WO2003031294A1 - Powder particle distribution device and shifter - Google Patents

Powder particle distribution device and shifter Download PDF

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Publication number
WO2003031294A1
WO2003031294A1 PCT/JP2002/010339 JP0210339W WO03031294A1 WO 2003031294 A1 WO2003031294 A1 WO 2003031294A1 JP 0210339 W JP0210339 W JP 0210339W WO 03031294 A1 WO03031294 A1 WO 03031294A1
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WO
WIPO (PCT)
Prior art keywords
distribution
granular material
powder
cylinder
distribution device
Prior art date
Application number
PCT/JP2002/010339
Other languages
French (fr)
Japanese (ja)
Inventor
Akihiro Tanaka
Shin Doi
Original Assignee
Nisshin Flour Milling Inc.
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nisshin Flour Milling Inc. filed Critical Nisshin Flour Milling Inc.
Priority to JP2003534287A priority Critical patent/JP4219272B2/en
Publication of WO2003031294A1 publication Critical patent/WO2003031294A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/60Mixing solids with solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/80Falling particle mixers, e.g. with repeated agitation along a vertical axis
    • B01F25/82Falling particle mixers, e.g. with repeated agitation along a vertical axis uniting flows of material taken from different parts of a receptacle or from a set of different receptacles

Definitions

  • the present invention relates to a powder / particle distributing apparatus for evenly distributing powder, such as flour, into a plurality of groups, and a shifter using the same.
  • the conventional powder and particle distribution apparatus proposed for such a purpose examples include, for example, a powder and particle distribution apparatus disclosed in Japanese Patent Publication No. 3-6092 of the present applicant, Japanese Patent Application Publication No. 2008-856 discloses a powder and particle distributor.
  • the apparatus for distributing powder and the like disclosed in Japanese Patent Publication No. Hei 3-69092 has a powder and particle central accumulation chamber having a powder supply port above and a horizontal bottom, and a central accumulation chamber. At least four chutes each extending from the central area to each chute and extending in the outer circumferential direction to supply the granules to the next processing step, each having a granule discharge port.
  • Positions corresponding to each of the chutes in the transfer area are approximately equal to the apexes or the center of the regular polygon centered on the central accumulation chamber, and at least two symmetry axes passing through the center.
  • a gate that can be adjusted in the horizontal direction to divide and distribute an equal amount of powder and granules in the horizontal direction from the central stacking chamber to each shout.
  • a motion imparting means for imparting a swinging or vibrating motion to the central stacking chamber one-piece assembly, wherein the granular material supplied into the central accumulating chamber from the granular material supply port is provided with the motion imparting means.
  • each gate is divided and distributed equally in the horizontal direction from each gate adjusted to a constant level and adjusted to a predetermined equal aperture.
  • the flow rate ratio of the powders and granules is determined by the gate. Therefore, when the total mass velocity of the powders and granules changes, the distribution ratio fluctuates. There was a problem.
  • the powder and particle dispenser disclosed in Japanese Patent Application Laid-Open No. H11-208856 is a distributing table having a conical upper surface surrounded by an annular outer peripheral wall, and applying vibration to the distributing table.
  • a plurality of discharge ports are provided on the outer peripheral wall at equal intervals in the circumferential direction, and a plurality of annular dams having different diameters around the top are provided between the top of the distribution table and the outer peripheral wall.
  • the height of each dam is gradually reduced from the first storage tank, including the top of the distribution table, by erecting the plates and making the height of each dam gradually lower toward the outer peripheral wall.
  • An annular storage tank is formed, and the same number of partitions as the number of outlets are provided at equal intervals in the circumferential direction between the outermost weir and the outer peripheral wall.
  • the granules supplied in a continuous manner are overflowed into the outer storage tank while being equalized by vibration. It is obtained so as to evenly distribute.
  • the powder and particle distributor disclosed in the publication requires a plurality of annular dams, and there is a problem in that the configuration of the distribution table becomes complicated and the cost increases.
  • the powder and particle distributor disclosed in the same gazette since there is a space between the input port for the powder and the innermost crevice plate, the powder supplied from the input port is in the first stage. In some cases, the powder was not stored in the first storage tank, but was directly supplied to the second and subsequent storage tanks, and the distribution ratio of the powder particles was large. Disclosure of the invention
  • An object of the present invention is to solve the above-mentioned problems based on the prior art, and to achieve a simpler structure, especially when the mass velocity of the granular material supplied at a large mass velocity fluctuates greatly.
  • An object of the present invention is to provide a powder and particle distributing apparatus and a shifter which can distribute particles equally with high precision.
  • the present invention provides a disk-shaped or conical distribution table, and a distribution cylinder which is coaxially disposed on an upper part of the distribution table and forms a storage chamber for powder and granules together with the distribution table.
