to the outside from the lower end of the air introduction duct 12 against the upward flow of the air 14 blown into the casing 1.

【0022】 従って上記実施例によれば、従来の篩式分級機の篩目のような磨耗の激しい部 分がない為、従来の篩式分級機と比較して補修、交換の頻度を著しく低減するこ とができ、しかも従来の篩式分級機より分級能力を大幅に向上することができる 。Therefore, according to the above-described embodiment, since there is no portion of the conventional sieve type classifier that is subject to severe wear like the sieve meshes, the frequency of repair and replacement is significantly reduced compared to the conventional sieve type classifier. In addition, it is possible to significantly improve the classification ability compared with the conventional sieve classifier.

【0023】 更に、一台で原料を微粉A、中径粒子B、大径粒子Cの三種類に精度良く、且 つ効率良く分級することができ、分級した粉体の粒径に応じた処理を必要とする 場合に極めて有効である。Furthermore, the raw material can be accurately and efficiently classified into three kinds of fine powder A, medium-sized particles B, and large-sized particles C by one unit, and the treatment depending on the particle size of the classified powder. It is extremely effective when you need

【0024】 図3は以上に述べた三方向分級機を用いた粉砕設備の一例を示すもので、クラ ッシャ或いはローラミル等の予備粉砕装置20と、横型のボールミル等の本粉砕 装置21とによって二段階の粉砕が行えるようにした粉砕設備23において、予 備粉砕装置20と本粉砕装置21との間の分級機として上述の三方向分級機を採 用したものである。FIG. 3 shows an example of the crushing equipment using the above-mentioned three-way classifier, which comprises a preliminary crushing device 20 such as a crusher or a roller mill and a main crushing device 21 such as a horizontal ball mill. In the crushing equipment 23 capable of performing stepwise crushing, the above-mentioned three-way classifier is used as a classifier between the preliminary crushing apparatus 20 and the main crushing apparatus 21.

【0025】 即ち、斯かる粉砕設備23では、前述した図1及び図2と同様に構成した三方 向分級機24が予備粉砕装置20と本粉砕装置21との間に設けられており、原 料ホッパ25からの原料26がコンベヤ27等を介して予備粉砕装置20に導入 されて粗粉砕され、該粗粉砕された予備粉砕物26’がバケットエレベータ28 等を介して前記三方向分級機24の原料投入シュート4に分級用原料として導か れるようにしてある。That is, in the crushing facility 23, a three-way classifier 24 having the same configuration as that of FIGS. 1 and 2 is provided between the preliminary crushing device 20 and the main crushing device 21, and The raw material 26 from the hopper 25 is introduced into the preliminary crushing device 20 via the conveyor 27 or the like and coarsely crushed, and the coarsely crushed preliminary crushed product 26 ′ of the three-way classifier 24 is passed through the bucket elevator 28 or the like. The material is fed to the raw material charging chute 4 as a raw material for classification.

【0026】 また、前記三方向分級機24の中径粒子排出口3より排出された中径粒子Bが 前記本粉砕装置21に導かれるようになっていると共に、前記三方向分級機24 の空気導入ダクト12下部より排出された大径粒子Cは、空気導入ダクト12下 端に空気導入室29を介して接続された大径粒子戻しシュート30により前記コ ンベヤ27に戻され、新たに供給される原料26と一緒に予備粉砕装置20に戻 されるようになっている。Further, the medium-sized particles B discharged from the medium-sized particle discharge port 3 of the three-way classifier 24 are introduced to the main crushing device 21, and the air of the three-way classifier 24 is discharged. The large-diameter particles C discharged from the lower part of the introduction duct 12 are returned to the conveyor 27 by the large-diameter particle return chute 30 connected to the lower end of the air introduction duct 12 through the air introduction chamber 29, and are newly supplied. The raw material 26 is returned to the preliminary crushing device 20.

【0027】 更に、前記三方向分級機24の微粉吸引口2には、微粉Aを吸引して回収する 微粉捕集装置31が接続されており、図示の例では前記微粉捕集装置31をバグ フィルタ32と吸引ファン33とにより構成している。Further, a fine powder collecting device 31 for sucking and collecting the fine powder A is connected to the fine powder suction port 2 of the three-way classifier 24. In the illustrated example, the fine powder collecting device 31 is a bag. It is composed of a filter 32 and a suction fan 33.

