JPS605489B2 - Screw conveyor for powder and granules - Google Patents
Screw conveyor for powder and granulesInfo
- Publication number
- JPS605489B2 JPS605489B2 JP50126631A JP12663175A JPS605489B2 JP S605489 B2 JPS605489 B2 JP S605489B2 JP 50126631 A JP50126631 A JP 50126631A JP 12663175 A JP12663175 A JP 12663175A JP S605489 B2 JPS605489 B2 JP S605489B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- screw conveyor
- cylindrical body
- spiral body
- 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
Links
Landscapes
- Screw Conveyors (AREA)
Description
【発明の詳細な説明】
本発明は、上下方向姿勢の筒体内面に沿って回転する連
続螺旋体により粉粒体を賜送する粉粒体用スクリューコ
ンベヤーに関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a screw conveyor for powder and granular material that conveys powder and granular material by a continuous spiral body that rotates along the inner surface of a cylindrical body in a vertical orientation.
従来では一般に、長さ方向で同一直径の円筒内に連続螺
旋体を収納してスクリューコンベヤーが構成されている
。Conventionally, a screw conveyor is generally constructed by housing a continuous spiral body within a cylinder having the same diameter in the length direction.
このようなスクリューコンベヤーを粉粒体の錫送に用い
るときには、粉粒体と前記螺旋体との共回りを避けて効
率のよい錫送を行うために、螺旋体のピッチを水平搬送
のときよりも小さくとることが考えられている。つまり
、これは螺旋体が回転軸と成す傾斜角を大きくして粉粒
体に与える回転方向の分力を減じ上方への分力を増強す
るものであって、通常技術の常識とされているが、この
ようなものであっても前記共回りに対する良好な対策と
はなっておらず、依然としてその錫送効率は低く、特に
、前記傾斜角が必然的に小さくなる回転軸付近では粉粒
体が全く揚送されずに滞留するのが実状であり、前記円
筒内で粉粒体の詰りが発生した場合にはそれを解消する
手段も見し、出し得ないものであった。本第1発明は、
上記実状に鑑みてなされたものであって、錫送効率が高
く、しかも粉粒体の筒体内での詰まりによる搬送トラブ
ルも防止できる有用な錫送用の粉粒体用スクリューコン
ベヤーを提供することを目的とし、また本第2発明は、
本第1発明の粉粒体用スクリューコンベヤーに更に改良
を加えてより一層滞留のない円滑確実な揚送を行える粉
粒体用スクリューコンベヤーを提供することを目的とす
る。When such a screw conveyor is used to transport powder and granules, the pitch of the spiral is made smaller than when horizontally conveying, in order to avoid co-rotation of the powder and the spiral body and carry out efficient tin transport. It is considered to be taken. In other words, this is a method that increases the angle of inclination that the helix forms with the axis of rotation, reduces the component force in the rotational direction applied to the powder, and increases the component force in the upward direction, which is considered common knowledge in the art. However, even such a device is not a good countermeasure against the co-rotation, and its tin feeding efficiency is still low, especially in the vicinity of the rotation axis where the inclination angle is inevitably small. The reality is that the powder remains without being pumped up at all, and when powder or granules become clogged in the cylinder, no means have been found to solve the problem. The first invention is
To provide a useful screw conveyor for powder and granular material for tin transport, which has been developed in view of the above-mentioned circumstances, and which has high tin transport efficiency and can prevent transport troubles due to clogging of the powder or granular material in a cylindrical body. The purpose of the second invention is to
It is an object of the present invention to further improve the screw conveyor for powder and granular materials of the first invention, and to provide a screw conveyor for powder and granular materials that can carry out smooth and reliable lifting without stagnation.
