JPH0556281U - Three-way classifier - Google Patents
Three-way classifierInfo
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- JPH0556281U JPH0556281U JP11363191U JP11363191U JPH0556281U JP H0556281 U JPH0556281 U JP H0556281U JP 11363191 U JP11363191 U JP 11363191U JP 11363191 U JP11363191 U JP 11363191U JP H0556281 U JPH0556281 U JP H0556281U
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Abstract
(57)【要約】
【目的】 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・小径粒子に精度
良く且つ効率良く分離することができ、分級した粉体の
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。
【構成】 原料投入シュート21から供給された原料2
0を原料分散器19により周囲に均等に分散して落下さ
せると、原料20中の中・小径粒子20b,20cは空
気導入部6から導入される空気5に吹き上げられてスリ
ットコーン18の開口部16からケーシング1内上部に
導かれて回転分級羽根14により更に分級され、小径粒
子20cは精粉吸引口2から、又、中径粒子20bは中
径粒子排出口17から取り出される。一方、空気5に乗
らない大径粒子20aは下方に落下して大径粒子排出口
3から取り出される。
(57) [Summary] [Purpose] Repairs and replacements are less frequent than conventional sieve classifiers, and the classifying capacity is higher than conventional sieve classifiers. (EN) Provided is an optimum three-way classifier which can separate particles and small-diameter particles accurately and efficiently and requires post-treatment according to the particle size of classified powder. [Structure] Raw material 2 supplied from raw material charging chute 21
When 0 is evenly dispersed and dropped by the raw material disperser 19 into the surroundings, the medium / small-diameter particles 20b and 20c in the raw material 20 are blown up by the air 5 introduced from the air introduction portion 6 to open the slit cone 18. The particles 16 are guided to the upper part of the casing 1 and further classified by the rotary classifying blade 14. The small-diameter particles 20c are taken out from the fine powder suction port 2, and the medium-sized particles 20b are taken out from the medium-sized particle discharge port 17. On the other hand, the large-diameter particles 20 a that do not get on the air 5 fall down and are taken out from the large-diameter particle discharge port 3.
Description
【0001】[0001]
本考案は、三方向分級機に関するものである。 The present invention relates to a three-way classifier.
【0002】[0002]
近年、セメント製造設備においてセメント原料を予備粉砕装置と本粉砕装置に より二段階に粉砕することにより粉砕効率を上げるようにした粉砕設備が考えら れている。 In recent years, a crushing facility has been considered in which cement raw materials are crushed in two stages by a preliminary crushing device and a main crushing device in a cement manufacturing facility to improve the crushing efficiency.
【0003】 即ち、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 粉砕機(予備粉砕装置)に導いて予備粉砕し、該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、該篩式分級機にて分離された篩上の大径粒子を前記予 備粉砕機に再び戻し、前記篩式分級機によって分離された篩下の中・小径粒子を 微粉細性能が優れた横型のボールミル(本粉砕装置)に導入して本粉砕を行うよ うにし、更に、前記ボールミルにて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前記ボールミルに再投入し、又、小径粒 子は精粉(製品)として取り出すようにしていた。That is, the cement raw material from the raw material hopper is guided to a preliminary crusher (preliminary crusher) such as a crusher or a roller mill for preliminary crushing, and the crushed crushed product is introduced to a sieve classifier for sieving. The large size particles on the sieve separated by the sieve classifier are returned to the preliminary crusher again, and the medium and small size particles under the sieve separated by the sieve classifier are excellent in fine pulverization performance. It is introduced into a horizontal ball mill (main crusher) to perform main crushing. Furthermore, the crushed product crushed by the ball mill is introduced into an air classifier and reclassified to a medium diameter where crushing is insufficient. The particles were reintroduced into the ball mill, and the small-diameter particles were taken out as refined powder (product).
【0004】[0004]
しかしながら、上記したような従来の粉砕設備では、予備粉砕機にて予備粉砕 した粉砕物を、単に篩式分級機により大径粒子と中・小径粒子とに分離するよう にしているが、前記篩式分級機では篩目の摩耗による補修、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 crusher is simply separated into large-sized particles and medium / small-sized particles by the sieve classifier. With a type classifier, repair and replacement due to abrasion of the sieve mesh are frequently required, and there is a problem that the classifying capacity has a mechanical limit.
