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JPH0132129B2 - - Google Patents
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JPH0132129B2 - - Google Patents

Info

Publication number
JPH0132129B2
JPH0132129B2 JP10075684A JP10075684A JPH0132129B2 JP H0132129 B2 JPH0132129 B2 JP H0132129B2 JP 10075684 A JP10075684 A JP 10075684A JP 10075684 A JP10075684 A JP 10075684A JP H0132129 B2 JPH0132129 B2 JP H0132129B2
Authority
JP
Japan
Prior art keywords
discharge tube
hopper
rotary table
powder
spacer
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
JP10075684A
Other languages
Japanese (ja)
Other versions
JPS60244715A (en
Inventor
Katsuya Mizui
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.)
Hosokawa Micron Corp
Original Assignee
Hosokawa Micron Corp
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 Hosokawa Micron Corp filed Critical Hosokawa Micron Corp
Priority to JP10075684A priority Critical patent/JPS60244715A/en
Publication of JPS60244715A publication Critical patent/JPS60244715A/en
Publication of JPH0132129B2 publication Critical patent/JPH0132129B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G65/00Loading or unloading
    • B65G65/30Methods or devices for filling or emptying bunkers, hoppers, tanks, or like containers, of interest apart from their use in particular chemical or physical processes or their application in particular machines, e.g. not covered by a single other subclass
    • B65G65/34Emptying devices
    • B65G65/40Devices for emptying otherwise than from the top
    • B65G65/48Devices for emptying otherwise than from the top using other rotating means, e.g. rotating pressure sluices in pneumatic systems
    • B65G65/4809Devices for emptying otherwise than from the top using other rotating means, e.g. rotating pressure sluices in pneumatic systems rotating about a substantially vertical axis
    • B65G65/4818Devices for emptying otherwise than from the top using other rotating means, e.g. rotating pressure sluices in pneumatic systems rotating about a substantially vertical axis and having the form of rotating tables or pans

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、粉粒体を送り出す供給、排出装置に
関し、送り出し量の多少を問わず広い範囲に亘つ
て定量的に、しかも、付着性の強い、あるいは凝
集塊を混在するような粉粒体の供給、排出を安定
して行わせることのできるテーブルフイーダであ
る。
[Detailed Description of the Invention] [Industrial Field of Application] The present invention relates to a supply and discharge device for sending out powder and granular materials, and is capable of quantitatively controlling the amount of adhesion over a wide range regardless of the amount of delivery. This is a table feeder that can stably supply and discharge powder that is strong or contains agglomerates.

〔従来技術〕[Prior art]

粉粒体の供給排出装置には種々のものがある
が、その内でも第5図に例示するテーブルフイー
ダは構造が簡単で、故障の原因となり易い可動部
も少く、また送り量の調節変更も容易にできるこ
と、大型化への設計変更も容易であるなど多くの
利点を有し、古くから粉粒体を扱う様々な分野で
使われて来た。また、各々の分野で使用に適した
改良も色々と加えられて来た。中でも付着の強
い、あるいは凝集塊を混在するような粉粒体を対
象とするものは、特にテーブル上への送り出しを
円滑に行わせるためにホツパに揺振動や衝撃を加
えたり、ホツパ内に空気を送り込んだり、又は回
転撹拌部材やかきとり羽根を設けたりするなどの
方法やそのための部材が付設されて来た。
There are various types of feeding and discharging devices for powder and granular materials, but among them, the table feeder illustrated in Figure 5 has a simple structure, has few moving parts that can easily cause trouble, and is easy to adjust and change the feed rate. It has many advantages, such as being easy to make and changing the design to make it larger, and has been used in various fields that handle powder and granular materials for a long time. Various improvements have also been made to suit the use in each field. Especially when dealing with powders and granules that have strong adhesion or coexist with agglomerates, it is necessary to apply shaking vibration or impact to the hopper or to blow air into the hopper to ensure smooth delivery onto the table. Methods and members for this purpose have been added, such as feeding a rotary agitator, or providing a rotating stirring member or a scraping blade.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

