JP3090555B2 - Quantitative feeder - Google Patents

Quantitative feeder

Info

Publication number
JP3090555B2
JP3090555B2 JP04329075A JP32907592A JP3090555B2 JP 3090555 B2 JP3090555 B2 JP 3090555B2 JP 04329075 A JP04329075 A JP 04329075A JP 32907592 A JP32907592 A JP 32907592A JP 3090555 B2 JP3090555 B2 JP 3090555B2
Authority
JP
Japan
Prior art keywords
rotating
disk
bottom plate
cylinder
outer cylinder
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
JP04329075A
Other languages
Japanese (ja)
Other versions
JPH06171765A (en
Inventor
修 吉川
秀男 森永
Original Assignee
修 吉川
吉川 博文
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 修 吉川, 吉川 博文 filed Critical 修 吉川
Priority to JP04329075A priority Critical patent/JP3090555B2/en
Publication of JPH06171765A publication Critical patent/JPH06171765A/en
Application granted granted Critical
Publication of JP3090555B2 publication Critical patent/JP3090555B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Special Conveying (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
  • Feeding Of Articles To Conveyors (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は粉粒体定量フィーダーに
おいて、流動性の良い粉粒体は勿論、流動性の悪い粉粒
体でも高精度での定量供給を実現したものであり、化
学、食品業界等粉粒体を扱う全ての分野で利用できる排
出装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a powdery material quantitative feeder which realizes high-precision quantitative supply of not only powders having good fluidity but also powders having poor fluidity. The present invention relates to a discharge device that can be used in all fields that handle powders such as the food industry.

【0002】[0002]

【従来の技術】従来の連続枡式定量フィーダーでは、流
動性の悪い粉粒体の場合、連続枡に充填することができ
ず使用できなかった。又なんとか充填できる粉粒体で
も、すり切りに固定刃を使っているために引掛って均一
なすり切りができず供給精度が悪かった。又このような
タイプのフィーダーは構造が複雑であり、クリーニング
が容易にできず難点となっていた。
2. Description of the Related Art In a conventional continuous-measuring-type fixed-quantity feeder, in the case of powder having poor fluidity, the continuous-measuring material cannot be filled and cannot be used. In addition, even powders that could be filled somehow could not be evenly cut because the fixed blade was used for cutting, and the supply accuracy was poor. In addition, such a type of feeder has a complicated structure, and cleaning is not easily performed, which is a drawback.

【0003】[0003]

【発明が解決しようとする課題】本発明は流動性の悪い
粉粒体であっても連続枡に収容でき、かつ円滑で連続均
一なすり切りが可能で供給精度良好な定量フィーダーが
得られ、かつ構造簡単で連続枡部のクリーニングが容易
な連続式定量フィーダーを得ることを目的とする。
SUMMARY OF THE INVENTION According to the present invention, even a powdery or granular material having poor fluidity can be accommodated in a continuous cell, and a smooth and continuous uniform cutting can be performed to obtain a fixed-quantity feeder with good supply accuracy. It is an object of the present invention to provide a continuous quantitative feeder having a simple structure and easy cleaning of a continuous measuring section.

【0004】[0004]

