JPH0394139A - Automatic measuring device for powder particle size - Google Patents
Automatic measuring device for powder particle sizeInfo
- Publication number
- JPH0394139A JPH0394139A JP11091689A JP11091689A JPH0394139A JP H0394139 A JPH0394139 A JP H0394139A JP 11091689 A JP11091689 A JP 11091689A JP 11091689 A JP11091689 A JP 11091689A JP H0394139 A JPH0394139 A JP H0394139A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- opening
- particle size
- sieve
- measuring 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.)
- Pending
Links
Landscapes
- Weight Measurement For Supplying Or Discharging Of Specified Amounts Of Material (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は粉体粒度の自動測定装置に関し、粉体粒度を精
度よくかつ迅速に簡便に測定しかつ粒度制御手段として
供し得る粉体粒度の自動測定装置に関する。Detailed Description of the Invention [Field of Industrial Application] The present invention relates to an automatic measuring device for powder particle size, which can accurately, quickly and easily measure powder particle size, and which can be used as a particle size control means. Regarding automatic measuring equipment.
[従来の技術]
この稲の粉体粒度の自動測定装置はすでに、特開昭61
− 18H34号公報に開示されている。[Prior art] This automatic measuring device for grain size of rice powder has already been published in Japanese Patent Application Laid-open No. 1983
- Disclosed in Publication No. 18H34.
即ち、ふるい枠に平面的に配置された複数の網目を異に
するふるい機に粉体を供給してふるい分りを行い、ふる
い網下を計量機に送入して計量し、次いで、ふるい粋に
設けられた仕切りを取除いてふるい網上はより粗い網目
のふるいに移動させ、該ふるいにてふるい分けを行って
、ふるい網下を計量機に送大して計量することを順次行
って、最も粗い網目のふるい網目と各網目のふるい網下
との計量値を制御器により演算することにより、粉体粒
度の自動測定が行われている。又別の技術として多段振
動篩、計量機、マイコン制御器を組合せた造粒体粒度の
自動測定装置も販売されている。That is, the powder is sieved by feeding it to a sieve machine with a plurality of different meshes arranged flat on the sieve frame, the bottom of the sieve screen is sent to a weighing machine and weighed, and then the sieve size is sieved. Remove the partition provided on the sieve screen, move the top of the sieve to a sieve with a coarser mesh, sieve with that sieve, and send the bottom of the sieve to a weighing machine for weighing. The powder particle size is automatically measured by calculating the measured values of the sieve mesh and the sieve bottom of each mesh using a controller. As another technique, an automatic granule particle size measuring device that combines a multistage vibrating sieve, a weighing machine, and a microcomputer controller is also available on the market.
[発明が解決しようとする課題〕
しかしながら、上記従来の粉体粒度の自動測定装置では
、横方向に並べて平面的に配置された複数の網目を有す
るふるい機にてふるい分け操作を行わせているので、粉
休粒度の自動測定のために占有される面積が増大してし
まうという問題があり、その他に、ふるい分け時間の設
定、変更などの調整や仕切りの開閉時点の変更などのた
めの制御手段を示してなく、しかも、上記パラメータは
粉体物性、あるいは粉体粒度、供給量などの変化により
変更させる必要があるにもかかわらず充分に考慮されて
いす、したがって、該装置は粒度管理用としては使用で
きるが、粒度制御用として用いるには機能が不足すると
言う問題があった。[Problem to be Solved by the Invention] However, in the above-mentioned conventional automatic powder particle size measuring device, the sieving operation is performed using a sieving machine having a plurality of meshes arranged horizontally and arranged in a plane. However, there is a problem in that the area occupied by automatic measurement of powder size increases, and in addition, control means for setting and changing the sieving time and changing the opening/closing time of the partitions are required. Moreover, the above parameters have been sufficiently considered even though they need to be changed due to changes in powder physical properties, powder particle size, supply amount, etc. Therefore, this device is not suitable for particle size control. Although it can be used, there is a problem in that it lacks functionality to be used for particle size control.
また、別の従来技術の場合は、ふるい分けを取出しが並
行操作であり比較的粒形の揃った造粒品には適用できて
も、粉砕品については、本来通過すべき粉体が絹上品と
共に排出されてそまつという問題があった。In addition, in the case of another conventional technique, sieving and extraction are performed in parallel, and although it can be applied to granulated products with relatively uniform particle shapes, for crushed products, the powder that should originally pass through is mixed with silk products. There was a problem with the amount of waste being emitted.