以上、種々の改良が積まれたにもかかわらず、
付着、凝集性の強い粉粒体に関しては、問題があ
つた。すなわち、このような原料を前記のテーブ
ルフイーダで送る場合、第5図にも示すようにホ
ツパ34下方傾斜部出口35付近にかけて架橋現
象やラツトホール等を発生し易く、円筒33部よ
りテーブル31への送り出しが円滑に行えず、安
定した供給、排出が不可能となり、あるいは閉塞
により送り出し困難ともなるなど重大な問題があ
り、これらは前記の手段によつてもなお解決され
ていない。本発明は、これら問題を解決して定量
性のすぐれたテーブルフイーダを提供することに
ある。
Despite the various improvements mentioned above,
There were problems with powders and granules that had strong adhesion and cohesive properties. That is, when such raw materials are fed by the table feeder, as shown in FIG. There are serious problems such as not being able to smoothly deliver the fluid, making stable supply and discharge impossible, or making it difficult to deliver due to blockage, and these problems have not yet been solved by the above-mentioned measures. The object of the present invention is to solve these problems and provide a table feeder with excellent quantitative performance.

〔問題を解決するための手段〕[Means to solve the problem]

本発明は、回転テーブルの回転の中心よりはず
れた上方位置に原料ホツパを配し、該ホツパの下
方開口に対して該ホツパとは別に排出筒を嵌合接
続させると共に、該排出筒を回転テーブル上面と
適度な間隔位置に保持させて回転させることによ
つてホツパ内より原料の円滑な送り出しを計るも
のであり、また、両部材間の間隔の維持には摺動
可能な材料よりなる一部に切欠き溝を有するスペ
ーサを配し、上方から流下の原料の圧力を以つて
一定容積内における充填の均一化を計ることによ
り安定した定量供給、定量排出を行わせるもので
ある。
In the present invention, a raw material hopper is disposed above the rotation center of the rotary table, a discharge tube is fitted and connected to the lower opening of the hopper separately from the hopper, and the discharge tube is connected to the rotary table. By rotating the hopper while holding it at an appropriate distance from the upper surface, it is possible to smoothly feed the raw material from inside the hopper.Also, to maintain the distance between the two members, a part made of a slidable material is used. A spacer having a notched groove is disposed in the spacer, and the pressure of the raw material flowing down from above is used to equalize the filling within a certain volume, thereby achieving stable quantitative supply and quantitative discharge.

〔作用〕[Effect]