【0005】 又、大径粒子に中・小径粒子が多量に付着混合したまま予備粉砕機に戻される 為に、予備粉砕機の粉砕効率が低下してしまう問題があり、更にボールミルに導 入される中・小径粒子には製品となるべき小径粒子が多量に含まれていることか ら前記ボールミルでは小径粒子を再び粉砕すること(過粉砕)になってボールミ ルの粉砕効率が著しく低下するといった問題を有していた。Further, since a large amount of medium- and small-sized particles adhere to the large-sized particles and are mixed and returned to the preliminary crusher, there is a problem that the pulverization efficiency of the preliminary crusher is lowered, and the particles are further introduced into the ball mill. Since small and medium-sized particles containing a large amount of small-sized particles to be products are included in the above-mentioned ball mill, the small-sized particles are crushed again (over-milling), resulting in a significant decrease in ball milling efficiency. Had a problem.
【0006】 又、既に稼働中のミル設備(ボールミルを含む粉砕設備)には、自ずと設備内 輸送機や、設備内分級機に制限能力があり、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、能力増大が 制限される問題を有していた。In addition, the mill equipment (crushing equipment including a ball mill) that is already in operation has a limited capacity for the in-equipment transportation machine and the in-equipment classifier, and the small-sized particles contained in the pre-milled pulverized material are However, there is a problem that the increase in capacity is limited because it must be handled within these limited capacities.
【0007】 本考案は上述の実情に鑑みてなしたもので、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・小径粒子に精度良く且つ効率良く分離することができ 、分級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 提供することを目的としている。The present invention has been made in view of the above-mentioned circumstances. It requires less repair and replacement than the conventional sieve type classifier, and has a higher classification capacity than the conventional sieve type classifier. A three-way classifier that can separate raw materials into large-sized particles, medium-sized particles, and small-sized particles with high precision and efficiency, and is suitable for post-treatment according to the particle size of the classified powder. It is intended to be provided.
【0008】[0008]
本考案は、上端に精粉吸引口を下端に大径粒子排出口を夫々有し且つ下部には 周方向から均等に空気を導入し得る空気導入部を備えたケーシングと、該ケーシ ング内部の上方位置に前記精粉吸引口を内側に連通せしめるよう配設された回転 分級羽根と、該回転分級羽根と前記空気導入部との間に前記ケーシング内部を上 下に区画するよう擂り鉢状に配設され周方向所要位置には外縁部を隆起させた開 口部を有し且つ下端には前記ケーシングを貫通する中径粒子排出口を有するスリ ットコーンと、該スリットコーンと前記空気導入部との間に配設され且つ上部を 錐状に形成した原料分散器と、該原料分散器の上方に前記ケーシングの外部より 原料を投入し得るよう該ケーシングを貫通する原料投入シュートとを備えたこと を特徴とする三方向分級機に係るものである。 The present invention has a casing having a fine powder suction port at the upper end and a large-diameter particle discharge port at the lower end, and an air inlet portion capable of uniformly introducing air from the circumferential direction at the lower portion, and a casing inside the casing. A rotary classifying blade arranged at the upper position so as to communicate the fine powder suction port with the inside, and a mortar shape so as to partition the inside of the casing between the rotary classifying blade and the air introduction section. A slit cone having an opening with a raised outer edge at a required circumferential position and a medium diameter particle discharge port penetrating the casing at the lower end, the slit cone and the air introduction part. And a raw material disperser having an upper part formed in a pyramid shape and a raw material feeding chute penetrating the casing so that raw material can be introduced from outside the casing above the raw material dispersing device. Characterized by three It relates to the direction classifier.