本発明はこのような従来の問題を解決するものであり、
粒度測定すべき粉体の各段ごとのふるい分けと、ふるい
分けした粉体の取出と粉体重量の計量にもとづく演算に
さいしての操作タイ主ングを制御して粉体粒度測定を自
動化するようにし、かつ上記の各操作タイ稟ングがそれ
ぞれ設定される開閉手段による粉体の取出しによって計
量誤差の発生を防止し精度よく簡便に測定しかつ粒度制
御手段として供し得る優れた粉休粒度の自動測定装置を
提供することを目的とするものである。The present invention solves these conventional problems,
Powder particle size measurement is automated by controlling the operation control for sieving each stage of powder to be measured, taking out the sieved powder, and calculating the powder weight. , and the powder is taken out by the opening/closing means in which each of the above-mentioned operation ties are set, thereby preventing the occurrence of measurement errors, accurately and easily measuring, and providing an excellent automatic measurement of powder size that can be used as a particle size control means. The purpose is to provide a device.
[課題を解決するための手段]
本発明は上記目的を達成するために、多段配置した枠付
き丸形ふるいおよび不平衡重錘を取付けた垂直軸を有す
る発振機からなる振動ふるいと、各段ごとにふるい分け
したふるい網上粉体を取出す開口部と、上記各段ごとの
開口部を順次、開閉させる開閉手段を有する取出口と、
上記取出口からの粉体を導く導路内に分級した粉体の重
量を加算計量する計量機とを具備するようにし、また、
粉体のふるい分けを開始後、設定時間にて作動する即時
動作手段と、即時動作手段の作動にもとづいて各段ごと
の開閉手段を開閉させる操作手段と、その開閉によりふ
るいより排出された分級済み粉体を受材に収容してその
重量を計測する計量機と、計量終了に引続いて受材の水
平軸を中心として180゜回転させる転回手段を作動さ
せる操作手段と前記の各手段を順次動作させ粉体粒度を
演算する演算処理装置と、を備えるようにしたものであ
り、さらに、取出口の開閉手段を順次動作させる粉体粒
度を横断して回動する仕切板からなるようにし、また、
発振機の不平衡重錘の位相差の調整手段を備えるように
したものである。[Means for Solving the Problems] In order to achieve the above object, the present invention uses a vibrating sieve consisting of a framed round sieve arranged in multiple stages, an oscillator having a vertical axis equipped with an unbalanced weight, and a vibrating sieve for each stage. an opening for taking out the sieved powder on each sieve, and an outlet having an opening/closing means for sequentially opening and closing the openings for each stage;
A weighing machine for adding and weighing the weight of the classified powder is provided in the conduit for guiding the powder from the outlet, and
Immediate operation means that operates at a set time after starting sieving of powder; operation means that opens and closes the opening/closing means for each stage based on the operation of the immediate operation means; and classified materials discharged from the sieve by opening and closing the operation means. A weighing machine that stores the powder in a receiving material and measures its weight, an operating means that operates a turning means that rotates the receiving material 180 degrees about the horizontal axis after the measurement is completed, and each of the above-mentioned means in sequence. and an arithmetic processing device that operates to calculate the powder particle size, and further includes a partition plate that rotates across the powder particle size that sequentially operates the opening/closing means of the extraction port, Also,
The oscillator is equipped with means for adjusting the phase difference of the unbalanced weight of the oscillator.
[作 用]
本発明は上記のような構成により次のような作用を有す
る。すなわち、測定すべき粉休は振動ふるいの各段ごと
にふるい分けされ、ふるい網上粉体は開閉手段をもちい
て取出口から導路内に順次導かれ、分級した粉体の重量
を計量機によって計量し、演算処理によってふるい網の
目開き寸法に対応した粒度分布をうることができ、しか
も、上記の動作は演算処理装置によって制御して行われ
るので精度よくかつ迅速に簡便に粉体粒度の自動測定を
行うことができる。[Function] The present invention has the following effects due to the above configuration. In other words, the powder to be measured is sieved by each stage of the vibrating sieve, and the powder on the sieve mesh is sequentially guided into the guide channel from the outlet using an opening/closing means, and the weight of the classified powder is measured by a weighing machine. It is possible to obtain a particle size distribution corresponding to the opening size of the sieve mesh by weighing and calculating, and since the above operations are controlled by a calculation processing device, it is possible to accurately, quickly and easily determine the particle size of the powder. Automatic measurements can be taken.
