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JP2653531B2 - Method and apparatus for supplying powder and granules - Google Patents
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JP2653531B2 - Method and apparatus for supplying powder and granules - Google Patents

Method and apparatus for supplying powder and granules

Info

Publication number
JP2653531B2
JP2653531B2 JP1321537A JP32153789A JP2653531B2 JP 2653531 B2 JP2653531 B2 JP 2653531B2 JP 1321537 A JP1321537 A JP 1321537A JP 32153789 A JP32153789 A JP 32153789A JP 2653531 B2 JP2653531 B2 JP 2653531B2
Authority
JP
Japan
Prior art keywords
granular material
rotating disk
powder
storage tank
opening
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 - Fee Related
Application number
JP1321537A
Other languages
Japanese (ja)
Other versions
JPH03182412A (en
Inventor
信男 荒木
俊一 菊田
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.)
NITSUTETSU YOSETSU KOGYO KK
Original Assignee
NITSUTETSU YOSETSU KOGYO KK
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 NITSUTETSU YOSETSU KOGYO KK filed Critical NITSUTETSU YOSETSU KOGYO KK
Priority to JP1321537A priority Critical patent/JP2653531B2/en
Publication of JPH03182412A publication Critical patent/JPH03182412A/en
Application granted granted Critical
Publication of JP2653531B2 publication Critical patent/JP2653531B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • 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] この発明は、粉粒体の連続供給の定量化、とりわけ
“瞬時”における流量の一定化を達成する粉粒体の供給
方法と装置に関する。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for supplying a granular material for quantifying the continuous supply of the granular material, and in particular, for stabilizing the flow rate instantaneously.

[従来の技術] 産業機械の高速化、直結化、ノンストップ化に伴っ
て、粉粒体の供給に係る要求も一段と高度なものにな
り、供給量(重量)の一定化では、従来の数秒間での一
定供給保証から1/10秒あるいは1/100秒の時間における
瞬時一定供給保証が求められるようになってきた。
[Prior art] With the increase in speed, direct connection, and non-stop of industrial machines, the demands related to the supply of powder and granules have become even more sophisticated. From a constant supply guarantee in seconds, an instantaneous constant supply guarantee in 1/10 second or 1/100 second time has been required.

本発明の利用分野は、以下に述べる溶接用粉粒体入り
ワイヤの製造に限るものではなく粉粒体の定重量供給性
がを要求される分野であれば利用することができる。以
下に粉粒体のて定重量供給性がとりわけ厳しく求められ
る分野の一つである溶接用粉粒体入りワイヤの製造を例
に説明する。
The field of application of the present invention is not limited to the production of wires containing powdered particles for welding described below, but can be used in fields where constant weight supply of powdered particles is required. Hereinafter, the manufacture of a wire containing a powdered material for welding, which is one of fields in which constant weight supply of powdered material is particularly strictly required, will be described as an example.

溶接用粉粒体入りワイヤは、金属帯(フープ)をこれ
の長手方向に送りながら管状に成形する過程で、長手方
向に沿って延びる開口から粉粒体を供給し、前記開口の
相対するエッジ面を高周波誘導溶接等で溶接するか、折
り曲げ加工で成形した後、所望の径に縮径し巻き取って
製品としている。
In the process of forming a tubular shape while feeding a metal band (hoop) in the longitudinal direction thereof, the wire containing the granular material for welding supplies the granular material from an opening extending along the longitudinal direction, and opposes the edge of the opening. The surface is welded by high-frequency induction welding or the like or formed by bending, then reduced to a desired diameter and wound up to obtain a product.

現在最も進んだ製造方法では、上記の製造工程が、連
続直結しており、その速度は粉粒体を供給し、開口のエ
ッジ面の溶接をして略1インチの粉粒体入り充填管とす
る工程で毎分30〜40mである。この略1インチの粉粒体
入り充填管は、溶接用ワイヤとするため外径が1.2mm程
度まで縮径して製品化されるが、この溶接用粉粒体入り
ワイヤは製品である溶接用ワイヤの全長にわたって充填
率を均一化し、もって溶接品質の均一化を確保する。
In the most advanced manufacturing method at present, the above-mentioned manufacturing process is directly connected, and the speed is such that the granular material is supplied, and the edge surface of the opening is welded to form an approximately 1-inch granular material-filled tube. 30 to 40m per minute in the process. This approximately 1-inch filled powder-filled tube is reduced to an outer diameter of about 1.2 mm in order to be used as a welding wire, and is commercialized. This welding powder-filled wire is a product for welding. Uniform filling rate over the entire length of the wire to ensure uniform welding quality.