【0028】 また、前記三方向分級機24の中径粒子排出口3から本粉砕装置21に導かれ た中径粒子Bは、本粉砕装置21で微粉砕されて本粉砕物26”として排出され 、バケットエレベータ34等を介してエアセパレータ35に導かれて微粉Aと細 粉A’とに分級され、分級された細粉A’がエアスライド36を介して前記本粉 砕装置21に戻され、微粉Aはエアスライド37を介して製品として取り出され るようになっている。The medium-sized particles B introduced from the medium-sized particle discharge port 3 of the three-way classifier 24 to the main pulverizer 21 are finely pulverized by the main pulverizer 21 and discharged as the main pulverized product 26 ″. , Is guided to the air separator 35 through the bucket elevator 34, etc., and is classified into fine powder A and fine powder A ′, and the classified fine powder A ′ is returned to the main crushing device 21 via the air slide 36. The fine powder A is taken out as a product through the air slide 37.

【0029】 上記実施例によれば、予備粉砕装置20からの予備粉砕物26’(分級用原料 )を三方向分級機24により微粉A、中径粒子B、大径粒子Cに精度良く、且つ 効率良く分級することができるので、予備粉砕装置20に微粉A、中径粒子Bを 随伴させることなく大径粒子Cのみを戻し、本粉砕装置21には既に十分粉砕さ れている微粉Aを随伴させることなく中径粒子Bのみを戻すことができ、これに よって予備粉砕装置20および本粉砕装置21の粉砕効率を著しく向上させるこ とができる。According to the above-described embodiment, the preliminary crushed product 26 ′ (raw material for classification) from the preliminary crushing device 20 is accurately divided into the fine powder A, the medium particle B, and the large particle C by the three-way classifier 24, and Since the particles can be efficiently classified, only the large particles C are returned to the preliminary crushing device 20 without accompanying the fine powder A and the medium particles B, and the fine powder A which has already been sufficiently crushed is returned to the main crushing device 21. Only the medium-sized particles B can be returned without being entrained, whereby the grinding efficiency of the preliminary crushing device 20 and the main crushing device 21 can be significantly improved.

【0030】 また、予備粉砕装置20からの予備粉砕物26’(分級用原料)中に含まれる 微粉Aを直ちに捕集することができるので、バケットエレベータ34、エアスラ イド36,37等の設備内輸送機やエアセパレータ35等の設備内分級機に対す る負荷を大幅に軽減することができ、粉砕設備23全体の能力増大を図ることが できる。Further, since the fine powder A contained in the preliminary crushed product 26 ′ (raw material for classification) from the preliminary crushing device 20 can be immediately collected, the equipment such as the bucket elevator 34, the air slides 36, 37, etc. The load on the classifier inside the equipment such as the transport machine and the air separator 35 can be significantly reduced, and the capacity of the entire crushing equipment 23 can be increased.

【0031】 尚、本考案の三方向分級機及び該分級機を用いた粉砕設備は、上述の実施例に のみ限定されるものではなく、本考案の要旨を逸脱しない範囲内において種々変 更を加え得ることは勿論である。The three-way classifier of the present invention and the crushing equipment using the classifier are not limited to the above-mentioned examples, and various modifications can be made without departing from the scope of the present invention. Of course, it can be added.

【0032】[0032]

【考案の効果】[Effect of device]

上記した本考案の三方向分級機及び該分級機を用いた粉砕設備によれば、下記 の如き種々の優れた効果を奏し得る。 According to the three-way classifier of the present invention and the crushing equipment using the classifier described above, various excellent effects as described below can be obtained.

【0033】 (I) 請求項1に記載した三方向分級機においては、従来の篩式分級機と比 較して補修、交換の頻度を著しく低減することができ、しかも従来の篩式分級機 より分級能力を大幅に向上することができる。(I) In the three-way classifier according to claim 1, the frequency of repairs and replacements can be significantly reduced compared to the conventional sieve classifier, and the conventional sieve classifier is also available. The classification ability can be greatly improved.

