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JPH0128826Y2 - - Google Patents

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Publication number
JPH0128826Y2
JPH0128826Y2 JP6902684U JP6902684U JPH0128826Y2 JP H0128826 Y2 JPH0128826 Y2 JP H0128826Y2 JP 6902684 U JP6902684 U JP 6902684U JP 6902684 U JP6902684 U JP 6902684U JP H0128826 Y2 JPH0128826 Y2 JP H0128826Y2
Authority
JP
Japan
Prior art keywords
round table
granular material
roller
distributor
crushing device
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP6902684U
Other languages
Japanese (ja)
Other versions
JPS60183038U (en
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to JP6902684U priority Critical patent/JPS60183038U/en
Publication of JPS60183038U publication Critical patent/JPS60183038U/en
Application granted granted Critical
Publication of JPH0128826Y2 publication Critical patent/JPH0128826Y2/ja
Granted legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Description

【考案の詳細な説明】 本案は回転する円卓と同円卓の外周部上で回転
する複数個のローラ状部材とにより、同円卓上に
供給された粒状物を粉砕する粒状物粉砕装置の供
給シユートの改良に関するものである。
[Detailed description of the invention] This invention is a supply chute for a granular material crushing device that uses a rotating round table and a plurality of roller-like members rotating on the outer periphery of the round table to crush granular materials supplied to the round table. This is related to the improvement of.

本件出願人がすでに提案したの粒状物粉砕装置
を第6,7,8図により説明すると、1が駆動装
置、2が同駆動装置1により水平面内回転する円
卓で、その上方には粉砕乾燥室3が上方に向い拡
開するように設けられ、粒塊状物を同乾燥室3へ
供給するシユート4が外部から同乾燥室3内に突
出するよう設けられている。また乾燥室3のミル
ケーシンダ6を貫通する軸7には、円卓2上に供
給された粒塊状物質を円卓2に押し付けて同円卓
2とともに回転する数個のローラ(またはボー
ル)5が支持されている。また円卓2とケーシン
グ6との間には、通風及び粗粒の落下を行なう環
状の開口部8が設けられ、同開口部8直下には、
排出路9が設けられ、上記開口部8の周りには、
同開口部8にガスを供給するための熱風室10が
設けられている。また粉砕乾燥室3の上方には、
円卓2と同心のモータ(図示しない)により回転
される回転翼11、並びに微粉含有ガス排出口1
2を具えた空気分級機13が設けられている。ま
たこの他に前記破砕物の排出路9に繋がる機械式
コンベア14と排出された粗粒を前記供給シユー
ト4に輸送するバケツトエレベータ15とが付設
されている。
The granular material crushing device already proposed by the present applicant will be explained with reference to FIGS. 6, 7, and 8. 1 is a drive device, 2 is a round table that is rotated in a horizontal plane by the drive device 1, and above the table is a pulverization drying chamber. A chute 4 for supplying granular material to the drying chamber 3 is provided so as to protrude into the drying chamber 3 from the outside. In addition, several rollers (or balls) 5 are supported on a shaft 7 passing through the milk case cinder 6 of the drying chamber 3, which presses the granular material supplied onto the round table 2 onto the round table 2 and rotates with the round table 2. There is. Further, an annular opening 8 is provided between the round table 2 and the casing 6 for ventilation and for coarse particles to fall, and directly below the opening 8,
A discharge passage 9 is provided, and around the opening 8,
A hot air chamber 10 for supplying gas to the opening 8 is provided. Moreover, above the grinding drying chamber 3,
A rotary blade 11 rotated by a motor (not shown) concentric with the round table 2, and a fine powder-containing gas outlet 1
An air classifier 13 comprising 2 is provided. In addition, a mechanical conveyor 14 connected to the crushed material discharge path 9 and a bucket elevator 15 for transporting the discharged coarse particles to the supply chute 4 are provided.