この粉粒体と外皮金属との割合である充填率は、単位
ワイヤ長さにおいて充填した粉粒体の重量を金属外皮と
粉粒体の重量の和で除した百分率で定義され、実際の充
填率をもって保証の根拠とする。
The filling ratio, which is the ratio between the powder and the shell metal, is defined as a percentage obtained by dividing the weight of the powder and the metal shell by the sum of the weight of the metal shell and the powder at a unit wire length. The rate shall be the basis of the guarantee.

例えば、1.2mmの外径のワイヤ1mで、充填率を12.0±
1.0%としたとき、外径22mm、肉厚2.0mmの開口した管に
管速度30m/minで粉粒体を充填する場合、時間で1/100
秒、管長で6mm以上の精度で充填率を管理していかねば
ならないことになる。
For example, with a wire of 1.2 mm outside diameter, the filling rate is 12.0 ±
When 1.0% is set, when filling a granular material at a pipe speed of 30 m / min into an open pipe having an outer diameter of 22 mm and a wall thickness of 2.0 mm, the time is 1/100
The filling rate must be controlled with an accuracy of 6 mm or more in seconds and pipe length.

従って、かかる要求を達成するため、従来から瞬時に
おける粉粒体の一定量供給方法が、数多く提案され、供
されてきたが、大別すると、二つの方法に分類される。
Therefore, in order to achieve such demands, a number of methods for instantaneously supplying a fixed amount of powder and granules have been proposed and provided, but they are roughly classified into two methods.

第一の方法は、直接供給重量値を検出して、装置を制
御して目標値に供給値を近づける方法があるが、信号処
理は瞬時に刻々供給重量値を検出して供給装置に制御信
号を発信できるが、その信号に応答する供給装置が、駆
動等機械系の応答遅れ等により制御遅れを生じて追従不
可能のため、前記溶接用粉粒体入りワイヤの製造に供さ
れる粉粒体供給装置としては、ラフすぎて均一な充填率
が保証できないという問題を生じた。
The first method is to directly detect the supply weight value and control the apparatus to bring the supply value closer to the target value.However, the signal processing instantaneously detects the supply weight value instantaneously and sends a control signal to the supply apparatus. However, since the supply device responding to the signal cannot follow up due to a control delay due to a response delay of a mechanical system such as a drive, the powder used for manufacturing the wire containing the powdered particles for welding is used. As a body supply device, there was a problem that it was too rough to guarantee a uniform filling rate.

第二の方法は、容積を一定にして供給することで供給
重量の一定化を図る方法、すなわち、スクリューフィー
ダ、オーガフィーダ、シリンダーとピストンによる往復
動フィーダでは粉粒体を一定の容積にする過程、その後
これを送り出す過程で粉粒体の密度が高くなる圧密化が
生じ、送り出す粉粒体の体積は変わらないが供給重量か
らみると変動が生じ、これもまた粉粒体の一定重量供給
は難があった。さらに、定容積フィーダに第4図に示す
ような上部の貯槽26に粉粒体7を貯蔵し、貯槽26の底板
開孔部から直下のモータ22により回転する円盤21に連続
して粉粒体7を落下堆積させた後、円盤の外周方向にス
クレーパ25により掻き取ってシュート23を経て供給する
テーブルフィーダがあり、粉粒体供給装置では最も定重
量供給性の良好なフィーダの一つであるが、前記溶接用
粉粒体入りワイヤの製造に供される粉粒体供給装置とし
てはこれも以下に述べるような問題があった。
The second method is a method of stabilizing the supply weight by supplying a constant volume, that is, a process of making a granular material a constant volume with a screw feeder, an auger feeder, a reciprocating feeder with a cylinder and a piston. Then, in the process of sending out the powder, the density of the granules increases and the consolidation occurs, and the volume of the granules to be sent out does not change, but the fluctuation occurs in terms of the supplied weight. There was difficulty. Further, the granular material 7 is stored in an upper storage tank 26 as shown in FIG. 4 in a constant volume feeder, and the granular material 7 is continuously connected to a disk 21 which is rotated by a motor 22 directly below a bottom plate opening of the storage tank 26. There is a table feeder which, after dropping and depositing 7, is scraped off by a scraper 25 in the outer circumferential direction of the disk and supplied through a chute 23, and is one of the feeders having the best constant weight supply in the powder and granular material supply apparatus. However, the powder and granular material supply device used for manufacturing the wire with the powder and granular material for welding also has the following problems.