取出口の開閉手段は仕切板によってふるい網上を流動し
ている粉体流れ方向を横断する形で回動させているので
開口部への粉体流れを確実かつ容易ならしめることがで
きる。Since the opening/closing means of the outlet is rotated by the partition plate in a manner transverse to the flow direction of the powder flowing on the sieve screen, the powder can be surely and easily flowed to the opening.
さらに、発振機の不平衡重錘に位相差をつけるように調
整できるので、ふるい網上における粉体流れ運動を粉体
の性状に適合するように強制させることにより、粉体の
排出を確実に行なわせて、粉体粒度の自動測定の精度を
さらに改善させることができる。Furthermore, since the unbalanced weight of the oscillator can be adjusted to create a phase difference, the powder flow motion on the sieve screen is forced to match the properties of the powder, ensuring powder discharge. By doing so, the accuracy of automatic measurement of powder particle size can be further improved.
[実施例]
第1図〜第3図は本発明の一実施例の構威をしめすもの
である。第1図〜第3図において、lOは自動測定装置
をしめし、振動ふるいl2、計fX機50などからなり
、振動するい12は筒状のふるい枠14を有し、ふるい
枠l4内に丸形ふるい1646゜を多段、例えば2段に
配置し、丸形ふるい16.18’の目開き寸法は上段か
ら下段に至るにしたがい順次細かくされているのが用い
られる。20.20゜はタッピングボール受板をしめし
、丸形ふるい網16.18゜を載せてふるい枠14内に
多段配置せられ、それぞれのふるい網下を通過させてい
る。丸形ふるい16とタッピングボール受板20および
丸形ふるい16゜とタッピングボール受板20′ との
それぞれの間隙にはふるい網1δ,16゜の清掃用タッ
ピングボール1717゛が押入されている、ふるい分け
操作を確実に行われている。[Embodiment] FIGS. 1 to 3 show the structure of an embodiment of the present invention. In FIGS. 1 to 3, lO indicates an automatic measuring device, which is composed of a vibrating sieve l2, a meter f The sieves 1646° are arranged in multiple stages, for example, in two stages, and the opening dimensions of the round sieves 16, 18' are gradually made finer from the upper stage to the lower stage. 20.20° indicates a tapping ball receiving plate, and round sieve screens 16.18° are placed on the sieve frame 14 in multiple stages, allowing the ball to pass under each sieve screen. A cleaning tapping ball 1717° of sieve net 1δ and 16° is pushed into the gaps between the round sieve 16 and the tapping ball receiving plate 20, and between the round sieve 16° and the tapping ball receiving plate 20′. The operation is being carried out reliably.
ふるい枠14の底部には発振機30が取付けられており
、中央部に垂直軸22を有し、垂直軸22の上、下部に
は不平衡重錘24.28がそれぞれ取付けられている。An oscillator 30 is attached to the bottom of the sieve frame 14, and has a vertical shaft 22 in the center, and unbalanced weights 24 and 28 are attached above and below the vertical shaft 22, respectively.
28は垂直軸22の下端に設けられたブーリをしめし、
駆動手段、例えば電動機34に設けられブーり32とベ
ルト手段3lを介して回転駆動される。33はふるい台
をしめし、ふるい枠工4を弾性支持させている。また、
40は基台をしめし、ふるい台33と基台40との間に
緩衝材3Bを押入し、振動ふるいl2の運動に伴う振動
が基台40に伝達されることを防止している。28 indicates a boule provided at the lower end of the vertical shaft 22;
It is provided in a driving means, for example, an electric motor 34, and is rotationally driven via a bobbin 32 and a belt means 3l. 33 denotes a sieve stand, which elastically supports the sieve frame 4. Also,
Reference numeral 40 indicates a base, and a cushioning material 3B is inserted between the sieve base 33 and the base 40 to prevent vibrations caused by the movement of the vibrating sieve l2 from being transmitted to the base 40.
自動測定装置10により測定すべき粉体試料はふるい枠
14の上部にある供給口l8から供給される。A powder sample to be measured by the automatic measuring device 10 is supplied from a supply port 18 at the top of the sieve frame 14.