  • the outer diameter is set smaller than the inner diameter of the distribution cylinder, and the lower end portion is disposed coaxially with the distribution cylinder so that the lower end is located in the distribution cylinder.
  • a supply tube to be introduced, and a plurality of discharge ports for individually discharging the particles passing through the distribution tube from the storage chamber to the outside from the distribution table are formed, and cover an outer periphery of the distribution table and the distribution tube.
  • the present invention provides a powdery and granular material distribution device comprising: an outer peripheral wall;
  • a plurality of notches are formed in a circumferential direction at an upper end portion of the distribution cylinder, and each of the plurality of notches is formed so as to become wider as going upward.
  • each of the plurality of notches is formed so as to become wider as going upward.
  • the lower end of the supply tube is disposed at a position between the upper end of the distribution tube and the lower end of the plurality of cutouts.
  • each of the powder and particle distribution devices further includes a disc-shaped ceiling provided at an upper end portion of the outer peripheral wall and having a circular opening at the center.
  • the well is attached so as to pass through the circular opening.
  • each of the powder and particle distribution apparatuses further includes height adjusting means for positioning a lower end of the supply cylinder in the distribution cylinder and adjusting a height of the lower end of the supply cylinder. . .
  • each of the powder and particle distribution apparatuses further includes an impact buffering member having a plurality of through holes attached to a lower end of the supply cylinder.
  • the shock absorbing member is attached so as to cover a lower end portion of the supply cylinder.
  • the shock absorbing member includes a shock absorbing net formed in a mesh shape.
  • the shock absorbing member preferably includes, as the plurality of through holes, an impact buffer plate having a central opening, a plurality of circular through holes, and a plurality of oblique through-holes inclined radially from the center thereof. preferable.
  • the shock-absorbing member includes a mesh-shaped shock-absorbing net, a plurality of through-holes, a central opening, a plurality of circular through-holes, and a plurality of inclined through-holes that are inclined radially from the center thereof.
  • the shock absorbing plate is positioned between an upper end portion of the distribution tube and a lower end portion of the plurality of notches. It is preferred that they are arranged in
  • each of the powder and particle distributing apparatuses further includes a slit provided between the lower end of the distribution tube and the distributing table over the entire periphery of the lower end of the distribution tube.
  • the dimensions of the slit between the lower end of the distribution cylinder and the distribution table are as follows:
  • It is preferably between 4 and 3 O mm.
  • each of the above-mentioned granular material distribution devices further includes a vibration generating unit that vibrates the granular material distribution device.
  • the present invention also provides a shifter body for simultaneously sieving the powders and granules distributed to a plurality of groups, vibration generating means for vibrating the shift body, and a shifter installed on an upper surface of the shift body.
  • the present invention also provides a shifter characterized by comprising the above-described powder and particle distribution apparatus.
  • vibration includes not only vertical (vertical) and horizontal vibrations, but also rotational movements in a substantially circular shape.
  • FIG. 1 is a side sectional view of an embodiment of the present invention.
  • FIG. 2 is a top cross-sectional view of one embodiment of the granular material distribution device of the present invention used in the shifter shown in FIG.
  • FIG. 3 is a schematic perspective view of one embodiment showing a positional relationship between a distribution cylinder and a partition plate in the granular material distribution device shown in FIG.
  • FIG. 4 is a side sectional view of another embodiment of the shifter of the present invention.
  • FIG. 5 is a plan view of an embodiment of the shock absorbing net shown in FIG.
  • FIG. 6 is a plan view of one embodiment of the shock absorbing plate shown in FIG.
  • FIG. 7 is a characteristic diagram of another example showing a result of distributing powders and granules into four groups using the powder and granules distribution apparatus of the present invention.
  • FIG. 1 is a side sectional view of an embodiment of the present invention.
  • FIG. 2 is a top cross-sectional view of one embodiment of the granular material distribution apparatus of the present invention used in the shifter shown in FIG. Note that the granular material distribution device shown in FIG. 1 is a side sectional view taken along line AA of the granular material distribution device shown in FIG.
  • the shifts 10 shown in these figures are obtained by uniformly distributing particles such as flour, and in the case of this embodiment, distributing the particles equally into three groups.
  • a powder / particle distributing device 14 for evenly distributing the bodies into three groups and supplying the same to the shifter body 12.
  • the powder material distribution device 14 In the shifter 10 shown in the figure, first, the powder material distribution device 14
  • An installation table 16 is arranged on the upper surface of the shifter body 12, and is installed on the installation table 16.
  • the installation table 16 may be configured to be separated from or integrated with the powder material distribution device 14.
  • the granular material distribution device 14 basically includes a conical distribution table 18 and a distribution table 18.