【0034】 (II) 一台で原料を大径粒子、中径粒子、微粉の三種類に精度良く、且つ 効率良く分離することができるので、分級した粉体を粒径に応じた後処理を必要 とする場合に極めて有効である。(II) Since the raw material can be accurately and efficiently separated into three types of large-sized particles, medium-sized particles, and fine powder with one unit, post-treatment according to the particle size of the classified powder can be performed. It is extremely effective when needed.

【0035】 (III) ケーシングの上端に微粉吸引口と原料投入シュートとを備え、ケ ーシングの下端に中径粒子排出口と空気導入ダクトとを備えている為、ケーシン グの側方に突出するものがなく、小さなスペースに設置することができる。(III) Since the fine powder suction port and the raw material charging chute are provided at the upper end of the casing, and the medium diameter particle discharge port and the air introduction duct are provided at the lower end of the casing, they project to the side of the casing. It is empty and can be installed in a small space.

【0036】 (IV) 請求項2に記載した三方向分級機を用いた粉砕設備においては、予 備粉砕装置からの粉砕物(分級用原料)を三方向分級機により微粉、中径粒子、 大径粒子に精度良く、且つ効率良く分級することができるので、予備粉砕装置に 微粉、中径粒子を随伴させることなく大径粒子のみを戻し、本粉砕装置には既に 十分粉砕されている微粉を随伴させることなく中径粒子のみを戻すことができ、 これによって予備粉砕装置および本粉砕装置の粉砕効率を著しく向上させること ができる。(IV) In the crushing equipment using the three-way classifier according to claim 2, the crushed material (classification raw material) from the preliminary crusher is finely pulverized, medium-sized particles, and large-sized particles by the three-way classifier. Since it is possible to classify fine particles accurately and efficiently, only large particles are returned to the preliminary crushing device without accompanying fine particles and medium particles, and fine particles that have already been sufficiently crushed are returned to this crushing device. Only the medium-sized particles can be returned without being entrained, whereby the pulverization efficiency of the preliminary pulverizer and the main pulverizer can be significantly improved.

【0037】 (V) 予備粉砕装置からの粉砕物(分級用原料)中に含まれる微粉を直ちに 捕集することができるので、設備内輸送機や設備内分級機に対する負荷を大幅に 軽減することができ、粉砕設備全体の能力増大を図ることができる。(V) Since the fine powder contained in the pulverized material (raw material for classification) from the preliminary pulverizing device can be immediately collected, the load on the in-equipment transportation machine and the in-equipment classification machine can be significantly reduced. It is possible to increase the capacity of the entire crushing equipment.

【図面の簡単な説明】[Brief description of drawings]

【図1】本考案の請求項1に記載した三方向分級機の一
実施例を示す縦断面図である。
FIG. 1 is a vertical sectional view showing an embodiment of a three-way classifier according to claim 1 of the present invention.

【図2】図1の分散板の他の実施例の側面図である。FIG. 2 is a side view of another embodiment of the dispersion plate of FIG.

【図3】本考案の請求項2に記載した三方向分級機を用
いた粉砕設備の一実施例を示す概略図である。
FIG. 3 is a schematic view showing an embodiment of a crushing facility using the three-way classifier according to claim 2 of the present invention.

【符号の説明】[Explanation of symbols]

1 ケーシング 2 微粉吸引口 3 中径粒子排出口 4 原料投入シュート 10 回転分級羽根 11 分散板 12 空気導入ダクト 20 予備粉砕装置 21 本粉砕装置 23 粉砕設備 24 三方向分級機 26’ 予備粉砕物(分級用原料) 31 微粉捕集装置 A 微粉 B 中径粒子 C 大径粒子 1 casing 2 fine powder suction port 3 medium particle discharge port 4 raw material charging chute 10 rotating classifying blade 11 dispersion plate 12 air introduction duct 20 preliminary crushing device 21 main crushing device 23 crushing equipment 24 three-way classifier 26 'preliminary crushed product (classification) Raw material) 31 Fine powder collector A Fine powder B Medium particle C Large particle

