JP4439659B2 - Powdering method and apparatus - Google Patents
Powdering method and apparatus Download PDFInfo
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Description
【0001】
【発明の属する技術分野】
本発明は、貯室に貯えられた粉粒体を外部へ必要量給粉する給粉機であって、粉圧の影響を少なくでき、高精度の給粉を可能にする方法及び給粉機に関する。
【0002】
【従来の技術】
従来、粉粒体の貯室の底部に回転する供給盤を設け、同回転体の上面の収容空間に粉粒体を所要量流入させ、供給盤を回転させて貯室外へ排出する構造の給粉機は広く使用されている。
供給盤の収容空間の回転路は排出部を残して開放されている構造のものが使用されていたが、貯室内の粉圧が収容空間に長く作用し、収容空間の粉粒体が上方からの粉圧によって加圧され、嵩密度が高くなったり、上方からの粉粒体を移動させるため流れが不安定となっていた。これを解消すべく供給盤の収容空間の回送路の上方に隔板を設け、同隔板に粉粒体を下方の収容空間に流入させる流入口を開口させる構造が開発された。この粉粒体流入口は1個所であって収容空間に粉粒体を充填させるに充分なやや広い開口面積を有するものであった。しかしながら、この粉粒体流入口から貯室内の粉圧が作用し、やはり粉圧によって加圧され、嵩比重が大きくなり、給粉精度を低下させていた。詳しく説明すると、
貯室の中心と同心に回転する粉粒体供給盤を配した1軸式の粉体定量供給機に於いては、供給盤羽根部に加わる粉体圧力が、貯室の粉面高さの変動、貯室へのチャージ衝撃の影響及びブリッジ現象やラットホール現象を防止するためのエアレーションやバイブレーターの影響による粉圧変動により、羽根部に充填される粉体の嵩密度が変動する現象に対し、従来の定量供給機に於いては、羽根部の粉体圧力変動防止対策として、隔板スポート方式や円筒・コーンスポート方式が広く採用されているが、いずれの方式も下記の欠点がある。
(1)隔板方式の欠点
本体円筒径と入り口径を同じ径にすることができるので、スポート式に比し装置がコンパクトになり、本機を小貯室に使用する場合、隔板スポートにより、供給盤上の粉面高さを一定にすることができるが、粉体によっては、隔板開口部の位置が中心部にあるため、上部撹拌体で隔板上を撹拌しても、開口部より外側の粉体は中心部に移動しにくいので、ホッパー側に開口径に相当するラットホールができ易い。又、上部の貯室が大型になると、ブリッジやラットホール防止のためのエアレーションやバイブレーターの影響で隔板が装備されていても供給盤上の粉圧は変動し易い。
供給盤と隔板間の空間には空マスの排出部の空気輸送用のエアーが持ち込まれ、上部空間内の空気圧力が上昇し、供給盤上の全粉面を加圧するので、空間内のエアー圧力が変動すると粉体の充填嵩密度が変動する。
(2)円筒・コーンスポート方式の欠点
円筒の場合、スポートの径は定量供給機の入り口径であり、その必要最小径は粉体の物性や供給能力等の要素で決まるため、スポートより大きい本体円筒径はスポートを使用しない場合に比し、本体の径が一回り大きくなるためコストが高くなる。
コーンスポート
コーンスポートの場合、スポートの入り口径より下端の径を小さくした逆円錐状のスポートを採用し、定量供給機の本体円筒径とスポート入り口径を同じにする方式があるが、逆円錐型のスポートは、粉体の嵩密度が低く、圧縮比が高い粉粒体(粉砕した廃プラ、やフラフ、溶融飛灰等)の場合スポート部にブリッジが発生し易い。
スポート方式は、回転体に対する粉圧緩和には大きな効果があるが、撹拌翼でスポートと底板の隙間より、本体円筒外周部の輸送空間に水平方向に粉体を掻き出す方式であり、スリキリ板がないスポート方式では、輸送空間内の粉面高さは粉圧変動の影響で変動するので、高い定量性能は得られない。
【0003】
【発明が解決しようとする課題】
本発明が解決しようとする課題は、従来のこれらの問題点を解消し、粉圧の影響を少なくでき、高精度の給粉を可能とする給粉方法及び装置を提供することにある。
【0004】
【課題を解決するための手段】
かかる課題を解決した本発明の構成は、
1) 粉粒体を貯えた貯室の底部に貯室内の粉粒体を上方開口から流下させて収容する収容空間を環状に形成した供給盤を回転自在に装置し、同収容空間の回送路の途中に収容空間内の粉粒体を貯室外へ排出する排出部を設け、収容空間の回送路の上方を粉粒体流下口を除いて閉鎖する隔板を設け、貯室内の粉粒体を粉粒体流下口から下方の供給盤の収容空間内へ流下させて充填し、排出部にて粉粒体を排出する給粉方法に於いて、
収容空間が供給盤外周に半径方向に突出させた羽根間に複数形成され、隔板を羽根の直上に設け、粉粒体流下口を複数箇所に分けて設けるとともに、隔板の粉粒体流下口の開口面積を排出部から回送方向まわりに大きくするようにし、排出部で排出した後の最初に流下させる粉粒体流下口を小さくして同粉粒体流下口からの粉粒体が収容空間の全空間に入らないようにし、最後に流下させる粉粒体流下口において全量が確実に充填させることによって粉圧の影響を少なくすることを特徴とする給粉方法
2) 最初に流下させる粉粒体流下口からの粉粒体が収容空間の容量の70%以下にしか収容されないようにした前記1)記載の給粉方法
3) 粉粒体を貯えた貯室の底部に貯室内の粉粒体を上方開口から流下させて収容する収容空間を環状に形成した供給盤を回転自在に装置し、同収容空間の回送路の途中に収容空間内の粉粒体を貯室外へ排出する排出部を設け、収容空間の回送路の上方を粉粒体流下口を除いて閉鎖する隔板を設け、粉粒体流下口を同隔板に複数設けるとともに、収容空間が供給盤外周に半径方向に突出させた羽根間に複数形成され、隔板を羽根の直上に設け、隔板の粉粒体流下口の開口面積を排出部から回送方向まわりに大きくするようにし、排出部で排出した後の最初に流下させる粉粒体流下口を小さくして同粉粒体流下口からの粉粒体が収容空間の全量が入らないようにし、最後に流下させる粉粒体流下口において全量が確実に充填させることによって粉圧の影響を少なくする給粉装置
4) 最初に流下させる粉粒体流下口からの粉粒体が収容空間の容量の70%以下にしか収容されないようにその粉粒体流下口の面積を小さくした前記3)記載の給粉装置
にある。
【0005】
【発明の実施の形態】
本発明の隔板は、供給盤の収容空間の回送路の上方を閉鎖するものでリング状又は円板状を普通とする。又隔板の粉粒体流下口は複数であるが最初に流下させる粉粒体流下口の面積は収容空間全部に粉粒体を充填させることがないように小さくし、3個の粉粒体流下口のときは4〜6割程を最初の粉粒体流下口で充填させ、残りの粉粒体流下口で全量充填するようにし、最後に流下させる粉粒体流下口において全量が確実に充填させるようにするのが好ましく、そのため回送方向にそって流下口の面積は大きくするのがよい。又最後に流下させる粉粒体流下口は排出部に近ずける方が粉圧の影響を少なくできるので好ましい。
供給盤の構造タイプとしては、外周に羽根を放射状に設け、羽根間に所要の粉粒体量を収容し、排出部で下方又は上方へ自重又は空気流で吐出させる構造、又は外周に環状溝又は棚を設け、排出部に設けたスクレーパーによって強制吐出する構造タイプが代表的な例である。
【0006】
【実施例】
以下、本発明の実施例を図面に基づいて説明する。本実施例はリングに羽根を放射状に複数枚突設し、羽根間と貯室の下部側面と底面とに囲われた空間に所定量の粉粒体を収容する収容空間を複数設け、同リングと羽根とから形成される供給盤を貯室中心に設けた回転軸でアームを介して回動し、又リング状の隔板を羽根の直上に貯室外壁側から固定させる。同隔板に4個所に粉粒体流下口を設け、回転方向に沿って漸次その開口面積を大きくした例である。最初の粉粒体流下口による充填率は略3〜4割程である。
図1は、実施例の縦断面図である。
図2は、実施例の平面図である。
図3は、実施例の隔板を示す拡大平面図である。
図4は、実施例の供給量と貯室粉粒体残量との関係図である。
図5は、排出部のみの隔板の場合の供給量と貯室粉粒体残量との関係図である。
【0007】
図中、Kは実施例の給粉装置、1は貯室、1aは貯室1の底面、1bは貯室1の側面、2は供給盤、2aは同供給盤のリング、2bは同リングから半径方向へ放射用に突出させた羽根、2cは同羽根と貯室1の底面1aと側面1bとによって囲われた収容空間、2dはリング2aを回転軸3に連結するアーム、3は回転軸、4は排出部、4aは同排出部4の底面1aに開口した排出口、4bは排出シュート、5は羽根2bの真上で貯室1の側面1bに取付けられた隔板、5a,5b,5c,5dは隔板5に設けた粉粒体の収容空間2cへの粉粒体流下口、6は回転軸3を回動するモータを用いた駆動部、Pは炭酸カルシウムの粉粒体である。