【0009】[0009]
従って本考案では、精粉吸引口を介し内部空気を吸引して空気導入管から空気 を導入し、且つ回転分級羽根を回転させた状態として、原料投入シュートから原 料を所定量ずつ供給すると、前記原料は錐状に形成された原料分散器上に落下し て周囲に均等に分散されて落下し、前記原料中の中・小径粒子は前記空気導入部 の周方向から均等に導入される空気に吹き上げられて前記スリットコーンの開口 部からケーシング内上部に導かれ、又、粒径の大きな大径粒子は前記空気に吹き 上げられることなく下方に落下して大径粒子排出口から取り出される。 Therefore, in the present invention, when the internal air is sucked through the fine powder suction port, the air is introduced from the air introduction tube, and the rotary classifying blade is rotated, when the raw material is supplied from the raw material chute in a predetermined amount, The raw material drops on a raw material disperser formed in a conical shape and is evenly dispersed and drops around the raw material, and medium- and small-sized particles in the raw material are uniformly introduced from the circumferential direction of the air introduction part. Is blown up to the inside of the casing through the opening of the slit cone, and large-diameter particles having a large particle diameter fall downward without being blown up by the air and are taken out from the large-diameter particle discharge port.
【0010】 一方、前記空気によりケーシング内上部に導入された中・小径粒子は、回転し ている回転分級羽根間を通過する際に小径粒子のみが通過され且つ中径粒子が前 記回転分級羽根に弾かれることにより分離され、前記回転分級羽根間を通過した 小径粒子は精粉吸引口を介して精粉(製品)として取り出され、又、前記回転分 級羽根にはじかれた中径粒子は遠心力により内側ケーシングの上部内周面及びス リットコーンの内周面に沿って落下し、中径粒子排出口から取り出される。On the other hand, as for the medium / small diameter particles introduced into the upper part of the casing by the air, only the small diameter particles are passed when passing between the rotating rotary classification blades, and the medium diameter particles are the aforementioned rotary classification blades. The small particles that were separated by being repelled by the rotating classifying blades and passed between the rotary classifying blades are taken out as fine powder (product) through the fine powder suction port, and the medium-sized particles repelled by the rotary classifying blades are The centrifugal force causes the particles to fall along the inner peripheral surface of the upper part of the inner casing and the inner peripheral surface of the slit cone, and is taken out from the medium diameter particle discharge port.
【0011】[0011]
以下本考案の実施例を図面を参照しつつ説明する。 Embodiments of the present invention will be described below with reference to the drawings.
【0012】 図1及び図2は本考案の三方向分級機の一実施例を示すもので、図中1は上端 に精粉吸引口2を有し且つ下端に大径粒子排出口3を備えたケーシングを示し、 該ケーシング1の下方向きに絞りこんだ下部には、周方向からルーバー4を介し て均等に空気5を導入し得る空気導入部6が設けられており、該空気導入部6に は空気導入管7が接続されている。1 and 2 show an embodiment of a three-way classifier of the present invention, in which 1 has a fine powder suction port 2 at the upper end and a large-diameter particle discharge port 3 at the lower end. In the lower part of the casing 1 which is squeezed downward, an air introducing portion 6 capable of uniformly introducing air 5 from the circumferential direction through the louver 4 is provided. An air introduction pipe 7 is connected to the.
【0013】 又、前記精粉吸引口2には、精粉捕集機8と吸引ファン9とからなる精粉捕集 装置10が接続されている。A fine powder collecting device 10 including a fine powder collector 8 and a suction fan 9 is connected to the fine powder suction port 2.
【0014】 更に、前記ケーシング1内部の上方位置には、回転駆動装置11にトルク伝達 可能に接続された駆動シャフト12及び取付板13により回転可能に支持された 多数の回転分級羽根14が、前記ケーシング1内周面に対し所要間隔を隔てて前 記精粉吸引口2を内側に連通せしめるよう配設されており、該回転分級羽根14 と前記空気導入部6との間には、ケーシング1内部を上下に区画するよう擂り鉢 状に形成され周方向所要位置に外縁部15を隆起させた開口部16を有し且つ下 端には前記ケーシング1を貫通する中径粒子排出口17を有するスリットコーン 18が配設されている。Further, a plurality of rotary classification blades 14 rotatably supported by a drive shaft 12 and a mounting plate 13 which are connected to a rotary drive device 11 so as to transmit torque, are provided at an upper position inside the casing 1. The fine powder suction port 2 is disposed so as to communicate with the inner peripheral surface of the casing 1 at a required interval, and the casing 1 is provided between the rotary classification blade 14 and the air introduction portion 6. It has a mortar-like shape that divides the interior into upper and lower parts, and has an opening 16 in which a peripheral edge 15 is raised at a required position in the circumferential direction, and has a medium diameter particle discharge port 17 that penetrates the casing 1 at the lower end. A slit cone 18 is provided.