  • a hollow cylindrical distribution tube 2 2 which is arranged around the center, that is, coaxially above the distribution table 18, forms a storage room 20 for the powder and granules together with the distribution table 18, and functions as a weir plate.
  • a hollow cylindrical supply cylinder 24 arranged around the center of the distribution table 18, that is, coaxially at the top of the distribution table 18, for introducing the granular material into the storage chamber 20;
  • a hollow cylindrical outer peripheral wall 26 covering the outer circumferences of the distribution table 18, the distribution cylinder 22 and the supply cylinder 24 is provided.
  • the distribution table 18 has a conical shape in the illustrated example, but may have a disk shape. It should be noted that the cone-shaped distribution table is more preferable than the disk-shaped distribution table because the powders are urged toward the outer peripheral wall 26 and are discharged quickly.
  • the hollow cylindrical outer peripheral wall 26 is provided with a ceiling part 27a having a circular opening at the center of the upper part, and the outer peripheral wall 26 and the ceiling part 27a are provided with a bottomed cylindrical casing.
  • a conical distribution table 18 is installed coaxially on the bottom surface of the bottomed cylindrical casing 27, and a hollow cylindrical distribution cylinder is provided above the distribution table 18. 22 are arranged coaxially.
  • the supply cylinder 24 for introducing the granular material into the storage chamber 20 is arranged so that the supply cylinder 24 is coaxially arranged with the distribution cylinder 22 so that the ceiling 2 of the casing 2 7 is disposed. It is inserted into the circular opening of 7a, and is preferably attached to the ceiling 27a so as to be vertically movable.
  • the upper end of the supply tube 24 extends outside the casing 27, that is, above the ceiling portion 27a attached to the outer peripheral wall 26, and can absorb vibration caused by vibration. Through a flexible hollow member, for example, it is connected to a discharge port of a granular material such as a hopper or a screw feeder.
  • a granular material such as a hopper or a screw feeder.
  • the powder stored in the hopper and the powder transported by the screw feeder are introduced into the storage chamber 20 of the powder distributor 14 via the supply tube 24.
  • the storage room 20 is a space for temporarily storing the powder and granules, the upper surface of the distribution table 18 being the bottom surface, and the inner wall of the distribution cylinder 22 functioning as a weir as the inner wall. You.
  • the outer diameter of the supply cylinder 24 is smaller than the inner diameter of the distribution cylinder 22, and the lower end of the supply cylinder 24 is higher than the distribution table 18, and is equal to or less than the upper end of the distribution cylinder 22. (The position of the upper end of the distribution tube 22 or a position lower than it). That is, the lower end of the supply tube 24 is disposed in the distribution tube 22. As a result, the granular material that has fallen into the storage chamber 20 comes into contact with the lower end of the supply cylinder 24. In this state, if the granular material distribution device 14 is vibrated, Granules can be more effectively leveled in the storage chamber 20.
  • the granular material distribution device 14 of the present invention a plurality of annular materials such as the granular material distribution machine disclosed in Japanese Patent Application Laid-Open No. 11-208856 No dams are required.
  • an adjusting means 28 for adjusting the height of the lower end of the supply tube 24 is provided as a preferred embodiment.
  • the height of the lower end of the supply cylinder 24 is appropriately adjusted according to the type and flow rate of the powder and the like, and There is an advantage that the distribution accuracy of the granules can be optimized.
  • the supply cylinder 24 is attached to the ceiling 27a of the casing 27, and the height of the lower end of the supply cylinder 24 is set within the above range. You may make it fix to a position.
  • the upper end of the distribution cylinder 22 is formed in a corrugated shape, and the notches of the plurality of corrugations are formed uniformly.
  • the lower end of the supply tube 24 is preferably located above the lower end of the cutout of the waveform at the upper end of the distribution tube 22, that is, the upper end of the distribution tube 22 (notch Preferably, it is located between the upper end) and the lower end of the notch.
  • the lower end of the distribution tube 22 is separated from the distribution table 18 by a predetermined distance, and a slit 30 extending over the entire lower end of the distribution tube 22 between the distribution table 18 and the distribution table 18. Is preferably provided.
  • the shape of the upper end of the distribution cylinder 22 is not limited to the waveform shown in the illustrated example, and may be any shape, and may be a flat shape without a slit-shaped notch. Is preferably formed.
  • a notch that is wider toward the top such as a waveform notch or a V-shaped notch in the illustrated example, More preferably, a number is provided.
  • the predetermined interval of the slit between the distribution table 18 and the distribution tube 22 may be appropriately determined according to the type of the granular material, but is usually preferably about 4 to 3 Omm. In this way, by providing a slit over the entire circumference between the distribution table 18 and the lower end of the distribution tube 22, at the time of the distribution of the powder, the powder is placed at the bottom of the storage chamber 20. This has the advantage that it can be prevented from staying and that the entire amount can be discharged from the device immediately after the supply of the large-mass-rate granular material.