まず、第1にホツパ内の原料を開口部付近にお
いて、開口部よりの送り出し前の静止状態におけ
る上方原料重量による圧密現象を緩和、又は抑制
させることによつて架橋現象やラツトホール等の
閉塞原因を防止し、あるいは閉塞を解除させるこ
とであり、ホツパ下方開口部に設けられた排出筒
を回転させると、ホツパから排出筒まで詰つた粉
体層自体がこの接合部において剪断される。この
剪断作用によつてこの付近の原料を中心に上方の
ホツパ下方開口部分の原料へと運動を伝えて原料
粒子間の接触を滑らかにし、粒子と壁面、及び粒
子同士の付着、凝集を抑え、かつ凝集塊生成を防
止して下方への流下を円滑化させるわけであり、
この状態から図中の矢印方向にテーブルが回転し
供給排出が開始されると原料粒子の相対運動も活
発化し、さらに安定した円滑な送り出しが可能と
なる。第2に排出筒が回転テーブルの中心よりは
ずれた位置に配設されていることにより、該下方
開口部と接するテーブル全面が一方向に移動し、
かつ中心位置に比べれば格段に速く大きな移送力
を有していること、又、第3に該開口部とテーブ
ル面との間に設けられたスペーサ及び切欠き溝に
よつて該テーブル面での送り出しを一時的に抑え
て全体として送り出し量の均一化を計ることであ
る。すなわち、上方より流下して来た原料は、排
出筒下方に設けられたスペーサによつてテーブル
面上での原料の安息角による広がりを抑えられ、
かつ、この空間において上方原料重量に加えて前
記排出筒とテーブルの回転に伴う移動力とを受け
て圧密充填化され、均一な密度とされて切欠き溝
より連続的に送り出される。以上、排出筒の回転
による第1の作用と、回転テーブルの中心をはず
れた位置のために受ける第2の作用と、スペーサ
及び切欠き溝の付設によつてなされる第3の作用
とによつて、原料の円滑な送り出しに加えて均一
で安定した供給排出を可能にするものである。そ
して、スペーサの切欠き溝より送り出された原料
は回転テーブル上を送られてスクレパによりかき
落され、次工程に供給、あるいは排出捕集され
る。
First, the material in the hopper is placed in the vicinity of the opening to alleviate or suppress the compaction phenomenon caused by the weight of the material above in a stationary state before being sent out from the opening, thereby eliminating the causes of blockage such as bridging and rat holes. The purpose is to prevent or release the blockage, and when the discharge pipe provided at the lower opening of the hopper is rotated, the powder layer itself packed from the hopper to the discharge pipe is sheared at this junction. This shearing action transmits motion from the raw material in this vicinity to the raw material in the lower opening of the hopper above, smoothing the contact between raw material particles and suppressing adhesion and aggregation between particles and the wall surface and between particles. It also prevents the formation of agglomerates and smoothes the downward flow.
From this state, when the table rotates in the direction of the arrow in the figure and supply/discharge is started, the relative movement of the raw material particles becomes active, making it possible to send out more stably and smoothly. Second, since the discharge tube is located at a position offset from the center of the rotary table, the entire surface of the table in contact with the lower opening moves in one direction.
In addition, compared to the center position, it has a much faster transfer force and, thirdly, the spacer and notch groove provided between the opening and the table surface allow the transfer to be performed at the table surface. The aim is to temporarily suppress the delivery and make the delivery amount uniform as a whole. In other words, the material flowing down from above is prevented from spreading due to the angle of repose of the material on the table surface by the spacer provided below the discharge tube.
Further, in this space, in addition to the weight of the upper raw material, the raw material is compressed and packed by the moving force caused by the rotation of the discharge tube and table, and is continuously sent out from the notch groove with a uniform density. As described above, the first effect due to the rotation of the ejection tube, the second effect due to the off-center position of the rotary table, and the third effect due to the provision of the spacer and notch groove are as follows. In addition to smooth feeding of raw materials, it also enables uniform and stable supply and discharge. Then, the raw material sent out from the notch groove of the spacer is sent on a rotary table, scraped off by a scraper, and supplied to the next process or discharged and collected.

〔発明の効果〕〔Effect of the invention〕

以上本発明の効果は、ホツパ内において発生し
易い架橋現象、ラツトホール等閉塞への発展原因
ともなる原料粒子同士の付着、凝集、凝結を抑え
てホツパ内の流路を確保でき、回転テーブルまで
の原料の円滑な送り出しが安定して得られるこ
と。そして、回転テーブル面上に送られて来た原
料に対しては、スペーサ部及び切欠き溝において
圧密充填作用を以つて原料密度の均一化と送り出
し容積の一定化が計れ、回転テーブルへの定量的
な送り出しが可能となり、定量供給、定量排出が
行えること。また、構造が簡単で、殊に故障の原
因となり易い粉接部については簡潔そのもので、
保守、掃除も至つて容易である点、スケールアツ
プ等についての設計変更をする場合にも自由度が
大きいなどの利点がある。
As described above, the effects of the present invention are that it is possible to secure a flow path in the hopper by suppressing the adhesion, aggregation, and coagulation of raw material particles that are likely to occur in the hopper, which can lead to blockages such as rat holes, and to secure a flow path in the hopper. To be able to stably and smoothly feed raw materials. Then, for the raw material sent onto the rotary table surface, the spacer part and the notch groove perform a compaction filling action to equalize the raw material density and constant the delivered volume, and the amount is transferred to the rotary table. It is possible to send out a fixed amount, and to be able to supply and discharge a fixed amount. In addition, the structure is simple, and the powder contact parts, which are particularly prone to failure, are simple.
It has the advantage of being extremely easy to maintain and clean, and having a large degree of freedom when making design changes for scale-up and the like.

〔実施例〕〔Example〕

第1図乃至第2図により実施例について説明す
る。15は機台で、該台上には回転テーブル1を
保持し、回転させるための変速機13と電動機1
4が取付けられている。そして、回転テーブル1
の上方に設けられる原料ホツパ11を回転テーブ
ル1の回転の中心をはずれた位置の適当な高さに
ブラケツト16で保持させ、その下方開口18に
対してはやや大径の直円筒状の排出筒4を嵌合接
続させる。これら両部材間の隙間および重なり部
分の寸法は排出筒4内との通気が可能で、原料が
漏出しない程度であればよい。そして、排出筒4
は、二つの回転軸8a,8bに回転自在に取り付
けられた各々2個づつ4個の受け車輪7とベルト
6とにより回転される。これら二つの回転軸8
a,8bの一方8aは駆動軸としてプーリー9が
取り付けられ、ベルトを介し図示省略の変速機お
よび電動機に接続されて回転駆動力を伝えるもの
で、他方8bは従動軸として受け車輪7を介し排
出筒4を支受するものである。これら回転軸8
a,8bはブラケツト16及びブラケツト17に
より保持されている。なお、排出筒4の上下方向
の支受は、該排出筒4の下方回転テーブル1との
間に固定された両面とも摺動可能なスペーサ2上
に載置されてなされる。該スペーサ2は、排出筒
4の取付位置内より回転テーブル1の回転の中心
に対し、円周に沿つた曲面部を有する切欠き溝3
と、かき取り用スクレパ部10とを具備形成させ
てある。このスペーサ2の厚さt、及び切欠き溝
3の幅bは回転テーブル1及び排出筒4の回転速
度と同様に供給、排出量に影響するもので、これ
ら相互の兼ね合わせの上、適宜設計変更されるも
のであり、該スペーサ2の固定は保持桿12を介
し前記ブラケツト16に取付けられてなされる。
また、排出筒4内の下方端部近くには、弾性板片
5を一端を固定し、他端を自由として付設させて
いる。この弾性板片5は、排出筒4内において原
料が少くなつて来た場合にかき出したり、あるい
は塊状の原料をほぐしたりするのに有効なもので
あり、数は複数個であつてもよく、又、弾性板片
5は凝集塊により、撓みを生ずる程度菲薄なもの
とし、凝集塊との接触時の衝撃を緩和させて排出
筒4の回転への影響を極力抑え、粉粒体の流下、
通過の抵抗を少なくするのに有益である。また、
ホツパ11の下方開口18部側に一、又は複数個
の仕切板を縦方向に取付け、排出筒4の回転によ
るホツパ11内原料の共回りを防いだり、ホツパ
11内の粉体圧を適度に支受させたりすることも
本発明の効果を引き出す上で有効であり、ホツパ
11の大きさや形状によつて採用される。
An embodiment will be described with reference to FIGS. 1 and 2. Reference numeral 15 denotes a machine base, on which the rotary table 1 is held and a transmission 13 and an electric motor 1 for rotating it are mounted.
4 is installed. And rotary table 1
The raw material hopper 11 provided above is held by a bracket 16 at an appropriate height off the center of rotation of the rotary table 1, and a right cylindrical discharge tube with a slightly larger diameter is connected to the lower opening 18. 4 and connect them by fitting. The dimensions of the gap and the overlapping portion between these two members are sufficient as long as they allow ventilation with the inside of the discharge tube 4 and prevent raw materials from leaking out. And the discharge tube 4
is rotated by four receiving wheels 7, two each rotatably attached to two rotating shafts 8a and 8b, and a belt 6. These two rotating shafts 8
One of a and 8b, 8a, is attached with a pulley 9 as a drive shaft, and is connected to a transmission and an electric motor (not shown) via a belt to transmit rotational driving force, and the other 8b is a driven shaft, which is used for discharging via a receiving wheel 7. It supports the tube 4. These rotating shafts 8
a and 8b are held by brackets 16 and 17. The vertical support of the discharge tube 4 is achieved by placing it on a spacer 2 which is fixed between the discharge tube 4 and the lower rotary table 1 and is slidable on both sides. The spacer 2 has a notched groove 3 having a curved surface extending along the circumference from the inside of the mounting position of the discharge tube 4 to the center of rotation of the rotary table 1.
and a scraper part 10 for scraping. The thickness t of the spacer 2 and the width b of the notch groove 3 affect the amount of supply and discharge, as do the rotational speeds of the rotary table 1 and the discharge tube 4, and are designed appropriately in consideration of these factors. The spacer 2 is fixed by being attached to the bracket 16 via the holding rod 12.
Further, near the lower end of the discharge tube 4, an elastic plate piece 5 is attached with one end fixed and the other end free. The elastic plate pieces 5 are effective for scraping out the raw material when it becomes low in the discharge pipe 4 or loosening the lumpy raw material, and the number of the elastic plate pieces 5 may be plural. In addition, the elastic plate piece 5 is made thin enough to be deflected by the agglomerates, so as to reduce the impact upon contact with the agglomerates and minimize the influence on the rotation of the discharge tube 4, thereby reducing the flow of powder and granules.
This is useful in reducing resistance to passage. Also,
One or more partition plates are installed vertically on the lower opening 18 side of the hopper 11 to prevent the raw materials in the hopper 11 from rotating together due to the rotation of the discharge tube 4, and to moderate the powder pressure in the hopper 11. Supporting the hopper 11 is also effective in bringing out the effects of the present invention, and may be adopted depending on the size and shape of the hopper 11.