【0015】 又、前記スリットコーン18と前記空気導入部6との間には、上部を円錐状に 形成した原料分散器19が配設されており、該原料分散器19の直上に原料20 を投入し得るよう前記ケーシング1を貫通して原料投入シュート21がケーシン グ1内部に挿入されている。A raw material disperser 19 having an upper conical shape is disposed between the slit cone 18 and the air introducing portion 6, and the raw material 20 is placed directly above the raw material disperser 19. A raw material charging chute 21 is inserted into the casing 1 so as to penetrate the casing 1 so as to be charged.
【0016】 ここで、前記原料投入シュート21は、前記スリットコーン18に沿って配置 され、隣あった開口部16の間のコーン底板を天板として構成されている。Here, the raw material charging chute 21 is arranged along the slit cone 18, and the cone bottom plate between the adjacent openings 16 is configured as a top plate.
【0017】 尚、20aは前記原料20中の大径粒子、20bは前記原料20中の中径粒子 、20cは前記原料20中の小径粒子、22は前記大径粒子排出口3の切出しダ ンパ、23は前記中径粒子排出口17の切出しダンパを示す。In addition, 20 a is a large particle in the raw material 20, 20 b is a medium particle in the raw material 20, 20 c is a small particle in the raw material 20, 22 is a cut-out damper of the large particle discharge port 3. Reference numerals 23 and 23 denote cut-out dampers of the medium-diameter particle discharge port 17.
【0018】 而して、精粉捕集装置10の吸引ファン9を駆動することにより精粉吸引口2 を介し内部空気を吸引して空気導入管7から空気5を導入し、且つ回転分級羽根 14を回転させた状態として、原料投入シュート21から原料20を所定量ずつ 供給すると、前記原料20は円錐状に形成された原料分散器19上に落下して周 囲に均等に分散されて落下し、前記原料20中の中・小径粒子20b,20cは 前記空気導入部6の周方向から均等に導入される空気5に吹き上げられて前記ス リットコーン18の開口部16からケーシング1内上部に導かれ、又、粒径の大 きな大径粒子20aは前記空気5に吹き上げられることなく下方に落下して大径 粒子排出口3から取り出される。Then, by driving the suction fan 9 of the fine powder collecting device 10, the internal air is sucked through the fine powder suction port 2 to introduce the air 5 from the air introduction pipe 7, and the rotary classification blade. When the raw material charging chute 21 supplies a predetermined amount of the raw material 20 in a state in which 14 is rotated, the raw material 20 is dropped onto the conical raw material disperser 19 and evenly dispersed around the circumference. However, the medium- and small-sized particles 20b, 20c in the raw material 20 are blown up by the air 5 that is evenly introduced from the circumferential direction of the air introduction part 6 and flow from the opening 16 of the slit cone 18 to the upper part inside the casing 1. The large particles 20 a having a large particle diameter are guided to the air 5 and fall downward without being blown up by the air 5 to be taken out from the large particle discharge port 3.
