JPH07106791B2 - Rotary feeder - Google Patents
Rotary feederInfo
- Publication number
- JPH07106791B2 JPH07106791B2 JP61277371A JP27737186A JPH07106791B2 JP H07106791 B2 JPH07106791 B2 JP H07106791B2 JP 61277371 A JP61277371 A JP 61277371A JP 27737186 A JP27737186 A JP 27737186A JP H07106791 B2 JPH07106791 B2 JP H07106791B2
- Authority
- JP
- Japan
- Prior art keywords
- rotor
- recess
- concave portion
- granular material
- angle
- 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 - Lifetime
Links
Landscapes
- 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〕 本発明は、ケーシング内に、周方向に複数の凹部を設け
たローターを、横軸芯周りで回転自在に設けると共に、
前記ローターへの粉粒体の自重供給路と、前記ローター
からの粉粒体の自重放出路を形成し、前記ローターを介
して前記自重供給路と自重放出路とを仕切る第1、第2
隔壁部を、前記ケーシングに設けてあるロータリーフィ
ーダーに関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention provides a rotor having a plurality of recesses provided in the casing in a circumferential direction so as to be rotatable about a horizontal axis,
First and second parts for forming a self-weight supply path for the powder and granules to the rotor and a self-weight discharge path for the powder and granules from the rotor, and partitioning the self-weight supply path and the self-weight discharge path through the rotor.
The present invention relates to a rotary feeder having a partition wall provided in the casing.
従来、上記ロータリーフィーダーでは、第11図に示すよ
うに、ローター(2)の回転に伴って粉粒体を収容した
凹部(3)が通過する側の第1隔壁部(4)と、粉粒体
を放出した空の凹部(3)が通過する側の第2隔壁部
(5)を、ローター(2)の回転軸芯(0)のレベルを
中心として上下にわたって形成してあると共に、前記凹
部(3)内面の回転方向に向かう第1面(8)と回転方
向後方に向かう第2面(9)とを、夫々平面に形成して
あった。Conventionally, in the above rotary feeder, as shown in FIG. 11, the first partition wall portion (4) on the side through which the concave portion (3) accommodating the powder and granules passes along with the rotation of the rotor (2) and the powder and granules. The second partition wall (5) on the side through which the empty recessed portion (3) having discharged the body passes is formed vertically above and below the level of the rotational axis (0) of the rotor (2), and the recessed portion is formed. (3) The first surface (8) directed in the rotational direction of the inner surface and the second surface (9) directed rearward in the rotational direction are each formed into a flat surface.
しかし、特に第1隔壁部(4)におけるローター(2)
の回転軸芯(0)のレベルより低い部分に、凹部(3)
内に収容した粉粒体が、自重で押付けられ、ローター
(2)が回転するに伴って、押付力の働いた粉粒体を摺
動させながら通過するために、第1隔壁部(4)が摩耗
しやすくなり、しかも、第1隔壁部(4)下端を凹部
(3)が通過すると、その凹部(3)は下向きに開口す
るために、凹部(3)内の粉粒体は一度に自重放出路
(Y)に落下してしまうおそれがあり、また、第2隔壁
部(5)においては、その上端を凹部(3)が通過する
に伴って、凹部(3)は上向きに開口して、急激に粉粒
体が凹部(3)内に侵入するために、粒度分布の広い粉
粒体にあっては、凹部(3)毎に収容する粉粒体の密度
及び重量にバラ付きが生じて、均一な供給ができなくな
るという問題があった。However, especially the rotor (2) in the first partition (4)
In the portion lower than the level of the rotary shaft core (0) of
The first partition wall portion (4) passes through while the powder or granular material contained therein is pressed by its own weight and the rotor (2) rotates and the powder or granular material on which the pressing force acts is slidably passed. Are easily worn, and when the concave portion (3) passes through the lower end of the first partition wall portion (4), the concave portion (3) opens downward, so that the powder or granular material in the concave portion (3) is removed at once. There is a risk of falling into the self-weight discharge path (Y), and in the second partition wall portion (5), the recess (3) opens upward as the recess (3) passes through the upper end thereof. Then, since the granular material rapidly invades into the concave portion (3), in the granular material having a wide particle size distribution, the density and weight of the granular material accommodated in each concave portion (3) vary. However, there is a problem in that uniform supply cannot be achieved.
第1発明の目的は、第1隔壁部を摩耗しにくくすると共
に、自重放出路に粉粒体を定量づつ連続的に落下放出で
きるようにする点にある。An object of the first invention is to make it difficult for the first partition wall to be worn, and to make it possible to continuously drop and discharge the powdery particles into the dead weight discharge path in a quantitative manner.
本第1発明のロータリーフィーダーの特徴構成は、ロー
ターの回転に伴って粉粒体を収容した凹部が通過する側
の第1隔壁部を、前記ローターの回転軸芯よりも高いレ
ベルに形成し、前記ローターの横断面視で、前記第1隔
壁部における前記ローター回転方向の下手側端縁を、前
記端縁を含む水平線とこの水平線が前記ローター外周と
交わる点の接線との間の角度が、前記凹部に収容した粉
粒体のほぼ安息角になる位置に設け、前記凹部内面のう
ち回転方向に向かう第1面を、前記凹部の回転方向先行
側端縁を中心とした円弧面に、かつ、回転方向後方に向
かう第2面を、前記ローターの半径と等しい曲率半径の
円弧面に夫々形成し、一つの前記凹部の回転方向先行側
端縁が、前記第1隔壁部における前記ローター回転方向
の下手側端縁と同一レベルにある時に、粉粒体放出終了
直前の別の前記凹部における前記第2面の弦が、水平線
に対して前記凹部に収容した粉粒体のほぼ安息角をなし
て傾斜するように、前記凹部を、前記ローターの周方向
に形成してあることにあり、その作用効果は、次の通り
である。The characteristic configuration of the rotary feeder of the first aspect of the present invention is that the first partition wall portion on the side through which the concave portion containing the powder and granules passes with the rotation of the rotor is formed at a level higher than the rotation axis of the rotor, In a cross-sectional view of the rotor, the lower side edge of the rotor in the rotor partition direction in the first partition wall, the angle between the horizontal line including the edge and the tangent of the point where this horizontal line intersects the rotor outer periphery, The first surface facing the rotation direction of the inner surface of the recess is provided at a position where the powder and granular material contained in the recess has a substantially repose angle, and the first surface facing the rotation direction of the recess is an arc surface. A second surface directed rearward in the rotational direction is formed on an arcuate surface having a radius of curvature equal to the radius of the rotor, and the one edge of the one recess in the rotational direction on the leading side in the rotational direction is the rotor rotational direction in the first partition wall. Same as the lower edge of In the level, the chord of the second surface in the another concave portion immediately before the end of the discharge of the granular material is inclined so as to form an angle of repose of the granular material accommodated in the concave portion with respect to the horizontal line. The concave portion is formed in the circumferential direction of the rotor, and the function and effect thereof are as follows.