[発明が解決しようとする課題] 先ず、粉粒体の定重量供給性の評価方法と粉粒体の流
量の実測方法について述べる。
[Problems to be Solved by the Invention] First, a method for evaluating the constant weight supply property of a granular material and a method for actually measuring the flow rate of the granular material will be described.

第5図は一般的な粉粒体の供給状態を縦軸に重量、横
軸に時間をとって表したものである。
FIG. 5 shows the state of supply of general powder and granular material, with the vertical axis representing weight and the horizontal axis representing time.

いずれも測定時間T秒間において Wmax:測定サイクル1/100秒毎に実測した時の最大供給重
量(g/0.01sec) Wmin:測定サイクル1/100秒毎に実測した時の最小供給重
量(g/0.01sec) Wave:測定サイクル1/100秒毎に実測した時の各供給重量
の単純平均値(g/0.01sec) とした時、次式で示す定量性指数Fで粉粒体の定重量供
給性の評価を行った。
In any case, in the measurement time T seconds, W max : the maximum supply weight when actually measured every 1/100 second of the measurement cycle (g / 0.01 sec) W min : the minimum supply weight when actually measured every 1/100 second of the measurement cycle ( g / 0.01sec) W ave: when the simple average of the supply weight when measured for every measurement cycle 1/100 seconds and (g / 0.01sec), a quantitative index F shown by the following formula granule The constant weight supply property was evaluated.

F=(Wmax−Wmin)/Wave×100 (%) 次に、粉粒体の流量の実測は、第6図の装置を用い
た。粉粒体供給装置aから、排出された粉粒体bを傾斜
測定板cに一旦あてて、その時の衝突力を定格荷重3kg
のロードセルdで1/100秒の測定サイクルで80秒間連続
してコンバータeを介してアナライジングレコーダfに
測定記録した。なお、測定板cは板面上に粉粒体が付着
せず、整流された状態で流下するよう表面をテフロンコ
ーティングをし、60度に傾斜させた。またロードセルの
偏心荷重の影響に対しては、偏心150mmで定格荷重の50
%を負荷した時のエラーが、0.02%R.0以内のものを使
用した。そこで、主要な成分がルチールで第1表に示し
た粒度分布の充填乾燥した溶接用フラックス(粉粒体)
を用い従来の最も定重量供給性の良好な粉粒体供給装置
である第4図に示すテーブルフィーダを用いて、0.83g/
0.01secの供給速度で実際の供給重量を調べた結果、こ
の従来のテーブルフィーダ方式では次のような問題点が
あった。
F = (W max -W min) / W ave × 100 (%) Next, the measured flow rate of the particulate material used was an apparatus FIG. 6. The granular material b discharged from the granular material supply device a is once applied to the inclination measuring plate c, and the collision force at that time is rated at 3 kg.
The measurement was recorded on the analyzing recorder f via the converter e for 80 seconds in a 1/100 second measurement cycle using the load cell d. The surface of the measurement plate c was coated with Teflon so that the powder did not adhere to the plate surface and flowed down in a rectified state, and was inclined at 60 degrees. In addition, for the effect of the eccentric load of the load cell,
The error when loading% was within 0.02% R.0. Therefore, the main component is rutile, and the filled and dried welding flux (granule) having the particle size distribution shown in Table 1
Using a table feeder shown in Fig. 4 which is a conventional powder feeder with the best constant weight feedability,
As a result of examining the actual supply weight at a supply speed of 0.01 sec, the conventional table feeder method has the following problems.

すなわち、第7図に示すように、重量の変動は、定量
性指数Fで46.1%で、瞬時の供給重量の変動幅(最大値
と最小値の差)が大きい。そこで本発明者らは、供給容
積と供給重量の関係を詳細に調べた結果、容積の変動は
ごく僅かであり、供給重量のみが大きく変動しているこ
とを知見した。この変動幅は粉粒体7の粉圧が回転円盤
21に堆積される時粉圧の影響を受け圧密化を生じ粉粒体
密度が高くなったことが最も大きな原因であるとの結論
に達した。言い換えれば、粉粒体の粉圧の影響を減少さ
せる目的で上部貯槽を設けたが、従来の方法および装置
では瞬時における供給重量の一定かを達成することはで
きないことが判った。
That is, as shown in FIG. 7, the change in weight is 46.1% in the quantitativeness index F, and the fluctuation width of the instantaneous supply weight (difference between the maximum value and the minimum value) is large. Then, the present inventors have examined the relationship between the supply volume and the supply weight in detail, and as a result, have found that the change in the volume is very small and only the supply weight fluctuates greatly. The range of this variation is that the powder pressure of the powder
It was concluded that the greatest cause was that the compaction was caused by the influence of the powder pressure when deposited on 21 and the density of the granular material was increased. In other words, although the upper storage tank is provided for the purpose of reducing the influence of the powder pressure of the granular material, it has been found that the conventional method and apparatus cannot achieve a constant supply weight instantaneously.