【0019】 一方、前記空気5によりケーシング1内上部に導入された中・小径粒子20b ,20cは、回転している回転分級羽根14間を通過する際に小径粒子20cの みが通過され且つ中径粒子20bが前記回転分級羽根14に弾かれることにより 分離され、前記回転分級羽根14間を通過した小径粒子20cは精粉吸引口2を 介して精粉捕集装置10の精粉捕集機8に回収されて精粉(製品)として取り出 され、又、前記回転分級羽根14にはじかれた中径粒子20bは遠心力によりケ ーシング1の上部内周面及びスリットコーン18の内周面に沿って落下し、中径 粒子排出口17から取り出される。この際、前記スリットコーン18の内周面に 沿って落下する中径粒子20bは、開口部16の隆起した外縁部15に阻まれる ことにより前記開口部16から落下することなく中径粒子排出口17に導かれる 。On the other hand, the medium / small diameter particles 20b, 20c introduced into the upper part of the casing 1 by the air 5 pass through only the small diameter particles 20c when passing between the rotating rotary classification blades 14 and The small-sized particles 20b are separated by being repelled by the rotary classification blades 14, and the small-sized particles 20c that have passed between the rotary classification blades 14 pass through the fine-particle suction port 2 and the fine-particle collecting device 10 has a fine-particle collecting device. 8 is collected as fine powder (product), and the medium-sized particles 20b repelled by the rotary classification blade 14 are subjected to centrifugal force on the upper inner peripheral surface of the casing 1 and the inner peripheral surface of the slit cone 18. And is taken out from the medium-sized particle discharge port 17. At this time, the medium-sized particles 20b falling along the inner peripheral surface of the slit cone 18 are blocked by the raised outer edge portion 15 of the opening 16 so that the medium-sized particles 20b do not fall from the opening 16 and the medium-sized particle discharge port. Guided to 17.
【0020】 従って上記実施例によれば、従来の篩式分級機の篩目ような摩耗の激しい部分 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。 更に、一台で原料20を大径粒子20a・中径粒子20b・小径粒子20cに 精度良く且つ効率良く分離することができ、分級した粉体の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。Therefore, according to the above-mentioned embodiment, since there is no part of the conventional sieve type classifier that is subject to severe wear like the sieve mesh, the frequency of repairs and replacements can be significantly reduced compared to the conventional sieve type classifier. In addition, the classification ability can be significantly improved as compared with the conventional sieve type classifier. Further, when the raw material 20 can be accurately and efficiently separated into the large particle 20a, the medium particle 20b, and the small particle 20c by one unit, and the post-treatment corresponding to the particle size of the classified powder is required. It is extremely effective for
【0021】 例えば、クラッシャ或いはローラミル等の予備粉砕機(予備粉砕装置)と横型 のボールミル(本粉砕装置)とにより二段階の粉砕が行えるようにした粉砕設備 において、本実施例の三方向分級機を前記予備粉砕機とボールミルとの間の分級 機として採用した場合には、予備粉砕機からの粉砕物(原料)を大径粒子20a ・中径粒子20b・小径粒子20cに精度良く且つ効率良く分離することができ るので、予備粉砕機に中・小径粒子20b,20cを随伴させることなく大径粒 子20aのみを戻し且つボールミルには既に十分粉砕された小径粒子20cを随 伴させることなく中径粒子20bのみを戻すことができ、依って予備粉砕機及び ボールミルの粉砕効率を著しく向上することができる。For example, in a crushing facility in which a preliminary crusher such as a crusher or a roller mill (preliminary crushing device) and a horizontal ball mill (main crushing device) can perform two-stage crushing, the three-way classifier of this embodiment is used. When is used as a classifier between the preliminary crusher and the ball mill, the crushed material (raw material) from the preliminary crusher is accurately and efficiently converted into large particles 20a, medium particles 20b, and small particles 20c. Since they can be separated, only the large particles 20a are returned to the preliminary crusher without accompanying the medium and small particles 20b and 20c, and the ball mill is not accompanied with the already sufficiently small particles 20c. Only the medium-sized particles 20b can be returned, so that the crushing efficiency of the preliminary crusher and the ball mill can be significantly improved.
【0022】 又、予備粉砕機からの粉砕物(原料)中に含まれる小径粒子20c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。Further, since the small-sized particles 20c contained in the pulverized material (raw material) from the preliminary pulverizer can be immediately collected, the load on the in-equipment transportation machine and the in-equipment classifier can be significantly reduced. It is possible to increase the capacity of the entire crushing equipment.