つまり、ローターの回転軸芯よりも高いレベルにある第
1隔壁部を、凹部が通過する時、凹部に収容された粉粒
体の自重による押付力は、凹部内面に作用するだけで第
1隔壁部には作用しないために、ローターが回転して
も、第1隔壁は摩耗されにくく、その上、第3図に示す
ように、粉粒体を収容した凹部(3)の回転方向下手側
端縁(D)が、第1隔壁部(4)におけるローター回転
方向の下手側端縁(E)を通過する時点で凹部(3)の
開口の傾きがほぼ安息角(θ)になるために、ローター
(2)の回転に伴って凹部(3)内の粉粒体は、急激に
多量が落下せずに少量づつ徐々に自重放出路(Y)に落
下していく。That is, when the concave portion passes through the first partition wall portion at a level higher than the rotation axis of the rotor, the pressing force due to the weight of the powder or granular material contained in the concave portion acts only on the inner surface of the concave portion, and Since the first partition wall is not easily abraded even when the rotor rotates because it does not act on the portion, the lower end of the concave portion (3) accommodating the granular material in the rotation direction is further suppressed as shown in FIG. Since the edge (D) passes through the lower edge (E) of the first partition wall (4) in the rotor rotation direction, the inclination of the opening of the recess (3) becomes approximately the angle of repose (θ). With the rotation of the rotor (2), the powder and granular material in the concave portion (3) does not suddenly drop in large amounts but gradually falls in small amounts gradually into its own weight discharge path (Y).
しかも、2つの円弧面で内面を形成してある凹部内の粉
粒体は、ローターの回転に伴って、第3図乃至第5図に
示すように、自重放出路(Y)に定量づつ連続的に落下
供給される。Moreover, as shown in FIGS. 3 to 5, the powder particles in the recess, which has the inner surface formed by the two circular arc surfaces, are continuously quantified in the dead weight discharge path (Y) as shown in FIGS. Is supplied as a drop.
即ち、ローター(2)の横断面視において、ローター
(2)の回転に伴って、凹部(3)内の粉粒体は、安息
角(θ)を保ちながら落下していき、凹部(3)におけ
る第2面(9)の弦(16)の傾斜角が、水平線に対して
ほぼ安息角(θ)になると、第2面(9)を形成する円
弧(15)と弦(16)で囲まれた凹曲部(17)に粉粒体が
残る。そこで、前記円弧(15)がローター(2)の半径
(R)と同じ曲率半径に形成してあるために、第3図中
の第1凹部(3A)における回転方向後行側端縁(F)と
先行側端縁(D)を通る弦(18)と円弧(19)によって
囲まれた凸曲部(20)の面積に対し、前記凹曲部(17)
の面積は等しくなると共に、一つの凹部(3)の回転方
向先行側端縁(D)が、第1隔壁部(4)におけるロー
ター(2)回転方向の下手側端縁(E)と同一レベルに
ある時に、粉粒体放出終了直前の別の凹部(3)におけ
る第2面(9)の弦(16)が、水平線に対して凹部
(3)に収容した粉粒体のほぼ安息角(θ)をなして傾
斜するように、凹部(3)を、前記ローター(2)の周
方向に形成してあるために、第3図に示す第1凹部(3
A)の凸曲部(20)を形成する粉粒体と、第3凹部(3
C)の凹曲部(17)内の粉粒体とは、ローター(2)の
回転に伴って同時に落下していき、そのために、第3図
の状態から第4図の状態に、ローター(2)が回転して
いくに伴って、凸曲部(20)を形成する粉粒体がくずれ
落ちる量は、漸次増加するけれども、凹曲部(17)内の
粉粒体は、漸次減少するために、自重放出路(Y)へ第
1凹部(3A)と第3凹部(3C)とから同時に落下供給さ
れる粉粒体量は定量づつになる。That is, in the cross-sectional view of the rotor (2), as the rotor (2) rotates, the granular material inside the recess (3) falls while maintaining the angle of repose (θ), and the recess (3) When the inclination angle of the chord (16) of the second surface (9) at the angle of repose (θ) with respect to the horizontal line is surrounded by the arc (15) and the chord (16) forming the second surface (9). Granules remain in the curved concave part (17). Therefore, since the arc (15) is formed to have the same radius of curvature as the radius (R) of the rotor (2), the trailing edge (F) in the rotational direction of the first recess (3A) in FIG. ) And the area of the convex curved portion (20) surrounded by the chord (18) and the arc (19) passing through the leading edge (D), the concave curved portion (17)
Are equal in area, and the front edge (D) in the rotation direction of one recess (3) is at the same level as the lower edge (E) in the rotation direction of the rotor (2) in the first partition wall (4). , The chord (16) of the second surface (9) in the other recess (3) immediately before the end of the discharge of the powder is approximately the angle of repose of the powder or granules contained in the recess (3) with respect to the horizontal line ( Since the concave portion (3) is formed in the circumferential direction of the rotor (2) so as to be inclined with respect to θ, the first concave portion (3) shown in FIG. 3 is formed.
The granular material forming the convex curved portion (20) of (A) and the third concave portion (3
The powder and granules in the concave curved portion (17) of (C) fall simultaneously with the rotation of the rotor (2). Therefore, from the state of Fig. 3 to the state of Fig. 4, the rotor ( As 2) rotates, the amount of powder or granular material forming the convex curved portion (20) collapses gradually, but the amount of powder or granular material in the concave curved portion (17) gradually decreases. Therefore, the amount of the powdery particles that are simultaneously dropped and supplied from the first recessed portion (3A) and the third recessed portion (3C) to the self-weight discharge path (Y) becomes quantitative.