Claims (2)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 上部に微粉吸引口を有し下部に中径粒子
排出口を有するケーシングと、該ケーシングの上端を貫
通し該ケーシングの内部に垂下された原料投入シュート
と、前記ケーシング内の上方位置で前記原料投入シュー
トの外周に設けられ中心側が前記微粉吸引口に連通され
た回転分級羽根と、前記ケーシング内の下方位置で前記
原料投入シュートの下端直下に設けられ下部が逆錐形状
に形成された分散板と、前記ケーシング下端を貫通し上
端が前記分散板の下部に沿って拡がる漏斗状に形成され
前記ケーシング内に空気を導入すると共に前記漏斗状部
上方で大径粒子と中径粒子を分離し大径粒子を排出する
空気導入ダクトとを備えたことを特徴とする三方向分級
機。
1. A casing having a fine powder suction port in the upper part and a medium particle discharge port in the lower part, a raw material charging chute penetrating the upper end of the casing and hanging inside the casing, and an upper part in the casing. A rotary classifying blade which is provided on the outer periphery of the raw material feeding chute at a position and communicates with the fine powder suction port on the center side, and a lower portion formed immediately below the lower end of the raw material feeding chute at a lower position inside the casing, and the lower portion is formed into an inverted pyramid shape. Dispersed plate, and the upper end is formed in a funnel shape that penetrates the lower end of the casing and extends along the lower part of the dispersion plate, and introduces air into the casing, and large-sized particles and medium-sized particles above the funnel-shaped portion. A three-way classifier, characterized in that it is provided with an air introducing duct for separating large particles and discharging large diameter particles.
【請求項2】 請求項1に記載の三方向分級機を、予備
粉砕装置と本粉砕装置との間に設け、前記予備粉砕機に
より粗粉砕された予備粉砕物を前記三方向分級機の原料
投入シュートに導き得るよう構成すると共に、前記三方
向分級機の中径粒子排出口より排出された中径粒子を前
記本粉砕装置に導き且つ前記三方向分級機の空気導入ダ
クトより排出された大径粒子を前記予備粉砕装置に戻し
得るよう構成し、更に前記三方向分級機の微粉吸引口に
は微粉を吸引して回収する微粉捕集装置を接続したこと
を特徴とする三方向分級機を用いた粉砕設備。
2. The three-way classifier according to claim 1 is provided between a preliminary crusher and a main crusher, and a preliminary crushed product roughly crushed by the preliminary crusher is used as a raw material for the three-way classifier. It is configured so that it can be guided to a charging chute, and the medium-sized particles discharged from the medium-sized particle discharge port of the three-way classifier are guided to the main pulverizer and discharged from the air introduction duct of the three-way classifier. A three-way classifier characterized in that it is configured to return the fine particles to the preliminary crushing device, and further a fine powder collecting device for sucking and collecting fine powder is connected to the fine powder suction port of the three-way classifier. The crushing equipment used.
JP5124993U 1993-02-09 1993-09-21 Three-way classifier and crushing equipment using the classifier Pending JPH0677864U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5124993U JPH0677864U (en) 1993-02-09 1993-09-21 Three-way classifier and crushing equipment using the classifier

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP901493 1993-02-09
JP5-9014 1993-02-09
JP5124993U JPH0677864U (en) 1993-02-09 1993-09-21 Three-way classifier and crushing equipment using the classifier

Publications (1)

Publication Number Publication Date
JPH0677864U true JPH0677864U (en) 1994-11-01

Family

ID=26343659

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5124993U Pending JPH0677864U (en) 1993-02-09 1993-09-21 Three-way classifier and crushing equipment using the classifier

Country Status (1)

Country Link
JP (1) JPH0677864U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007136299A (en) * 2005-11-16 2007-06-07 Ube Machinery Corporation Ltd Cement clinker grinding facility
KR101513054B1 (en) * 2014-11-12 2015-04-17 임상혁 Two stage vertical centrifugal classifier
CN110064592A (en) * 2019-03-31 2019-07-30 新郑市宝德高技术有限公司 A kind of corundum powder air-swirl classifying equipoment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007136299A (en) * 2005-11-16 2007-06-07 Ube Machinery Corporation Ltd Cement clinker grinding facility
KR101513054B1 (en) * 2014-11-12 2015-04-17 임상혁 Two stage vertical centrifugal classifier
CN110064592A (en) * 2019-03-31 2019-07-30 新郑市宝德高技术有限公司 A kind of corundum powder air-swirl classifying equipoment
CN110064592B (en) * 2019-03-31 2024-04-26 新郑市宝德高技术有限公司 Corundum micropowder air vortex classification equipment

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