【0008】
この実施例では、粉粒体Pとして炭酸カルシウムが貯室1内に貯えられ、駆動部6を作動させて供給盤2を回転させる。貯室1内の粉粒体Pは隔板5及び中央の円状の底面1aの上に載り、隔板5の4個所の粉粒体流下口5a〜5dから下方へ落下して下方で回転している供給盤2の収容空間2cへ流入する。供給盤2の回転に伴ってアーム2dによって貯室1内の粉粒体は撹拌されている。
粉粒体流下口5a〜5dは、最初の粉粒体流下口5aの面積は最も小さく、この粉粒体流下口5aによって収容空間2cへ充填される粉粒体量は3〜4割程度であり、次の流下口5bの面積はやや大きく、これによって充填される割合は6〜8割程となり、次の流下口5cはかなり広く開口され、充填率は85〜95%程度であり、最後の流下口5dは最も広く開口され、100%以上の充填となり、軽く粉圧を受けるが排出部4に近いので粉圧を受けて強く加圧される前に排出部4へ到達し、同排出部4において底面1aの排出口4aから下方へ排出される。
この供給盤2の収容空間2cには4回に分けて粉粒体Pが流入するが、1〜2番目の粉粒体流下口5a,5bでは収容空間2cは充填されていない空間があり、充填に伴う空気の排気を容易にし、又充填された粉粒体Pの加圧はなされずに済む。そして3番目の粉粒体流下口5cで満杯に近く収容空間2dに充填されるが、加圧は強く作用されない。そして4番目の粉粒体流下口5dで完全に充填され、やや加圧状態になるが排出部4までの時間が短かいので加圧による影響はほとんどなく排出部4から下方へ排出される。
本実施例の粉粒体流下口5a〜5dと隔板5の作用を排出部4以外の隔板5を取り除いて開放した構造とし、同じ量の貯室1内の粉粒体量、実施例と同じ粉粒体、同じ供給盤回転数9rpmで回転させた場合と、本実施例の場合とでの供給量を貯室内粉粒体量(残量)との関係で計測した結果を図4,5に示す。
この図5から分るように、隔板5を取り除いた場合は、貯室の粉粒体残量が多いと供給量が高く残量が減少するにつれて供給量が低下し変動する。これは残量が粉圧として作用し、収容空間4の粉粒体が加圧され圧密状態であることが分る。
一方、本実施例の場合は、図4に示すように残量が大巾に減るまで略一定の供給量を得ることができるものである。即ち、残量(貯室内の粉粒体圧力)の影響を受けないことが分る。尚残量が大巾に低下して供給量が変化する前に貯室に粉粒体を補充することで残量が著しく減少したときの供給量の低下は解消できる。
【0009】
【発明の効果】
以上の様に、本発明によれば隔板に複数の流下口を設け、最初から満杯に充填させないようにすることで、貯室内の粉粒体の粉圧及びその変化(貯室内の粉粒体量の変化)による供給量の影響を大巾に遮断でき、より高精度の給粉を可能にできるものとした。
【図面の簡単な説明】
【図1】実施例の縦断面図である。
【図2】実施例の平面図である。
【図3】実施例の隔板を示す拡大平面図である。
【図4】実施例の供給量と貯室粉粒体残量との関係図である。
【図5】排出部のみの隔板の場合の供給量と貯室粉粒体残量との関係図である。
【符号の説明】
K 給粉装置
P 粉粒体
1 貯室
1a 底面
1b 側面
2 供給盤
2a リング
2b 羽根
2c 収容空間
2d アーム
3 回転軸
4 排出部
4a 排出口
4b 排出シュート
5 隔板
5a,5b,5c,5d 流下口
6 駆動部[0001]
BACKGROUND OF THE INVENTION
The present invention is a powder feeder that powders a necessary amount of powder stored in a storage chamber to the outside, and a method and a powder feeder capable of reducing the influence of powder pressure and enabling highly accurate powder feeding About.
[0002]
[Prior art]
Conventionally, a supply disk that rotates at the bottom of the storage room for the granular material is provided, and a required amount of the granular material flows into the storage space on the upper surface of the rotary body, and the supply disk is rotated and discharged outside the storage room. Powder machines are widely used.
The rotation path of the storage space of the supply panel was used with an open structure leaving the discharge part. However, the powder pressure in the storage chamber acts on the storage space for a long time, and the powder particles in the storage space are seen from above. The pressure was increased by the powder pressure, and the bulk density became high, or the flow was unstable because the powder particles from above were moved. In order to solve this problem, a structure has been developed in which a partition plate is provided above the feeding path of the storage space of the supply board, and an inflow port through which the granular material flows into the storage space below is opened. This granular material inlet has one opening and has a slightly wide opening area sufficient to fill the accommodating space with the granular material. However, the powder pressure in the storage chamber acts from this granular material inlet and is also pressurized by the powder pressure, increasing the bulk specific gravity and reducing the powder feeding accuracy. In detail,
In a single-shaft powder metering machine equipped with a powder supply plate that rotates concentrically with the center of the storage chamber, the powder pressure applied to the blades of the supply plate is equal to the powder surface height of the storage chamber. For the phenomenon in which the bulk density of the powder filled in the blades fluctuates due to fluctuations, the influence of charge impact on the storage chamber, and the fluctuation of powder pressure due to the influence of aeration and vibrator to prevent bridge phenomenon and rathole phenomenon In conventional quantitative feeders, the diaphragm sport method and the cylindrical / cones sport method are widely used as measures for preventing fluctuations in powder pressure in the blades, but each method has the following drawbacks.
(1) Disadvantages of the diaphragm system Since the cylinder diameter and the entrance diameter of the main body can be made the same diameter, the device is more compact than the sport system, and when this machine is used in a small storage chamber, The height of the powder surface on the supply board can be made constant, but depending on the powder, the position of the opening of the partition plate is in the center, so even if the upper stirring body is stirred on the partition plate, the opening Since the powder outside the portion hardly moves to the center, a rat hole corresponding to the opening diameter is easily formed on the hopper side. In addition, when the upper storage chamber is large, the powder pressure on the supply panel is likely to fluctuate even if a partition plate is equipped due to the influence of aeration and a vibrator for preventing bridges and ratholes.
Air for air transportation of the empty mass discharge part is brought into the space between the supply panel and the partition plate, the air pressure in the upper space rises and pressurizes all powder surfaces on the supply panel, so When the air pressure varies, the filling bulk density of the powder varies.
(2) Cylinder / conesport type defects In the case of a cylinder, the diameter of the sport is the entrance diameter of the metering feeder, and the required minimum diameter is determined by factors such as the physical properties and supply capacity of the powder. The diameter of the cylinder is higher than that in the case where no sport is used, so the diameter of the main body becomes one size larger and the cost becomes higher.
In the case of Cornsport Cone Sport, there is a method that uses an inverted conical sport with a lower end diameter smaller than the entrance diameter of the sport and makes the cylindrical diameter of the meter feeder and the sport entrance diameter the same. In the case of a powder, when the powder has a low bulk density and a high compression ratio (such as pulverized waste plastic, fluff, molten fly ash, etc.), bridging is likely to occur in the sport part.
The sport method has a great effect on reducing the powder pressure on the rotating body, but it is a method that scrapes the powder horizontally in the transport space of the outer periphery of the main body cylinder from the gap between the sport and the bottom plate with a stirring blade. With no sport system, the powder surface height in the transport space fluctuates due to fluctuations in powder pressure, so high quantitative performance cannot be obtained.
[0003]
[Problems to be solved by the invention]
The problem to be solved by the present invention is to provide a powder feeding method and apparatus that eliminates these conventional problems, reduces the influence of powder pressure, and enables highly accurate powder feeding.
[0004]
[Means for Solving the Problems]
The configuration of the present invention that solves this problem is as follows.
1) A feed board in which a storage space in which the powder particles in the storage chamber are flowed down from the upper opening and accommodated in an annular shape is rotatably installed at the bottom of the storage chamber in which the powder particles are stored, and the transfer path of the storage space In the middle of the storage space, a discharge part for discharging the granular material in the storage space to the outside of the storage chamber is provided, and a partition plate for closing the upper part of the storage space except the granular material outlet is provided, and the granular material in the storage space In the powder feeding method, the powder is flowed down from the lower part of the granular material flow into the storage space of the lower supply panel, and the granular material is discharged at the discharge part.
A plurality formed between the accommodation space is projected in the radial direction to the feed plate outer peripheral vanes, it provided the diaphragm directly above the blade, provided with separately granular material falling port at a plurality of locations, granular material stream of diaphragm The opening area of the mouth is increased from the discharge part around the direction of forwarding, and the powder flow from the discharge part is accommodated by reducing the first drop of the powder that flows down after discharge from the discharge part. Powder supply method characterized by reducing the influence of powder pressure by ensuring that the entire amount is filled at the outlet of the granular material to be flown down last so that it does not enter the entire space 2) Powder to be flowed down first The powder feeding method according to 1) above, wherein the granular material from the lower outlet of the granular material is accommodated only in 70% or less of the capacity of the accommodating space. 3) Powder in the storage chamber at the bottom of the storage chamber storing the granular material An accommodation space for accommodating particles by flowing down from the upper opening is formed in an annular shape. The formed supply board is rotatably installed, and a discharge unit is provided in the middle of the transfer path of the storage space to discharge the powder in the storage space to the outside of the storage chamber. A partition plate that is closed except for the mouth is provided, and a plurality of granular material flow-down ports are provided in the partition plate, and a plurality of storage spaces are formed between the blades that protrude radially from the outer periphery of the supply plate. It is provided directly above, and the opening area of the granule flow outlet of the partition plate is increased from the discharge part around the feeding direction.
[0005]
DETAILED DESCRIPTION OF THE INVENTION
The partition plate of the present invention closes the upper part of the feeding path of the accommodation space of the supply board, and is usually ring-shaped or disk-shaped. In addition, there are a plurality of powder outlets on the partition plate, but the area of the powder outlet to be flowed down first is small so that the entire accommodation space is not filled with powder, and three powders At the flow outlet, about 40 to 60% is filled at the first granule flow outlet, and the remaining powder flow is filled at all, and the final flow at the final flow is ensured. It is preferable to make it fill, so that the area of the flow-down port should be increased along the direction of feeding. In addition, it is preferable that the outlet of the granular material flowed down last is closer to the discharge portion because the influence of the powder pressure can be reduced.
As the structure type of the supply board, blades are provided radially on the outer periphery, the required amount of powder is accommodated between the blades, and the discharge part is discharged downward or upward by its own weight or air flow, or an annular groove on the outer periphery Or the structure type which provides a shelf and forcibly discharges it with the scraper provided in the discharge part is a typical example.
[0006]
【Example】
Embodiments of the present invention will be described below with reference to the drawings. In this embodiment, a plurality of blades project radially from the ring, and a plurality of storage spaces for storing a predetermined amount of powder particles are provided in a space surrounded by the blades and the lower side surface and bottom surface of the storage chamber. A supply board formed of a blade and a blade is rotated through an arm by a rotation shaft provided at the center of the storage chamber, and a ring-shaped partition plate is fixed directly above the blade from the storage chamber outer wall side. This is an example in which the granular material flow outlets are provided at four locations on the partition plate and the opening area is gradually increased along the rotation direction. The filling rate by the first granular material lowering port is about 30 to 40%.
FIG. 1 is a longitudinal sectional view of the embodiment.
FIG. 2 is a plan view of the embodiment.
FIG. 3 is an enlarged plan view showing the partition plate of the embodiment.
FIG. 4 is a diagram showing the relationship between the supply amount of the example and the remaining amount of powder in the storage chamber.
FIG. 5 is a diagram showing the relationship between the supply amount and the remaining amount of powder in the storage chamber in the case of the partition plate having only the discharge part.
[0007]
In the figure, K is a powdering device of the embodiment, 1 is a storage chamber, 1a is a bottom surface of the
[0008]
In this embodiment, calcium carbonate is stored in the
The granular material flow
Although the granular material P flows into the
It is set as the structure which removed the
As can be seen from FIG. 5, when the
On the other hand, in this embodiment, as shown in FIG. 4, a substantially constant supply amount can be obtained until the remaining amount is greatly reduced. That is, it can be seen that there is no influence of the remaining amount (powder body pressure in the storage chamber). In addition, the fall of supply amount when the remaining amount reduces remarkably can be eliminated by replenishing a granular material to a storage chamber before the remaining amount falls greatly and a supply amount changes.
[0009]
【The invention's effect】
As described above, according to the present invention, by providing a plurality of flow-down openings in the partition plate so as not to be filled completely from the beginning, the powder pressure in the reservoir and its change (powder in the reservoir) The effect of the supply amount due to changes in body weight can be largely blocked, and more accurate powder feeding can be achieved.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view of an embodiment.
FIG. 2 is a plan view of the embodiment.
FIG. 3 is an enlarged plan view showing a partition plate according to an embodiment.
FIG. 4 is a diagram showing the relationship between the supply amount of the example and the remaining amount of powder in the storage chamber.
FIG. 5 is a diagram showing the relationship between the supply amount and the remaining amount of powder in the storage chamber in the case of a partition plate with only a discharge part.
[Explanation of symbols]
K powder supply device P
Claims (4)
収容空間が供給盤外周に半径方向に突出させた羽根間に複数形成され、隔板を羽根の直上に設け、粉粒体流下口を複数箇所に分けて設けるとともに、隔板の粉粒体流下口の開口面積を排出部から回送方向まわりに大きくするようにし、排出部で排出した後の最初に流下させる粉粒体流下口を小さくして同粉粒体流下口からの粉粒体が収容空間の全空間に入らないようにし、最後に流下させる粉粒体流下口において全量が確実に充填させることによって粉圧の影響を少なくすることを特徴とする給粉方法。At the bottom of the storage chamber for storing the powder particles, a feeding board in which a storage space for storing the powder particles in the storage chamber by flowing down from the upper opening is annularly rotated, and the transfer space of the storage space is on the way Provided with a discharge part that discharges the granular material in the storage space to the outside of the storage room, and provided with a partition that closes the upper part of the feeding path of the storage space except for the powder flow outlet, to powder the granular material in the storage room In the powder supply method of flowing and filling from the lower part of the granular material flow into the storage space of the lower supply board, and discharging the granular material at the discharge part,
A plurality formed between the accommodation space is projected in the radial direction to the feed plate outer peripheral vanes, it provided the diaphragm directly above the blade, provided with separately granular material falling port at a plurality of locations, granular material stream of diaphragm The opening area of the mouth is increased from the discharge part around the direction of forwarding, and the powder flow from the discharge part is accommodated by reducing the first drop of the powder that flows down after discharge from the discharge part. A powder feeding method characterized by reducing the influence of powder pressure by ensuring that the entire amount is filled at the outlet of the granular material flowing down so as not to enter the entire space and finally flowing down .
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JP2000040836A JP4439659B2 (en) | 2000-02-18 | 2000-02-18 | Powdering method and apparatus |
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JP2000040836A JP4439659B2 (en) | 2000-02-18 | 2000-02-18 | Powdering method and apparatus |
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JP4439659B2 true JP4439659B2 (en) | 2010-03-24 |
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