〔実験例〕[Experiment example]

第3図は本実施例の実験結果を表わしたもの
で、原料の酸化チタンは平均粒径0.5ミクロンで、
きわめて凝集性の強い粉体であり、前記第5図に
示したような従来のテーブルフイーダ、及び本実
施例において排出筒4を静止させた状態の場合で
は共にわずかの時間で供給、排出が不可能になつ
たものである。(図中グラフの)このグラフで
は、横軸に経過時間(分)を、縦軸に供給、排出
量を積算した値(グラム)を取つたもので、図中
矢印のグラフ、は排出筒4のみの回転速度を
各々変えたものであり、グラフの方がより速い
回転であつた。しかし、定量性については、いず
れのグラフもほぼ直線上に進行していることから
も判るように共に安定した経時定量供給、排出で
あつたことを示している。
Figure 3 shows the experimental results of this example. The raw material titanium oxide had an average particle size of 0.5 microns.
The powder is extremely cohesive, and can be fed and discharged in a short time using both the conventional table feeder as shown in FIG. It has become impossible. In this graph (in the graph in the figure), the horizontal axis shows the elapsed time (minutes), and the vertical axis shows the integrated value (grams) of the amount of supply and discharge. The rotation speed of the chisel was changed, and the rotation speed of the graph was faster. However, in terms of quantitative performance, as can be seen from the fact that both graphs progressed almost linearly, it was shown that the supply and discharge were stable over time.

〔別実施例〕[Another example]

他の実施例として、前記排出筒4の回転方向を
周期的、あるいは間欠的に反転させて内部の原料
に揺振りを与えたり、排出筒4の形状を下方に向
つてややすそ拡がりにするなどの対応も粉接部を
滑らかにしたり、材料を付着性が少く静電気を帯
びにくいものにするなどの対策とも併わせ本発明
の効果をより引き出す上で有効である。また、ス
ペーサ2の形状、及び排出筒4駆動部の構造や取
付支持方法については、機構の筒潔化やコンパク
ト化など使用条件に即した種々の設計変更が加え
られるものである。たとえば、第4図に示すよう
に排出筒4に回転力を伝えるベルト6′を二つの
回転軸8a′,8b′と受け車輪7′に加えてテンシ
ヨンプーリ19を設け、二つの受け車輪7′間に
おいて排出筒4をベルト6′に押し当て、排出筒
4の反対側から押し車20、アーム21、バネ2
2とよりなる押圧部材を以つて保持させてもよ
く、この場合には排出筒4の脱着がワンタツチで
行え、保守点検、掃除面での筒便さを進めた構成
である。
As other embodiments, the direction of rotation of the discharge tube 4 may be reversed periodically or intermittently to shake the raw material inside, or the shape of the discharge tube 4 may be slightly expanded downward. These measures, along with measures such as smoothing the powder contact area and making the material less adhesive and less likely to be charged with static electricity, are effective in bringing out the effects of the present invention even more. Furthermore, various design changes may be made to the shape of the spacer 2 and the structure and attachment/support method of the drive section of the discharge tube 4 in accordance with usage conditions, such as making the mechanism more compact and compact. For example, as shown in FIG. 4, a belt 6' that transmits rotational force to the discharge tube 4 is attached to two rotating shafts 8a', 8b' and a receiving wheel 7', and a tension pulley 19 is provided. ', press the discharge tube 4 against the belt 6', and then push the push wheel 20, arm 21, and spring 2
2 may be used to hold the discharge tube 4. In this case, the discharge tube 4 can be attached and detached with a single touch, making maintenance, inspection, and cleaning more convenient.