そこで、本発明は、精度の高い瞬時レベルの定重量供
給を可能とする方法および装置を提供しようとするもの
である。
Accordingly, an object of the present invention is to provide a method and an apparatus which enable a highly accurate instantaneous level constant weight supply.

[課題を解決するための手段] この発明の粉粒体の供給方法は、上部の貯槽の底板開
孔部から下方の回転する円盤に連続して粉粒体を落下堆
積させた後、回転円盤の堆積面に堆積した粉粒体の上部
を略水平にすり切り、粉粒体を回転円盤の外周方向に掻
き取って排出する粉粒体の供給方法において、上部の貯
槽の底板開孔部より予め設定した堆積高さとなるように
落下量を調整しながら、底板開孔部直下から回転円盤の
堆積面に向かって傾斜する傾斜面に粉粒体を落下させ、
傾斜面を滑落させて圧密化した粉粒体を分散、平均化し
て回転円盤に供給することを特徴としている。
[Means for Solving the Problems] According to the method for supplying a granular material of the present invention, the granular material is dropped and deposited continuously from a bottom plate opening of an upper storage tank to a rotating disk below, and then the rotating disk is rotated. In the method of supplying the granular material which is substantially horizontally scraped off the upper part of the granular material deposited on the accumulation surface of the rotating disk, the granular material is scraped in the outer peripheral direction of the rotating disk and discharged, While adjusting the amount of fall so as to reach the set stacking height, the powder and granules are dropped from directly below the bottom plate opening on the inclined surface inclined toward the stacking surface of the rotating disk,
The method is characterized in that the compacted powdery material by sliding down the inclined surface is dispersed, averaged and supplied to the rotating disk.

また本発明の粉粒体の供給装置は、上部の貯槽の底板
開孔部から下方の回転する円盤に連続して粉粒体を落下
堆積させた後、回転円盤の外周方向に掻き取って排出す
る粉粒体の供給装置において、粉粒体を開孔部に掻き寄
せるアジテータを具備した貯槽と、前記開孔部の直下に
あって傾斜角度調整自在の粉粒体を案内して整流する傾
斜板と該傾斜板の下方に配設され、堆積面を有する回転
円盤と、該堆積面の粉粒体の堆積高さの検知器と該検知
器の出力信号で上部の貯槽のアジテータの回転数を増減
する駆動制御装置と回転円盤の外周に固定して設けた交
換自在の外周ガイドと堆積した粉粒体の上部を略水平に
すり切るカッターと、すり切った粉粒体を回転円盤の外
周方向に掻き取るスクレーパで構成したことを特徴とす
る。
Further, the powder and granular material supply device of the present invention continuously drops and deposits the powder and granular material from the bottom plate opening of the upper storage tank to the rotating disk below, and scrapes and discharges the powder to the outer peripheral direction of the rotating disk. In a supply device for a granular material, a storage tank provided with an agitator that rakes the granular material to an opening portion, and a slope that guides and regulates a granular material that is directly under the opening portion and that can adjust an inclination angle. A rotating disk disposed below the plate and the inclined plate and having a stacking surface, a detector for detecting the height of the granular material deposited on the stacking surface, and the number of rotations of the agitator in the upper storage tank based on an output signal of the detector A drive control device for increasing or decreasing the diameter, a replaceable outer guide fixed to the outer periphery of the rotating disk, a cutter for cutting the upper portion of the accumulated powder substantially horizontally, and an outer periphery of the rotating disk for the worn powder It is characterized by comprising a scraper that scrapes in the direction.

上部貯槽の底板開孔部から落下させる粉体量は、堆積
面の堆積高さで調整され、当該堆積高さを検知し設定量
を上回った時は、アジテータの回転数を減少あるいは停
止させ、下回ったときは回転数を増加させて常に設定範
囲内の堆積高さになるようにしている。
The amount of powder dropped from the bottom plate opening of the upper storage tank is adjusted by the accumulation height of the accumulation surface, and when the accumulation height is detected and exceeds the set amount, the rotation speed of the agitator is reduced or stopped, When it falls below, the number of rotations is increased so that the deposition height is always within the set range.

堆積高さの設定範囲は、すり切る厚さを超える高さで
あって余剰高さが最小限である方がより好ましい結果が
得られる。
A more preferable result is obtained when the set range of the deposition height is a height exceeding the worn thickness and the surplus height is minimized.