次に、凸曲部(20)及び凹曲部(17)の粉粒体が落下し
た後は、例えば、ローター(2)がθ1の角度づつ回転
すると(第4図から第5図)、第1凹部(3A)及び第2
凹部(3B)内で、安息角(θ)を保つ粉粒体の表面
(f)が、常に端縁(D)を中心とした半径(r)の円
弧を描きながらθ1づつくずれ落ちる(fからf′)の
で、各凹部(3)からは、常に一定量づつ連続的に自重
放出路(Y)に粉粒体が落下する。Next, after the particles of the convex curved portion (20) and the concave curved portion (17) have fallen, for example, the rotor (2) rotates by an angle of θ 1 (FIGS. 4 to 5), First recess (3A) and second
Inside the recess (3B), the surface (f) of the granular material that keeps the angle of repose (θ) always shifts by θ 1 while drawing an arc of radius (r) centered on the edge (D) (f From f to f '), the granular material always drops continuously from the recesses (3) to the self-weight discharge path (Y) by a constant amount.
従って、摩耗に伴って大きくなった第1隔壁部とロータ
ーとの間の隙間を通って、粉粒体が自重供給路から自重
放出路に排出され、全体の粉粒体放出量が大きく変化し
てしまうという不都合を抑制でき、長期にわたって安定
した量を供給できるようになった。その上、粉粒体は自
重放出路に一度に多量落下することなく、定量づつ連続
的に落下供給することが可能となり、ロータリーフィー
ダーによる粉粒体の供給制御が、より安定的に行いやす
くなった。Therefore, the powder and granules are discharged from the self-weight supply passage to the self-weight discharge passage through the gap between the first partition wall portion and the rotor, which have become large due to the wear, and the total discharge amount of the powder and granules changes significantly. It has become possible to suppress the inconvenience that it will occur and to supply a stable amount over a long period of time. In addition, the powder and granules can be continuously dropped and supplied quantitatively without dropping a large amount into the discharge path of their own weight at once, making it easier and more stable to control the supply of powder and granules by the rotary feeder. It was
更には、凹部内の粉粒体は、少しづつ安息角を保ちなが
ら粉粒体上を滑り落ち、凹部内面との摩擦力が作用しに
くいので、ローター自身の摩耗を抑制でき、結局、ロー
タリーフィーダー全体の耐久性能をより向上させること
ができた。また、第2発明の目的は、第1隔壁部を摩耗
しにくくすると共に、自重放出路に粉粒体をその粒度分
布の大小かかわらず定量づつ連続的に落下放出できるよ
うにする点にある。Furthermore, the powder and granules in the recess gradually slide down on the powder and granule while keeping the angle of repose little, and the frictional force with the inner surface of the recess does not act easily, so it is possible to suppress wear of the rotor itself, and in the end, the rotary feeder. The overall durability performance could be improved. Another object of the second invention is to make the first partition wall less likely to be worn and to allow the powder particles to be continuously dropped and discharged into the self-weight discharge path quantitatively regardless of the size of the particle size distribution.
本第2発明のロータリーフィーダーの特徴構成は、ロー
ターの回転に伴って粉粒体を収容した凹部が通過する側
の第1隔壁部を、前記ローターの回転軸芯よりも高いレ
ベルに形成すると共に、前記ローターの回転に伴って粉
粒体を放出した空の凹部が通過する側の第2隔壁部を、
前記ローターの回転軸芯よりも低いレベルに形成し、前
記ローターの横断面視で、前記第1隔壁部における前記
ローター回転方向の下手側端縁を、前記端縁を含む水平
線とこの水平線が前記ローター外周と交わる点の接線と
の間の角度が、前記凹部に収容した粉粒体のほぼ安息角
になる位置に設けると共に、前記第2隔壁部における前
記ローター回転方向の下手側端縁を、前記端縁を含む水
平線とこの水平線が前記ローター外周と交わる点の接線
との間の角度が、粉粒体のほぼ安息角になる位置に設
け、前記凹部内面のうち回転方向に向かう第1面を、前
記凹部の回転方向先行側端縁を中心とした円弧面に、か
つ、回転方向後方に向かう第2面を、前記ローターの半
径と等しい曲率半径の円弧面に夫々形成し、一つの前記
凹部の回転方向先行側端縁が、前記第1隔壁部における
前記ローター回転方向の下手側端縁と同一レベルにある
時に、粉粒体放出終了直前の別の前記凹部における前記
第2面の弦が、水平線に対して前記凹部に収容した粉粒
体のほぼ安息角をなして傾斜するように、前記凹部を、
前記ローターの周方向に形成してあることにあり、その
作用効果は、次の通りである。The rotary feeder according to the second aspect of the present invention is characterized in that the first partition wall on the side through which the recess containing the powder or granules passes along with the rotation of the rotor is formed at a level higher than the rotation axis of the rotor. , The second partition wall portion on the side through which the empty concave portion that has discharged the powder and granules with the rotation of the rotor passes,
The rotor is formed at a level lower than the axis of rotation of the rotor, and in the cross-sectional view of the rotor, a lower side edge of the first partition wall in the rotor rotation direction is a horizontal line including the edge and the horizontal line is The angle between the tangent line of the point intersecting with the rotor outer periphery is provided at a position that is substantially the angle of repose of the powder or granular material accommodated in the recess, and the lower edge of the rotor in the rotor rotation direction of the second partition wall, The first surface of the inner surface of the recess facing the rotation direction, the angle between the horizontal line including the end edge and the tangent of the point where the horizontal line intersects the outer circumference of the rotor is substantially the angle of repose of the granular material, Is formed on an arcuate surface centered on the leading edge in the rotational direction of the recess and a second surface facing rearward in the rotational direction is formed on an arcuate surface having a radius of curvature equal to the radius of the rotor. Direction of rotation of the recess When the edge is at the same level as the lower edge in the rotor rotation direction of the first partition wall, the chord of the second surface in the other concave portion immediately before the end of the discharge of the granular material is horizontal to the horizontal line. The concave portion is formed so that the powder or granular material housed in the concave portion is inclined so as to form a substantially angle of repose.
It is formed in the circumferential direction of the rotor, and its operation and effect are as follows.
つまり、ローターの回転軸芯よりも高いレベルにある第
1隔壁部を、凹部が通過する時、凹部に収容された粉粒
体の自重による押付力は、凹部内面に作用するだけで第
1隔壁部には作用しないために、ローターが回転して
も、第1隔壁は摩耗されにくく、その上、第3図に示す
ように、粉粒体を収容した凹部(3)の回転方向下手側
端縁(D)が、第1隔壁部(4)におけるローター回転
方向の下手側端縁(E)を通過する時点で、凹部(3)
の開口の傾きがほぼ安息角(θ)になるために、ロータ
ー(2)の回転に伴って凹部(3)内の粉粒体は急激に
多量が落下せずに少量づつ徐々に自重放出路(Y)に落
下していく。That is, when the concave portion passes through the first partition wall portion at a level higher than the rotation axis of the rotor, the pressing force due to the weight of the powder or granular material contained in the concave portion acts only on the inner surface of the concave portion, and Since the first partition wall is not easily abraded even when the rotor rotates because it does not act on the portion, the lower end of the concave portion (3) accommodating the granular material in the rotation direction is further suppressed as shown in FIG. When the edge (D) passes through the lower edge (E) of the first partition wall (4) in the rotor rotation direction, the recess (3) is formed.
