JP2009256026A - Powder and grain feeder - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a powder and grain feeder preventing co-rotation of material, and discharging a fixed quantity of the material without segregation of the material. <P>SOLUTION: In the powder and grain feeder, an outer tube is raised on a bottom plate to form a powder and grain feeding case, an inner tube is disposed above the bottom plate and is supported through a powder and grain discharging clearance, a plurality of spokes positioned on the bottom plate are disposed to a rotational shaft of the bottom plate, a tubular outer edge of a rotor is set close to an inner periphery of the outer tube to form an annular passage, a plurality of scrapers for transfer in a direction of the annular passage are disposed to the tubular outer edge, the powder and grain dispersed from the powder and grain discharge clearance to the annular passage are transferred to a powder and grain discharge port by the scrapers. A plurality of projections for preventing rotation along with the steering blade are disposed to an inner surface of the inner tube, and each projection has an approximately triangle pole shape with two face projected in a center direction of the inner tube. An angle made by the two faces of the projection is obtuse, and the maximum length of the projection is 2%-3% of a radius of the inner tube. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

  The present invention relates to a granular material supply machine having a function of preventing the rotation of raw materials.

  Conventionally, a material passage has an inner cylinder and an outer cylinder to which powder particles are supplied, an annular passage of material is provided between the inner cylinder and the outer cylinder, and the material is stirred by a stirring blade that rotates on the bottom surface of the outer cylinder. There is a powder feeder that discharges powder from a discharge port provided above.

  In such a feeder, the granular material spread at a predetermined angle of repose to the material passage outside the inner cylinder is conveyed to the discharge port by the stirring blade rotating on the bottom surface of the outer cylinder, thereby enabling quantitative discharge. (Patent Document 1).

Utility Kaihei 6-35235

  By the way, the above-mentioned conventional granular material supply machine, when the granular material raw material in the hopper (inner cylinder) decreases, depending on the physical properties of the granular material, the wall surface ( The friction resistance with the bottom surface, the inner surface of the inner cylinder, etc.) is smaller than the stirring force by the stirring blade, and a phenomenon in which the entire granular material rotates with the stirring blade in the inner cylinder, so-called rotation may occur.

  When this phenomenon occurs, there is no force to guide the granular material in the inner cylinder to the material passage, and the material cannot be discharged from the discharge port to the outside of the machine.

  As a measure for preventing the rotation of the granular material, conventionally, protrusions (baffle plates) 30 are provided at two positions opposite to the inner surface of the inner cylinder (see FIG. 11). It has been proposed to provide resistance and prevent rotation (see FIG. 11, Patent Document 1, and FIG. 5).

  However, since the baffle plate 30 has a shape in which the left and right plate surfaces of the baffle plate protrude larger inward than the inner cylinder inner surface 2a (see FIG. 11), the effect of preventing the rotation and guiding the granular material to the material passage. However, since the opposing surface 30a intersects with the rotation direction A of the stirring blade with a large inclination angle, a large pressure is applied to the granular material by the colliding granular material colliding with the opposing surface 30a. In some cases, the powder particles in the vicinity of the baffle plate 30 become dense and dense. And since this occurs only at two opposing locations in the inner cylinder 2, if the powder material is a mixed material having different physical properties, segregation (the uneven distribution of components due to the difference in physical properties of the material) may occur. There is.

  The present invention has been made in view of the above-described conventional problems, and provides a powder and particle feeder that can prevent the material from circulating in the hopper and can quantitatively discharge the material without causing segregation of the material. For the purpose.

In order to achieve the above object, the present invention
First, an outer cylinder is erected on the bottom plate to form a powder supply case, and 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 rotating body is formed by providing a plurality of spokes located on the bottom plate on the rotating shaft, and an annular passage between the inner and outer cylinders is formed by bringing the cylindrical outer edge of the rotating body close to the inner periphery of the outer cylinder. The cylindrical outer edge is provided with a plurality of scrapers for material transfer in the annular passage direction, and the granular material diffused into the annular passage at a predetermined angle of repose from the granular material discharge gap is discharged into the granular material by the scraper. In the granular material feeder for transferring to the inner surface of the inner cylinder, a plurality of rotation preventions having a substantially triangular prism shape in the vertical direction having two surfaces protruding in the center direction of the inner cylinder at equal intervals along the inner circumference of the inner cylinder Protrusions are provided, and the angle formed by the two surfaces of the anti-rotation protrusions is an obtuse angle, and Maximum height around prevention protrusion, is formed using the granular material feeder, which is a 2% to 3% with respect to the radius of the inner cylinder.

  The two surfaces of the anti-rotation projection can be constituted by, for example, projecting surfaces (10a, 10b) of the anti-rotation projection (10). The longitudinal direction means a direction orthogonal to the rotation direction of the stirring blade. If comprised in this way, the inclination of two surfaces of a rotation prevention protrusion will become a gentle inclined surface which cross | intersects at a small angle with respect to the rotation direction of a stirring blade, and since the maximum height is also low, one rotation prevention protrusion is The pressure applied to the powder can be reduced, and as a result, the pressure applied to the powder can be evenly distributed along the inner circumference of the inner cylinder, preventing the powder from being rotated. And segregation of the material can be prevented.

  Second, an outer cylinder is erected on the bottom plate to form a powder supply case, and 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 rotating body is formed by providing a plurality of spokes located on the bottom plate on the rotating shaft, and an annular passage between the inner and outer cylinders is formed by bringing the cylindrical outer edge of the rotating body close to the inner periphery of the outer cylinder. The cylindrical outer edge is provided with a plurality of scrapers for material transfer in the annular passage direction, and the granular material diffused into the annular passage at a predetermined angle of repose from the granular material discharge gap is discharged into the granular material by the scraper. A plurality of vertical columnar anti-rotation protrusions having an arc surface protruding in the center direction of the inner cylinder on the inner surface of the inner cylinder at equal intervals along the inner circumference thereof. And the maximum height of the anti-rotation protrusion is 2% to 3% with respect to the radius of the inner cylinder. It constituted by granular material feeder according to claim.

  If comprised in this way, since the circular arc surface of a rotation prevention protrusion will become a gentle inclined surface (curved surface) which cross | intersects at a small angle with respect to the rotation direction of a stirring blade, and the maximum height is also low, one rotation prevention protrusion Can reduce the pressure applied to the granular material, and as a result, the pressure applied to the granular material can be evenly distributed along the inner periphery of the inner cylinder, thereby preventing the granular material from rotating. And segregation of the material can be prevented. Moreover, since it is a circular arc surface, the rapid disturbance of a granular material can be suppressed and segregation of a material can be suppressed effectively.

  Thirdly, instead of the circular arc surface of the anti-rotation protrusion, a curved body projecting toward the center of the inner cylinder is used.

  The curved surface is a concept in which a cylindrical surface is a longitudinal curved surface other than a circular arc surface and includes a curved surface.

  4thly, each said rotation prevention protrusion is provided in the predetermined range of the inner cylinder upper end direction from the lower end of the said inner cylinder, The powder in any one of said 1st-3rd characterized by the above-mentioned. Consists of a granule feeder.

  If comprised in this way, a pressure can be effectively made to act on the said granular material at the time of the reduction | decrease of the granular material which a rotation tends to produce.

  Fifthly, six or eight of the rotation prevention protrusions are provided at equal intervals along the inner periphery of the inner cylinder. Consists of a powder feeder.

  If comprised in this way, the pressure given to a granular material for rotation prevention can be disperse | distributed equally along the inner periphery of an inner cylinder, and rotation can be prevented effectively and segregation can also be prevented. obtain.

  Since the present invention is configured as described above, the resistance for preventing the granular material from being rotated by the anti-rotation protrusion is distributed substantially uniformly throughout the inner periphery of the inner cylinder. In addition to being able to effectively prevent the material from being disturbed, segregation of the material can also be prevented, and stable quantitative discharge of the material is enabled.

  DESCRIPTION OF EMBODIMENTS Hereinafter, embodiments of a powder and particle feeder according to the present invention will be described in detail with reference to the accompanying drawings.

  First, the basic configuration of the powder and particle feeder according to the present invention will be described with reference to FIGS. 1 and 2. As shown in FIGS. 1 and 2, a concentric inner cylinder 2 is arranged inside an outer cylinder 1 (bottomed outer cylinder) having a bottom plate 1 ′, and between the lower end 2 ′ of the inner cylinder 2 and the bottom plate 1 ′. The annular upper end opening 1 ″ of the outer cylinder 1 is closed by supporting the annular lid 3 provided on the outer periphery of the inner cylinder 2 with the discharge gap t of the granular material interposed therebetween at the upper end of the outer cylinder 1, Further, the gap t is maintained, an annular passage 4 of discharged powder particles is formed between the inner and outer cylinders 1 and 2, and a discharge port 5 is formed in the passage 4.

  And the base part 7b of the rotary blade (stirring blade) 7 arrange | positioned along the bottom-plate upper surface 1a is fixed to the upper end part of the upright rotating shaft 6 protrudingly provided in the center of the said baseplate 1 ', and the granular material feeder F is formed. The bottomed outer cylinder 1 is used as a granular material supply case.

  As shown in FIG. 1, the rotary blade 7 is composed of four spokes 7a every 90 degrees from the base portion 7b toward the inner periphery of the outer tube 1, and at the tip thereof, the inner portion of the outer tube 1 is formed. A rotating ring (cylindrical outer edge) 8 is provided along the circumference. The rotating ring 8 is provided with 12 material transfer scrapers (inward rotating blades) 9 in the direction of the inner cylinder 2 at the same height as the spokes 7a.

  The granular material P is accommodated in the inner cylinder 2 and spreads toward the annular passage 4 from the interval t toward the annular passage 4 with a predetermined angle of repose q. In this state, the upright rotating shaft 6 is driven in the direction of arrow A, the spokes 7a and the scraper 9 are rotated in the direction of arrow A in the granular material P, whereby the granular material P in the inner cylinder 2 is moved to the annular passage 4 side. The scraped powder particles are moved in the direction of the arrow A by the scraper 9 and discharged from the discharge port 5 to the outside by a fixed amount.

  The spokes 7a of the rotary blade 7 perform the action of forcibly sending the powder particles to the outer peripheral portion (annular passage 4) side by the rotation. Reference numeral 7a ′ denotes an edge (edge) on the rotation direction A side (traveling direction side) of each spoke 7a, and its thickness is reduced in the direction of the edge 7a ′ along the rotation direction (traveling direction) A. A tapered surface is formed.

  Reference numeral 10 denotes a rotation prevention protrusion provided on the inner surface of the inner cylinder 2, and these rotation prevention protrusions 10 are arranged at equal intervals along the inner circumference (60 in FIG. 1) on the inner surface 2 a of the inner cylinder 2. Are provided at six locations (see FIG. 7).

Since these rotation prevention protrusions 10 have the same shape, focusing on one of them, as shown in FIG. 4, the rotation prevention protrusions 10 are arranged on a virtual line R on the inner cylinder radius on the inner surface 2 a of the inner cylinder 2. In the direction of the perpendicular vertical center line S, there are two projecting surfaces 10a and 10b that rise from the left and right directions at the same gentle inclination angle. Both the upper surface 10c and the bottom surface 10c ′ of the rotation preventing projection 10 are closed, and as a whole, the vertical direction (the vertical direction perpendicular to the rotational direction A of the rotary blade 7) with the center line S directed toward the center of the inner cylinder 2 is used. Direction). The projecting surfaces 10a and 10b have a length from the upper end 2 ″ to the lower end 2 ′ of the inner cylinder, and the cross-sectional shape thereof is such that the angle θ ₁ formed by the apex is about 140 degrees (obtuse angle). It has a substantially isosceles triangle shape (see FIG. 9A).

That is, on the inner periphery of the inner cylinder 2, there are provided a plurality of rotation prevention projections 10 having a substantially triangular prism shape in the vertical direction and having vertical projecting surfaces (two surfaces) 10a and 10b projecting in the center direction of the inner cylinder. is and, the protruding surface 10a, the angle theta ₁ of 10b of the respective co-rotation preventing projection 10 is configured to be obtuse.

Further, as shown in FIG. 9A, the projecting surfaces 10a and 10b of the anti-rotation projection 10 have a small angle (A direction, tangent line m in the rotational direction) with respect to the rotation direction of the rotary blade 7 (in the drawing). (θ ₂ = about 20 degrees), and so as to have a gentle slope intersecting with each other, whereby the pressure per protrusion 10 exerted on the granular material P is configured to be smaller than that of the conventional protrusion. Yes.

  The inner cylinder 2 can be further extended above the upper end portion 2 ″ shown in FIG. 2 to increase the capacity of the inner cylinder 2. Even in this case, the amount of the granular material P is small. Each of the anti-rotation projections 10 is formed in a predetermined range from the lower end 2 ′ of the inner cylinder 2 to the upper end of the inner cylinder (range from the lower end 2 ′ to the upper end 2 ″ in FIG. 2). It is preferable to provide it.

  And the maximum height T from the inner surface 2a of the inner cylinder 2 of the anti-rotation projection 10, that is, the height from the inner surface 2 of the inner cylinder 2 to the center line S (vertex of the isosceles triangle in the cross section). The length T is configured to be 2 to 3% (= T / r (%)) with respect to the radius r of the inner cylinder 2 (see FIG. 7).

  In this way, the anti-rotation projection 10 is formed to have a lower height than the conventional anti-rotation projection 10 and is formed on the inner surface of the inner cylinder 2 at six locations every 60 degrees, thereby preventing one rotation prevention. Although the pressure exerted by the protrusion 10 on the granular material to be reduced is reduced, by providing the anti-rotation protrusion at six locations, the protrusion 10 is evenly dispersed in the granular material at six locations on the inner periphery of the inner cylinder 2. The said pressure can be exerted and the surroundings of a granular material can be prevented like the past.

  In addition, by providing the anti-rotation projections 10 at six locations at equal intervals over the entire circumference of the inner surface 2a of the inner cylinder 2, the pressure applied to the granular material P per one projection 10 is small. Since the pressure is evenly distributed over the entire inner surface of the inner cylinder 2, the disturbance K (the dense portion of the granular material) of the granular material P in the vicinity of the anti-rotation projection 10 can be reduced (FIG. 3). FIG. 7). That is, since the disturbance K of the granular material P is small and the disturbance K is dispersed at equal intervals on the inner peripheral surface of the inner cylinder 2, segregation can be prevented even in the case of a mixed material. .

  Note that the inclined surface 10a of the anti-rotation projection 10 is a gentle inclined surface in the longitudinal direction whose longitudinal direction is perpendicular to the virtual line R (or the longitudinal direction is perpendicular to the rotational direction A of the stirring blade 7). The cross-sectional shape of the protrusion 10 is not limited to the isosceles triangle shape, and may be another cross-sectional triangle shape. As described above, the inclined surface of the protrusion 10 forms a surface having no inclination in the direction (vertical direction) orthogonal to the virtual line R, and the inclined surface (10a, 10b) in the direction orthogonal to the vertical direction (horizontal direction). ) Is preferably formed (see FIG. 9A).

  The rotation prevention protrusion 11 shown in FIG. 6 is another embodiment of the present invention, and is formed so that the cross-sectional shape is an arc. The rotation prevention protrusion 11 is a column in the vertical direction (vertical direction perpendicular to the rotation direction A of the rotary blade 7) on the inner surface 2a of the inner cylinder 2 by an arc surface 11a having a length extending from the upper end to the lower end of the inner surface 2a. It is provided in the shape. That is, on the inner surface 2a of the inner cylinder 2, a plurality of vertical columnar rotation prevention projections having arcuate surfaces 11a protruding in the inner circumferential direction are provided at equal intervals along the inner circumference. Further, the upper surface 11c and the bottom surface 11c 'of the projection 11 are closed, and as a whole, has a circular arc column shape in the vertical direction. As shown in FIG. 8, the rotation prevention protrusions 11 are also formed at six locations every 60 degrees along the inner periphery of the inner surface 2 a of the inner cylinder 2, as with the protrusions 10.

  The circular arc on the circular arc surface 11a of the anti-rotation projection 11 is formed by an arc centered at one point on the extension line of the virtual line R on the radius r of the inner cylinder 2, and its maximum height T, that is, The distance T from the inner surface 2a to the maximum height of the circular arc is configured to be 2 to 3% (T / r (%)) of the radius of the inner cylinder 2 in the same manner as the rotation preventing projection 10 ( (See FIG. 8).

As shown in FIG. 9B, the circular arc surface 11a of the anti-rotation projection 11 has a tangent n on the circular arc surface with respect to the rotation direction of the rotary blade 7 (arrow A direction, tangent m in the rotation direction). It is configured to have a gentle slope (curved surface) that intersects at a small angle (θ ₃ = about 20 degrees in FIG. 9B), whereby the pressure per protrusion 11 exerted on the granular material is It is comprised so that it may become smaller than the conventional protrusion. Moreover, since it is a circular arc surface, it has the effect | action which can suppress the rapid disorder K of the granular material P and can suppress the segregation of material more effectively.

  In addition, the inner cylinder 2 can be further extended above the upper end portion 2 ″ shown in FIG. 2 to increase the capacity of the inner cylinder 2. In this case as well, as in the above embodiment, The rotation preventing protrusion 11 is preferably provided in a predetermined range from the lower end 2 ′ of the inner cylinder 2 to the upper end direction of the inner cylinder (a range from the lower end 2 ′ to the upper end 2 ″ in FIG. 2).

  In this way, the height of the anti-rotation projection 11 is made lower than that of the conventional anti-rotation projection, and at the same time as the above-described protrusion 10 by forming it on the inner surface of the inner cylinder 2 at six locations every 60 degrees. In addition, although the pressure exerted on the granular material P to be rotated by one rotation prevention protrusion 11 is reduced, by providing the rotation prevention protrusions 11 at 6 positions, 6 positions on the inner circumference 2a of the inner cylinder 2 are provided. By applying the above pressure evenly to the granular material, the surrounding of the granular material can be prevented as in the conventional case.

  In addition, by providing the anti-rotation projections 11 at six locations at equal intervals over the entire circumference of the inner surface 2a of the inner cylinder 2, the pressure applied to the granular material per projection 11 is small, and the pressure Is distributed evenly over the entire circumference of the inner cylinder, so that the turbulence K of the granular material in the vicinity of the anti-rotation projection 11 (the dense portion of the granular material) can be reduced (see FIG. 5). That is, since the disturbance K of the granular material P is small and the disturbance K is distributed at equal intervals on the inner peripheral surface of the inner cylinder 2, segregation can be prevented even in the case of a mixed material.

  The arc surface 11a may be a vertical curved surface in which the arc surface is a curved surface other than an arc. That is, a gentle arc surface or curved surface in the longitudinal direction in the direction in which the longitudinal direction of the projecting surface of the anti-rotation projection 11 is orthogonal to the virtual line R (or the longitudinal direction is orthogonal to the rotational direction A of the stirring blade 7). The arc surface or curved surface may be a surface including an arc or a curve that is orthogonal to the longitudinal direction of the protrusion 11. Thus, the arc surface or curved surface of the projection 11 is linear in the direction (vertical direction) orthogonal to the virtual line R, and has a certain curvature in the direction orthogonal to the vertical direction (horizontal direction). It is preferable to form a curved surface.

  In each of the above-described embodiments, an example in which six rotation prevention protrusions 10 and 11 are provided every 60 degrees has been shown. However, as shown in FIG. 10, eight protrusions 10 and 11 may be provided every 45 degrees. good.

  In FIG. 2, 12 is a speed reducer, 13 is an electric motor for driving a stirring blade, and 14 is a flow rate adjusting ring for powder particles.

  Since the powder feeder of the present invention is configured as described above, its operation will be described next.

  The granular material P accommodated in the inner cylinder 2 is diffused from the discharge gap t into the material passage 4 with an angle of repose q. When the electric motor 13 is rotated in this state, the spoke 7a rotates in the direction of arrow A, and at the same time, the material transfer scraper 9 rotates.

  Then, with the rotation of the spoke 7a, the granular material in the inner cylinder 2 moves to the material passage 4, and at the same time, the granular material in the material passage 4 is conveyed in the direction of arrow A by the rotation of the scraper 9. Then, it is carried to the discharge port 5 and discharged from the discharge port 5 by a certain amount.

  At this time, the frictional resistance between the granular material P and the bottom plate 1 'or the frictional resistance between the granular material and the inner cylinder 2 inner surface 2a is relatively small because the material in the inner cylinder 2 is reduced. However, the granular material P receives resistance (pressure) equally from the six projecting surfaces 10a and 10b of the rotation preventing projections 10 provided at six locations at equal intervals on the inner periphery of the inner surface 2a of the inner cylinder 2. Therefore, the frictional resistance between the granular material P and the protrusions 10 (six locations) is increased at six equal locations on the inner circumference of the inner cylinder 2, and the frictional resistance is smaller than the stirring force of the spokes 7a. There is nothing, and as a result, the rotation of the powder P can be prevented.

  Therefore, the six anti-rotation protrusions 10 that are evenly arranged on the inner cylinder 2 can uniformly distribute the resistance to the granular material, thereby effectively preventing the supply of the material. Can do.

  Further, the maximum height T of the rotation preventing projection 10 is very low, 2 to 3% of the radius r of the inner cylinder 2, and the protruding surface 10 a of the rotation preventing projection 10 is in the rotation direction of the stirring blade 7. Since it is gently inclined (see FIG. 9A), the pressure applied to the powder body P in the vicinity of one rotation prevention protrusion 10 is small, and the disturbance K of the powder body P in the vicinity of the protrusion 10 is Since there are very few, the segregation of the granular material P can also be prevented.

  That is, the disturbance K of the granular material P in the vicinity of one rotation prevention protrusion 10 is reduced, and the rotation prevention protrusions 10 are provided on the inner peripheral surface of the inner cylinder 2 in a distributed manner at six intervals. Thus, segregation of the granular material P as a whole can be prevented by reducing the disturbance K of the granular material P while dispersing the resistance applied to the granular material P.

  The same applies to the case where the rotation preventing projection 11 is used, and the frictional resistance between the granular material P and the bottom plate 1 'or the frictional resistance between the granular material and the inner cylinder 2 inner surface 2a becomes relatively small. Even so, the granular material P receives resistance (pressure) evenly from the six arcuate surfaces 11a in the anti-rotation projections 11 provided at six locations on the inner periphery of the inner surface 2a of the inner cylinder 2 at equal intervals. In addition, the frictional resistance between the granular material P and the protrusions 10 (six locations) is increased, and the frictional resistance is not smaller than the stirring force of the spokes 7a, and the circulation of the granular material P can be prevented. it can.

  That is, the six anti-rotation projections 11 that are evenly arranged on the inner cylinder 2 can uniformly distribute and provide resistance to the granular material, thereby effectively preventing the supply of the material. Can do. Further, the height T of the rotation preventing projection 11 is very low, 2 to 3% of the radius r of the inner cylinder 2, and the circular arc surface 11a (the surface facing the rotation direction) of the rotation preventing projection 11 is the stirring blade 7. (See FIG. 9B), the pressure applied to the granular material P in the vicinity of one rotation prevention projection 11 is small, and the granular material in the vicinity of the projection 11 Since the disturbance K of the body is very small, segregation of the granular material P can also be prevented.

  That is, the disturbance K of the granular material P in the vicinity of one rotation prevention protrusion 11 is reduced, and the rotation prevention protrusions 11 are distributed on the inner peripheral surface of the inner cylinder 2 at six equal intervals. Thus, segregation of the granular material P as a whole can be prevented by reducing the disturbance K of the granular material P while dispersing the resistance applied to the granular material P.

  As described above, according to the present invention, since the resistance for preventing the rotation of the powder body P by the rotation prevention protrusions 10 and 11 is distributed substantially uniformly over the entire inner periphery 2a of the inner cylinder 2, Since it is possible to effectively prevent the circulation of the body P and less disturb the powder material, even when using a mixed material in which a plurality of materials having different physical properties are mixed, Segregation of the material can be effectively prevented, and stable quantitative discharge of the material is enabled.

  Since the present invention can effectively prevent the rotation and segregation of the powder material, it can be used in various fields as a powder supply machine for quantitatively supplying the powder material of various physical properties. Can be used.

It is a partially notched top view of the granular material supply machine which concerns on this invention. It is the XX sectional view taken on the line of FIG. It is sectional drawing of the rotation prevention protrusion vicinity of an apparatus same as the above. It is a perspective view of the surrounding prevention protrusion vicinity of an apparatus same as the above. It is sectional drawing of the rotation prevention protrusion of an apparatus same as the above. It is a perspective view of the rotation prevention protrusion of an apparatus same as the above. It is a schematic plan view of the inner cylinder which has the rotation prevention protrusion of an apparatus same as the above. It is a schematic plan view of the inner cylinder which has the rotation prevention protrusion of an apparatus same as the above. (A), (b) is explanatory drawing which shows the relationship between the rotation prevention protrusion of the same apparatus as above, and the rotation direction of a stirring blade. It is a schematic plan view of other embodiment of the inner cylinder which has a rotation prevention protrusion of an apparatus same as the above. It is sectional drawing of the rotation prevention protrusion vicinity of the conventional granular material supply machine.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Outer cylinder 1 'Bottom plate 2 Inner cylinder 2a Inner surface 4 Annular passage 5 Outlet 6 Upright rotating shaft 7 Stirring blade (rotary body)
7a Spoke 8 Rotating ring (cylindrical outer edge)
9 Scraper 10 for material transfer Rotation prevention projection 10a Projection surface 10b Projection surface 11 Rotation prevention projection 11a Arc surface P Granule T Maximum height r Radius t Granule discharge interval q Repose angle

Claims (5)

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,
The inner surface of the inner cylinder is provided with a plurality of rotation prevention protrusions having a substantially triangular prism shape in the longitudinal direction having two surfaces protruding in the center direction of the inner cylinder at equal intervals along the inner periphery thereof.
The angle formed by the two surfaces of each of the anti-rotation projections is an obtuse angle,
And the maximum height of the said rotation prevention protrusion is 2%-3% with respect to the radius of an inner cylinder, The granular material supply machine characterized by the above-mentioned. 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,
On the inner surface of the inner cylinder, a plurality of vertical columnar anti-rotation protrusions having an arc surface protruding in the inner cylinder center direction are provided at equal intervals along the inner circumference,
And the maximum height of the said rotation prevention protrusion is 2%-3% with respect to the radius of an inner cylinder, The granular material supply machine characterized by the above-mentioned.   3. The powder and granular material supply machine according to claim 2, wherein instead of the circular arc surface of the rotation preventing projection, the powder body is a curved surface projecting toward the center of the inner cylinder.   The powder supply unit according to any one of claims 1 to 3, wherein each of the rotation prevention protrusions is provided in a predetermined range from a lower end of the inner cylinder to an upper end direction of the inner cylinder. .   The granular material supply according to any one of claims 1 to 4, wherein six or eight of the rotation prevention protrusions are provided at equal intervals along the inner periphery of the inner cylinder. Machine.

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