【0023】[0023]
上記した本考案の三方向分級機によれば、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、更に、一台で原料を大径粒子・中径粒子・小径粒 子に精度良く且つ効率良く分離することができ、分級した粉体の粒径に応じた後 処理を必要とする場合に極めて有効である等の種々の優れた効果を奏し得る。 According to the above-described three-way classifier of the present invention, the frequency of repairs and replacements can be significantly reduced as compared with the conventional sieve classifier, and the classification ability is greatly improved over the conventional sieve classifier. In addition, the raw material can be separated into large-sized particles, medium-sized particles, and small-sized particles accurately and efficiently with one unit, and post-treatment according to the particle size of the classified powder is required. In this case, various excellent effects such as being extremely effective can be obtained.
【図面の簡単な説明】[Brief description of drawings]
【図1】本考案の一実施例を示す断面図である。FIG. 1 is a sectional view showing an embodiment of the present invention.
【図2】図1のII−II方向の矢視図である。FIG. 2 is a view taken along line II-II in FIG.
1 ケーシング 2 精粉吸引口 3 大径粒子排出口 5 空気 6 空気導入部 14 回転分級羽根 15 外縁部 16 開口部 17 中径粒子排出口 18 スリットコーン 19 原料分散器 20 原料 21 原料投入シュート DESCRIPTION OF SYMBOLS 1 Casing 2 Fine powder suction port 3 Large particle discharge port 5 Air 6 Air introduction part 14 Rotating classification blade 15 Outer edge 16 Opening 17 Medium diameter particle discharge port 18 Slit cone 19 Raw material disperser 20 Raw material 21 Raw material input chute
Claims (1)
口を夫々有し且つ下部には周方向から均等に空気を導入
し得る空気導入部を備えたケーシングと、該ケーシング
内部の上方位置に前記精粉吸引口を内側に連通せしめる
よう配設された回転分級羽根と、該回転分級羽根と前記
空気導入部との間に前記ケーシング内部を上下に区画す
るよう擂り鉢状に配設され周方向所要位置には外縁部を
隆起させた開口部を有し且つ下端には前記ケーシングを
貫通する中径粒子排出口を有するスリットコーンと、該
スリットコーンと前記空気導入部との間に配設され且つ
上部を錐状に形成した原料分散器と、該原料分散器の上
方に前記ケーシングの外部より原料を投入し得るよう該
ケーシングを貫通する原料投入シュートとを備えたこと
を特徴とする三方向分級機。1. A casing having a fine powder suction port at an upper end and a large-diameter particle discharge port at a lower end, and an air introduction part capable of uniformly introducing air from a circumferential direction at a lower part, and a casing inside the casing. A rotary classifying blade arranged to communicate the inside of the fine powder suction port at an upper position, and a mortar-like arrangement so as to vertically divide the inside of the casing between the rotary classifying blade and the air introducing section. Between the slit cone and the air introducing portion, which is provided at a predetermined position in the circumferential direction, has an opening portion in which the outer edge portion is raised, and has a medium diameter particle discharge port penetrating the casing at the lower end. And a raw material disperser having an upper part formed in a pyramid shape and a raw material feeding chute that penetrates through the casing so that the raw material can be introduced from outside the casing above the raw material dispersing device. And three directions Classifier.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11363191U JP2545322Y2 (en) | 1991-12-28 | 1991-12-28 | Three-way classifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11363191U JP2545322Y2 (en) | 1991-12-28 | 1991-12-28 | Three-way classifier |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0556281U true JPH0556281U (en) | 1993-07-27 |
JP2545322Y2 JP2545322Y2 (en) | 1997-08-25 |
Family
ID=14617132
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11363191U Expired - Lifetime JP2545322Y2 (en) | 1991-12-28 | 1991-12-28 | Three-way classifier |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2545322Y2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101695000B1 (en) * | 2015-11-30 | 2017-01-10 | 주식회사 태산플랜트 | Distributing apparatus for powder type raw material or fuel |
-
1991
- 1991-12-28 JP JP11363191U patent/JP2545322Y2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JP2545322Y2 (en) | 1997-08-25 |
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