Since the inclination of the opening of the rotor becomes almost at the angle of repose (θ), a large amount of the granular material in the concave portion (3) does not suddenly drop with the rotation of the rotor (2) but gradually decreases gradually by its own weight discharge path. It falls to (Y).
しかも、2つの円弧面で内面を形成してある凹部内の粉
粒体は、ローターの回転に伴って、第3図乃至第5図に
示すように、自重放出路(Y)に定量づつ連続的に落下
供給される。Moreover, as shown in FIGS. 3 to 5, the powder particles in the recess, which has the inner surface formed by the two circular arc surfaces, are continuously quantified in the dead weight discharge path (Y) as shown in FIGS. Is supplied as a drop.
即ち、ローター(2)の横断面視において、ローター
(2)の回転に伴って、凹部(3)内の粉粒体は、安息
角(θ)を保ちながら落下していき、凹部(3)におけ
る第2面(9)の弦(16)の傾斜角が水平線に対してほ
ぼ安息角(θ)になると、第2面(9)を形成する。That is, in the cross-sectional view of the rotor (2), as the rotor (2) rotates, the granular material inside the recess (3) falls while maintaining the angle of repose (θ), and the recess (3) The second surface (9) is formed when the inclination angle of the chord (16) of the second surface (9) at the angle of repose (θ) with respect to the horizontal line.
円弧(15)と弦(16)で囲まれた凹曲部(17)に粉粒体
が残る。そこで、前記円弧(15)がローター(2)の半
径(R)と同じ曲率半径に形成してあるために、第3図
中の第1凹部(3A)における回転方向後行側端縁(F)
と先行側端縁(D)を通る弦(18)と円弧(19)によっ
て囲まれた凸曲部(20)の面積に対し、前記凹曲部(1
7)の面積は等しくなるとと共に、一つの凹部(3)の
回転方向先行側端縁(D)が、第1隔壁部(4)におけ
るローター(2)回転方向の下手側端縁(E)と同一レ
ベルにある時に、粉粒体放出終了直前の別の凹部(3)
における第2面(9)の弦(16)が、水平線に対して凹
部(3)に収容した粉粒体のほぼ安息角(θ)をなして
傾斜するように、凹部(3)を、前記ローター(2)の
周方向に形成してあるために、第3図に示す第1凹部
(3A)の凸曲部(20)を形成する粉粒体と、第3凹部
(3C)の凹曲部(17)内の粉粒体とは、ローター(2)
の回転に伴って同時に落下していき、そのために、第3
図の状態から第4図の状態に、ローター(2)が回転し
ていくに伴って、凸曲部(20)を形成する粉粒体がくず
れ落ちる量は、漸次増加するけれども、凹曲部(17)内
の粉粒体は、漸次減少するために、自重放出路(Y)へ
第1凹部(3A)と第3凹部(3C)とから同時に落下供給
される粉粒体量は定量づつになる。The granular material remains in the concave curved part (17) surrounded by the arc (15) and the string (16). Therefore, since the arc (15) is formed to have the same radius of curvature as the radius (R) of the rotor (2), the trailing edge (F) in the rotational direction of the first recess (3A) in FIG. )
With respect to the area of the convex curved portion (20) surrounded by the chord (18) and the circular arc (19) passing through the front side edge (D), the concave curved portion (1
The area of 7) becomes equal, and the edge (D) of the one recessed portion (3) on the leading side in the rotation direction is the same as the edge (E) on the lower side of the rotor (2) in the rotation direction of the first partition wall (4). At the same level, another concave portion (3) immediately before the end of discharge of the granular material.
The concave portion (3) is formed so that the chords (16) of the second surface (9) in the above incline at an angle of repose (θ) of the granular material contained in the concave portion (3) with respect to the horizontal line. Since it is formed in the circumferential direction of the rotor (2), the powder and granular material forming the convex curved portion (20) of the first concave portion (3A) shown in FIG. 3 and the concave curved portion of the third concave portion (3C) are formed. The powder in the part (17) is the rotor (2)
It will fall simultaneously with the rotation of the
As the rotor (2) rotates from the state shown in FIG. 4 to the state shown in FIG. 4, the amount of the powder or granular material forming the convex curved portion (20) is gradually increased, but the concave curved portion is increased. The amount of powder and granules in (17) gradually decreases, so the amount of powder and granules that are simultaneously dropped and supplied from the first recess (3A) and the third recess (3C) to the self-weight discharge path (Y) is quantified. become.
次に、凸曲部(20)及び凹曲部(17)の粉粒体が落下し
た後は、例えば、ローター(2)がθ1の角度づつ回転
すると(第4図から第5図)、第1凹部(3A)及び第2
凹部(3B)内で、安息角(θ)を保つ粉粒体の表面
(f)が、常に端縁(D)を中心とした半径(r)の円
弧を描きながらθ1づつくずれ落ちる(fからf′)の
で、各凹部(3)からは、常に一定量づつ連続的に自重
放出路(Y)に粉粒体が落下する。Next, after the particles of the convex curved portion (20) and the concave curved portion (17) have fallen, for example, the rotor (2) rotates by an angle of θ 1 (FIGS. 4 to 5), First recess (3A) and second
Inside the recess (3B), the surface (f) of the granular material that keeps the angle of repose (θ) always shifts by θ 1 while drawing an arc of radius (r) centered on the edge (D) (f From f to f '), the granular material always drops continuously from the recesses (3) to the self-weight discharge path (Y) by a constant amount.