本第1発明は、上下方向姿勢の筒体内面に沿って回転す
る連続螺旋体により粉粒体を揚送する粉粒体用スクリュ
ーコンベヤーにおいて、前記連続螺旋体を薄板から構成
して前記筒体と同芯状の回転軸に架設すると共に、前記
筒体の内部空間横断面積を上方に向かうに従い連続的に
拡大し、且つ、前記螺旋体の外径をト前記筒体と前記螺
旋体との間隙をほぼ一定にしながらその筒体の内面に沿
うべく上方に向かうに従い連続的に拡大してある点を特
徴とする。The first invention provides a screw conveyor for powder and granular materials that transports powder and granular materials by a continuous spiral body that rotates along the inner surface of a cylindrical body in an up-down direction, in which the continuous spiral body is constructed from a thin plate, and is identical to the cylindrical body. The cylindrical body is installed on a core-shaped rotating shaft, and the cross-sectional area of the internal space of the cylindrical body is continuously expanded upward, and the outer diameter of the helical body is set such that the gap between the cylindrical body and the helical body is approximately constant. It is characterized by the fact that it expands continuously as it goes upward along the inner surface of the cylindrical body.
このような構成によって、粉粒体には楊送方向上方側ほ
ど回転半径が拡大する薄板から構成された螺旋体の広い
受面によって、遠心力に起因した筒体内面への押し付け
力が確実に上方側ほど強く作用する。With this configuration, the pushing force against the inner surface of the cylindrical body due to centrifugal force is reliably applied upward to the powder body due to the wide receiving surface of the helical body made of thin plates whose rotation radius increases upward in the pumping direction. It acts more strongly on the side.
この力のためにト粉粒体は筒体内面との抵抗で前記螺旋
体との共回りから開放され、粉粒体は上方に至るほど筒
体内面に沿って回転する薄板状の螺旋体の揚送力を受け
易い形となり、またこの粉粒体には傾斜する筒内面への
押し付けによって生じる上方への錫送分力が確実に作用
し、更に粉粒体を受ける螺旋体の受面が上方側ほど大き
くなるために、搬送される粉粒体は上方に至るほど筒体
内空間に対する単位体積当りの密度が減少して、筒体内
での語りなく錫送能力が一層増大する。しかも、粉粒体
の錫送には薄板の螺旋体を、上下方向姿勢の筒体内面に
沿わせて回転させることによって「筒体と螺旋体との間
に粉が挟圧されてしまうことも当然少なく、全体として
粉粒体の楊送を効率良く確実に行なうことができる。Due to this force, the powder and granules are released from co-rotation with the spiral body due to the resistance with the inner surface of the cylinder, and the powder and granules are lifted up by the thin plate-shaped spiral body that rotates along the inner surface of the cylinder as it reaches the upper part. The powder is shaped to be easily susceptible to force, and the upward tin feeding force generated by pressing against the inclined cylinder inner surface acts reliably on the powder, and the receiving surface of the spiral body that receives the powder is more likely to Because of the increased size, the density per unit volume of the transported granular material with respect to the space inside the cylinder decreases as it reaches upward, and the ability to feed tin without any interference inside the cylinder further increases. Moreover, in order to feed powder and granules, a thin plate spiral body is rotated along the inner surface of a cylindrical body in an up-and-down direction, which naturally reduces the possibility of powder being pinched between the cylindrical body and the spiral body. As a whole, the powder can be transported efficiently and reliably.
また仮に、前記筒体内部の中間部で詰りが生じても「前
述した筒体上下方向での筒体内空間に対する単位体積当
りの粉粒体密度の差等の要因によって上方へ移行し易い
状態が現出されているのでその語り等も容易に解消され
る利点がある。Furthermore, even if clogging occurs in the middle part of the inside of the cylinder, it is likely that it will move upward due to factors such as the difference in powder density per unit volume with respect to the space inside the cylinder in the vertical direction of the cylinder. There is an advantage that the story etc. can be easily solved because it is exposed.