このさい、図示を省略した供給装置などを用いることが
好適である。駆動手段34の回転による振動ふるい12
の振動によって、粉体試料は各段のふるい16.16゜
を通過したふるい網下と、通過しないふるい網上とに分
級され、ふるい枠l4の各段ごとに設けた取出口42,
42゜および42″から取出される。At this time, it is preferable to use a supply device, which is not shown. Vibrating sieve 12 by rotation of drive means 34
Due to the vibration of the sieve frame 14, the powder sample is sorted into the lower portion of the sieve screen that has passed through the 16.16° sieve of each stage and the upper portion of the sieve screen that has not passed through the screen.
42° and 42″.
取出口42はふるい16のふるい網上と、取出口42゜
はふるい16のふるい網下にしてふるいl6゜のふるい
網上と、取出口42′′はふるい16′のふるい網下に
対応するよう&:設けられたものである。The outlet 42 corresponds to the top of the sieve screen of the sieve 16, the outlet 42° corresponds to the bottom of the sieve 16 and above the sieve screen of the sieve 16°, and the outlet 42'' corresponds to the bottom of the sieve 16'. Yo &: It is something that has been established.
第2図は振動ふるいl2の上段における取出口42の詳
細をしめすのものである。ふるい枠工4の外側に取出口
42が設けられ、52は取出口42の入口部をなす開口
部である。開口部52は開閉手段53をもって開閉自在
にされ、54は仕切板をしめし、56は仕切板の端部に
設けたヒンジ材である。58は仕切板54の中央部に設
けた案内材をしめし、例えば溝部などが設けられている
。案内材58にはピン材62が滑動自在に挿入されてい
る。FIG. 2 shows details of the outlet 42 in the upper stage of the vibrating screen 12. An outlet 42 is provided on the outside of the sieve frame 4, and 52 is an opening that serves as an inlet of the outlet 42. The opening 52 can be opened and closed by an opening/closing means 53, 54 is a partition plate, and 56 is a hinge member provided at the end of the partition plate. Reference numeral 58 indicates a guide member provided at the center of the partition plate 54, and is provided with, for example, a groove. A pin member 62 is slidably inserted into the guide member 58.
60はふるい網16の上部に設けられた圧力シリンダを
しめし、圧力シリンダ60のロッド64は上記ビン材6
2と固着され、圧力シリンダ60の他端は接続材66を
介してふるい枠14に設けられた受台68によって支持
されている。圧力シリンダ60は図示を省略した出入口
から圧力流体を出入させてロット64を移動させ仕切板
54をヒンジ56の廻りに所定開度をもって回動させ、
例えば二重鎮線にてしめすごとく仕切板54を回動させ
て開口部52を開放させ、また実線にてしめすごとく開
口部52を閉鎖させることができる。矢印Aはふるい網
l6表面における粉体流れ方向をしめし、開閉手段53
を順次動作させる粉体粒度に沿って回動し、粉体が取出
口42に円滑に流れて取出されることを可能としている
。Reference numeral 60 indicates a pressure cylinder provided above the sieve mesh 16, and a rod 64 of the pressure cylinder 60 is connected to the bottle material 6.
2, and the other end of the pressure cylinder 60 is supported by a pedestal 68 provided on the sieve frame 14 via a connecting member 66. The pressure cylinder 60 allows pressure fluid to enter and exit from an inlet and exit port (not shown) to move the lot 64 and rotate the partition plate 54 around the hinge 56 with a predetermined opening degree.
For example, the opening 52 can be opened by rotating the partition plate 54 as indicated by a double line, and the opening 52 can be closed as indicated by a solid line. Arrow A indicates the powder flow direction on the surface of the sieve screen 16, and the opening/closing means 53
is sequentially rotated according to the particle size of the powder, allowing the powder to smoothly flow into the outlet 42 and be taken out.
第3図は振動ふるいl2の各段における取出口42.
42゜, 4 2 ”および対応する開閉手段53,
53“.53″の配置をそれぞれしめしたものである。FIG. 3 shows the outlet ports 42 in each stage of the vibrating sieve l2.
42°, 42” and corresponding opening/closing means 53,
53".53" respectively.
各段の取出口42. 42’,42゜゜の開口部はそれ
ぞれ若干の間隔のもとで変位させて設けられており、い
ずれも粉体がそれぞれの取出口42. 42’,42”
へ順次、円滑に流れ取出されることを可能としている。Outlet port 42 of each stage. The openings 42' and 42° are displaced with a slight distance from each other, so that the powder can be removed from the respective outlet 42. 42', 42"
This allows for smooth flow and removal.
取出口42, 42゜,42゜′の開口部と他端の出口
部は直線上に位置するごとく配置され、第1図にしめす
ごとくそれぞれの連結材42a,42b,42cを介し
て導路43に集合して連結されており、取出口42.
42゜,42″から取出された分級した粉体を導路43
に導くとともに、導路43の下部のホッパ一部45内に
設けた受材46に上記粉体を収容し、受材46に取付け
た転回手段48を介して計量機50、例えば、ロートセ
ルに接続され、計量機50によって受材46に収容した
粉体の重量が受材46、転回手段48および取付具など
とともに計量される。The openings of the outlets 42, 42°, 42°' and the outlet at the other end are arranged on a straight line, and the guide path 43 is connected through the respective connecting members 42a, 42b, 42c as shown in FIG. are gathered and connected to the outlet 42.
The classified powder taken out from 42° and 42″ is passed through the conduit 43
At the same time, the powder is stored in a receiving material 46 provided in a hopper part 45 at the lower part of the conduit 43, and connected to a weighing machine 50, for example, a funnel cell, via a turning means 48 attached to the receiving material 46. Then, the weight of the powder contained in the receiving material 46 is measured by the weighing machine 50 together with the receiving material 46, the turning means 48, the fixture, and the like.
計量機50には演算IA理装置70を接続することが可
能であって、計量機50の重量検出値は演算処理装置7
0の検出回路を径て演算処理回路において加算演算をは
しめとするデータ処理が行われ、演算結果は表示部にて
表示されるとともに制御操作部からの出力信号は自動測
定装置10の運動手順などを規制し、最適な粉体粒度の
自動測定を確実に繰返へすことができる。It is possible to connect a calculation IA processing device 70 to the weighing machine 50, and the weight detection value of the weighing machine 50 is processed by the calculation processing device 7.
Data processing including addition calculation is performed in the arithmetic processing circuit via the zero detection circuit, and the calculation result is displayed on the display unit, and the output signal from the control operation unit is used to record the movement procedure of the automatic measuring device 10, etc. can be regulated and automatic measurement of the optimum powder particle size can be reliably repeated.
上記において、半導体ロジックやパソコンなどとの組合
せによりプログラムの作成の可能な論理シーケンスを用
いて順次動作の制御を行うことができる。In the above, sequential operations can be controlled using a logic sequence that can be programmed in combination with semiconductor logic, a personal computer, or the like.
上記の自動化装置70の詳細な構成は以下に示すとおり
である。測定すべき粉体のふるい分け操作は電動機34
の回転のもとで行われ予め設定した所定時間を経過する
と、粉体のふるい分けが終了するので、図示を省略した
限時動作手段の動作により、開閉手段53に取付けた圧
力シリンダ60に出入する圧力流体の回路に設けた操作
手段、例えば切換弁に入力するようにされている。受材
46に取付けた転回手段48は、例えば、ステップモー
タなどが用いられ、分級した粉体を収容して計量機50
、例えばロードセルにて計量し、計量データの安定化を
まって、計量終了信号を出力し計量終了、信号は転回手
段48を作動させる操作手段、例えば、開閉装置などに
人力されるようにされている。The detailed configuration of the automation device 70 described above is as shown below. The sieving operation of the powder to be measured is performed by an electric motor 34.
The sieving of the powder is completed after a preset period of time has elapsed under the rotation of The input signal is inputted to an operating means provided in the fluid circuit, for example, a switching valve. The turning means 48 attached to the receiving material 46 is, for example, a step motor or the like, and accommodates the classified powder and transfers it to the weighing machine 50.
For example, the measurement is performed using a load cell, and after the measurement data has stabilized, a measurement end signal is outputted, and the measurement is completed.The signal is manually inputted to an operating means for operating the turning means 48, such as a switchgear. There is.
次は上記実施例の動作について説明する。上記実施例に
おいて、各段の取出口42, 42゜,42”の開閉手
段53, 53゜, 5 3 ”をそれぞれ閉鎮するよ
うに演算処理装置70の出力信号により作動し、粉体試
料を供給口l8から供給してふるい分け操作によって分
級が行われ、ふるい網16目開き寸法以上、ふるい網1
6および1B’ 目開き寸法区間、ふるい網16目開き
寸法以下の各群に分級される。前記の演算処理装置70
から設定時間が命令された限時動作手11
1 2
段の動作により開閉手段53を回勅させて開口部52を
開口し、ふるい網l6のふるい網上の粉体を取出したの
ち、開閉手段53を逆回動させて開口部52を開鎖し、
上記の粉体を受材46に収容し計量機50によって計量
される。計量データの安定化による計量終了を待って転
回手段48を作動させて受材46を転回させてホッパ4
5から粉体を排出した後、転回手段48を逆作動させて
受材46は定位置に復帰される。次いで開閉手段53゛
を回動させて開口部52“を開口し、ふるい16゜のふ
るい網上の粉体を取出したのち、開閉手段53゜を逆回
動させて開口部52゜を閉鎖し、上記の粉体を受材46
に収容し、計量機50によって計量される。以下、上記
と実質上同様な動作が行われ、ふるい16゜のふるい網
下の粉体についても同様な順序動作が繰返久される。Next, the operation of the above embodiment will be explained. In the above embodiment, the opening/closing means 53, 53°, 53'' of the outlet ports 42, 42°, 42'' of each stage are operated by the output signal of the arithmetic processing unit 70 to close the opening/closing means 53, 53°, 53'', respectively, to remove the powder sample. Classification is performed by a sieving operation by supplying from the supply port 18.
6 and 1B' mesh size range, and each group is classified into each group with 16 mesh size or less. The arithmetic processing device 70
The opening/closing means 53 is rotated to open the opening 52 by the operation of the time-limited operation means 11 1 2 in which the set time is commanded from to open and close the opening 52 by rotating it in the opposite direction.
The above-mentioned powder is stored in a receiving material 46 and weighed by a weighing machine 50. Waiting for the end of weighing due to stabilization of the weighing data, the turning means 48 is operated to turn the received material 46 and move it to the hopper 4.
After the powder is discharged from 5, the turning means 48 is reversely operated to return the receiving material 46 to its normal position. Next, the opening/closing means 53'' is rotated to open the opening 52'' and the powder on the sieve screen of the 16° sieve is taken out, and then the opening/closing means 53'' is rotated in the opposite direction to close the opening 52''. , the above powder is received as a material 46
and weighed by a weighing machine 50. Thereafter, substantially the same operations as above are performed, and the same sequence of operations is repeated for the powder under the 16° sieve screen.
上記において、ふるい分け時間の設定値をはじめとして
、開閉手段の回動にさいしての時間設定はいずれもプロ
グラムにもとづいて任意に設定することができる。上記
の設定値は、処理すべき粉体の性状を考慮して予じめ、
予備処理などによって最適パラメータが得られるように
決定される。In the above, the setting value of the sieving time and the time setting for rotating the opening/closing means can all be set arbitrarily based on a program. The above setting values are determined in advance by considering the properties of the powder to be processed.
The parameters are determined by preliminary processing or the like to obtain the optimum parameters.
また、ふるい分け時間の設定にさいしては、多段のふる
いを用いてふるい分けを行うさいに、ふるい分けが終了
するまでの所要時間が最長となるふるいを基準として行
うこととしているので、すべてのふるいのふるい分けが
終了している。In addition, when setting the sieving time, when sieving is performed using multiple sieves, the sieve that takes the longest time to complete sieving is used as the standard, so the sieving time for all sieves is has ended.
なお、各段ごとの開閉手段53. 53゜, 5 3
”を順次開閉させて、分級した粉体を受材に収容するご
とに累積重量を計量したのち、累積粉体を収容した受材
46を転回させてホッパ45から上記粉体を排出した後
、受材46を定位置に復帰させることも可能である。In addition, opening/closing means 53 for each stage. 53°, 5 3
After measuring the accumulated weight each time the classified powder is stored in the receiving material by sequentially opening and closing the ``, the receiving material 46 containing the accumulated powder is turned and the powder is discharged from the hopper 45. It is also possible to return the receiving material 46 to its home position.
上記のごとく、粉体のふるい分けが終了したのちに受材
46に粉体を収容するごとに計量機50によって収容し
た粉体の重量が計量されて、演算処理装置70における
演算処理によって各群に分級された粉体重量、供給粉体
総重量、粒度分布、粒度特性数、平均粒度などが演算さ
れて演算結果は表示部にて表示される。上記の操作は制
御操作部の人出力信号にもとづいて行われる。As mentioned above, each time the powder is stored in the receiving material 46 after the sieving of the powder is completed, the weight of the stored powder is measured by the weighing machine 50, and the weight of the stored powder is measured by the calculation processing in the calculation processing unit 70. The weight of the classified powder, the total weight of the supplied powder, the particle size distribution, the particle size characteristic number, the average particle size, etc. are calculated, and the calculation results are displayed on the display section. The above operations are performed based on human output signals from the control operation section.
[発明の効果]
このように本発明によれば、振動ふるいを駆動させるこ
とにより試料粉体を各段に分級することができ、演算処
理装置による制御によって分級した粉体を開閉手段によ
り順次取出して、その重量を計量機により測定させ、上
記演算処理によって試料粉体の粒度分布などの演算IA
理によってつることができて、装置および粒度測定の手
順が簡便となり精度よくかつ迅速に自動測定することが
できる。[Effects of the Invention] As described above, according to the present invention, the sample powder can be classified into each stage by driving the vibrating sieve, and the classified powder can be sequentially taken out by the opening/closing means under the control of the arithmetic processing unit. Then, the weight is measured by a weighing machine, and the calculation IA such as the particle size distribution of the sample powder is performed by the above calculation process.
The particle size measurement procedure and apparatus are simple, and accurate and rapid automatic measurement is possible.
また取出口の開閉手段の仕切板58はふるい網表面上を
流動している粉休流れ方向を横断ずる形に案内している
ので開口部への粉休流れを確実かつ容易ならしめるとと
もに、粉体流れを確実に遮断させることができ、装置の
運転および粉体粒度の自動測定を確実にすることができ
る。In addition, the partition plate 58 of the opening/closing means for the outlet is guided in a shearing shape across the direction of the powder flow flowing on the surface of the sieve screen, so that the powder flow to the opening is ensured and easy. The body flow can be reliably interrupted, and the operation of the device and automatic measurement of powder particle size can be ensured.
さらに、発振機の不平衡重錘に位相差をつけるように調
整できるので、ふるい網上にお番づる粉体流れ運動を粉
体の性状に適合するように強制させることにより、粉体
の分級を確実に行なわせて、粉体粒度の自動測定の精度
をさらに改善させることができる。Furthermore, since the unbalanced weight of the oscillator can be adjusted to create a phase difference, the powder flow motion on the sieve screen is forced to match the properties of the powder, thereby classifying the powder. This can further improve the accuracy of automatic measurement of powder particle size.
また、装置および粒度測定の手順が簡便となり、精度よ
くかつ迅速に粉体粒度を自動測定することができる。こ
れらの機能により粉砕操作などにおけるオンライン粒度
制御手段として使用することができ、粉砕製品粒度の安
定性を確保できるという実用上の効果を奏する。Furthermore, the apparatus and particle size measurement procedure are simplified, and the powder particle size can be automatically measured accurately and quickly. These functions allow it to be used as an on-line particle size control means in pulverization operations, etc., and have the practical effect of ensuring the stability of the pulverized product particle size.
第11図は本発明の一実施例における粉体粒度の自動測
定装置の全体構成図、第2図は同装置の要部詳細図、第
3図は同装置の取出口の開閉手段の配置図である。
10・・・・・・・・自動測定装置 12・・・・・・
・・振動ふるいl4・・・・・・・・ふるい枠 1
6,18“・・・・ふるい網22・・・・・・・・垂直
軸
24.28・・・・平衡重錘
15
16
30・・・・・・・・発振機
42, 42゜.42゜゜・・取出口
43・・・・・・・・導 路
50・・・・・・・・計量機
52・・・・・・・・開口部
53・・・・・・・・開閉手段
54・・・・・・・・仕切板Fig. 11 is an overall configuration diagram of an automatic powder particle size measuring device according to an embodiment of the present invention, Fig. 2 is a detailed view of the main parts of the device, and Fig. 3 is a layout diagram of the opening/closing means for the outlet of the device. It is. 10... Automatic measuring device 12...
... Vibrating sieve l4... Sieve frame 1
6,18"... Sieve net 22... Vertical axis 24.28... Balance weight 15 16 30... Oscillator 42, 42°.42゜ ゜ ・ ・ Exit 43 ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ Measuring machine 52 ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・・・・・・・・・・Partition plate
Claims (4)
を取付けた垂直軸を有する発振機からなる振動ふるいと
、各段ごとにふるい分けしたふるい網上粉体を取出す開
口部と、上記各段ごとの開口部を順次、開閉させる開閉
手段を有する取出口と、上記取出口からの粉体を導く導
路内に分級した粉体の重量を計量する計量機とを具備し
たことを特徴とする粉体粒度自動測定装置。(1) A vibrating sieve consisting of a round sieve with a frame arranged in multiple stages and an oscillator with a vertical axis equipped with an unbalanced weight, an opening for taking out the powder on the sieve mesh screened in each stage, and each of the above It is characterized by comprising an outlet having an opening/closing means for sequentially opening and closing the openings of each stage, and a weighing machine for measuring the weight of the classified powder in a conduit that guides the powder from the outlet. Powder particle size automatic measuring device.
限時動作手段と、限時動作手段の作動にもとづいて各段
ごとの開閉手段を開閉させる操作手段と、その開閉によ
りふるいより排出された分級済み粉体を受材に収容して
、その重量を計測する計量機と、計量終了に引続いて受
材の水平軸を中心として180゜回転させる転回手段を
作動させる操作手段と、前記の各手段を順次動作させる
粉体粒度を演算する演算処理装置と、を備えたことを特
徴とする請求項1記載の粉砕粒度の自動測定装置。(2) A time-limited operation means that operates at a set time after the start of sifting the powder, an operation means that opens and closes the opening/closing means for each stage based on the operation of the time-limited operation means, and a control means for opening and closing the opening/closing means for each stage based on the operation of the time-limited operation means; a weighing machine for storing the classified powder in a receiving material and measuring its weight; an operating means for operating a turning means for rotating the receiving material by 180 degrees about the horizontal axis after the measurement is completed; 2. The automatic measuring device for pulverized particle size according to claim 1, further comprising an arithmetic processing device for calculating the powder particle size by sequentially operating each means.
する仕切板からなることを特徴とする請求項1記載の粉
体粒度の自動測定装置。(3) The automatic powder particle size measuring device according to claim 1, wherein the opening/closing means for the outlet comprises a partition plate that rotates across the powder flow direction.
ことを特徴とする請求項1記載の粉体粒度の自動測定装
置。(4) The automatic powder particle size measuring device according to claim 1, further comprising means for adjusting the phase difference of the unbalanced weight of the oscillator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11091689A JPH0394139A (en) | 1989-04-28 | 1989-04-28 | Automatic measuring device for powder particle size |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11091689A JPH0394139A (en) | 1989-04-28 | 1989-04-28 | Automatic measuring device for powder particle size |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0394139A true JPH0394139A (en) | 1991-04-18 |
Family
ID=14547885
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11091689A Pending JPH0394139A (en) | 1989-04-28 | 1989-04-28 | Automatic measuring device for powder particle size |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0394139A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013086016A (en) * | 2011-10-18 | 2013-05-13 | Fuji Paudal Co Ltd | Vibration sieve |
| JP2013530399A (en) * | 2010-06-15 | 2013-07-25 | エンパイア テクノロジー ディベロップメント エルエルシー | Air pretreatment device |
| CN104749074A (en) * | 2015-04-10 | 2015-07-01 | 国家电网公司 | Online continuous pulverized coal fineness tester and control method thereof |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6043189A (en) * | 1983-08-17 | 1985-03-07 | Kobe Steel Ltd | Controlling method of discharge temperature in oil- cooled positive displacement type rotary compressor |
| JPS6391178A (en) * | 1986-10-06 | 1988-04-21 | 品川白煉瓦株式会社 | Grain size controller with two sieving device |
-
1989
- 1989-04-28 JP JP11091689A patent/JPH0394139A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6043189A (en) * | 1983-08-17 | 1985-03-07 | Kobe Steel Ltd | Controlling method of discharge temperature in oil- cooled positive displacement type rotary compressor |
| JPS6391178A (en) * | 1986-10-06 | 1988-04-21 | 品川白煉瓦株式会社 | Grain size controller with two sieving device |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013530399A (en) * | 2010-06-15 | 2013-07-25 | エンパイア テクノロジー ディベロップメント エルエルシー | Air pretreatment device |
| JP2013086016A (en) * | 2011-10-18 | 2013-05-13 | Fuji Paudal Co Ltd | Vibration sieve |
| CN104749074A (en) * | 2015-04-10 | 2015-07-01 | 国家电网公司 | Online continuous pulverized coal fineness tester and control method thereof |
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