更に、第2隔壁部におけるローター回転方向の下手側端
縁が、ローターの回転軸芯よりも低いレベルで、且つ、
端縁を含む水平線とこの水平線がローター外周と交わる
点の接線との間の角度が、粉粒体のほぼ安息角になる位
置に設けられているために、粉粒体放出の完了した空の
凹部が、前記端縁を通過するに伴って、第3図に示すよ
うに、自重供給路(X)におけるローターの回転軸芯よ
りも低い部分(H)で粉粒体が、凹部(3)の回転方向
先行側端縁(D)と第1面(8)との間で安息角(θ)
を保ちながら徐々に凹部(3)内に供給され、粉粒体の
粒度分布が大きい場合でも、凹部(3)内に、特定の粒
度範囲の粒子が選択的に充満されることはなく、凹部
(3)ごとに、ほぼ等しい密度及び重量づつ粉粒体が充
満される。Furthermore, the lower edge of the second partition wall in the rotor rotation direction is at a level lower than the rotation axis of the rotor, and
Since the angle between the horizontal line including the edge and the tangent line at the point where this horizontal line intersects the outer circumference of the rotor is provided at a position approximately at the angle of repose of the powder or granules, it is possible to measure As the recess passes through the end edge, as shown in FIG. 3, the granular material becomes recessed (3) at the portion (H) lower than the rotation axis of the rotor in the dead weight supply path (X). Angle of repose (θ) between the leading edge (D) in the direction of rotation and the first surface (8)
Even if the particle size distribution of the granular material is large while the powder is gradually supplied to the concave portion (3) while maintaining the above, the concave portion (3) is not selectively filled with particles in a specific particle size range. In every (3), the granular material is filled with almost equal density and weight.
従って、摩耗に伴って大きくなった第1隔壁部とロータ
ーとの間の隙間を通って、粉粒体が自重供給路から自重
放出路に排出され、全体の粉粒体放出量が大きく変化し
てしまうという不都合を抑制でき、長期にわたって安定
した量を供給できるようになった。その上、粉粒体は自
重放出路に一度に多量落下することなく、粉粒体の粒度
分布の大小にかかわらず、常に定量づつ連続的に落下供
給することが可能となり、ロータリーフィーダーによる
粉粒体の供給制御が、より安定的に行いやすくなった。Therefore, the powder and granules are discharged from the self-weight supply passage to the self-weight discharge passage through the gap between the first partition wall portion and the rotor, which have become large due to the wear, and the total discharge amount of the powder and granules changes significantly. It has become possible to suppress the inconvenience that it will occur and to supply a stable amount over a long period of time. In addition, the powder and granules do not drop into the discharge path of their own weight at a time, and it is possible to continuously drop and feed the powder and granules regardless of the size distribution of the powder and granules. It became easier and more stable to control body supply.
更には、凹部に対して粉粒体は、少しづつ安息角を保っ
て、粉粒体上を滑りながら侵入していくと共に、凹部内
の粉粒体は、少しづつ安息角を保ちながら自重放出路に
粉粒体上を滑り落ちるために、凹部内面との摩擦力が作
用しにくく、ローター自身の摩耗を抑制でき、結局、ロ
ータリーフィーダー全体の耐久性をより向上させること
ができた。Furthermore, the granular material maintains the angle of repose little by little with respect to the concave portion, and enters while sliding on the granular material, and the granular material inside the concave portion gradually releases its own weight while maintaining the angle of repose little by little. Since the powder slides down the road, frictional force with the inner surface of the recess is less likely to act, wear of the rotor itself can be suppressed, and the durability of the entire rotary feeder can be further improved.
次に、本発明の実施例を、図面に基づいて説明する。 Next, an embodiment of the present invention will be described with reference to the drawings.
第1図乃至第5図に示すように、ケーシング(1)内
に、周方向に複数の凹部(3)を設けたローター(2)
を、横軸芯(0)周りで回転自在に設けると共に、ロー
ター(2)への粉粒体の自重供給路(X)と、ローター
(2)からの粉粒体の自重放出路(Y)を形成し、ロー
ター(2)を介して自重供給路(X)と自重放出路
(Y)とを仕切る第1、第2隔壁部(4),(5)を、
ケーシング(1)に設けて、ローター(2)の回転に伴
って、凹部(3)内に自重供給路(X)からの粉粒体を
収容しながら自重放出路(Y)に定量づつ落下放出して
いくロータリーフィーダーを構成してある。As shown in FIGS. 1 to 5, a rotor (2) having a plurality of recesses (3) circumferentially provided in a casing (1).
Is provided so as to be rotatable around the horizontal axis (0), and the weight (G) feed path (X) of the powder to the rotor (2) and the weight release path (Y) of the powder from the rotor (2). And partitioning the self-weight supply path (X) and the self-weight discharge path (Y) via the rotor (2), the first and second partition parts (4), (5),
It is provided in the casing (1), and while the rotor (2) is rotated, the powder particles from the dead weight supply path (X) are accommodated in the recess (3) while being dropped into the dead weight discharge path (Y) in a fixed amount. It is composed of a rotary feeder.
前記ローター(2)の回転に伴って粉粒体を収容した凹
部(3)が通過する側の第1隔壁部(4)をローター
(2)の回転軸芯(0)よりも高いレベルに形成し、ロ
ーター(2)の横断面視で、第1隔壁部(4)における
ローター(2)回転方向の下手側端縁(E)を、端縁
(E)を含む水平線とこの水平線がローター(2)外周
と交わる点の接線との間の角度が、前記凹部(3)に収
容した粉粒体の安息角(θ)又は、ほぼ安息角(θ)に
なる位置に設けると共に、上手側端縁(A)を、軸芯
(0)のほぼ鉛直上方に配置し、この端縁(A)には、
上方に突出する突起(6)を一体連設することによっ
て、突起(6)とケーシング(1)上部とで形成される
溜り部(7)に粉粒体を滞溜させ、自重供給路(X)を
流下する粉粒体がケーシング(1)内を滑らずに、溜り
部(7)の粉粒体上面を常時滑落するようにして、ケー
シング(1)内面の摩耗を少くしてある。With the rotation of the rotor (2), the first partition wall portion (4) on the side where the concave portion (3) accommodating the granular material passes is formed at a level higher than the rotation axis (0) of the rotor (2). Then, in a cross-sectional view of the rotor (2), the lower edge (E) of the first partition wall (4) in the rotation direction of the rotor (2) is a horizontal line including the edge (E) and this horizontal line is a rotor ( 2) The angle between the outer circumference and the tangent to the intersection is the angle of repose (θ) of the powder or granular material contained in the recess (3), or the angle of repose (θ), and the end on the upper hand side. The edge (A) is arranged almost vertically above the axis (0), and the edge (A) is
By integrally arranging the protrusions (6) projecting upward, powder particles are retained in the reservoir (7) formed by the protrusions (6) and the upper part of the casing (1), and the weight feeding path (X ) Does not slip in the casing (1), and the upper surface of the powder in the reservoir (7) always slides down to reduce wear on the inner surface of the casing (1).