【課題を解決するための手段】上記の目的を達成するた
め本発明は中心線を共有する内外筒によって形成され、
外筒の底板と内筒の下端との間に間隙を有し、粉粒体の
輪状移送空間を内外筒間に設けてなり、底板の中心部に
突設した直立回転軸に設けた中央回転羽根の先端に外筒
の内周に沿って設けた外周回転リングを接続し、該リン
グには内部に向う複数の外周回転羽根を設けてなり、上
記移送空間から上記粉粒体を機外に排出する機構におい
て、上記底板の上面と同一平面内に上面を有する回転円
盤を設け、該円盤の上面に該円盤と同心円の粉粒体排出
溝を形成し、該溝が上記外筒の内外に亘って配設されて
なる定量フィーダー 外筒の外側において上記溝内に粉粒体排出スクレーパを
挿入してなる上記発明記載の定量フィーダー 上記外周回転リングの内周縁に刃先を形成し、上記輪状
移送空間において上記刃先によって上記粉粒体排出溝の
すり切りを行うよう形成した上記第1又は第2発明記載
の定量フィーダー 内筒の内面に粉粒体排出溝への粉粒体圧力を回避するバ
ッフルプレートを設けてなる上記第1、第2又は第3発
明にそれぞれ記載の定量フィーダー 中央回転羽根及び外周回転羽根の外端側が回転方向に向
って直径方向と交差してなる上記第1、第2、第3又は
第4発明にそれぞれ記載の定量フィーダー 上記回転円盤及びその支持装置を上記底板から着脱自在
に支持してなる上記第1、第2、第3、第4又は第5発
明にそれぞれ記載の定量フィーダーによって構成され
る。
In order to achieve the above object, the present invention is formed by inner and outer cylinders sharing a center line,
A center rotation provided on an upright rotating shaft protruding from the center of the bottom plate, with a gap between the bottom plate of the outer tube and the lower end of the inner tube, and a ring-shaped transfer space for the granular material provided between the inner and outer tubes. An outer peripheral rotating ring provided along the inner periphery of the outer cylinder is connected to the tip of the blade, and a plurality of outer peripheral rotating blades facing the inside are provided on the ring. In the discharging mechanism, a rotating disk having an upper surface in the same plane as the upper surface of the bottom plate is provided, and a powder discharge groove concentric with the disk is formed on the upper surface of the disk, and the grooves are formed inside and outside the outer cylinder. The fixed-quantity feeder according to the invention, in which a powdery material discharge scraper is inserted into the groove outside the outer cylinder, and a cutting edge is formed on the inner peripheral edge of the outer peripheral rotating ring, and the annular transfer is performed. In the space, the cutting edge of the powdery material is cut by the cutting edge. The first, second, or third baffle plate provided on the inner surface of the inner cylinder of the quantitative feeder according to the first or second aspect of the invention, the baffle plate avoiding pressure of the granular material to the granular material discharge groove. The quantitative feeder according to the first, second, third or fourth invention, wherein the outer end sides of the central rotating blade and the outer peripheral rotating blade intersect with the diametric direction in the rotational direction. It is constituted by the fixed-quantity feeder according to the first, second, third, fourth or fifth invention, wherein the rotating disk and its supporting device are detachably supported from the bottom plate.

【0005】[0005]

【作用】本発明では内筒1内に粉粒体eを投入し、直立
回転軸13を矢印a方向に回転させることによって中央
回転羽根11、外周回転リング8及び外周回転羽根12
を底板3の上面及び回転円盤4の上面に接して回転させ
ると同時に回転円盤4を矢印b方向に回転させる。
According to the present invention, the granular material e is charged into the inner cylinder 1 and the upright rotating shaft 13 is rotated in the direction of arrow a to thereby rotate the central rotating blade 11, the outer circumferential rotating ring 8 and the outer circumferential rotating blade 12.
Is rotated in contact with the upper surface of the bottom plate 3 and the upper surface of the rotating disk 4, and at the same time, the rotating disk 4 is rotated in the direction of arrow b.

【0006】このようにすると内筒1内の粉粒体eが上
記円盤4の上面の粉粒体排出溝6内を充満し、その状態
で該溝6は外筒2の内部から外部に回動し矢印a方向に
回転している外周回転リング8の内側縁による内側縁方
向への摺動すり切りが行われ、外筒2の外側で粉粒体e
を上記溝6から連続的に機外に取卸すことができる。
In this manner, the granular material e in the inner cylinder 1 fills the granular material discharge groove 6 on the upper surface of the disk 4, and in this state, the groove 6 is turned from the inside of the outer cylinder 2 to the outside. The inner peripheral edge of the outer peripheral rotating ring 8 rotating in the direction of the arrow a is slid in the inner peripheral direction, and the granular material e is disposed outside the outer cylinder 2.
Can be continuously taken out of the machine from the groove 6.

【0007】上記取卸しは外筒2の外側において上記溝
6内に挿入した排出スクレーパ7によって溝6外に排出
することができる。又上記すり切りは上記回転リング8
に形成した上記刃先8’の矢印a方向(刃先8’の方
向)への摺動によって行うことができる(恰も刀で物を
切るように)。
The unloading can be discharged out of the groove 6 by a discharge scraper 7 inserted into the groove 6 outside the outer cylinder 2. Also, the above-mentioned cutting is performed by using the rotating ring 8.
The cutting can be performed by sliding the cutting edge 8 'formed in the direction of arrow a (direction of the cutting edge 8') (just like cutting an object with a sword).