また、貯槽の底板は粉粒体の目標供給量、性状、粒度
構成等で適宜開孔部口径の異なった底板に交換する。ま
た、上部の貯槽の底板開孔部の直下には、傾斜角度調整
自在の粉粒体を案内して整流する傾斜板を設け、粉粒体
を傾斜面に向けて落下させるが、傾斜面は粉粒体が整流
状態で滑らかに滑落し、しかも付着しにくい表面、例え
ばテフロンコーティング処理した表面とする。また、傾
斜角度は粉粒体の目標供給量、性状、粒度構成等で調整
する。供給量の変更は、回転円盤の回転が独立変速駆動
であるため回転速度の変更で通常行い、必要により粉粒
体の堆積高さまたは幅あるいはその両者の変更で行う。
Further, the bottom plate of the storage tank is appropriately replaced with a bottom plate having a different opening diameter depending on the target supply amount, properties, particle size configuration, and the like of the granular material. Immediately below the bottom plate opening of the upper storage tank, there is provided an inclined plate for guiding and rectifying the particles whose tilt angle can be adjusted, and the particles are dropped toward the inclined surface. The surface is such that the powder particles smoothly slide down in a rectified state and hardly adhere thereto, for example, a surface treated with Teflon coating. Further, the inclination angle is adjusted by the target supply amount, the property, the particle size configuration, and the like of the granular material. The change of the supply amount is usually performed by changing the rotation speed because the rotation of the rotating disk is an independent speed change drive, and is performed by changing the accumulation height and / or width of the granular material as necessary.

[作用] 上部の貯槽に貯蔵した粉粒体を、回転円盤の堆積面の
レベルに応じて貯槽底板の開孔部より直下の傾斜面に向
けて落として斜面を滑落流下させた後、回転円盤の堆積
面に堆積させ、堆積した粉粒体の上面をすり切って、さ
らに円盤外周方向に掻き取って排出供給する。
[Action] The powder and granules stored in the upper storage tank are dropped toward the inclined surface immediately below the opening of the storage tank bottom plate according to the level of the accumulation surface of the rotating disk, and the slope is slid down, and then the rotating disk And the upper surface of the deposited powder is scraped off and further scraped in the outer peripheral direction of the disk to discharge and supply.

すなわち、上部の貯槽で貯蔵時に圧密化を生じた粉粒
体であっても開孔部から落下して傾斜面に当たり滑落す
る過程で粉粒体の分散化、平均化が行われる。さらに滑
落した粉粒体は、堆積高さが規制されるため粉圧の影響
が殆ど無視でき、そのままの状態ですり切られてスクレ
ーパで排出供給されるため、供給された粉粒体は密度変
化が極めて少ないものとなる。従って、供給される粉粒
体の瞬時における定重量供給性が、飛躍的に向上する。
That is, even in the case of a granular material that has been compacted during storage in the upper storage tank, the granular material is dispersed and averaged in the process of falling from the opening and sliding down the inclined surface. In addition, the impact of the powder pressure can be almost ignored because the height of the deposited granules is regulated, and it is cut off as it is and discharged and supplied by a scraper. Is extremely small. Therefore, the constant-weight supply property of the supplied granular material at a moment is dramatically improved.

[実施例] 以下本発明を溶接用粉粒体入りワイヤの製造に適用し
た場合の実施例を説明する。
[Example] Hereinafter, an example in which the present invention is applied to the production of a wire containing a powdered material for welding will be described.

第2図はワイヤ製造装置の主要部の構成図、第1A図は
本発明の装置の一実施例を示す縦断面図である。
FIG. 2 is a structural view of a main part of the wire manufacturing apparatus, and FIG. 1A is a longitudinal sectional view showing one embodiment of the apparatus of the present invention.

第2図に示すように、管1の送り方向に沿って成形ロ
ール群2aが順次配列されている。成形ロール2aの間に粉
粒体供給装置3が配置されている。溶接位置では、高周
波電流をワークコイル5に流し、管1に誘導電流を生じ
させ、スクイズロール4により加熱溶接する。溶接され
た管1は縮径ロール2bにより所望径に縮径される。
As shown in FIG. 2, forming roll groups 2a are sequentially arranged along the feeding direction of the tube 1. The powder supply device 3 is arranged between the forming rolls 2a. At the welding position, a high-frequency current is applied to the work coil 5 to generate an induced current in the tube 1, and the tube 1 is heated and welded by the squeeze roll 4. The welded pipe 1 is reduced in diameter to a desired diameter by a diameter reducing roll 2b.

第1A図に示すように粉粒体供給装置3は、上部の貯槽
6に粉粒体7を貯蔵し、かつ該貯槽6の底板6aには孔径
20mmの開孔部6bを設けている。
As shown in FIG. 1A, the granular material supply device 3 stores the granular material 7 in an upper storage tank 6 and a bottom plate 6a of the storage tank 6 having a hole diameter.
An opening 6b of 20 mm is provided.

一方、上部の貯槽6の粉粒体7を開孔部6bに掻き寄せ
るアジテータ8は、無段階変速モータ9によって独立し
て0〜20RPMで堆積面11aの堆積高さに応じて無段階に変
速回転し、粉粒体7を開孔部6bに掻き寄せる。第1B図は
アジテータ8の平面図である。開孔部6bの下方には、滑
らかな傾斜面を持つ粉粒体を案内する傾斜板10と、傾斜
板10を経て落下した粉粒体7の堆積面11aを有し無段階
変速モータ12によって他に独立して回転する回転円盤11
が配置されている。第1C図は回転円盤11の平面図であ
る。傾斜板10に対して堆積面11aが谷になるよう回転円
盤11の外周に外周ガイド13が設けられている。落下した
粉粒体は、傾斜板10の斜面を滑落して谷となる堆積面11
aに堆積される。堆積した粉粒体の高さをレベル検知器1
7(例えば静電容量形)で検知してレベル信号を発信
し、そのレベル信号に基づき制御器18を介してアジテー
タ8の回転数を増減させることで粉粒体の落下量を制御
する。堆積面11aの回動により、粉粒体はその上面をカ
ッター14ですり切られ、さらに回動してスクレーパ15で
掻き出されてシュート16を介して成形途中の管1の谷部
へ供給される。
On the other hand, the agitator 8 which rakes the granular material 7 in the upper storage tank 6 toward the opening 6b is independently steplessly shifted by a stepless speed change motor 9 at 0 to 20 RPM according to the height of the stacking surface 11a. Then, the powder 7 is swept up to the opening 6b. FIG. 1B is a plan view of the agitator 8. Below the opening 6b, there is provided an inclined plate 10 for guiding a granular material having a smooth inclined surface, and a deposition surface 11a of the granular material 7 dropped through the inclined plate 10, and has a stepless speed-change motor 12. Rotating disk 11 that rotates independently
Is arranged. FIG. 1C is a plan view of the rotating disk 11. FIG. An outer periphery guide 13 is provided on the outer periphery of the rotating disk 11 so that the accumulation surface 11a becomes a valley with respect to the inclined plate 10. The fallen granular material slides down the slope of the inclined plate 10 and forms a valley.
deposited on a. Level detector 1 detects the height of the deposited powder
7 (for example, a capacitance type), a level signal is transmitted, and the number of rotations of the agitator 8 is increased / decreased via the controller 18 based on the level signal, thereby controlling the amount of the granular material falling. Due to the rotation of the stacking surface 11a, the granular material is cut off by the cutter 14 on its upper surface, further rotated and scraped off by the scraper 15, and supplied to the valley of the tube 1 being formed via the chute 16. You.

ここで、以上のように構成された本発明の装置により
製造した溶接用粉粒体入りワイヤの製造結果について説
明する。
Here, a description will be given of the result of manufacturing the welding wire containing the granular material for welding manufactured by the apparatus of the present invention configured as described above.

鋼フープ材を外径22.0mm、肉厚2.2mm、管送り速度30m
/minで管に成形した。成形途中で前記第1表に示す粉粒
体を目標充填率12.0±1.0%で充填した。供給速度を0.8
3g/0.01sec、アジテータ回転数を6RPM、上部貯槽の粉粒
体の貯蔵量を160kgとし、回転円盤の回転数を30RPMと
し、堆積高さ30〜50mm、すり切り高さ10mm、すり切り幅
20mmとした。また、供給重量の変動の検出は第6図の粉
粒体の流量実測装置を使い、測定板すなわちシュートか
ら流れた粉粒体を直接成形途中の管1の谷部へ供給し
た。ロードセルdからの出力信号は、コンバータeを介
して分解能1/100秒のアナライジングレコーダfに接続
し、80秒間にわたって連続測定した。
Steel hoop material with outer diameter 22.0mm, wall thickness 2.2mm, pipe feed speed 30m
The tube was molded at a rate of / min. During the molding, the powders shown in Table 1 were filled at a target filling rate of 12.0 ± 1.0%. Feed rate 0.8
3g / 0.01sec, the agitator rotation speed is 6RPM, the storage amount of the granular material in the upper storage tank is 160kg, the rotation speed of the rotating disk is 30RPM, the pile height is 30 ~ 50mm, the cutting height is 10mm, the cutting width
20 mm. The fluctuation of the supply weight was detected by using the apparatus for measuring the flow rate of the granular material shown in FIG. 6, and the granular material flowing from the measuring plate, that is, the chute, was directly supplied to the valley of the pipe 1 during the molding. The output signal from the load cell d was connected to an analyzing recorder f having a resolution of 1/100 second via a converter e, and continuously measured for 80 seconds.