前記ローター(2)の回転に伴って粉粒体放出完了した
空の凹部(3)が通過する側の第2隔壁部(5)は、ロ
ーター(2)の回転軸芯(0)より低いレベルに形成し
てあり、第2隔壁部(5)におけるローター(2)回転
方向の下手側端縁(C)を、端縁(C)を含む水平線
と、この水平線がローター(2)外周と交わる点の接線
との間の角度が、前記安息角(θ)又は、ほぼ安息角
(θ)になる位置に設けて、自重供給路(X)からの粉
粒体が、第2隔壁部(5)とローター(2)との隙間に
侵入しにくく、しかも、凹部(3)ごとに収容する粉粒
体の密度を一定になるようにしてある。The second partition wall portion (5) on the side through which the empty concave portion (3), which has completed the discharge of powder and granules as the rotor (2) rotates, has a lower level than the rotation axis (0) of the rotor (2). And the lower edge (C) of the second partition wall (5) in the rotation direction of the rotor (2) intersects with the horizontal line including the edge (C) and the outer periphery of the rotor (2). The angle between the point and the tangent is the angle of repose (θ) or the angle of repose (θ), and the powder and granules from the dead weight supply path (X) are connected to the second partition wall (5). ) And the rotor (2) are less likely to enter, and the density of the powder particles accommodated in each recess (3) is kept constant.
尚、第2隔壁部(5)におけるローター(2)回転方向
の上手側端縁(B)は、軸芯(0)の鉛直下方よりも少
し回転方向上手側に位置させてある。The upper edge (B) of the second partition wall portion (5) in the rotational direction of the rotor (2) is located slightly on the upstream side in the rotational direction of the shaft (0).
また、第1、第2隔壁部(4),(5)は、夫々少くと
も凹部(3)の回転方向における巾以上に、その内面を
形成してある。The inner walls of the first and second partition walls (4) and (5) are formed to be at least wider than the width of the recess (3) in the rotation direction.
前記ローター(2)に対する凹部(3)は、その内面の
うち回転方向に向かう第1面(8)を、凹部(3)の回
転方向先行側端縁(D)を中心とした曲率半径(r)の
円弧面に、かつ、回転方向後方に向かう第2面(9)
を、前記ローター(2)の半径(R)と等しい曲率半径
の円弧面に夫々形成してある。The concave portion (3) with respect to the rotor (2) has a radius of curvature (r) with the first surface (8) of the inner surface facing the rotational direction as the center of the rotational direction leading edge (D) of the concave portion (3). ) The second surface (9) which is an arc surface and is directed rearward in the rotation direction.
Are formed on arcuate surfaces having a radius of curvature equal to the radius (R) of the rotor (2).
ローター(2)の横断面視で前記凹部(3)の先行側端
縁(D)と、第1面(8)と第2面(9)との交点
(G)とを結ぶ第2面(9)の弦(16)の延長線が、ロ
ーター(2)の回転軸芯(0)を通るように形成して、
一つの凹部(3A)の回転方向先行側端縁(D)が、第1
隔壁部(4)におけるローター(2)回転方向の下手側
端縁(E)と同一レベルにある時に、粉粒体放出終了直
前の別の凹部(3C)における第2面(9)の弦(16)
が、水平線に対して凹部(3C)に収容した粉粒体のほぼ
安息角(θ)をなして傾斜するように、各凹部(3)を
形成すると共に、凹部(3A)に対して周方向に90度
(δ)の位置に凹部(3C)を配置し、ローター(2)の
周方向に、8個の凹部(3A)を45度ピッチごとに設けて
ある。In a cross-sectional view of the rotor (2), a second surface (connecting the leading edge (D) of the recess (3) and the intersection (G) of the first surface (8) and the second surface (9) ( Form the extension of the string (16) of 9) so as to pass through the rotation axis (0) of the rotor (2),
The edge (D) on the leading side in the rotation direction of one recess (3A) is the first
When it is at the same level as the lower edge (E) in the direction of rotation of the rotor (2) in the partition wall (4), the chords of the second surface (9) in the other recess (3C) ( 16)
, Each concave portion (3) is formed so that the granular material contained in the concave portion (3C) inclines at an angle of repose (θ) of the granular material, and in the circumferential direction with respect to the concave portion (3A). The recesses (3C) are arranged at 90 ° (δ) positions, and eight recesses (3A) are provided in the circumferential direction of the rotor (2) at every 45 ° pitch.
また、第2図に示すように、ローター(2)の軸芯
(0)に沿った断面では、凹部(3)の軸芯方向両端側
には、夫々側壁部(10)を、ローター(2)に一体連設
してあり、凹部(3)内に収容する粉粒体をローター
(2)の軸受部(11)に流入させないように構成してあ
り、更には、側壁部(10)とケーシング(1)との間を
回転軸(12)回りにシールするメカニカルシール部(1
3)が設けてある。Further, as shown in FIG. 2, in a cross section taken along the axis (0) of the rotor (2), side wall portions (10) are respectively provided at both ends of the recess (3) in the axial direction, and the rotor (2 ) Are integrally connected to each other and are configured so as not to allow the powder or granular material contained in the concave portion (3) to flow into the bearing portion (11) of the rotor (2), and further to the side wall portion (10). Mechanical seal part (1) that seals with the casing (1) around the rotating shaft (12)
3) is provided.
図中(14)は、軸受部(11)におけるグランドパッキン
である。In the figure, (14) is a gland packing in the bearing section (11).
(21)は、ブッシュである。(21) is a bush.
前記凹部(3)は、弦(16)の延長線がローター(2)
の軸芯(0)を通るように形成する場合、粉粒体放出開
始直前の凹部(3A)に対して、粉粒体放出終了直前の凹
部(3C)を回転方向に90度の位置になるように配置すれ
ば良く、例えば第6図に示すように、ローター(2)の
周方向に、4個の凹部(3)を90度ピッチ毎に配置すれ
ば、隣接するものどうしが、凹部(3A)と凹部(3C)の
関係と同様になる。In the recess (3), the extension line of the string (16) is the rotor (2).
When it is formed so as to pass through the shaft core (0), the concave portion (3C) immediately before the end of the discharge of the granular material is at a position of 90 degrees with respect to the concave portion (3A) immediately before the start of the discharge of the granular material. If, for example, as shown in FIG. 6, four recesses (3) are arranged at intervals of 90 degrees in the circumferential direction of the rotor (2), adjacent recesses (3) It becomes the same as the relationship between 3A) and the recess (3C).