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

第1図及び第2図は本発明の一実施例を示す要
部断面図、第3図は本実施例における実験結果を
示したグラフ、第4図は第2図における要部を示
す他の実施例、第5図は従来例をそれぞれ示した
ものである。 図において、1……回転テーブル、2……スペ
ーサ、3……切欠き溝、4……排出筒、5……弾
性板片、10……スクレパ部、11……原料ホツ
パ、18……下方開口である。
1 and 2 are cross-sectional views of essential parts showing one embodiment of the present invention, FIG. 3 is a graph showing experimental results in this embodiment, and FIG. 4 is a cross-sectional view of the main parts of FIG. The embodiment and FIG. 5 each show a conventional example. In the figure, 1...rotary table, 2...spacer, 3...notch groove, 4...discharge tube, 5...elastic plate piece, 10...scraper section, 11...raw material hopper, 18...downward It is an opening.

Claims (1)

【特許請求の範囲】 1 回転テーブル1の回転の中心よりはずれた上
方位置に原料ホツパ11を配し、該ホツパ11の
下方開口18に対して該ホツパ11とは別に排出
筒4を嵌合接続させると共に、該排出筒4と回転
テーブル1上面との間隔を保持し、回転テーブル
1の回転方向側に開口した切欠き溝3を有するス
ペーサ2を具備させ、排出筒4を回転テーブル1
とは別個に回転させるように構成させたことを特
徴とする粉粒体用テーブルフイーダ。 2 前記スペーサ2は回転テーブル1の回転の中
心に対し、排出筒4下部切欠き溝3より円周に沿
つた曲面部aと、スクレパ部10とを具備してな
る前記特許請求の範囲第1項記載の粉粒体用テー
ブルフイーダ。 3 前記排出筒4内下部には、一又は複数の弾性
板片5が一端を固定、他端を自由として付設され
ている前記特許請求の範囲第1項記載の粉粒体用
テーブルフイーダ。
[Claims] 1. A raw material hopper 11 is arranged above the center of rotation of the rotary table 1, and a discharge tube 4 is fitted and connected to the lower opening 18 of the hopper 11 separately from the hopper 11. At the same time, a spacer 2 is provided to maintain the distance between the discharge tube 4 and the upper surface of the rotary table 1, and has a notch groove 3 opened on the rotation direction side of the rotary table 1.
A table feeder for powder and granular materials, characterized in that it is configured to be rotated separately from the table feeder. 2. The spacer 2 has a curved surface portion a extending along the circumference from the lower notch groove 3 of the discharge tube 4 with respect to the center of rotation of the rotary table 1, and a scraper portion 10. Table feeder for powder and granular materials as described in Section 1. 3. The table feeder for powder and granular material according to claim 1, wherein one or more elastic plate pieces 5 are attached to the inner lower part of the discharge tube 4 with one end fixed and the other end free.
JP10075684A 1984-05-18 1984-05-18 Table feeder for powdery and granular material Granted JPS60244715A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10075684A JPS60244715A (en) 1984-05-18 1984-05-18 Table feeder for powdery and granular material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10075684A JPS60244715A (en) 1984-05-18 1984-05-18 Table feeder for powdery and granular material

Publications (2)

Publication Number Publication Date
JPS60244715A JPS60244715A (en) 1985-12-04
JPH0132129B2 true JPH0132129B2 (en) 1989-06-29

Family

ID=14282358

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10075684A Granted JPS60244715A (en) 1984-05-18 1984-05-18 Table feeder for powdery and granular material

Country Status (1)

Country Link
JP (1) JPS60244715A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2599722B1 (en) * 1986-06-06 1989-10-20 Prady Max AUTOMATIC DISPENSER OF A DOSED QUANTITY OF A GRANULAR MATERIAL
JP2022163884A (en) * 2021-04-15 2022-10-27 アルファ株式会社 Compounding equipment

Also Published As

Publication number Publication date
JPS60244715A (en) 1985-12-04

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