次に前記粒状物粉砕装置の作用をセメント原料
の粉砕に例をとり説明すると、焼成装置サスペン
シヨンプレヒータ(図示しない)の排出ガスは、
誘引フアン(図示しない)により熱風室10→開
口部8を通つて粉砕乾燥室3に噴出し、円卓2の
回転によつて生じた遠心力により、開口部8に移
動してきた粒塊状物のうち、比較的細かい粒子の
みを上方へ吹き飛ばし、それを同伴して空気分級
機13まで導く。このとき、同分級機13では回
転翼11が回転して、旋回流が形成されており、
粗粉を分離して、微粉を含むガスを頂部中心の微
粉含有ガス排出口12からミル外へ排出する。一
方、粒塊状物供給シユート4より円卓2上へ供給
された粒塊状物は、同円卓2の回転によつて生ず
る遠心力により円卓2の外周部へ移動し、ここに
設けられたローラ5の下方への押し付け力によ
り、前記円卓2との間に挾まれて、圧潰粉砕され
る。なお熱風は、乾燥に必要な程度とし、また開
口部8での上昇風速は、10〜25m/sに設定され
ているので、開口部8まで移動してきた破砕物の
うち、比較的細かい粒子、ガス噴流により吹き飛
ばされ、その一部は、空気分級機13へ導かれ、
残りは、円卓2上へ吹き戻される。また開口部8
で吹き飛ばされなかつた比較的粗い粒子は、開口
部8より破砕物排出路9を通つて機械式コンベア
14上に落下し、同機械式コンベア14及びバケ
ツトエレベータ15を介して供給シユート4へ導
かれる。また空気分級機13まで導かれた粉体
は、回転翼11により叩かれ、遠心力を与えられ
て、粗粉は周壁方向に飛ばされ、次いで壁面に沿
い落下して、円卓2上に戻される。一方、回転翼
11をすり抜けた微粉は、上方の微粉含有ガス排
出口12から排出され、捕集器(図示しない)で
製品として捕集されるようになつている。
Next, to explain the operation of the granular material crushing device using the example of crushing cement raw materials, the exhaust gas from the suspension preheater (not shown) of the firing device is as follows.
Among the granules, which are ejected from the hot air chamber 10 through the opening 8 into the crushing drying chamber 3 by an induction fan (not shown), and moved to the opening 8 by the centrifugal force generated by the rotation of the round table 2, , only relatively fine particles are blown upward and guided to the air classifier 13 along with them. At this time, the rotor blades 11 of the classifier 13 rotate to form a swirling flow.
The coarse powder is separated and the gas containing the fine powder is discharged to the outside of the mill from the fine powder-containing gas outlet 12 located at the center of the top. On the other hand, the granular material supplied from the granular material supply chute 4 onto the round table 2 is moved to the outer periphery of the round table 2 by the centrifugal force generated by the rotation of the round table 2, and is moved to the outer periphery of the round table 2 by the roller 5 provided here. Due to the downward pressing force, it is caught between the round table 2 and crushed and crushed. Note that the amount of hot air is limited to the level necessary for drying, and the rising wind speed at the opening 8 is set to 10 to 25 m/s, so that among the crushed materials that have moved to the opening 8, relatively fine particles, It is blown away by the gas jet, and a part of it is guided to the air classifier 13,
The rest is blown back onto Round Table 2. Also, the opening 8
The relatively coarse particles that were not blown away fall from the opening 8 through the crushed material discharge path 9 onto the mechanical conveyor 14 and are led to the supply chute 4 via the mechanical conveyor 14 and bucket elevator 15. It will be destroyed. Further, the powder guided to the air classifier 13 is beaten by the rotary blade 11 and centrifugal force is applied to it, causing the coarse powder to be blown toward the surrounding wall, then fall along the wall surface, and returned to the round table 2. . On the other hand, the fine powder that has passed through the rotary blade 11 is discharged from the upper fine powder-containing gas outlet 12 and collected as a product by a collector (not shown).

前記粒状物粉砕装置では、粒塊状物が第8図に
示すシユート4の幅a〜bで矢印22方向に回転
する円卓2上に落ち、その後は回転する円卓2か
ら遠心力を受けて、矢印21方向に移動しながら
幅a′〜b′に拡散していたので、その途中では、粒
塊状物が3つのローラ5のうち、2つのローラ5
と回転する円卓2との間でしか圧潰粉砕されてい
なくて、各ローラ5の負荷が不均等になり、各ロ
ーラ5に不均等な摩耗が生ずる。また上記のよう
に各ローラ5の負荷が不均等になるので、振動の
発生、粉砕効率の低下等を生じていた。なお第8
図の点線矢印は、円卓2外周のガス噴流により円
卓2上へ吹き戻される粒状物を示している。
In the granular material crushing device, the granular material falls onto the round table 2 rotating in the direction of the arrow 22 with the width a to b of the chute 4 shown in FIG. 21 direction while spreading across widths a' to b'.
Since the material is crushed and crushed only between the rollers 5 and the rotating round table 2, the load on each roller 5 becomes uneven, causing uneven wear on each roller 5. Furthermore, as mentioned above, the load on each roller 5 becomes uneven, which causes vibrations and a decrease in grinding efficiency. Furthermore, the 8th
The dotted arrows in the figure indicate particulate matter blown back onto the round table 2 by the gas jet around the outer periphery of the round table 2.

また図示を省略したが粒状物粉砕装置の他の従
来例としては、供給シユートを円卓の中心上方に
延長するとともに同供給シユートの下端を鉛直方
向下方に開口して、粒塊状物を円卓の中心上に落
下させるものもある。この場合、供給シユートか
ら円卓上に落下した粒塊状物は、円卓上を全外周
に向い均一に分散移動するので、各ローラの負荷
が均一になるが、第8図から明らかなようにロー
ラ(圧下部)の円卓上に占める割合は比較的小さ
く、大半の粒塊状物はローラに噛込まれることな
くローラ部を通過して、円卓外周部から溢流す
る。そのため、前記第6,7図に示す粒状物粉砕
装置と同様に粉砕効率の低下を生じていた。また
円卓の外周部から溢流する粒塊状物が多いので、
コンベア動力を増大させていた。
Although not shown, in another conventional example of a granular material crushing device, the supply chute is extended above the center of the round table, and the lower end of the supply chute is opened vertically downward, so that the granular material is transported to the center of the round table. There are also things that can be dropped upwards. In this case, the granules that have fallen from the supply chute onto the round table are evenly dispersed and moved toward the entire outer circumference of the round table, so the load on each roller becomes uniform, but as is clear from FIG. The ratio of the rolling part (rolling part) to the round table top is relatively small, and most of the granules pass through the roller part without being bitten by the rollers and overflow from the outer periphery of the round table. As a result, the pulverizing efficiency was reduced as in the granular material pulverizing apparatus shown in FIGS. 6 and 7. Also, since there are many granular materials overflowing from the outer periphery of the round table,
Conveyor power was increased.

本案は前記の問題点に対処するもので、回転す
る円卓と同円卓の外周部上で回転する複数個のロ
ーラ状部材とにより、同円卓上に供給された粒状
物を粉砕する粒状物粉砕装置において、前記円卓
の中心上方へ粒状物を導く供給シユートの下部に
有底の分配器を設けるとともに同分配器の側部に
複数個の粒状物供給口を前記各ローラ状部材に対
応して設けたことを特徴とする粒状物粉砕装置に
係り、その目的とする処は、各ローラ状部材の負
荷を均等にできて、各ローラ状部材の不均一な摩
耗を防止できる。また各ローラ状部材を経ずに通
過してしまう粒塊状物の量を少なくできて、粉砕
効率を向上できる改良された粒状物粉砕装置の供
給シユートを供する点にある。
This proposal addresses the above-mentioned problems, and is a granular material crushing device that uses a rotating round table and a plurality of roller-like members that rotate on the outer periphery of the round table to crush granular materials supplied to the round table. A bottomed distributor is provided at the bottom of the supply chute that guides the granular material above the center of the round table, and a plurality of granular material supply ports are provided on the side of the distributor corresponding to each of the roller-like members. The purpose of the granular material crushing device is to equalize the load on each roller-shaped member and prevent uneven wear of each roller-shaped member. Another object of the present invention is to provide an improved supply chute for a granular material crushing device that can reduce the amount of granular materials that pass through without passing through each roller-like member and improve the pulverizing efficiency.

次に本案の粒状物粉砕装置の供給シユートを第
1,2,5図に示す一実施例により説明すると、
2が回転する円卓、4は同円卓2の中心上方へ延
びた供給シユート、5は本実施例の場合3個のロ
ーラ(またはボール)、40が上記供給シユート
4の下部に設けられた円筒状の分配器、41が同
分配器40の底部を閉じる底蓋、42が同分配器
40の側部に設けられた粒状物供給口で、本実施
例の場合、同粒状物供給口42が3個あり、それ
ぞれが前記各ローラ5に対応している。なお、上
記底蓋41は円卓2の中心直上に位置している。
その他の構成は前記第6,7図と同様である。
Next, the supply chute of the granular material crushing device of the present invention will be explained with reference to an embodiment shown in FIGS. 1, 2, and 5.
2 is a rotating round table, 4 is a supply chute extending above the center of the round table 2, 5 is three rollers (or balls) in this embodiment, and 40 is a cylindrical shape provided at the bottom of the supply chute 4. 41 is a bottom cover that closes the bottom of the distributor 40, 42 is a granular material supply port provided on the side of the distributor 40, and in the case of this embodiment, the granular material supply port 42 is 3 There are two rollers, each corresponding to each roller 5. Note that the bottom cover 41 is located directly above the center of the round table 2.
The other configurations are the same as those shown in FIGS. 6 and 7 above.

次に前記粒状物粉砕装置の供給シユートの作用
を説明する。シユート4を通つて分配器40に入
つた粒塊状物は、底蓋41上へ落下し、さらに粒
状物供給口42から円卓2上へ排出される。同供
給口42は、分配器40の側壁に各ローラ5に対
応して設けられており、同各供給口42から円卓
2上へ排出された粒塊状物は、第5図の矢印23
のように集束した状態で各ローラ5に向うことに
なる。つまり各供給口42の開口幅及び円周方向
位置は、第5図に示すように、粒塊状物が円卓2
上を移動するときの彎曲した軌跡を考慮して設定
されており、粒塊状物は各ローラ5の圧下部30
へ導かれる。また各供給口42の開口面積は、分
配器40内で粒塊状物が閉塞しないように設定さ
れている。また分配器40の下端は、円卓2の上
面に近接しており、各供給口42から円卓2への
粒塊状物の落下時の衝撃による飛散をできるだけ
少くしている。但し分配器40は円卓2と分配器
40との間に粒塊状物が噛込まれて機器が破損す
ることのない高さに保持されている。以上の第
1,2図では、分配器40が円筒状であるが、第
3,4図では、分配器40の下部ををコーン状と
し、そこに設けた各供給口42を傾斜させてお
り、粒塊状物の分配器40から円卓2への排出が
さらに容易になる。
Next, the operation of the supply chute of the granular material crushing device will be explained. The granular material that has entered the distributor 40 through the chute 4 falls onto the bottom cover 41 and is further discharged onto the round table 2 from the granular material supply port 42 . The supply ports 42 are provided on the side wall of the distributor 40 in correspondence with the respective rollers 5, and the granular material discharged onto the round table 2 from the respective supply ports 42 is directed to the arrow 2 in FIG.
It heads toward each roller 5 in a converged state as shown in FIG. In other words, the opening width and the circumferential position of each supply port 42 are such that the granular material can reach the round table 2 as shown in FIG.
It is set in consideration of the curved trajectory when moving on the top, and the granular material is placed in the rolling part 30 of each roller 5.
be led to. Further, the opening area of each supply port 42 is set so that the particulate matter does not block the inside of the distributor 40. Further, the lower end of the distributor 40 is close to the upper surface of the round table 2 to minimize scattering due to impact when the granules fall from each supply port 42 to the round table 2. However, the distributor 40 is maintained at a height that prevents particles from getting caught between the round table 2 and the distributor 40 and damaging the device. In Figures 1 and 2 above, the distributor 40 has a cylindrical shape, but in Figures 3 and 4, the lower part of the distributor 40 is shaped like a cone, and each supply port 42 provided therein is inclined. , the discharge of the agglomerates from the distributor 40 to the round table 2 becomes easier.

本案の粒状物粉砕装置の供給シユートは前記の
ように構成されており、円卓上へ供給される粒塊
状物は各ローラ状部材へ均等に、かつ、集束した
状態で供給されて、噛込まれるので、各ローラ状
部材の負荷を均等にできて、ローラ状部材の不均
一な摩耗を防止できる。また上記のように構成さ
れており、各ローラ状部材を経ずに通過してしま
う粒塊状物の量を少なくできて、粉砕効率を向上
できる効果があり、天然鉱石、人工鉱石等の粉砕
用ローラミル、ボールレスミル等に適用して有益
である。
The supply chute of the granular material crushing device of the present invention is configured as described above, and the granular material supplied to the round table is supplied to each roller-shaped member evenly and in a focused state, and is bitten. Therefore, the load on each roller-shaped member can be made equal, and uneven wear of the roller-shaped members can be prevented. In addition, with the structure described above, it is possible to reduce the amount of granular material that passes through each roller member without passing through, thereby improving the crushing efficiency. It is useful for application to roller mills, ballless mills, etc.

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

第1図は本案に係る粒状物粉砕装置の供給シユ
ートの一実施例を示す側面図、第2図は第1図の
矢視−線に沿う横断平面図、第3図は他の実
施例を示す側面図、第4図は第3図矢視−線
に沿う横断平面図、第5図はその作用説明図、第
6図は従来の粒状物粉砕装置の第7図の矢視−
線に沿う平面図、第7図はその側面図、第8図
はその作用説明図である。 2……円卓、4……供給シユート、5……ロー
ラ状部材、40……分配器、41……その底蓋、
42……粒状物供給口。
Fig. 1 is a side view showing one embodiment of the supply chute of the granular material crushing device according to the present invention, Fig. 2 is a cross-sectional plan view taken along the arrow line in Fig. 1, and Fig. 3 shows another embodiment. FIG. 4 is a cross-sectional plan view taken along the arrow line in FIG. 3, FIG. 5 is an explanatory diagram of its operation, and FIG.
FIG. 7 is a plan view taken along the line, FIG. 7 is a side view thereof, and FIG. 8 is an explanatory diagram of its operation. 2... Round table, 4... Supply chute, 5... Roller-shaped member, 40... Distributor, 41... Bottom cover thereof,
42... Granular material supply port.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 回転する円卓と同円卓の外周部上で回転する複
数個のローラ状部材とにより、同円卓上に供給さ
れた粒状物を粉砕する粒状物粉砕装置において、
前記円卓の中心上方へ粒状物を導く供給シユート
の下部に有底の分配器を設けるとともに同分配器
の側部に複数個の粒状物供給口を前記各ローラ状
部材に対応して設けたことを特徴とする粒状物粉
砕装置の供給シユート。
A granular material crushing device for pulverizing granular materials supplied onto the round table using a rotating round table and a plurality of roller-like members rotating on the outer periphery of the round table,
A bottomed distributor is provided at the bottom of the supply chute that guides the granular material above the center of the round table, and a plurality of granular material supply ports are provided on the side of the distributor, corresponding to each of the roller-shaped members. A supply chute for a granular material crushing device characterized by:
JP6902684U 1984-05-14 1984-05-14 Supply chute for granular material crushing equipment Granted JPS60183038U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6902684U JPS60183038U (en) 1984-05-14 1984-05-14 Supply chute for granular material crushing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6902684U JPS60183038U (en) 1984-05-14 1984-05-14 Supply chute for granular material crushing equipment

Publications (2)

Publication Number Publication Date
JPS60183038U JPS60183038U (en) 1985-12-04
JPH0128826Y2 true JPH0128826Y2 (en) 1989-09-01

Family

ID=30604314

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6902684U Granted JPS60183038U (en) 1984-05-14 1984-05-14 Supply chute for granular material crushing equipment

Country Status (1)

Country Link
JP (1) JPS60183038U (en)

Also Published As

Publication number Publication date
JPS60183038U (en) 1985-12-04

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