また、弦(16)の延長線がローター(2)の軸芯(0)
を通らないように第2面(9)を形成する場合には、ロ
ーター(2)の周方向に等ピッチごとに配置する凹部
(3)の数によって、凹部(3)の形状が異なり、例え
ば、3個の凹部(3)を配設する場合は第7図に示し、
5個の凹部(3)を配置する場合を第8図に示し、6個
の凹部(3)を配置する場合は第9図に示し、7個の凹
部(3)を配置する場合は第10図に示すように、形成す
れば良く、結局、一つの凹部(3)の回転方向先行側端
縁(D)が、第1隔壁部(4)におけるローター(2)
回転方向の下手側端縁(E)と同一レベルにある時に、
粉粒体放出終了直前の別の凹部(3)における第2面
(9)の弦(16)が、水平線に対して、凹部(3)に収
容した粉粒体のほぼ安息角(θ)をなして傾斜するよう
に各凹部(3)を形成してあれば良い。The extension of the string (16) is the axis (0) of the rotor (2).
When the second surface (9) is formed so as not to pass through, the shape of the concave portions (3) differs depending on the number of the concave portions (3) arranged at equal pitches in the circumferential direction of the rotor (2). FIG. 7 shows the case where three recesses (3) are provided,
Fig. 8 shows the case of arranging 5 recesses (3), Fig. 9 shows the case of arranging 6 recesses (3), and Fig. 10 shows the case of arranging 7 recesses (3). As shown in the figure, it may be formed, and in the end, the one edge (D) in the rotational direction of one concave portion (3) is formed on the rotor (2) in the first partition wall portion (4).
When it is at the same level as the lower edge (E) in the direction of rotation,
The chords (16) of the second surface (9) in the other recess (3) immediately before the end of the discharge of the powder and the horizontal line make the angle of repose (θ) of the powder and the particles accommodated in the recess (3) approximately the horizontal line. However, it suffices if each recess (3) is formed so as to be inclined.
尚、特許請求の範囲の項に図面との対照を便利にする為
に符号を記すが、該記入により本発明は添付図面の構造
に限定されるものではない。It should be noted that reference numerals are added to the claims for convenience of comparison with the drawings, but the present invention is not limited to the structures of the accompanying drawings by the entry.
図面は本発明に係るロータリーフィーダーの実施例を示
し、第1図はロータリーフィーダーの軸芯方向から見た
断面図、第2図は、軸芯に沿う要部断面図、第3図、第
4図、第5図は、夫々要部断面の作用説明図、第6図、
第7図、第8図、第9図、第10図は、夫々ローターの別
実施例、第11図は、従来例を示す断面図である。 (1)……ケーシング、(2)……ローター、(3)…
…凹部、(4)……第1隔壁部、(5)……第2隔壁
部、(8)……第1面、(9)……第2面、(D),
(E),(C)……端縁、(0)……軸芯、(θ)……
安息角、(R)……半径、(X)……自重供給路、
(Y)……自重放出路。The drawings show an embodiment of a rotary feeder according to the present invention. FIG. 1 is a sectional view as seen from the axial center direction of the rotary feeder, and FIG. 2 is a sectional view of main parts along the axial center, FIG. 3, FIG. FIG. 5 and FIG. 5 are operation explanatory views of the cross section of the main part, FIG.
FIG. 7, FIG. 8, FIG. 9, and FIG. 10 are cross-sectional views showing another embodiment of the rotor, and FIG. 11 is a conventional example. (1) …… Casing, (2) …… Rotor, (3)…
... Recessed part, (4) ... 1st partition part, (5) ... 2nd partition part, (8) ... 1st surface, (9) ... 2nd surface, (D),
(E), (C) ... Edge, (0) ... Shaft core, (θ) ...
Angle of repose, (R) ... radius, (X) ... deadweight supply path,
(Y) …… The deadweight discharge path.
Claims (2)
部(3)を設けたローター(2)を、横軸芯(0)周り
で回転自在に設けると共に、前記ローター(2)への粉
粒体の自重供給路(X)と、前記ローター(2)からの
粉粒体の自重放出路(Y)を形成し、前記ローター
(2)を介して前記自重供給路(X)と自重放出路
(Y)とを仕切る第1、第2隔壁部(4),(5)を、
前記ケーシング(1)に設けてあるロータリーフィーダ
ーであって、 前記ローター(2)の回転に伴って粉粒体を収容した凹
部(3)が通過する側の第1隔壁部(4)を、前記ロー
ター(2)の回転軸芯(0)よりも高いレベルに形成
し、前記ローター(2)の横断面視で、前記第1隔壁部
(4)における前記ローター(2)回転方向の下手側端
縁(E)を、前記端縁(E)を含む水平線とこの水平線
が前記ローター(2)外周と交わる点の接線との間の角
度が、前記凹部(3)に収容した粉粒体のほぼ安息角
(θ)になる位置に設け、前記凹部(3)内面のうち回
転方向に向かう第1面(8)を、前記凹部(3)の回転
方向先行側端縁(D)を中心とした円弧面に、かつ、回
転方向後方に向かう第2面(9)を、前記ローター
(2)の半径(R)と等しい曲率半径の円弧面に夫々形
成し、一つの前記凹部(3)の回転方向先行側端縁
(D)が、前記第1隔壁部(4)における前記ローター
(2)回転方向の下手側端縁(E)と同一レベルにある
時に、粉粒体放出終了直前の別の前記凹部(3)におけ
る前記第2面(9)の弦(16)が、水平線に対して前記
凹部(3)に収容した粉粒体のほぼ安息角(θ)をなし
て傾斜するように、前記凹部(3)を、前記ローター
(2)の周方向に形成してあるロータリーフィーダー。1. A rotor (2) provided with a plurality of recesses (3) in the circumferential direction in a casing (1) so as to be rotatable around a horizontal axis (0) and to the rotor (2). And a self-weight supply path (X) for forming the self-weight discharge path (Y) of the powder and granules from the rotor (2), and the self-weight supply path (X) via the rotor (2). The first and second partition walls (4) and (5) for partitioning the self-weight discharge path (Y) are
A rotary feeder provided in the casing (1), wherein the first partition wall portion (4) on the side through which the concave portion (3) accommodating the granular material passes with the rotation of the rotor (2), The rotor (2) is formed at a level higher than the rotation axis (0) of the rotor (2), and the lower end of the first partition wall (4) in the rotation direction of the rotor (2) in the cross-sectional view of the rotor (2). The angle between the horizontal line including the edge (E) and the tangent at the point where the horizontal line intersects with the outer circumference of the rotor (2) is substantially equal to that of the powder or granular material accommodated in the recess (3). The first surface (8) of the inner surface of the concave portion (3), which faces the rotational direction, is provided at the position where the angle of repose (θ) is formed, and the rotational direction leading edge (D) of the concave portion (3) is the center. The radius of the rotor (2) is defined by the second surface (9) facing the circular arc surface and rearward in the rotational direction. R), each of which is formed on an arc surface having a radius of curvature equal to that of the first partition wall (4) in the rotational direction of the rotor (2). When it is at the same level as the lower edge (E), the chord (16) of the second surface (9) of the other recess (3) immediately before the end of the discharge of the granular material is the recess (with respect to the horizontal line). A rotary feeder in which the concave portion (3) is formed in the circumferential direction of the rotor (2) so as to incline at an angle of repose (θ) of the granular material contained in 3).