また本第2発明は上下方向姿勢の筒体内面に沿って回転
する連続螺旋体により粉粒体を錫送する粉粒体用スクリ
ューコンベヤーにおいて「前記連続螺旋体を薄板から構
成して前記筒体と同芯状の回転軸に架設すると共に、前
記筒体の内部空間横断面積を上方に向かうに従い連続的
に拡大し、且つ、前記螺旋体の外径を、前記筒体と前記
螺旋体との間隙をほぼ一定にしながらその筒体の内面に
沿うべく上方に向かうに従い連続的に拡大してある粉粒
体用スクリューコンベヤーであって、前記螺旋体の回転
軸における軸径を上方側ほど拡大してある事を特徴とす
る。すなわち、錫送力が外周部よりも極めて小さい螺旋
体の回転軸付近では粉粒体の滞留が生じ易く、この点に
着目したものが本第2発明であって「 この本第2発明
では積極的に軸部分の径を上方に至るほど拡大し、楊送
力が大きい螺旋体外周部近くに粉粒体を押し出すことに
よって前記滞留の問題を解消し、長期に亘つて滞留する
粉粒体が変質や腐敗することによる悪影響を回避できる
とともに、前述第1発明において述べた効果をより一層
確実なものとできる利点がある。In addition, the second invention provides a screw conveyor for powder and granular material that transports powder and granular material by means of a continuous spiral body rotating along the inner surface of a cylinder in an up-down direction. The cylindrical body is installed on a core-shaped rotating shaft, and the cross-sectional area of the internal space of the cylindrical body is continuously expanded upward, and the outer diameter of the helical body is kept constant, and the gap between the cylindrical body and the helical body is approximately constant. A screw conveyor for powder and granular materials, which continuously expands upward along the inner surface of the cylindrical body, and is characterized in that the shaft diameter of the rotating shaft of the spiral body increases upwardly. In other words, particles tend to stagnate near the rotating shaft of the helix where the tin feeding force is much smaller than that at the outer periphery, and this second invention focuses on this point. In this case, the diameter of the shaft portion is actively expanded upward, and the powder and granules are pushed out near the outer periphery of the helix where the pumping force is large. This solves the problem of stagnation. This has the advantage that it is possible to avoid the adverse effects caused by deterioration and decay of the material, and to further ensure the effects described in the first invention.
次に、本発明の実施例を図面に基づいて説明する。Next, embodiments of the present invention will be described based on the drawings.
両端が閉じられた筒体1内に、同芯状に回転軸2を架設
すると共に、回転軸2に薄板から成る連続螺旋体3を装
着し、もつて、モーター4により螺旋体3を筒体1の内
面に沿って回転駆動させて、下方の供給口5から上方の
排出口6に向かって回転軸芯方向に錫送するためのスク
リューコンベヤーを構成してある。A rotating shaft 2 is installed concentrically within a cylinder 1 with both ends closed, and a continuous spiral body 3 made of a thin plate is attached to the rotating shaft 2. Then, a motor 4 moves the spiral body 3 into the cylinder body 1. A screw conveyor is configured to be driven to rotate along the inner surface and to feed tin in the direction of the rotation axis from the lower supply port 5 toward the upper discharge port 6.
筒体1‘ま、その内部空間横断面積が搬送方向側ほど連
続的に拡大すべく、回転軸2軸芯に対して筒体】内壁面
を傾斜させてあり、この傾斜する内壁面と螺旋体3との
間隙をほぼ一定にしながら、その内壁面に沿うように螺
旋体の外径も拡大し、かつ「螺旋体3のピッチLは全体
にわたって一定であり、その結果、螺旋体3のリード角
(回転軸に直交する面に対して螺旋体3が成す角)は上
方側ほど小さくなっている。The inner wall surface of the cylinder 1' is inclined with respect to the two rotational axes so that the cross-sectional area of the internal space thereof increases continuously toward the conveyance direction, and this inclined inner wall surface and the spiral body 3 The outer diameter of the helical body is expanded along the inner wall surface while keeping the gap between the helical body and the helical body almost constant. The angle formed by the spiral body 3 with respect to a perpendicular plane becomes smaller toward the upper side.
排出口5を、第2図に示すように、螺旋体3のほぼ接線
方向に向かって関口ごせると共に、排出口5に向かって
螺旋体3の粉粒体を掻出すための、好ましくは角度変更
可能なスクレーバー7を筒体1に付設し、もって、粉粒
体が円滑かつ確実に排出されるべく構成してある。As shown in FIG. 2, the discharge port 5 can be moved in a substantially tangential direction to the spiral body 3, and preferably the angle can be changed in order to scrape out the granular material of the spiral body 3 toward the discharge port 5. A scraper 7 is attached to the cylindrical body 1, so that the powder and granules can be smoothly and reliably discharged.
上述のように、筒体1の内部空間横断面積を搬送方向側
ほど拡大させる事によって「螺旋体3どうしの間に位置
する空間の容積を搬送方向側ほど増大させ、もって「筒
体1上方側における粉粒体の筒体内空間に対する単位体
積当りの密度を減少し、上方へ移行し易い形態を現出さ
せて粉粒体の詰りを回避できる。As mentioned above, by increasing the cross-sectional area of the internal space of the cylinder 1 toward the conveyance direction, the volume of the space located between the helical bodies 3 increases toward the conveyance direction. It is possible to reduce the density per unit volume of the powder and granular material with respect to the space within the cylindrical body, and to create a form in which the powder and granular material can easily move upward, thereby avoiding clogging of the powder and granular material.
同時に、搬送方向側ほど螺旋体3の羽根外周部分は水平
姿勢に近づくので螺旋体3と粉粒体との共回りが一層生
じにくくなって、搬送遅れの蓄積が抑制され、しかも、
螺旋体3のピッチは一定であるから、効率の良い搬送機
能は据われない。第3図に示すスクリューコンベヤーは
「回転軸2の形状のみを先の実施例に対して変更したも
のであり、回転軸2の径を搬送方向側ほど増大させてあ
る。At the same time, since the outer circumferential portion of the blade of the spiral body 3 approaches the horizontal position as it approaches the conveyance direction, co-rotation of the spiral body 3 and the granular material becomes more difficult to occur, and the accumulation of conveyance delays is suppressed.
Since the pitch of the spiral body 3 is constant, an efficient conveyance function cannot be established. In the screw conveyor shown in FIG. 3, only the shape of the rotating shaft 2 is changed from the previous embodiment, and the diameter of the rotating shaft 2 is increased toward the conveying direction.
すなわち、螺旋体3の回転軸芯に対する筒体1内壁面の
傾斜角を大きくしても、筒体1内壁面と回転軸2との距
離が必要以上に増大しないように、回転軸2の径を搬送
方向側ほど増大すべ〈構成し、もって、回転軸2付近の
螺旋体3上に載った搬送物が、螺旋体3と一体的に回転
して、搬送されなくなる事を防止してある。尚、本発明
において、螺旋体3のリード角が搬送方向側ほど増大し
ない範囲において、螺旋体3のピッチを搬送方向側ほど
増長させても良く、その場合、搬送速度を高められる効
果がある。That is, even if the inclination angle of the inner wall surface of the cylinder 1 with respect to the rotation axis of the spiral body 3 is increased, the diameter of the rotation shaft 2 is adjusted so that the distance between the inner wall surface of the cylinder 1 and the rotation shaft 2 does not increase more than necessary. The conveyance direction increases as the conveyance direction increases, thereby preventing the conveyed object placed on the spiral body 3 near the rotating shaft 2 from rotating integrally with the spiral body 3 and not being conveyed. In the present invention, the pitch of the spiral body 3 may be increased toward the conveyance direction as long as the lead angle of the helix 3 does not increase toward the conveyance direction. In this case, the conveyance speed can be increased.