【0008】又内筒1内の粉粒体eの重量の影響による
上記溝6内への粉粒体eの圧密現象が認められる場合に
は内筒1の内面に設けたバッフルプレート10の下端か
ら安息角を形成して該プレート10の外側に排出される
粉粒体eを上記溝6内に供給し、かつ輪状移送空間9を
移送される粉粒体eを該溝6内に供給することができ
る。
If a compaction phenomenon of the granular material e into the groove 6 due to the influence of the weight of the granular material e in the inner cylinder 1 is observed, the lower end of the baffle plate 10 provided on the inner surface of the inner cylinder 1 The particles e formed at an angle of repose and discharged to the outside of the plate 10 are supplied into the groove 6, and the particles e transferred through the annular transfer space 9 are supplied into the groove 6. be able to.

【0009】上記中央及び外周回転羽根11、12が矢
印a方向に回転すると両羽根11、12は直径方向との
交差によって内筒1内及び輪状移送空間9内の粉粒体e
を内側に寄せるように移送し外側への偏移動を阻止する
ことができる。
When the central and outer peripheral rotating blades 11 and 12 rotate in the direction of the arrow a, the two blades 11 and 12 intersect with the diametrical direction, so that the powder particles e in the inner cylinder 1 and the ring-shaped transfer space 9 e.
Can be conveyed so as to be brought inward, and the eccentric movement to the outside can be prevented.

【0010】上記回転円盤4のクリーニングに際しては
該円盤4の支持装置5を底板3から該円盤4を伴って摺
動分離することができるし、クリーニング後反対動作に
よって元の所定位置に装着することができる。
When cleaning the rotating disk 4, the supporting device 5 for the disk 4 can be slid and separated from the bottom plate 3 with the disk 4, and after cleaning, the supporting device 5 can be mounted at the original predetermined position by the opposite operation. Can be.

【0011】[0011]

【実施例】中心線cを共有する直立円形内外筒1、2を
フランジ14によって一体に設け、外筒2には底板3が
設けられる。この底板3と内筒1の下端との間には僅か
な間隙tを介在させ、内外筒1、2間に粉粒体の輪状移
送空間9を形成し、底板3の上記中心線c上に直立回転
軸13の上端を突設する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Upright circular inner and outer cylinders 1 and 2 sharing a center line c are integrally provided by a flange 14, and a bottom plate 3 is provided on the outer cylinder 2. A small gap t is interposed between the bottom plate 3 and the lower end of the inner cylinder 1 to form a ring-shaped transfer space 9 for the granular material between the inner and outer cylinders 1 and 2. The upper end of the upright rotation shaft 13 is protruded.

【0012】上記直立回転軸13には底板3の上面に接
する複数(4個)のスポーク状中央回転羽根11の基部
を設け、該羽根11の先端は上記間隙tを潜って外筒2
の内周面に接する外周回転リング8に接続し、該リング
8には内部に向う複数の短い外周回転羽根12を底板3
の上面に接して設ける。
The upright rotary shaft 13 is provided with a base portion of a plurality of (four) spoke-shaped central rotary blades 11 which are in contact with the upper surface of the bottom plate 3, and the tips of the blades 11 extend through the gap t to form the outer cylinder 2.
Is connected to an outer peripheral rotating ring 8 which is in contact with the inner peripheral surface of the bottom plate 3.
It is provided in contact with the upper surface of.

【0013】このようにした底板3にはその上面と同一
平面内に上面を有し外筒2の内外に亘る回転円盤4を設
け、該円盤4の外周に上記平面と同一平面内に上面を有
する長方形支持装置5を底板3の下面にボルト15で接
着し、該装置5の外側に長方形排出口16を開口する。
The bottom plate 3 is provided with a rotating disk 4 having an upper surface in the same plane as the upper surface thereof and extending inward and outward of the outer cylinder 2, and having an upper surface on the outer periphery of the disk 4 in the same plane as the above-mentioned plane. The rectangular support device 5 having the same is bonded to the lower surface of the bottom plate 3 with bolts 15, and a rectangular discharge port 16 is opened outside the device 5.

【0014】この支持装置5は図1に示すように回転円
盤4の下部に駆動軸16’を有し、該駆動軸16’の回
りに該円盤4を水平方向に回転させ減速機17を介して
インバーター等による可変速モータ18を設けるもので
ある。
As shown in FIG. 1, the support device 5 has a drive shaft 16 'at the lower portion of the rotary disk 4, and rotates the disk 4 in a horizontal direction around the drive shaft 16' so as to rotate through a speed reducer 17. A variable speed motor 18 such as an inverter.

【0015】上記回転円盤4の上面には該円盤4と同心
円の粉粒体排出溝6を形成し、その縦断面は図4(イ)(ロ)
(ハ) 図に示すように各種のものが用いられる。そして外
筒2の外側において上記溝6の斜断面形状と同一雄形状
の粉粒体排出スクレーパ7を斜方向に挿入することによ
って該溝6内の粉粒体eを上記排出口16に排出するこ
とができる。
On the upper surface of the rotary disk 4, there is formed a powdery material discharge groove 6 which is concentric with the disk 4, and its vertical cross section is shown in FIGS.
(C) Various types are used as shown in the figure. Then, outside the outer cylinder 2, the powder / particles e in the groove 6 are discharged to the discharge port 16 by obliquely inserting a powder / particle discharge scraper 7 having the same male shape as the oblique cross-sectional shape of the groove 6. be able to.

【0016】上記外周回転リング8の内周縁には片刃面
8”を形成し、これを矢印a方向に回転させ、該片刃面
8”の先端の鋭い刃先8’によって矢印bの方向に回動
している上記溝6内の粉粒体eを該刃先8’の水平方向
摺動によってすり切りすることができる。このすり切り
によって残った粉粒体eは外周回転羽根12によって上
記円盤4上を矢印a方向に移送され、上記スクレーパ7
によって掻出されて空となった反対側の上記溝6内に投
入することができ該溝6の矢印b方向の回転に伴って再
び内筒1内に循環するし、内筒1内に循環しない残留粉
粒体eは輪状移送空間9を外周回転羽根12によって矢
印a方向に回動移送される動作を繰返し、該移送空間9
内の粉粒体eが圧密されることはない。
A single blade surface 8 "is formed on the inner peripheral edge of the outer peripheral rotary ring 8 and is rotated in the direction of arrow a, and is rotated in the direction of arrow b by the sharp edge 8 'at the tip of the single blade surface 8". The granular material e in the groove 6 can be abraded by sliding the cutting edge 8 'in the horizontal direction. The granular material e remaining after the cutting is transferred by the outer peripheral rotating blades 12 on the disk 4 in the direction of arrow a, and the scraper 7 is moved.
Can be thrown into the groove 6 on the opposite side that has been emptied and emptied. The unremoved residual particles e are repeatedly rotated and moved in the direction of arrow a by the outer peripheral rotating blades 12 in the annular transfer space 9.
The powders e in the inside are not compacted.

【0017】内筒1内における粉粒体eの自重による圧
密は上記円盤4の上方に内筒1に設けたバッフルプレー
ト10によって回避される。又中央及び外周回転羽根1
1、12は外端側が矢印a方向に向って直径方向と斜交
しているため該羽根11、12の回動によって粉粒体e
は内外筒1、2の内側に寄せられるように回動移行す
る。
Consolidation due to the weight of the granular material e in the inner cylinder 1 due to its own weight is avoided by the baffle plate 10 provided on the inner cylinder 1 above the disk 4. Center and outer peripheral rotating blades 1
Since the outer ends 1 and 12 are obliquely oblique to the diametric direction in the direction of arrow a, the rotation of the blades 11 and 12 causes the granular material e.
Pivotally move so as to be brought inside the inner and outer cylinders 1 and 2.

【0018】勿論内外筒1、2の直径が大きい大形装置
では図8、図9に示すように回転円盤4が内筒1内に入
ることは無く、間隙tから外側の輪状移送空間9に排出
された粉粒体のみ排出することができる。
Of course, in a large-sized apparatus in which the inner and outer cylinders 1 and 2 have a large diameter, the rotating disk 4 does not enter the inner cylinder 1 as shown in FIGS. Only the discharged powder can be discharged.

【0019】尚図中12’で示すものは外周回転羽根1
2の回転方向側に形成した片刃面による刃先、11’は
中央回転羽根11の回転方向側に形成した片刃面による
刃先、図1中17’は減速機、18’は可変速電動機、
図10中19は底板3に切欠形成した支持装置5用の嵌
込部、20はカバー、21は内外筒1、2の直径方向で
ある。
Reference numeral 12 'in FIG.
2, a cutting edge with a single blade surface formed on the rotation direction side of 11; 11 ', a cutting edge with a single blade surface formed on the rotation direction side of the central rotary blade 11; 17' in FIG. 1; a speed reducer; 18 ', a variable speed motor;
In FIG. 10, reference numeral 19 denotes a fitting portion for the support device 5 formed by cutting out the bottom plate 3, reference numeral 20 denotes a cover, and reference numeral 21 denotes a diameter direction of the inner and outer cylinders 1 and 2.

【0020】[0020]

【発明の効果】本発明は上述のように構成したので流動
性良好な粉粒体は勿論、流動性不良な粉粒体でも連続回
転可能な上記円形の排出溝6によって圧密されるおそれ
がなく、かつ刃先8’の方向への摺動によって鋭利にす
り切りし得て高精度の連続定量供給を実現し得る効果が
ある。又装置を簡略に形成し得る便益がある。
Since the present invention is constructed as described above, there is no danger that not only powders having good fluidity but also powders having poor fluidity are compacted by the circular discharge groove 6 which can be continuously rotated. In addition, there is an effect that the cutting can be sharply sharpened by sliding in the direction of the cutting edge 8 ′, thereby realizing high-precision continuous quantitative supply. There is also an advantage that the device can be simply formed.

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

【図1】本発明の定量フィーダーを示す縦断正面図であ
る。
FIG. 1 is a vertical sectional front view showing a quantitative feeder of the present invention.

【図2】図1の平面図である。FIG. 2 is a plan view of FIG.

【図3】図2の一部拡大図である。FIG. 3 is a partially enlarged view of FIG. 2;

【図4】(イ)(ロ)(ハ) 図は粉粒体排出溝の拡大縦断面図で
ある。
FIGS. 4 (a), (b) and (c) are enlarged vertical cross-sectional views of the granular material discharge groove.

【図5】(イ) 図は図3A−A線による縦断面図である。
(ロ) 図は(イ) 図B−B線による縦断面図である。(ハ) 図
は図3C−C線による縦断面図である。
FIG. 5 (a) is a longitudinal sectional view along the line AA in FIG. 3;
(B) The figure is (a) a longitudinal sectional view along the line BB in FIG. (C) The figure is a longitudinal sectional view taken along the line CC of FIG.

【図6】バッフルプレートを備えた定量フィーダーの平
面図である。
FIG. 6 is a plan view of a quantitative feeder provided with a baffle plate.

【図7】図6の縦断面図である。FIG. 7 is a longitudinal sectional view of FIG.

【図8】大形定量フィーダーの平面図である。FIG. 8 is a plan view of a large quantitative feeder.

【図9】図8の縦断面図である。FIG. 9 is a longitudinal sectional view of FIG.

【図10】回転円盤分離状態の平面図である。FIG. 10 is a plan view of a rotating disk separated state.

【図11】分離部の縦断面図である。FIG. 11 is a longitudinal sectional view of a separation unit.

【図12】分離した回転円盤の平面図である。FIG. 12 is a plan view of a separated rotating disk.

【図13】図12の縦断面図である。FIG. 13 is a longitudinal sectional view of FIG.

【符号の説明】[Explanation of symbols]

1 内筒 2 外筒 3 底板 4 回転円盤 5 支持装置 6 粉粒体排出溝 7 粉粒体排出スクレーパ 8 外周回転リング 8’ 刃先 9 輪状移送空間 10 バッフルプレート 11 中央回転羽根 12 外周回転羽根 DESCRIPTION OF SYMBOLS 1 Inner cylinder 2 Outer cylinder 3 Bottom plate 4 Rotating disk 5 Supporting device 6 Granular material discharge groove 7 Granular material discharge scraper 8 Outer peripheral rotating ring 8 'Blade edge 9 Annular transfer space 10 Baffle plate 11 Center rotating blade 12 Outer rotating blade

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平3−166126(JP,A) 特開 昭64−56417(JP,A) 実開 平4−37128(JP,U) (58)調査した分野(Int.Cl.7,DB名) B65G 65/30 - 65/48 ──────────────────────────────────────────────────続 き Continuation of front page (56) References JP-A-3-166126 (JP, A) JP-A-64-56417 (JP, A) JP-A-4-37128 (JP, U) (58) Survey Field (Int.Cl. 7 , DB name) B65G 65/30-65/48

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 中心線を共有する内外筒によって形成さ
れ、外筒の底板と内筒の下端との間に間隙を有し、粉粒
体の輪状移送空間を内外筒間に設けてなり、底板の中心
部に突設した直立回転軸に設けた中央回転羽根の先端に
外筒の内周に沿って設けた外周回転リングを接続し、該
リングには内部に向う複数の外周回転羽根を設けてな
り、上記移送空間から上記粉粒体を機外に排出する機構
において、上記底板の上面と同一平面内に上面を有する
回転円盤を設け、該円盤の上面に該円盤と同心円の粉粒
体排出溝を形成し、該溝が上記外筒の内外に亘って配設
されてなる定量フィーダー。
1. A space formed between an inner cylinder and an outer cylinder sharing a center line with a gap between a bottom plate of the outer cylinder and a lower end of the inner cylinder, and a ring-shaped transfer space for the granular material is provided between the inner cylinder and the outer cylinder. An outer peripheral rotating ring provided along the inner periphery of the outer cylinder is connected to the tip of a central rotating blade provided on an upright rotating shaft protruding from the center of the bottom plate, and a plurality of inwardly rotating outer rotating blades are connected to the ring. A rotating disk having an upper surface in the same plane as an upper surface of the bottom plate, wherein a powder particle concentric with the disk is provided on the upper surface of the disk. A fixed-quantity feeder having a body discharge groove formed therein, the groove being disposed inside and outside the outer cylinder.
【請求項2】 外筒の外側において上記溝内に粉粒体排
出スクレーパを挿入してなる請求項(1) 記載の定量フィ
ーダー。
2. The fixed-quantity feeder according to claim 1, wherein a powdery material discharging scraper is inserted into the groove outside the outer cylinder.
【請求項3】 上記外周回転リングの内周縁に刃先を形
成し、上記輪状移送空間において上記刃先によって上記
粉粒体排出溝のすり切りを行うよう形成した請求項(1)
又は(2) 記載の定量フィーダー。
3. A cutting edge is formed on an inner peripheral edge of said outer peripheral rotating ring, and said powdery material discharge groove is cut off by said cutting edge in said annular transfer space.
Or the quantitative feeder according to (2).
【請求項4】 内筒の内面に粉粒体排出溝への粉粒体圧
力を回避するバッフルプレートを設けてなる請求項(1)
(2) 又は(3) にそれぞれ記載の定量フィーダー。
4. A baffle plate is provided on the inner surface of the inner cylinder to avoid the pressure of the granular material to the granular material discharge groove.
The quantitative feeder according to (2) or (3), respectively.
【請求項5】 中央回転羽根及び外周回転羽根の外端側
が回転方向に向って直径方向と交差してなる請求項(1)
(2) (3) 又は(4) にそれぞれ記載の定量フィーダー。
5. The outer peripheral side of the central rotary blade and the outer peripheral rotary blade intersects the diametric direction in the direction of rotation.
(2) The quantitative feeder according to (3) or (4), respectively.
【請求項6】 上記回転円盤及びその支持装置を上記底
板から着脱自在に支持してなる請求項(1) (2) (3) (4)
又は(5) にそれぞれ記載の定量フィーダー。
6. The disk (1), (2), (3) and (4), wherein the rotating disk and its supporting device are detachably supported from the bottom plate.
Or the quantitative feeder according to (5).
JP04329075A 1992-12-09 1992-12-09 Quantitative feeder Expired - Fee Related JP3090555B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04329075A JP3090555B2 (en) 1992-12-09 1992-12-09 Quantitative feeder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04329075A JP3090555B2 (en) 1992-12-09 1992-12-09 Quantitative feeder

Publications (2)

Publication Number Publication Date
JPH06171765A JPH06171765A (en) 1994-06-21
JP3090555B2 true JP3090555B2 (en) 2000-09-25

Family

ID=18217344

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04329075A Expired - Fee Related JP3090555B2 (en) 1992-12-09 1992-12-09 Quantitative feeder

Country Status (1)

Country Link
JP (1) JP3090555B2 (en)

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Publication number Priority date Publication date Assignee Title
SE524932C2 (en) 2002-12-13 2004-10-26 Saxlund Internat Ab Container dispensing device
JP4884718B2 (en) * 2005-08-17 2012-02-29 株式会社ヨシカワ Powder supply machine in material supply equipment
JP2012066211A (en) * 2010-09-27 2012-04-05 Yoshikawa:Kk Method for supplying material for powder and granular material supply machine, and powder and granular material supply machine
CN114229438A (en) * 2021-12-31 2022-03-25 安徽麦尔客生物科技有限公司 Lossless packing mechanism and food processing packing equipment based on same

Cited By (4)

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Publication number Priority date Publication date Assignee Title
WO2014065005A1 (en) 2012-10-25 2014-05-01 株式会社ヨシカワ Metering feeder
CN104755399A (en) * 2012-10-25 2015-07-01 株式会社吉川 Metering feeder
CN104755399B (en) * 2012-10-25 2016-06-29 株式会社吉川 Constant feeder
US9688488B2 (en) 2012-10-25 2017-06-27 Yoshikawa Corporation Metering feeder

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