部(3)を設けたローター(2)を、横軸芯(0)周り
で回転自在に設けると共に、前記ローター(2)への粉
粒体の自重供給路(X)と、前記ローター(2)からの
粉粒体の自重放出路(Y)を形成し、前記ローター
(2)を介して前記自重供給路(X)と自重放出路
(Y)とを仕切る第1、第2隔壁部(4),(5)を、
前記ケーシング(1)に設けてあるロータリーフィーダ
ーであって、 前記ローター(2)の回転に伴って粉粒体を収容した凹
部(3)が通過する側の第1隔壁部(4)を前記ロータ
ー(2)の回転軸芯(0)よりも高いレベルに形成する
と共に、前記ローター(2)の回転に伴って粉粒体を放
出した空の凹部(3)が通過する側の第2隔壁部(5)
を、前記ローター(2)の回転軸芯(0)よりも低いレ
ベルに形成し、前記ローター(2)の横断面視で、前記
第1隔壁部(4)における前記ローター(2)回転方向
の下手側端縁(E)を、前記端縁(E)を含む水平線と
この水平線が前記ローター(2)外周と交わる点の接線
との間の角度が、前記凹部(3)に収容した粉粒体のほ
ぼ安息角(θ)になる位置に設けると共に、前記第2隔
壁部(5)における前記ローター(2)回転方向の下手
側端縁(C)を、前記端縁(C)を含む水平線とこの水
平線が前記ローター(2)外周と交わる点の接線との間
の角度が、粉粒体のほぼ安息角(θ)になる位置に設
け、前記凹部(3)内面のうち回転方向に向かう第1面
(8)を、前記凹部(3)の回転方向先行側端縁(D)
を中心とした円弧面に、かつ、回転方向後方に向かう第
2面(9)を、前記ローター(2)の半径(R)と等し
い曲率半径の円弧面に夫々形成し、一つの前記凹部
(3)の回転方向先行側端縁(D)が、前記第1隔壁部
(4)における前記ローター(2)回転方向の下手側端
縁(E)と同一レベルにある時に、粉粒体放出終了直前
の別の前記凹部(3)における前記第2面(9)の弦
(16)が、水平線に対して前記凹部(3)に収容した粉
粒体のほぼ安息角(θ)をなして傾斜するように、前記
凹部(3)を、前記ローター(2)の周方向に形成して
あるロータリーフィーダー。2. A rotor (2) provided with a plurality of recesses (3) in the circumferential direction in a casing (1) so as to be rotatable around a horizontal axis (0) and to the rotor (2). And a self-weight supply path (X) for forming the self-weight discharge path (Y) of the powder and granules from the rotor (2), and the self-weight supply path (X) via the rotor (2). The first and second partition walls (4) and (5) for partitioning the self-weight discharge path (Y) are
A rotary feeder provided in the casing (1), wherein the rotor is provided with a first partition wall portion (4) on a side through which a concave portion (3) accommodating the granular material passes along with the rotation of the rotor (2). The second partition wall portion formed on a level higher than that of the rotating shaft core (0) of (2) and on the side through which the empty recessed portion (3) that has discharged the powder and granules with the rotation of the rotor (2) passes. (5)
Is formed at a level lower than the rotation axis (0) of the rotor (2), and in a cross-sectional view of the rotor (2), the rotor (2) rotation direction in the first partition part (4) is shown. The powdery grain which accommodates the lower edge (E) in the recess (3) at an angle between a horizontal line including the edge (E) and a tangent at a point where the horizontal line intersects with the outer circumference of the rotor (2). It is provided at a position where the angle of repose (θ) of the body is almost the same, and the lower edge (C) of the second partition wall (5) in the rotation direction of the rotor (2) is a horizontal line including the edge (C). The angle between this horizontal line and the tangent of the intersection of the outer circumference of the rotor (2) is substantially the angle of repose (θ) of the granular material, and the inner surface of the recess (3) is oriented in the rotational direction. The first surface (8) is connected to the leading edge (D) in the rotation direction of the recess (3).
And a second surface (9) directed rearward in the rotational direction is formed on an arc surface having a radius of curvature equal to the radius (R) of the rotor (2) to form one recess ( When the leading edge (D) in the rotating direction of 3) is at the same level as the lower edge (E) in the rotating direction of the rotor (2) in the first partition wall portion (4), the end of discharge of the particulate material is completed. The chord (16) of the second surface (9) in the other concave portion (3) immediately before is inclined with respect to the horizontal line at an angle of repose (θ) of the granular material accommodated in the concave portion (3). Thus, the rotary feeder in which the concave portion (3) is formed in the circumferential direction of the rotor (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61277371A JPH07106791B2 (en) | 1986-11-19 | 1986-11-19 | Rotary feeder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61277371A JPH07106791B2 (en) | 1986-11-19 | 1986-11-19 | Rotary feeder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63127922A JPS63127922A (en) | 1988-05-31 |
| JPH07106791B2 true JPH07106791B2 (en) | 1995-11-15 |
Family
ID=17582589
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61277371A Expired - Lifetime JPH07106791B2 (en) | 1986-11-19 | 1986-11-19 | Rotary feeder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07106791B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0586939U (en) * | 1991-08-27 | 1993-11-22 | 株式会社日本アルミ | Rotary valve |
| KR100420271B1 (en) * | 2000-10-26 | 2004-03-02 | 고관영 | Rotary airlock valve for supplying synthetic resin chip |
| JP5118857B2 (en) * | 2007-02-02 | 2013-01-16 | 三井住友建設株式会社 | Powder and particle feeder |
| JP5047657B2 (en) * | 2007-03-19 | 2012-10-10 | 勝三 川西 | Hopper device and combination weigher using the same |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0312747U (en) * | 1989-06-23 | 1991-02-08 |
-
1986
- 1986-11-19 JP JP61277371A patent/JPH07106791B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63127922A (en) | 1988-05-31 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |