JPH0119948B2 - - Google Patents

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Publication number
JPH0119948B2
JPH0119948B2 JP60284684A JP28468485A JPH0119948B2 JP H0119948 B2 JPH0119948 B2 JP H0119948B2 JP 60284684 A JP60284684 A JP 60284684A JP 28468485 A JP28468485 A JP 28468485A JP H0119948 B2 JPH0119948 B2 JP H0119948B2
Authority
JP
Japan
Prior art keywords
chute
powder
classification
duct
dust
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
JP60284684A
Other languages
Japanese (ja)
Other versions
JPS62144787A (en
Inventor
Yasunobu Fukuhiro
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
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 by Individual filed Critical Individual
Priority to JP28468485A priority Critical patent/JPS62144787A/en
Publication of JPS62144787A publication Critical patent/JPS62144787A/en
Publication of JPH0119948B2 publication Critical patent/JPH0119948B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 産業上の利用分野 粉粒体の処理方法には乾式と湿式の二つの方法
があり、原料の水分率が2%以下のものは乾式、
それ以上のものは湿式方法で処理されるのが一般
的である。本発明は、乾式の分級装置に関するも
のである。
[Detailed description of the invention] Industrial application field There are two methods for processing powder and granules: dry method and wet method.For raw materials with a moisture content of 2% or less, dry method,
Anything larger than that is generally processed using a wet method. The present invention relates to a dry classification device.

従来の技術 風力分級機は分級原理上、流体による抗力の方
向とは方向の違う力、つまり、分級力が作用する
ことにより、粒子径に応じ分類する装置である。
BACKGROUND TECHNOLOGY A wind classifier is a device that classifies particles according to their size based on the principle of classification, by applying a force in a direction different from the direction of the drag force caused by the fluid, that is, a classifying force.

分級力として重力、慣性力、遠心力が考えら
れ、実際にはこれらの二つ以上の力が同時に作用
することが多い。
Gravitational force, inertial force, and centrifugal force can be considered as classification forces, and in reality, two or more of these forces often act simultaneously.

風力分級機は、株式会社産業技術センター発
行、最新粉粒体プロセス技術集成70〜72頁、表
3.1 風力分級機の分級表に示す通りであるが、
No.12に示されるエアーセパレーター形式のものを
使用する場合が多く、これが基本型とされ、それ
に変形を加えたものが多い。
The wind classifier is published by Industrial Technology Center Co., Ltd., Latest Powder Process Technology Collection, pages 70-72, Table
3.1 As shown in the classification table of the wind classifier,
The air separator type shown in No. 12 is often used, and this is considered the basic model, with many variations added to it.

考案が解決しようとする問題点 従来の乾式分級装置はエアセパレーター、サイ
クロン、バツグフイルター等の組合せのものが多
く使用れているが、乾式分級方法はいづれも原料
水分の影響が大きく、安定操業のためには乾燥設
備を設ける場合もあり、原料及び製品の装置内で
の附着、目詰まり、固形化による分級精度の低下
等多くの欠点があつた。
Problems that the invention aims to solve Many conventional dry classification devices use a combination of air separators, cyclones, bag filters, etc. However, all dry classification methods are greatly affected by the moisture content of the raw material, making stable operation difficult. In order to do this, drying equipment is sometimes installed, which has many drawbacks, such as a drop in classification accuracy due to adhesion of raw materials and products inside the equipment, clogging, and solidification.

問題点を解決するための手段 含水率が3%以下の粉粒体を、含水率が3%以
下の粉粒体を受け入れる投入シユートと、筐体内
に網目状篭体を有する分級篭を高速回転するよう
に支承して、前面室と背面室を区画形成し、前記
分級篭中央部内面に対向して、その軸線方向より
送風するア圧送パイプと、その軸線に対し傾斜し
て前記投入シユートに連通する供給シユートを併
設した分級機を具備し、上記前面室の下部に整粒
製品を外部に取出す取出シユートを連設し、上記
背面室の下部に取出シユートと排風ダクトを介し
て排風機の吸引力により微粉および粉塵を回収
し、かつ外部に取出すサイクロン及び集塵機を連
設したものである。
Measures to solve the problem A charging chute that receives powder and granular materials with a moisture content of 3% or less, and a classification basket that has a mesh-like cage inside the casing are rotated at high speed. A pressure-feeding pipe which faces the inner surface of the central part of the classification basket and blows air from the axial direction thereof, and a pressure-feeding pipe which is inclined with respect to the axis and which is connected to the input chute to form a front chamber and a rear chamber. It is equipped with a classifier equipped with a supply chute that communicates with it, and a take-out chute for taking out the sized products outside is installed in the lower part of the front chamber, and an air exhaust machine is installed in the lower part of the rear chamber through the take-out chute and the exhaust duct. This system is equipped with a cyclone and a dust collector that collect fine powder and dust using the suction power and take it out to the outside.

作 用 投入シユートを通過する間に流れの方向を変
え、粗粒の流下と再分散を繰返す構造とし、発生
する粉塵は排風機の吸引力によつて吸引する。投
入シユートを通つた原料は筐体内で高速回転して
いる分級篭の中央部内面の近傍に供給される。分
級篭に投入された原料は、分級篭の回転により発
生する風力と遠心力とによつて製品と微粉とに分
級され、製品はホツパーよりコンベアーにより機
外に出される。分級篭の網目より分級篭の回転に
より発生する風力と遠心力と排風機の吸引力とに
より排出された微粉および粉塵は、排風機の吸引
力により乾燥されながらサイクロン及びバツクフ
イルターにいたり、微粒子は回収され、エアーは
外部に排出される。
Function The flow direction is changed while passing through the input chute, and the coarse particles are repeatedly flowed down and redispersed, and the generated dust is sucked up by the suction force of the exhaust fan. The raw material that has passed through the input chute is supplied to the vicinity of the inner surface of the central portion of the classification basket, which is rotating at high speed within the housing. The raw materials put into the classification basket are classified into products and fine powder by the wind and centrifugal force generated by the rotation of the classification basket, and the products are delivered from the hopper to the outside of the machine by a conveyor. Fine particles and dust are discharged from the mesh of the classification basket by the wind force generated by the rotation of the classification basket, the centrifugal force, and the suction force of the exhaust fan, and are dried by the suction force of the exhaust fan, and then enter the cyclone and back filter. The air is collected and exhausted to the outside.

実施例 第1図乃至第4図は本発明の実施例を示す。第
1図において、1は投入シユート2を備えた分級
機、3はサイクロン、4はコンプレツサ付の集塵
機であり、5は排風機である。
Embodiment FIGS. 1 to 4 show embodiments of the present invention. In FIG. 1, 1 is a classifier equipped with an input chute 2, 3 is a cyclone, 4 is a dust collector with a compressor, and 5 is an exhaust fan.

分級機1の筐体6内は、第2図に示す如く、製
品を集める前面室7と、微粉、粉塵等を集める背
面室8に区割されており、背面室8内には截頭円
錐形状の分級篭9が開口側を前面室7に向けて筐
体6の外部のモータ10で高速回転させられる如
く配設してある。上記分級篭9は回転板11と、
上記回転板11の周囲に固設された所定の網目を
有する篭体12とで構成されている。13は筐体
6外から前面室7内に挿入され、先端の噴出口1
3aを上記分級篭9の回転板11と間隔をおいて
対向設置したエア圧送パイプで、このエア圧送パ
イプ13の後端の送風口13bは筐体6の外部に
設置した送風機14に連なつている。尚、分級篭
9の開口縁と筐体6の内周面との間には筐体6側
に固設した仕切板17が設けられており、この仕
切板17により前面室7と背面室8とが区割され
ている。分級篭9の篭体12は金網、多孔板ある
いはスリツト板等を用いて構成する。更に回転板
11は図示した凹形状の他に、円錐形状、凸形
状、平板形状等のものを用いる。上記篭体の種
類、回転板の形状は分級処理される粉粒体の粒径
が含水度合、送風量、分級篭9の回転速度等の諸
条件に応じて選択される。
As shown in Fig. 2, the inside of the housing 6 of the classifier 1 is divided into a front chamber 7 for collecting products and a rear chamber 8 for collecting fine powder, dust, etc. A sorting basket 9 having the same shape as that shown in FIG. The classification basket 9 has a rotary plate 11,
It is comprised of a housing 12 having a predetermined mesh fixed around the rotating plate 11. 13 is inserted into the front chamber 7 from outside the housing 6, and is connected to the spout 1 at the tip.
3a is an air pressure pipe installed facing the rotary plate 11 of the classification basket 9 at a distance, and the air outlet 13b at the rear end of this air pressure pipe 13 is connected to a blower 14 installed outside the housing 6. There is. A partition plate 17 fixed to the case 6 is provided between the opening edge of the classification basket 9 and the inner peripheral surface of the case 6, and this partition plate 17 separates the front chamber 7 and the rear chamber 8. are separated. The housing 12 of the classification basket 9 is constructed using a wire mesh, a perforated plate, a slit plate, or the like. Further, the rotary plate 11 may have a conical shape, a convex shape, a flat plate shape, etc. in addition to the concave shape shown in the figure. The type of the housing and the shape of the rotary plate are selected depending on various conditions such as the particle size of the powder to be classified, the degree of water content, the amount of air blown, and the rotational speed of the classification basket 9.

前記筐体6の上部に設けた投入シユート2は、
第3図に示す如く、内板18と外板19とによつ
て後面以外の面が閉塞された二重壁構造となつて
おり、内板18には多数の小孔あるいはスリツト
〔図示せず〕を設けてある。20は集塵装置に連
なる吸引ダクト21の接続口で、内板18と外板
19とで形成される横断面コ字状の隙間22内を
減圧して通路23内で発生する粉塵等を小孔から
隙間22、吸引ダクト21を介して吸い取り、後
続のサイクロン、集塵装置で処理する。24は粉
粒体の搬入コンベアで、この搬入コンベア24
は、上記投入シユート2の端部を内板18の後面
上部に形成した搬入窓25に挿入してある。26
は上記搬入窓25の上縁から垂らした多数の細幅
のゴムシートからなる覆いである。また内板18
で形成される通路23の上端は頂板27で閉塞す
る。28,29,30は上記内板18の対向する
内面に交互に設けた堰体で、この複数の堰体2
8,29,30でジグザグ状の通路23を形成し
ている。31は上記投入シユート2のジグザグ状
の通路23の下部に接続した供給シユートで、こ
の供給シユート31は筐体6内に下り傾斜に設け
てあり、先端開口部31aを分級篭9の回転板1
1と対向させ、かつ、上記エア圧送パイプ13の
噴出口13aの上部に近接させて配置してある。
The input chute 2 provided at the top of the housing 6 is
As shown in FIG. 3, it has a double-walled structure in which surfaces other than the rear surface are closed by an inner plate 18 and an outer plate 19, and the inner plate 18 has many small holes or slits (not shown). ] is provided. Reference numeral 20 denotes a connection port of a suction duct 21 connected to a dust collector, which reduces the pressure in a gap 22 formed by an inner plate 18 and an outer plate 19 and has a U-shaped cross section to reduce dust generated in a passage 23. It is sucked out from the hole through the gap 22 and the suction duct 21, and processed by a subsequent cyclone and dust collector. 24 is a conveyor for carrying in powder and granular materials; this conveyor 24
The end of the input chute 2 is inserted into a carry-in window 25 formed at the upper rear surface of the inner plate 18. 26
is a cover made of a large number of narrow rubber sheets hanging from the upper edge of the carry-in window 25. In addition, the inner plate 18
The upper end of the passage 23 formed by the above is closed by a top plate 27. Numerals 28, 29, and 30 are weir bodies provided alternately on the opposing inner surfaces of the inner plate 18, and the plurality of weir bodies 2
8, 29, and 30 form a zigzag-shaped passage 23. Reference numeral 31 denotes a supply chute connected to the lower part of the zigzag-shaped passage 23 of the input chute 2. This supply chute 31 is provided in the housing 6 with a downward slope, and its tip opening 31a is connected to the rotary plate 1 of the classification basket 9.
1 and is disposed close to the upper part of the spout 13a of the air pressure pipe 13.

32は筐体6の前面室7の下部に形成した製品
取出シユートで、このシユート32の下方位置に
製品搬出用ベルトコンベア33を設ける。34は
筐体6の背面室8の下部に形成した粉塵取出シユ
ートで、このシユート34と、架台35に設置さ
れた前記サイクロン3の上部3aとをJ字状のダ
クト36で連結すると共に、該ダクト36のサイ
クロン3側の端部に前記投入シユート2に連通す
る吸引ダクト21を接続開口する。上記ダクト3
6の途中には第4図にすように下方に伸びる先細
り状の分岐通路37が形成してあり、該分岐通路
37の下部開口部38にロータリーバルブ40を
設けてある。このロータリーバルブ40は、断面
が円弧状に膨隆するケース本体30内に、複数枚
の羽根41を放射状に設けて複数の収容室42を
区画形成した回転体59を枢軸43を支点に回転
可能に設けた構成である。44は分岐通路37の
上部開口部45の上流側に枢軸46を介して回動
可能に装着した風量調節ダンパ、47a,47b
は分岐通路37にそつて垂直方向に所定の間隔を
おいて枢軸48a,48bを中心に回動可能に設
けた変流羽根で、変流羽根47aは上部開口部4
5の下流側に風量調節ダンパ44と隣接させて設
けてある。そして、上記風量調節ダンパ44と細
長形の変流羽根47a,47bを回動しその角度
姿勢を適宜調整することにより、排風機5の吸引
力でダクト36を通る空気流に分岐通路37の上
部開口部45の付近で乱流を生じさせ、この乱流
で粉塵中の比重の大きな粒体を分岐通路37に分
岐落下させる。48は分岐通路37の周壁49の
開口部50に装着した内部点検用の扉、51は点
検扉48と対向させて周壁49の内面に固設した
反撥板である。
Reference numeral 32 denotes a product take-out chute formed at the lower part of the front chamber 7 of the housing 6, and a belt conveyor 33 for taking out the product is provided at a position below this chute 32. 34 is a dust extraction chute formed at the lower part of the rear chamber 8 of the casing 6. This chute 34 and the upper part 3a of the cyclone 3 installed on the pedestal 35 are connected by a J-shaped duct 36, and A suction duct 21 communicating with the input chute 2 is connected to the end of the duct 36 on the cyclone 3 side. Above duct 3
6, a tapered branch passage 37 extending downward is formed as shown in FIG. 4, and a rotary valve 40 is provided at a lower opening 38 of the branch passage 37. This rotary valve 40 is rotatable about a pivot 43 around a rotating body 59, which has a plurality of blades 41 radially provided in a case body 30 whose cross section swells into an arc shape to define a plurality of storage chambers 42. This is the configuration provided. Reference numeral 44 denotes an air volume adjusting damper 47a, 47b rotatably mounted on the upstream side of the upper opening 45 of the branch passage 37 via a pivot 46.
are flow transformation vanes rotatably provided around pivot shafts 48a and 48b at a predetermined interval in the vertical direction along the branch passage 37;
The damper 5 is provided adjacent to the air volume adjusting damper 44 on the downstream side of the damper 5 . By rotating the air volume adjusting damper 44 and the elongated current transformation vanes 47a and 47b and adjusting their angular postures as appropriate, the suction force of the exhaust fan 5 directs the air flow through the duct 36 to the upper part of the branch passage 37. A turbulent flow is generated in the vicinity of the opening 45, and this turbulent flow causes particles with large specific gravity in the dust to branch and fall into the branch passage 37. 48 is a door for internal inspection attached to the opening 50 of the peripheral wall 49 of the branch passage 37, and 51 is a repulsion plate fixed to the inner surface of the peripheral wall 49 facing the inspection door 48.

52は第1の排風ダクト、53は第2の排風ダ
クトで、第1の排風ダクト52の一端をサイクロ
ン3の上面部3bに接続開口し、かつ、他端を架
台54に設置されたコンプレツサ付の集塵機4の
側面部4aに接続開口すると共に、第2の排風ダ
クト53の両端を上記集塵機4の他方の側面上部
4bおよび排風機5にそれぞれ接続開口する。5
5は集塵機4の下部開口部4cに装着したスクリ
ユーコンベアからなるロータリーフイーダ、56
はサイクロン3と集塵機4との間に設置した粉塵
搬出用ベルトコンベア、57はサイクロン3の下
部開口部3cの下方位置と粉塵搬出用ベルトコン
ベア56の端部上方位置との間に傾斜させて設置
したスクリユーコンベア、58はロータリーフイ
ーダ55の端部下方位置と粉塵搬出用ベルトコン
ベア56の端部上方位置との間に傾斜させて設置
したスクリユーコンベアである。
52 is a first air exhaust duct, and 53 is a second air exhaust duct, one end of the first air exhaust duct 52 is connected and opened to the upper surface part 3b of the cyclone 3, and the other end is installed on the pedestal 54. A connection opening is made to the side surface 4a of the dust collector 4 with a compressor, and both ends of the second exhaust duct 53 are connected to the other side upper part 4b of the dust collector 4 and the exhaust fan 5, respectively. 5
5 is a rotary leaf feeder 56 consisting of a screw conveyor attached to the lower opening 4c of the dust collector 4;
57 is a belt conveyor for discharging dust installed between the cyclone 3 and the dust collector 4, and 57 is installed at an angle between a position below the lower opening 3c of the cyclone 3 and a position above the end of the belt conveyor 56 for discharging dust. The screw conveyor 58 is a screw conveyor installed at an angle between a position below the end of the rotary feeder 55 and a position above the end of the belt conveyor 56 for carrying out dust.

60は前記ダクト36に形成した分岐通路37
の下部に設けたロータリーバルブ40により回収
された粒体を製品搬出用ベルトコンベア33に搬
送するスクリユーコンベアである。
60 is a branch passage 37 formed in the duct 36.
This is a screw conveyor that conveys the granules collected by a rotary valve 40 provided at the lower part of the screw conveyor to a belt conveyor 33 for carrying out products.

而して、上記構成の分級装置により粉粒体を分
級処理するには、粉粒体を搬入コンベア24で投
入シユート2内に搬入する。上記投入シユート2
内に搬入された粉粒体はジグザグ状の通路23を
通過し、供給シユート31を介して分級篭9の回
転板11の内面近傍に供給される。粉粒体が投入
シユート2の通路23を通過するとき、該粉粒体
は通路23に設けられた堰体28,29,30に
衝突して粉塵等が発生する。このときサイクロン
3に連通する吸引ダクト21の接続口20が投入
シユート(2)の隙間22に接続開口しているので、
通路23内の粉塵等は内板18の小孔を介して上
記隙間22に吸引された後、吸引ダクト21を通
つてサイクロン3に流入する。他方送風機14に
よつてエア圧送パイプ13内に送風口13bから
所定流量で流入した空気は、エア圧送パイプ13
を通つたのち噴出口13aから噴出する。する
と、上記供給シユート31の先端開口部31aか
ら分級篭9の回転板11の内面近傍に供給された
粉粒体は、エア圧送パイプ13の噴出口13aか
ら噴出する空気流によつて分級篭9の回転板11
の内面に吹き付けられる。空気流によつて分級篭
9に吹き付けられた粉粒体は回転板11に衝突
し、上記空気流によつて分散乾燥作用を受けなが
ら分級篭9内に分散する。分級篭9内に分散した
粉粒体は、分級篭9の回転により発生する遠心力
とエア圧送パイプからの風力および背面室8に作
用する排風機5の吸引力とで製品たる粒体と、微
粉、粉塵および残留水分とに完全に分級される。
分級された製品は、回転する分級篭9の遠心力に
よりその傾斜内面に誘導されて該分級篭9から前
面室7に入り、その下方の製品取出シユート32
から排出用ベルトコンベア33上に排出され、か
つ、適所に搬出される。他方製品より分離した粉
塵等は、分級篭9の遠心力と風力および筐体6の
背面室8に作用する排風機5の吸引力とで分級篭
9の網目より該背面室8に入る。上記筐体6の背
面室8に入つた粉塵等は空気と共に該背面室8に
作用する排風機5の吸引力により粉塵取出シユー
ト34からダクト36を介してサイクロン3に吸
引され、ここで遠心分離され、該サイクロン3の
下部に集められ、下部開口部3cからスクリユー
コンベア57上に回収される。上記粉塵等が通る
ダクト36には、風量調節ダンパ44および変流
羽根47a,47bを設けた分岐通路37が形成
してあるので、この風量調節ダンパ44および変
流羽根47a,47bの角度姿勢を適宜調整し、
分岐通路37の上部開口部45の付近で乱流を生
じさせると、この乱流によりダクト36内を通過
する粉塵の中から比重の大きな残留粒体が分級さ
れ分岐通路37内に落下する。分岐通路37内に
落下した粒体は、分岐通路37の下部開口部38
に設けたロータリーバルブ40の収容室42に収
容され、該収容室42に粒体が堆積すると、回転
体59が枢軸43を中心に回転し、収容室42内
の粒体はロータリーバルブ40から搬出されてス
クリユーコンベア60上に回収される。この回収
された粒体はスクリユーコンベア60により製品
搬出用ベルトコンベア33に送られる。前記サイ
クロン3で遠心分離されて排出された空気は第1
の排風ダクト52を介して集塵機4に送られ、こ
こでさらに空気に残存した微細な粉塵等が分離さ
れ、空気は第2の排風ダクト53を介して排風機
5に送られ、他方分離された残存粉塵等は集塵機
4の下部開口部4cからロータリーフイーダ55
上に回収された後、スクリユーコンベア58上に
落下搬出される。
In order to classify the powder or granular material using the classification apparatus having the above-mentioned configuration, the powder or granular material is carried into the input chute 2 by the carrying-in conveyor 24. Above input chute 2
The granular material carried into the container passes through the zigzag-shaped passage 23 and is supplied to the vicinity of the inner surface of the rotary plate 11 of the classification basket 9 via the supply chute 31. When the powder passes through the passage 23 of the input chute 2, the powder collides with the weirs 28, 29, and 30 provided in the passage 23, generating dust and the like. At this time, since the connection port 20 of the suction duct 21 communicating with the cyclone 3 is connected to the gap 22 of the input chute (2),
Dust and the like in the passage 23 are sucked into the gap 22 through the small holes in the inner plate 18, and then flow into the cyclone 3 through the suction duct 21. On the other hand, the air flowing into the air pressure feeding pipe 13 from the air outlet 13b at a predetermined flow rate by the blower 14 flows into the air pressure feeding pipe 13.
After passing through, it is ejected from the ejection port 13a. Then, the powder and granules supplied from the tip opening 31a of the supply chute 31 to the vicinity of the inner surface of the rotary plate 11 of the classification basket 9 are transferred to the classification basket 9 by the air flow jetted from the jet port 13a of the air pressure pipe 13. rotating plate 11
sprayed onto the inside surface of the The powder particles blown onto the classification basket 9 by the air flow collide with the rotary plate 11, and are dispersed within the classification basket 9 while being subjected to a dispersion drying effect by the air flow. The powder and granules dispersed in the classification basket 9 are transformed into granules as products by the centrifugal force generated by the rotation of the classification basket 9, the wind force from the air pressure pipe, and the suction force of the exhaust fan 5 acting on the rear chamber 8. Completely classified into fine powder, dust and residual moisture.
The classified products are guided to the inclined inner surface of the rotating classification basket 9 by the centrifugal force, enter the front chamber 7 from the classification basket 9, and enter the product extraction chute 32 below.
From there, it is discharged onto the discharge belt conveyor 33 and carried out to an appropriate location. On the other hand, dust and the like separated from the product enter the rear chamber 8 through the mesh of the classification basket 9 due to the centrifugal force and wind force of the classification basket 9 and the suction force of the exhaust fan 5 acting on the rear chamber 8 of the housing 6 . Dust etc. that have entered the back chamber 8 of the casing 6 are sucked together with air by the suction force of the exhaust fan 5 acting on the back chamber 8 from the dust extraction chute 34 through the duct 36 to the cyclone 3, where they are centrifuged. are collected at the lower part of the cyclone 3 and collected onto the screw conveyor 57 through the lower opening 3c. The duct 36 through which the dust and the like pass is formed with a branch passage 37 provided with an air volume adjustment damper 44 and current transformation vanes 47a, 47b. Adjust as appropriate,
When a turbulent flow is generated near the upper opening 45 of the branch passage 37, residual particles with a large specific gravity are classified from the dust passing through the duct 36 due to the turbulence and fall into the branch passage 37. The particles that have fallen into the branch passage 37 are removed from the lower opening 38 of the branch passage 37.
When the particles are deposited in the storage chamber 42, the rotating body 59 rotates around the axis 43, and the particles in the storage chamber 42 are carried out from the rotary valve 40. and collected on the screw conveyor 60. The recovered granules are sent by a screw conveyor 60 to a belt conveyor 33 for carrying out the product. The air centrifuged and discharged by the cyclone 3 is
The air is sent to the dust collector 4 through the second exhaust duct 52, where fine dust remaining in the air is further separated, and the air is sent to the exhaust fan 5 through the second exhaust duct 53, where it is separated. The remaining dust, etc., is transferred from the lower opening 4c of the dust collector 4 to the rotary feeder 55.
After being collected at the top, the screws fall onto the screw conveyor 58 and are carried out.

そして、前記サイクロン3からスクリユーコン
ベア57上に排出された粉塵等および集塵機4か
らスクリユーコンベア58上に排出された粉塵等
は、該スクリユーコンベア57,58で搬送され
て粉塵搬出用ベルトコンベア56上に落下搬出さ
れた後、適所へ運ばれる。
The dust discharged from the cyclone 3 onto the screw conveyor 57 and the dust discharged from the dust collector 4 onto the screw conveyor 58 are transported by the screw conveyors 57 and 58 to a belt conveyor for carrying out dust. 56 and then transported to the appropriate location.

発明の効果 本発明によれば、分級篭に投入された原料は、
分級篭の回転により発生する風力と遠心力および
分級篭の背面室に作用する排風機の吸引とによつ
て製品と微粉に分級されるので、大量の粉粒体を
短時間で分級することが可能となり、分級処理能
力および作業能率の大幅な向上を図ることができ
る。また、粉粒体の投入シユートをジグザグ状に
して流れの方向を急激に変え、粗粒の流下と再分
散を繰り返す構造とし、発生する粉塵を排風機の
吸引力によつて吸引するので、粉粒体の分級処理
を効率よく行うことができる。さらに、筐体の背
面室下部の取出シユートとサイクロンとを連結す
るダクトの途中に分岐通路を設け、かつ、分岐通
路の開口部に風量調節ダンパと変流羽根を設け、
該分岐通路の開口部近傍に乱流を生じさせるよう
にしたので、この乱流でダクト内を通過する粉塵
の中から比重の大きな残留粒体を分級することが
でき、分級処理能力がきわめてよい。
Effects of the Invention According to the present invention, the raw material charged into the classification basket is
The product and fine particles are classified by the wind and centrifugal force generated by the rotation of the classification basket and the suction of the exhaust fan acting on the back chamber of the classification basket, making it possible to classify large amounts of powder and granules in a short time. This makes it possible to significantly improve classification processing capacity and work efficiency. In addition, the powder input chute is shaped like a zigzag pattern to rapidly change the flow direction, and the coarse particles are repeatedly flowed down and redispersed. It is possible to efficiently classify particles. Furthermore, a branch passage is provided in the middle of the duct connecting the take-out chute at the lower part of the rear chamber of the casing and the cyclone, and an air volume adjustment damper and a current transformation vane are provided at the opening of the branch passage.
Since a turbulent flow is generated near the opening of the branch passage, this turbulent flow can classify residual particles with a large specific gravity from the dust passing through the duct, and the classification processing capacity is extremely high. .

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

第1図は本発明に係る分級装置の実施例を示し
た説明図、第2図は分級機の縦断側面図、第3図
は投入シユートの概略斜視説明図、第4図は分級
機とサイクロンとを連結するダクトの途中に設け
た分岐通路の縦断側面図である。 2…投入シユート、3…サイクロン、4…集塵
機、5…排風機、6…筐体、7…前面室、8…背
面室、9…分級篭、13…エア圧送パイプ、13
a…噴出口、23…通路、32,34…取出シユ
ート、36…ダクト。
Fig. 1 is an explanatory diagram showing an embodiment of the classifier according to the present invention, Fig. 2 is a longitudinal cross-sectional side view of the classifier, Fig. 3 is a schematic perspective explanatory diagram of the input chute, and Fig. 4 is the classifier and cyclone. FIG. 2...Input chute, 3...Cyclone, 4...Dust collector, 5...Exhaust fan, 6...Casing, 7...Front chamber, 8...Back chamber, 9...Classifying basket, 13...Air pressure pipe, 13
a... Spout port, 23... Passage, 32, 34... Takeout chute, 36... Duct.

Claims (1)

【特許請求の範囲】 1 含水率が3%以下の粉粒体を受け入れる投入
シユートと、筐体内に網目状篭体を有する分級篭
を高速回転するように支承して、前面室と背面室
を区画形成し、前記分級篭中央部内面に対向し
て、その軸線方向より送風するエア圧送パイプ
と、その軸線に対し傾斜して前記投入シユートに
連通する供給シユートを併設した分級機を具備
し、 上記前面室の下部に整粒製品を外部に取出す取
出シユートを連設し、 上記背面室の下部に取出シユートと排風ダクト
を介して排風機の吸引力により微粉および粉塵を
回収し、かつ外部に取出すサイクロン及び集塵機
を連設したことをことを特徴とする粉粒体の乾式
分級装置。 2 投入シユートを、内板と外板とからなり上記
内板と外板との間に閉塞された二重壁状をなす空
隙部を形成し、上記空隙部をダクトを介して集塵
機に連結すると共に、上記内板に多数の小孔を穿
設し、上記内板で形成される通路を内面に設けた
堰体でジグザグ状通路となしたことを特徴とする
特許請求の範囲1に記載の粉粒体の乾式分級装
置。 3 筐体の背面室下部の取出シユートとサイクロ
ンとを連結するダクトの途中に、下方に伸びる分
岐通路を設け、この分岐通路の開口部に風量調節
ダンパおよび細長形の変流羽根を回動可能に設
け、分岐通路の下部開口部に収容室を有するロー
タリーバルブを設けたことを特徴とする特許請求
の範囲1に記載の粉粒体の乾式分級装置。
[Scope of Claims] 1. A front chamber and a back chamber are provided by supporting an input chute for receiving powder and granular material having a moisture content of 3% or less and a classification basket having a mesh-like housing inside the housing so as to rotate at high speed. A classifier is provided with an air pressure pipe which is formed into a compartment, faces the inner surface of the central part of the classification basket and blows air from the axial direction thereof, and a supply chute which is inclined with respect to the axis and communicates with the input chute, At the bottom of the front chamber, there is a take-out chute for taking out the sized product to the outside, and at the bottom of the back room, the fine powder and dust are collected by the suction force of the exhaust fan through the take-out chute and the exhaust duct. 1. A dry classification device for powder and granular materials, characterized in that a cyclone and a dust collector are installed in series. 2. The input chute is made up of an inner plate and an outer plate, forming a closed double-walled gap between the inner plate and the outer plate, and connecting the gap to the dust collector via a duct. In addition, a large number of small holes are bored in the inner plate, and the passage formed by the inner plate is formed into a zigzag passage by a weir body provided on the inner surface. Dry classification equipment for powder and granular materials. 3 A branch passage extending downward is provided in the middle of the duct that connects the take-out chute at the bottom of the rear chamber of the housing and the cyclone, and an air volume adjustment damper and an elongated current transformation vane can be rotated at the opening of this branch passage. 2. The dry classification apparatus for powder and granular materials according to claim 1, further comprising a rotary valve provided at the lower opening of the branch passage and having a storage chamber.
JP28468485A 1985-12-17 1985-12-17 Dry type sorter for powdered and granular body Granted JPS62144787A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28468485A JPS62144787A (en) 1985-12-17 1985-12-17 Dry type sorter for powdered and granular body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28468485A JPS62144787A (en) 1985-12-17 1985-12-17 Dry type sorter for powdered and granular body

Publications (2)

Publication Number Publication Date
JPS62144787A JPS62144787A (en) 1987-06-27
JPH0119948B2 true JPH0119948B2 (en) 1989-04-13

Family

ID=17681639

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28468485A Granted JPS62144787A (en) 1985-12-17 1985-12-17 Dry type sorter for powdered and granular body

Country Status (1)

Country Link
JP (1) JPS62144787A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015160199A (en) * 2014-02-28 2015-09-07 清水建設株式会社 Separate processor for processed product

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5354358A (en) * 1976-10-26 1978-05-17 Yasunobu Fukuhiro Dehydrating apparatus
JPS55157365A (en) * 1979-05-28 1980-12-08 Hosokawa Micron Kk Classifying method and classifying device
JPS5748274A (en) * 1980-09-05 1982-03-19 Nippon Telegr & Teleph Corp <Ntt> Rectifying device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4922068U (en) * 1972-05-29 1974-02-25

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5354358A (en) * 1976-10-26 1978-05-17 Yasunobu Fukuhiro Dehydrating apparatus
JPS55157365A (en) * 1979-05-28 1980-12-08 Hosokawa Micron Kk Classifying method and classifying device
JPS5748274A (en) * 1980-09-05 1982-03-19 Nippon Telegr & Teleph Corp <Ntt> Rectifying device

Also Published As

Publication number Publication date
JPS62144787A (en) 1987-06-27

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