またWmax、Wmin、Waveは、当該アナライジングレコー
ダfで演算し、その結果に基づき定量性指数Fを出し
た。
W max , W min , and Wave were calculated by the analyzing recorder f, and a quantitative index F was obtained based on the result.

粉粒体の供給結果を第3図に、充填した管の充填率測
定結果を第2表に示す。
FIG. 3 shows the supply results of the powder and granules, and Table 2 shows the measurement results of the filling rate of the filled tubes.

第3図から明らかなように、定量性指数Fは、従来の
方法によれば46.1%であったが、本発明では、25.7%と
なり、飛躍的に向上したことがわかる。また、供給状態
は、第3図からわかるように変動幅が小さくなり、極め
て安定した供給状態であることが実証された。
As is clear from FIG. 3, the quantitativeness index F was 46.1% according to the conventional method, but was 25.7% according to the present invention, which is a dramatic improvement. Further, as can be seen from FIG. 3, the supply state has a small fluctuation range, and it has been proved that the supply state is extremely stable.

さらに、充填した管の充填率測定結果は、目標の充填
率(12.0±1.0%)に対して従来の10.7〜13.8%と目標
の充填率を外れるものがでていたが、本発明によって1
1.5〜12.8%と全てが目標の充填率(12.0±1.0%)の範
囲に入っていることが確認された。
Furthermore, the result of measuring the filling rate of the filled pipes shows that the target filling rate (12.0 ± 1.0%) was out of the target filling rate of 10.7 to 13.8%, which was the conventional value.
It was confirmed that all of 1.5 to 12.8% were within the range of the target filling rate (12.0 ± 1.0%).

[発明の効果] この発明によれば、粉粒体の供給において粉粒体の圧
密化を防止し、容積と密度を一定に保って切出し供給を
行うことで、1/100秒の瞬時においても粉粒体重量の一
定供給化を達成しうる。本発明の粉粒体の供給方法およ
び装置を利用して製造された溶接用粉粒体入りワイヤの
充填率は目標充填率(12.0±1.0%)の範囲に収めるこ
とが可能となり極めてバラツキの少ない安定したワイヤ
となる。
[Effects of the Invention] According to the present invention, the compaction of the granular material is prevented in the supply of the granular material, and the cutout supply is performed while keeping the volume and the density constant, so that even in the instant of 1/100 second, A constant supply of the weight of the granular material can be achieved. The filling rate of the welding wire containing the granular material for welding manufactured by using the method and the apparatus for supplying the granular material of the present invention can be kept within the range of the target filling rate (12.0 ± 1.0%), and the dispersion is extremely small. It becomes a stable wire.

