JP2009263090A - Powder and grain feeder - Google Patents

Powder and grain feeder Download PDF

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JP2009263090A
JP2009263090A JP2008114950A JP2008114950A JP2009263090A JP 2009263090 A JP2009263090 A JP 2009263090A JP 2008114950 A JP2008114950 A JP 2008114950A JP 2008114950 A JP2008114950 A JP 2008114950A JP 2009263090 A JP2009263090 A JP 2009263090A
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bottom plate
powder
passage
discharge port
cylinder
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JP4579308B2 (en
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Osamu Yoshikawa
修 吉川
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YOSHIKAWA KK
Yoshikawa Corp
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YOSHIKAWA KK
Yoshikawa Corp
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Priority to JP2008114950A priority Critical patent/JP4579308B2/en
Priority to KR1020080117852A priority patent/KR101455869B1/en
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    • 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
    • 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
    • B65G19/00Conveyors comprising an impeller or a series of impellers carried by an endless traction element and arranged to move articles or materials over a supporting surface or underlying material, e.g. endless scraper conveyors
    • B65G19/18Details
    • B65G19/22Impellers, e.g. push-plates, scrapers; Guiding means therefor
    • 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
    • B65G47/00Article or material-handling devices associated with conveyors; Methods employing such devices
    • B65G47/02Devices for feeding articles or materials to conveyors
    • B65G47/04Devices for feeding articles or materials to conveyors for feeding articles
    • 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
    • B65G65/02Loading or unloading machines comprising essentially a conveyor for moving the loads associated with a device for picking-up the loads
    • B65G65/08Loading or unloading machines comprising essentially a conveyor for moving the loads associated with a device for picking-up the loads with reciprocating pick-up conveyors
    • B65G65/10Raking or scraping devices
    • 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
    • B65G65/4836Devices 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 moving material over a stationary surface, e.g. sweep arms or wheels

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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a powder and grain feeder which forms a repose angle within a circular passage formed by a cylinder spacing between upright inner and outer cylinders having a shared axis; impellers disposed on a pivot shaft at the axis along the outer cylinder's bottom plate, the inner cylinder's lower end, and along a bottom plate of a circular passage formed by the outer cylinder's bottom plate; a rotary ring; and by equally-spaced rotary claws, and which supplies (discharges) "small spherical particles", "piece-like or easy-to-mix waste plastic particles", and the like supplied naturally from the lower end of the inner cylinder, uniformly or by fixed-rate dropping, while preventing pulsative or nonuniform dropping from a discharge port formed in the circular passage. <P>SOLUTION: The powder and grain feeder turns powder and grain 7 in the passage 4 along the passage 4, using the impellers 5 and the rotary claws 6 which connect from the spacing, leading from the lower end of the upright inner cylinder to the bottom plate 3 of the upright outer cylinder 2, to the circular passage 4 formed between the inner cylinder and the outer cylinder 2 and which turn along the bottom plate 3 of the passage 4; wherein a powder and grain dropping discharge port 8 is opened in the passage 4 and a plurality of guide rods 9, 9' toward a terminating end edge 8 of the discharge port 8 are provided at the starting end edge 8' thereof. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は粉粒体供給機によって各種の粉粒体を排出口から定量供給する装置に関するものである。   The present invention relates to an apparatus for quantitatively supplying various types of granular materials from a discharge port using a granular material supply machine.

従来、内筒と外筒との間の円形材料通路に排出口を設けてなる粉粒体供給機では、上記円形材料通路に内筒下端の間隙から粉粒体が安息角を形成して一定量進入し、該通路内の粉粒体は、一定間隙毎に設けた回転羽根及び回転爪の回転によって押されて回動し、上記排出口から一定量ずつ落下し、コンベア等に供給される構成である。   Conventionally, in a granular material feeder in which a discharge port is provided in a circular material passage between an inner cylinder and an outer cylinder, the granular material forms an angle of repose from the gap at the lower end of the inner cylinder in the circular material passage and is constant. The powder particles in the passage are pushed and rotated by the rotation of the rotating blades and the rotating claws provided for each fixed gap, and fall by a fixed amount from the discharge port, and are supplied to a conveyor or the like. It is a configuration.

このような従来の粉粒体供給機は、上記排出口から粉粒体が急に落下排出されることによる脈動排出を防止すべく、排出口の幅を粉粒体の進行方向に徐々に広く形成したものがある(図5、例えば特許文献1)。   In such a conventional powder feeder, the width of the discharge port is gradually widened in the advancing direction of the granular material in order to prevent pulsation discharge due to sudden drop and discharge of the granular material from the discharge port. Some are formed (FIG. 5, for example, Patent Document 1).

実開平6−31829号Utility Kaihei 6-31829

ところで、上記従来の粉粒体供給機の排出口は、微粉粒体の脈動排出を防止して定量供給を実現するには適しているが、例えば廃棄プラスチック等の片状や絡み易い材料(粉粒体)の場合は、上記排出口の狭いエリアにおいては落下せず、広いエリアに至って急に落下するという脈動排出が生ずる可能性がある。   By the way, the discharge port of the above-mentioned conventional powder and particle feeder is suitable for realizing the quantitative supply by preventing the pulsation discharge of the fine particles, but for example, a piece of material such as waste plastic or an easily entangled material (powder In the case of (granular material), there is a possibility that pulsation discharge occurs that does not fall in a narrow area of the discharge port, but suddenly falls to a wide area.

本発明は共通中心軸を有する直立内外円筒間の円筒間隔、外筒底板及び内筒下端と外筒底板によって形成される環状通路の底板に沿って上記中心軸にある回動軸に設けた回転羽根、回転リング及び等間隔回転爪によって形成される環状通路内に安息角を形成して上記内筒下端から自然に供給される「小球粒」「片状又は絡み易い廃プラ小片」等を上記環状通路に形成した排出口から脈動又は不均等落下を防止し、均等又は定量落下供給(排出)することを目的とする。   The present invention provides a cylindrical space between upright inner and outer cylinders having a common central axis, an outer cylinder bottom plate, and a rotation provided on the pivot shaft at the central axis along the bottom plate of the annular passage formed by the inner cylinder lower end and the outer cylinder bottom plate. “Small particles”, “Scrap or tangled waste plastic pieces” that are naturally supplied from the lower end of the inner cylinder by forming an angle of repose in an annular passage formed by blades, rotating rings and equally spaced rotating claws An object is to prevent pulsation or unequal drop from the discharge port formed in the annular passage and to supply (discharge) the drop evenly or quantitatively.

上記の目的を達成するため本発明は
第1に、底板に外筒を立設して粉粒体供給ケースとし、上記底板の上方に粉粒体排出間隙を介して内筒を同心に支持し、上記底板の中心に直立回転軸を設け、該回転軸に上記底板上に位置する複数のスポークを設けて回転体を形成し、該回転体の筒状外縁を外筒の内周に近接して内外筒間の環状通路を形成し、上記筒状外縁に上記環状通路方向の材料移送用スクレーパを複数設け、上記粉粒体排出間隙から所定の安息角にて上記環状通路に拡散した粉粒体を上記スクレーパにより粉粒体排出口に移送する粉粒体供給機において、上記排出口の始端縁に該排出口の終端縁に向う複数の案内杆を設けてなる粉粒体供給機により構成されるものである。
In order to achieve the above object, the present invention firstly provides an outer cylinder standing on the bottom plate as a powder supply case, and supports the inner cylinder concentrically above the bottom plate via a powder discharge gap. An upright rotating shaft at the center of the bottom plate, a plurality of spokes located on the bottom plate are provided on the rotating shaft to form a rotating body, and a cylindrical outer edge of the rotating body is brought close to the inner periphery of the outer cylinder. Forming an annular passage between the inner and outer cylinders, providing a plurality of material transfer scrapers in the annular passage direction at the outer edge of the cylinder, and the particles dispersed in the annular passage at a predetermined angle of repose from the powder discharge gap In the powder supply machine for transferring the body to the powder discharge port by the scraper, it is constituted by a powder supply machine provided with a plurality of guide rods facing the terminal edge of the discharge port at the start edge of the discharge port It is what is done.

第2に上記案内杆の長さが調節可能である上記第1記載の粉粒体供給機により構成されるものである。   Secondly, the length of the guide rod is adjustable, and is constituted by the powder and particle feeder according to the first aspect.

第3に複数の上記案内杆が長短平行に支持され、上記内筒側の案内杆が長く外筒側の案内杆が短い上記第1又は第2記載の粉粒体供給機により構成されるものである。   Thirdly, the plurality of guide rods are supported in parallel with each other, and the inner tube side guide rod is long and the outer tube side guide rod is short. It is.

従って直立内筒内に片状又は絡み易い粒体を投入すると該粒体は上記内筒の下端と上記外筒の底板との間隙θから上記環状通路内に安息角αを形成して排出される。   Therefore, when a granular or easily entangled granule is introduced into the upright inner cylinder, the granule is discharged from the gap θ between the lower end of the inner cylinder and the bottom plate of the outer cylinder, forming a repose angle α in the annular passage. The

この状態において上記回転羽根及び回転爪が上記環状通路の底板に沿って中心軸の回りに回動し、上記粒体を上記排出口の始端部から複数の案内杆に倣って排出口の終端部に向って摺動し、案内杆間の間隙から一定量宛落下し、均等落下することができる。このとき、複数の案内杆によって材料は上記間隙から分散して落下するので、例えば絡み合った材料を解しながら排出することができ、脈動排出を防止することができる。   In this state, the rotating blades and the rotating claws rotate around the central axis along the bottom plate of the annular passage, and the particles are moved from the start end of the discharge port to the end of the discharge port following a plurality of guide rods. It can slide toward the center, fall to a certain amount from the gap between the guide rods, and can fall evenly. At this time, since the material is dispersed and dropped from the gap by the plurality of guide rods, for example, the entangled material can be discharged while being released, and pulsation discharge can be prevented.

上記複数の案内杆の長さ及び間隙又は数は上記粒体の大小、形状及び物性等に適応するよう適宜選定することができる。   The lengths, gaps, or number of the plurality of guide rods can be appropriately selected so as to adapt to the size, shape, physical properties, etc. of the granules.

本発明は上述のように構成したので、片状や絡み易い粉粒体でも排出口からの落下を分散させることにより、脈動を防止し得て上記排出口から均等に落下供給し得る効果がある。   Since the present invention is configured as described above, it is possible to prevent pulsation and evenly drop and supply from the discharge port by dispersing the fall from the discharge port even in the form of particles or particles that are easily entangled. .

底板3に外筒2を立設して粉粒体供給ケースとし、上記底板3の上方に粉粒体排出間隙θを介して内筒1を同心に支持し、上記底板3の中心に直立回転軸10を設け、該回転軸10に上記底板3上に位置する複数のスポーク5を設けて回転体を形成し、該回転体の筒状外縁11を外筒2の内周に近接して内外筒間の環状通路4を形成し、上記筒状外縁11に上記環状通路方向の材料移送用スクレーパ6を複数設け、上記粉粒体排出間隙θから所定の安息角αにて上記環状通路4に拡散した粉粒体を上記スクレーパ6により粉粒体排出口8に移送するように粉粒体供給機を構成する(図1、図3参照)。   The outer cylinder 2 is erected on the bottom plate 3 to form a powder supply case, the inner cylinder 1 is supported concentrically above the bottom plate 3 via a powder discharge gap θ, and is rotated upright to the center of the bottom plate 3. A shaft 10 is provided, and a rotating body is formed by providing a plurality of spokes 5 positioned on the bottom plate 3 on the rotating shaft 10, and a cylindrical outer edge 11 of the rotating body is placed close to the inner periphery of the outer cylinder 2 and placed inside and outside. An annular passage 4 between the cylinders is formed, and a plurality of material transfer scrapers 6 in the annular passage direction are provided on the cylindrical outer edge 11, and the annular passage 4 enters the annular passage 4 at a predetermined repose angle α from the powder discharge gap θ. The powder supply unit is configured so that the diffused powder is transferred to the powder discharge port 8 by the scraper 6 (see FIGS. 1 and 3).

即ち、直立共通中心軸c上に直立内外筒1,2を配置し、該内外筒1,2間に上記環状通路4を形成し、外筒2の底板3上方に内筒1の下端を材料通路間隙(粉粒体排出間隙)θを介して支持し、上記外筒2の底板3の中心部に突設した直立回動軸10の上端部に上記底板3に沿う複数の回転羽根(スポーク)5を設け、これらの回転羽根5の先端に上記外筒2の内周に沿う回転リング(筒状外縁)11を設け、該リング11に上記底板3に沿って複数の材料押爪(材料移送用スクレーパ)6を上記環状通路4内に設け、かつ上記環状通路4の上記底板3に粉粒体落下排出口8を開口することにより粉粒体供給機が構成される(図1、図3参照)。   That is, the upright inner and outer cylinders 1 and 2 are arranged on the upright common center axis c, the annular passage 4 is formed between the inner and outer cylinders 1 and 2, and the lower end of the inner cylinder 1 is made of the material above the bottom plate 3 of the outer cylinder 2. A plurality of rotating blades (spokes) along the bottom plate 3 are supported at the upper end portion of the upright rotating shaft 10 supported through a passage gap (powder particle discharge gap) θ and projecting from the center portion of the bottom plate 3 of the outer cylinder 2. ) 5, and a rotating ring (cylindrical outer edge) 11 along the inner periphery of the outer cylinder 2 is provided at the tip of the rotating blades 5, and a plurality of material claws (materials) are formed on the ring 11 along the bottom plate 3. A granular material feeder is constructed by providing a transfer scraper 6 in the annular passage 4 and opening a granular material falling discharge port 8 in the bottom plate 3 of the annular passage 4 (FIG. 1, FIG. 3).

このような粉粒体供給機の上記粉粒体落下排出口8は図1、図2に示すように始端縁8’及び終端縁8”が平行対向縁であって該排出口8の中心を通る内外筒1,2の直径線Dと平行であり、かつ該排出口8の幅は環状通路4の幅tとほぼ同一幅であるが、図1、図2に示すように内筒1側に弧形フランジ8aを形成し上記幅tより多少小とする。   The granular material dropping outlet 8 of such a granular material feeder has a leading edge 8 ′ and a trailing edge 8 ″ parallel to each other as shown in FIGS. Although the width of the discharge port 8 is substantially the same as the width t of the annular passage 4, it is parallel to the diameter line D of the inner and outer cylinders 1, 2 that pass through, but as shown in FIGS. An arc-shaped flange 8a is formed on the base plate and is slightly smaller than the width t.

上述のように形成した粉粒体落下排出口8の始端縁8’に終端縁8”に向う複数(2個)の案内杆9,9’を上記始端縁8’の中央部に間隔e,e’,e”を介して配置し、該案内杆9,9’のそれぞれ基端部を上記始端縁8’の下面に固定した上向溝12,12に摺動自在に水平に支持し、止めネジ13,13で締付けて上記案内杆9,9’を上記終端縁8”に向って外側案内杆9’を短く、内側案内杆9を長く支持することができる(図3参照)。   A plurality of (two) guide rods 9 and 9 ′ facing the terminal edge 8 ″ are provided at the start edge 8 ′ of the granular material falling discharge port 8 formed as described above at the center e of the start edge 8 ′. e ', e "are arranged via slidably supported horizontally in the upward grooves 12, 12 fixed to the lower surface of the starting edge 8'. The outer guide rod 9 'can be shortened and the inner guide rod 9 can be supported longer by tightening the set screws 13 and 13 toward the end edge 8 "of the guide rod 9, 9' (see FIG. 3).

上記案内杆9,9’の長短及び上記排出口8の環状通路4の方向の長さの調節は上記内筒1に投入した粉粒体7の物理的特性、大きさ、即ち片状や絡み性状等による特性及び上記間隙θから環状通路4への流出状態、安息角α等によって適宜調節することができるし、上記案内杆9,9’の長短及び長さ等の調節は内筒1への投入材料の一定の特性に応じて上記始端縁8’に予め固定して設けても良い。   Adjustment of the length of the guide rods 9 and 9 ′ and the length of the discharge port 8 in the direction of the annular passage 4 is performed by adjusting the physical characteristics and size of the granular material 7 charged into the inner cylinder 1, that is, flakes and entanglements. It can be adjusted as appropriate depending on the characteristics depending on the properties and the like, the outflow state from the gap θ to the annular passage 4, the angle of repose α, and the like. Depending on certain characteristics of the input material, it may be fixed in advance to the starting edge 8 '.

即ち、上記案内杆9,9’の長短は、各々上記止めネジ13,13を緩めて各案内杆9,9’を上記上向溝12,12に沿って摺動させることにより、調整することができる。   That is, the length of the guide rods 9 and 9 'is adjusted by loosening the set screws 13 and 13 and sliding the guide rods 9 and 9' along the upward grooves 12 and 12, respectively. Can do.

従って、廃プラスチック微粒子、小片(約5mm程度)等の再生粒子、分別ごみ粒子、小片等の粉粒体7が上記内筒1の上端開部から供給されると、上記粉粒体7は上記間隙θから安息角αを形成して上記環状通路4内に円環状に排出される。   Accordingly, when powder particles 7 such as waste plastic fine particles, regenerated particles such as small pieces (about 5 mm), separated dust particles, small pieces, etc. are supplied from the upper end opening of the inner cylinder 1, the powder particles 7 are A repose angle α is formed from the gap θ and discharged into the annular passage 4 in an annular shape.

そして、上記回転羽根5,5,5,5及びその先端に内筒1の内周に沿って設けた回転リング11に一定間隔毎に設けた上記押爪6,6・・・によって上記通路4内の粉粒体7は該通路4に沿って移動し、上記排出口8の始端縁8’から上記案内杆9,9’上を終端縁8”に向って移動すると同時に弧形フランジ8aと内側案内杆9との間隙e’、案内杆9,9’相互間隙e及び外側案内杆9と上記回転リング11との間隙e”から排出シュート8b(図3)を経て機外に設けた排出コンベア14(図3)上に落下する。   The passage 4 is formed by the push claws 6, 6,... Provided at regular intervals on the rotary blades 5, 5, 5, 5 and the rotary ring 11 provided at the tip thereof along the inner periphery of the inner cylinder 1. The inner granular material 7 moves along the passage 4, and moves from the start edge 8 'of the discharge port 8 on the guide rods 9 and 9' toward the end edge 8 "and at the same time the arc-shaped flange 8a and Discharge provided outside the machine through the discharge chute 8b (FIG. 3) from the gap e ′ with the inner guide rod 9, the mutual gap e between the guide rods 9, 9 ′ and the gap e ″ between the outer guide rod 9 and the rotating ring 11. It falls on the conveyor 14 (FIG. 3).

このとき、上記排出口8の始端縁8’側は、上記案内杆9,9’によって3つの狭い間隙e,e’,e”に分割されているので、仮に廃棄プラスチック等の材料であって互いに絡まっている材料の場合、上記案内杆9,9’上に位置したときに、これら案内杆9,9’によって解されながら下方に落下していくため、絡み合った材料が一度に落下するということは起こり得ず、脈動排出を防止して定量供給を実現することができる。   At this time, the start edge 8 ′ side of the discharge port 8 is divided into three narrow gaps e, e ′, e ″ by the guide rods 9, 9 ′. In the case of materials that are entangled with each other, when they are positioned on the guide rods 9 and 9 ', they fall downward while being solved by the guide rods 9 and 9'. This cannot happen, and it is possible to prevent a pulsating discharge and realize a quantitative supply.

また、絡み合った材料を上記間隔e,e’,e”により分散して落下させることが可能であるため、同様に脈動を防止して、定量供給を実現し得る。   Further, since the intertwined materials can be dispersed and dropped at the intervals e, e ', e ", it is possible to prevent pulsation and realize a constant supply.

また、案内杆9,9’の長さが異なるので、押爪6の回転方向に沿って材料を徐々に分散して排出することができ、即ち、材料の絡みを徐々に解しながら排出することができ、脈動防止効果をより高めることができる。   Further, since the lengths of the guide rods 9 and 9 ′ are different, the material can be gradually dispersed and discharged along the rotation direction of the push claw 6, that is, the material is discharged while gradually solving the entanglement of the material. And the pulsation preventing effect can be further enhanced.

又上記長短案内杆9,9’の先端から上記終端縁8”までの空間では、上記案内杆9,9’によって既に材料の絡みは解されているので、粉粒体7の大小片又は絡み性状に応じて上記シュート8bから搬出コンベア14上にほぼ均等に落下排出される。   Further, in the space from the leading end of the long and short guide rods 9 and 9 ′ to the end edge 8 ″, the entanglement of the material has already been solved by the guide rods 9 and 9 ′. Depending on the properties, the chute 8b is dropped and discharged almost uniformly onto the carry-out conveyor 14.

尚、上記実施形態では、上記案内杆を2本設けた実施形態を示したが、これに限定されず、上記案内杆を材料通路4の内周側から外周側に向けて3本、或いはそれ以上の本数を設けて良い。この場合、絡み合った材料を段階的に解していくという機能からすると、案内杆の長さは、最内周の案内杆を最も長く形成し、内周側から外周側に向けてその長さを徐々に短く構成することが好ましい。   In the above-described embodiment, an embodiment in which two guide rods are provided has been described. However, the present invention is not limited to this. Three guide rods are provided from the inner peripheral side to the outer peripheral side of the material passage 4, or The above number may be provided. In this case, the length of the guide rod is the length of the innermost guide rod formed from the inner periphery side toward the outer periphery side in view of the function of solving the entangled material step by step. Is preferably configured to be gradually shortened.

図中15は上記内外筒1,2の環状接続板、1’は上記内筒1の外周に設けた昇降円板で材料通路間隙θを調節する。図3中16は直立回動軸10の回動装置である。   In the figure, reference numeral 15 denotes an annular connecting plate of the inner and outer cylinders 1 and 2, and 1 ′ is a lifting disk provided on the outer periphery of the inner cylinder 1 to adjust the material passage gap θ. In FIG. 3, reference numeral 16 denotes a rotating device for the upright rotating shaft 10.

本発明は上述のように構成したので廃プラスチック等の片状又は絡み易い粉粒体7の物性に応じて脈動又は片寄りなく均等排出し、次の工程に均等供給することができる。   Since the present invention is configured as described above, it can be discharged evenly without pulsation or deviation according to the physical properties of the granular material 7 such as waste plastic or the like, which can easily be entangled, and can be equally supplied to the next step.

本発明の粉粒体供給機の切欠平面図である。It is a notch top view of the granular material supply machine of this invention. 図1の一部拡大平面図である。FIG. 2 is a partially enlarged plan view of FIG. 1. 図1のA−A線による縦断面図である。It is a longitudinal cross-sectional view by the AA line of FIG. 図1B−B線による縦断面図である。It is a longitudinal cross-sectional view by FIG. 1B-B line. 従来の粉粒体落下排出口の平面図である。It is a top view of the conventional granular material fall discharge port.

符号の説明Explanation of symbols

1 直立内筒
2 直立外筒
3 底板
4 環状通路
θ 間隙
5 回転羽根
6 回転爪
7 粉粒体
8 粉粒体落下排出口
8’ 始端縁
8” 終端縁
9,9’ 案内杆
DESCRIPTION OF SYMBOLS 1 Upright inner cylinder 2 Upright outer cylinder 3 Bottom plate 4 Annular channel | path (theta) gap | interval 5 Rotary blade 6 Rotating claw 7 Granule body 8 Granule body fall discharge port 8 'Start edge 8 "End edge 9, 9' Guide rod

Claims (3)

底板に外筒を立設して粉粒体供給ケースとし、上記底板の上方に粉粒体排出間隙を介して内筒を同心に支持し、上記底板の中心に直立回転軸を設け、該回転軸に上記底板上に位置する複数のスポークを設けて回転体を形成し、該回転体の筒状外縁を外筒の内周に近接して内外筒間の環状通路を形成し、上記筒状外縁に上記環状通路方向の材料移送用スクレーパを複数設け、上記粉粒体排出間隙から所定の安息角にて上記環状通路に拡散した粉粒体を上記スクレーパにより粉粒体排出口に移送する粉粒体供給機において、
上記排出口の始端縁に該排出口の終端縁に向う複数の案内杆を設けてなる粉粒体供給機。
An outer cylinder is erected on the bottom plate to form a powder supply case, the inner cylinder is concentrically supported above the bottom plate via a powder discharge gap, and an upright rotating shaft is provided at the center of the bottom plate. A plurality of spokes located on the bottom plate are provided on the shaft to form a rotating body, and the cylindrical outer edge of the rotating body is close to the inner periphery of the outer cylinder to form an annular passage between the inner and outer cylinders. A plurality of scrapers for material transfer in the direction of the annular passage are provided on the outer edge, and the powder that is diffused into the annular passage at a predetermined angle of repose from the particulate discharge gap is transferred to the powder outlet by the scraper. In the granule feeder,
A granular material supply machine in which a plurality of guide rods facing the end edge of the discharge port are provided at the start edge of the discharge port.
上記案内杆の長さが調節可能である請求項1記載の粉粒体供給機。   The granular material supply machine according to claim 1, wherein the length of the guide rod is adjustable. 複数の上記案内杆が長短平行に支持され、上記内筒側の案内杆が長く外筒側の案内杆が短い請求項1又は2記載の粉粒体供給機。   The granular material supply machine according to claim 1 or 2, wherein the plurality of guide rods are supported in parallel in a long and short direction, the guide rod on the inner cylinder side is long, and the guide rod on the outer cylinder side is short.
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Cited By (3)

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Publication number Priority date Publication date Assignee Title
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
KR101306251B1 (en) 2011-12-09 2013-09-09 주식회사 세종파마텍 A feeder
JP2014024634A (en) * 2012-07-26 2014-02-06 Yoshikawa:Kk Discharge flow rate adjusting device in granular material feeder

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5742594B2 (en) * 2010-08-31 2015-07-01 株式会社ニコン Powder supply apparatus, injection processing system, and electrode material manufacturing method
JP5856037B2 (en) * 2012-10-25 2016-02-09 株式会社ヨシカワ Metering feeder

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JPS6047733U (en) * 1984-07-31 1985-04-04 芹沢 暢夫 Quantitative feeding device for fibrous materials and powder materials
JPH0631829U (en) * 1992-10-06 1994-04-26 修 吉川 Outlet in circle feeder

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4039885B2 (en) 2002-05-17 2008-01-30 株式会社ヨシカワ Powder and particle feeder
JP2007302373A (en) 2006-05-09 2007-11-22 Yoshikawa:Kk Powder and grain feeder

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6047733U (en) * 1984-07-31 1985-04-04 芹沢 暢夫 Quantitative feeding device for fibrous materials and powder materials
JPH0631829U (en) * 1992-10-06 1994-04-26 修 吉川 Outlet in circle feeder

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
KR101306251B1 (en) 2011-12-09 2013-09-09 주식회사 세종파마텍 A feeder
JP2014024634A (en) * 2012-07-26 2014-02-06 Yoshikawa:Kk Discharge flow rate adjusting device in granular material feeder

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