図面は本発明に係る粉粒体用スクリューコンベヤーの実
施例を示し、第1図は第1発明を示す縦断面図、第2図
は第1図におけるローロ線断面図、第3図は第2発明を
示す縦断面図である。
1・・・・・・筒体「 2…・・・回転軸、3・・・螺
旋体。
第1図第2図
第3図The drawings show an embodiment of the screw conveyor for powder and granular materials according to the present invention, FIG. 1 is a longitudinal sectional view showing the first invention, FIG. 2 is a sectional view taken along the Rollo line in FIG. 1, and FIG. FIG. 2 is a longitudinal cross-sectional view showing the invention. 1... Cylindrical body 2... Rotating shaft, 3... Spiral body. Figure 1 Figure 2 Figure 3
Claims (1)
旋体3により粉粒体を揚送する粉粒体用スクリユーコン
ベヤーにおいて、前記連続螺旋体3を薄板から構成して
前記筒体1と同芯状の回転軸2に架設すると共に、前記
筒体1の内部空間横断面積を上方に向かうに従い連続的
に拡大し、且つ、前記螺旋体3の外径を、前記筒体1と
前記螺旋体3との間隙をほぼ一定にしながらその筒体1
の内面に沿うべく上方に向かうに従い連続的に拡大して
あることを特徴とする粉粒体用スクリユーコンベヤー。 2 上下方向姿勢の筒体1内面に沿って回転する連続螺
旋体3により粉粒体を揚送する粉粒体用スクリユーコン
ベヤーにおいて、前記連続螺旋体3を薄板から構成して
前記筒体1と同芯状の回転軸2に架設すると共に、前記
筒体1の内部空間横断面積を上方に向かうに従い連続的
に拡大し、且つ、前記螺旋体3の外径を、前記筒体1と
前記螺旋体3との間隙をほぼ一定にしながらその筒体1
の内面に沿うべく上方に向かうに従い連続的に拡大して
ある粉粒体用スクリユーコンベヤーであって、前記螺旋
体3の回転軸2における軸径を上方側ほど拡大してある
ことを特徴とする粉粒体用スクリユーコンベヤー。[Scope of Claims] 1. A screw conveyor for powder and granular materials that transports powder and granular materials by a continuous spiral body 3 that rotates along the inner surface of a cylinder 1 in a vertical orientation, wherein the continuous spiral body 3 is constructed from a thin plate. The helical body 3 is installed on a rotating shaft 2 concentric with the cylindrical body 1, and the cross-sectional area of the internal space of the cylindrical body 1 is continuously expanded upward, and the outer diameter of the helical body 3 is 1 and the spiral body 3 while keeping the gap substantially constant.
1. A screw conveyor for powder and granular material, characterized in that the screw conveyor is continuously enlarged upward to follow the inner surface of the powder. 2. In a screw conveyor for powder and granular materials that transports powder and granular material by a continuous spiral body 3 rotating along the inner surface of a cylinder 1 in a vertical orientation, the continuous spiral body 3 is constructed from a thin plate and is the same as the cylinder 1. The cylindrical body 1 is installed on a core-shaped rotating shaft 2, and the internal space cross-sectional area of the cylindrical body 1 is continuously expanded upward, and the outer diameter of the helical body 3 is made different from that of the cylindrical body 1 and the helical body 3. While keeping the gap almost constant, the cylindrical body 1
This screw conveyor for powder and granular materials is continuously enlarged upward to follow the inner surface of the screw conveyor, and is characterized in that the shaft diameter of the rotating shaft 2 of the spiral body 3 is enlarged upward. Screw conveyor for powder and granular materials.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US424311A US3917753A (en) | 1972-12-15 | 1973-12-13 | Phosphorothionoamidates |
JP50126631A JPS605489B2 (en) | 1975-10-20 | 1975-10-20 | Screw conveyor for powder and granules |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50126631A JPS605489B2 (en) | 1975-10-20 | 1975-10-20 | Screw conveyor for powder and granules |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5251675A JPS5251675A (en) | 1977-04-25 |
JPS605489B2 true JPS605489B2 (en) | 1985-02-12 |
Family
ID=14939958
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP50126631A Expired JPS605489B2 (en) | 1972-12-15 | 1975-10-20 | Screw conveyor for powder and granules |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS605489B2 (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3056487A (en) * | 1959-12-30 | 1962-10-02 | Wyatt & Kipper Engineers Inc | Screw conveyor for fibrous material |
JPS442182Y1 (en) * | 1965-07-30 | 1969-01-27 |
-
1975
- 1975-10-20 JP JP50126631A patent/JPS605489B2/en not_active Expired
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3056487A (en) * | 1959-12-30 | 1962-10-02 | Wyatt & Kipper Engineers Inc | Screw conveyor for fibrous material |
JPS442182Y1 (en) * | 1965-07-30 | 1969-01-27 |
Also Published As
Publication number | Publication date |
---|---|
JPS5251675A (en) | 1977-04-25 |
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