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

第1A図は本発明の装置の一実施例を示す縦断面図、第1B
図はアジテータの平面図、第1C図は回転円盤の平面図、
第2図は溶接用粉粒体入りワイヤの製造装置の主要部を
示す図、第3図は本発明の粉粒体供給装置による粉粒体
の供給状態を示す図、第4図は従来の粉粒体供給装置を
示す斜視図、第5図は一般的な粉粒体の供給状態を示す
図、第6図は粉粒体の流量実測装置、第7図は従来の粉
粒体供給装置による粉粒体の供給状態を示す図である。 1……管、3……粉粒体の供給装置、6,26……貯槽、7
……粉粒体、8……アジテータ、10……傾斜板、11,21
……回転円盤、13……外周ガイド、14……カッター、1
5,15……スクレーパ、16,23……シュート、17……レベ
ル検知器。
FIG. 1A is a longitudinal sectional view showing one embodiment of the apparatus of the present invention, FIG.
Figure is a plan view of the agitator, Figure 1C is a plan view of the rotating disk,
FIG. 2 is a view showing a main part of an apparatus for manufacturing a wire containing a powder for welding, and FIG. 3 is a view showing a state of supply of powder by a powder supply apparatus of the present invention, and FIG. FIG. 5 is a perspective view showing a granular material supply device, FIG. 5 is a view showing a general state of supplying granular material, FIG. 6 is a flow rate measuring device for granular material, and FIG. 7 is a conventional granular material supply device. It is a figure which shows the supply state of the granular material by. 1 ... pipe, 3 ... powder and granular material supply device, 6, 26 ... tank, 7
…… Powder and granules, 8 …… Agitator, 10 …… Slope plate, 11,21
…… Rotating disk, 13 …… Outer circumference guide, 14 …… Cutter, 1
5,15… Scraper, 16,23 …… Shoot, 17 …… Level detector.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】上部の貯槽の底板開孔部から下方の回転す
る円盤に連続して粉粒体を落下堆積させた後、回転円盤
の堆積面に堆積した粉粒体の上部を略水平にすり切り、
粉粒体を回転円盤の外周方向に掻き取って排出する粉粒
体の供給方法において、上部の貯槽の底板開孔部より予
め設定した堆積高さとなるように落下量を調整しなが
ら、底板開孔部直下から回転円盤の堆積面に向かって傾
斜する傾斜面に粉粒体を落下させ、傾斜面を滑落させて
圧密化した粉粒体を分散、平均化して回転円盤に供給す
ることを特徴とする粉粒体の供給方法。
After the particles are continuously dropped and deposited on a rotating disk below from an opening of a bottom plate of an upper storage tank, the upper part of the particles deposited on the deposition surface of the rotating disk is made substantially horizontal. Wear,
In the method of supplying the granular material, which scrapes the granular material in the outer circumferential direction of the rotating disk and discharges the material, the bottom plate is opened while adjusting the drop amount so as to have a predetermined deposition height from the bottom plate opening of the upper storage tank. The powder and granules are dropped on the inclined surface that is inclined from just below the hole toward the deposition surface of the rotating disk, and the inclined surface is slid down to disperse and consolidate the powdered particles, averaged and supplied to the rotating disk. The method of supplying the granular material.
【請求項2】上部の貯槽の底板開孔部から下方の回転す
る円盤に連続して粉粒体を落下堆積させた後、回転円盤
の外周方向に掻き取って排出する粉粒体の供給装置にお
いて、粉粒体を開孔部に掻き寄せるアジテータを具備し
た貯槽と、前記開孔部の直下にあって傾斜角調整自在の
粉粒体を案内して整流する傾斜板と、該傾斜板の下方に
配設され、堆積面を有する回転円盤と、該堆積面の粉粒
体の堆積高さの検知器と、該検知器の出力信号で上部の
貯槽のアジテータの回転数を増減する駆動制御装置と、
回転円盤の外周に固定して設けた交換自在の外周ガイド
と、堆積した粉粒体の上部を略水平にすり切るカッター
と、すり切った粉粒体を回転円盤の外周方向に掻き取る
スクレーパで構成したことを特徴とする粉粒体の供給装
置。
2. An apparatus for supplying a granular material which continuously drops and deposits a granular material from a bottom plate opening of an upper storage tank onto a rotating disk below, and scrapes and discharges the granular material in an outer peripheral direction of the rotating disk. In the above, a storage tank having an agitator that rakes the granular material to the opening, an inclined plate that is located immediately below the opening and guides and regulates the granular material having an adjustable inclination angle, and an inclined plate. A rotating disk disposed below and having a stacking surface, a detector for detecting the height of the granular material deposited on the stacking surface, and a drive control for increasing or decreasing the rotation speed of the agitator in the upper storage tank based on an output signal of the detector Equipment and
An exchangeable outer peripheral guide fixed to the outer periphery of the rotating disk, a cutter that cuts the upper part of the accumulated powder substantially horizontally, and a scraper that scrapes the worn powder toward the outer periphery of the rotating disk An apparatus for supplying a granular material, comprising:
JP1321537A 1989-12-13 1989-12-13 Method and apparatus for supplying powder and granules Expired - Fee Related JP2653531B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1321537A JP2653531B2 (en) 1989-12-13 1989-12-13 Method and apparatus for supplying powder and granules

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1321537A JP2653531B2 (en) 1989-12-13 1989-12-13 Method and apparatus for supplying powder and granules

Publications (2)

Publication Number Publication Date
JPH03182412A JPH03182412A (en) 1991-08-08
JP2653531B2 true JP2653531B2 (en) 1997-09-17

Family

ID=18133668

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1321537A Expired - Fee Related JP2653531B2 (en) 1989-12-13 1989-12-13 Method and apparatus for supplying powder and granules

Country Status (1)

Country Link
JP (1) JP2653531B2 (en)

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CN102430878A (en) * 2011-10-13 2012-05-02 天津市旭智机电设备开发有限公司 Powder adding machine
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Also Published As

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