  • a hollow arm 34 having a predetermined angle of inclination is connected to transport the powdery material after being distributed to the supply port of the powdery material of the shifter main body 12.
  • the openings of the arms 34 and the supply ports of the shifter body 12 are connected by a flexible hollow member 36.
  • the space between the distribution cylinder 22 and the outer peripheral wall 26 is divided into three spaces corresponding to each of the three outlets 32.
  • the shape of the waveform at the upper end of the distribution cylinder 22 should be the same.
  • T JP02 / 10339 The same applies to the case where a shape other than the waveform is formed.
  • the distribution cylinder 22 is fixed to the inner wall of the side wall of the outer peripheral wall 26 except for the position of the discharge port 32 by three fixing members 40 provided between the partition plates 38 adjacent to each other. Have been.
  • the ceiling 27 a (the upper surface of the casing 27) attached to the outer peripheral wall 26 has powder particles covered by the outer peripheral wall 26 and the ceiling 27 a (casing 27).
  • three transparent inspection windows 42 are provided corresponding to the three outlets 32 respectively.
  • the shifter main body 12 is, in the present embodiment, for example, a three-sieving section configured by stacking a sieve frame having a plurality of sieve nets having different meshes. It has.
  • the shifter main body 12 is vibrated by the vibration generating means, and simultaneously sieves three groups of the granular materials supplied from the granular material distribution device 14 by three sieving sections.
  • the powder and granules discharged from the shift main body 12 are supplied to the next process, for example, bagging.
  • the configuration of the shifter main body 12 is not limited at all, and any conventionally known shifter main body can be applied.
  • the granular material is introduced into the storage chamber 20 of the granular material distribution device 14 via the supply cylinder 24.
  • the granular material distribution device 14 is simultaneously vibrated when the shifter main body 12 is vibrated by the vibration generating means, and due to this vibration, the granular material stored in the storage chamber 20 is moved to the distribution cylinder 22. It spills almost evenly from the cutout of the waveform at the upper end and the slit 30 between the distribution tube 22 and the distribution table 18 into three spaces separated by the partition plate 38.
  • the vibration generated by the vibration generating means is preferably a horizontal rotational vibration in order to efficiently distribute the powder having a large mass velocity.
  • the three groups of powder particles spilled into the three spaces separated by the partition plates 38 pass from the three outlets 32 provided on the outer peripheral wall 26 via the arms 34 and the hollow members 36. Are supplied to the supply ports of the shifter body 12 respectively. Then, the sift body 1 12 is vibrated by the vibration generating means, and the three sieving sections sift the three groups of granules supplied from the granule distributor 14 at the same time.
  • the powder and granules are equally distributed into three groups and sieved at the same time.
  • the present invention is not limited to this.
  • the granules may be distributed into any number of groups.
  • the present invention is not limited to this, and the granular material distribution device 14 is It may be used alone, or may be used in combination with another device other than the shifter body 12. In this case, when the vibration generating means is not provided as in the shifter main body 12, it is necessary to separately provide a vibration generating means for vibrating the powder material distribution device 14.
  • Table 1 shows the results of actually distributing powders and granules into four groups using the powder and granules distribution apparatus of the present invention.
  • the interval between the slits between the distribution table and the distribution tube was about 1 Omm, and the position of the lower end of the supply tube was 45 mm below the upper end of the distribution tube.
  • each of the intakes A, B, C, D The weight ratio varies up to ⁇ 2%. This is because by increasing the feed rate, It can be inferred that the granular material introduced into the storage room of the granular material distribution device via the supply cylinder was eccentric, and that the impact caused a large amount of granular material to be distributed to the intake near the drop position. .
  • the distribution weight ratio of the granular material is about 2% or less, and when the granular material is distributed using the granular material distribution device of the present invention, the granular material is evenly distributed with extremely high accuracy. You can see that they can be distributed.
  • the above-described powder and granular material distribution apparatus and the shifter of the present invention are arranged such that the lower end position of the supply tube 24 is located below the upper end portion of the distribution tube 22, that is, the inside of the distribution tube 22.
  • a plurality of corrugated notches are formed at the upper end of the distribution cylinder 22 to distribute the powder particles supplied from the supply cylinder 24 into the storage chamber 20 evenly.
  • the present invention is not limited to the embodiment, and it is also possible to equip the lower end portion of the supply cylinder with a shock-absorbing member to evenly distribute the powder and granules supplied from the supply cylinder into the storage chamber.
  • FIG. 4 shows an embodiment of the powder and particle distribution apparatus provided with such an impact buffer plate.
  • the granular material distribution device 50 shown in FIG. 4 is attached to the granular material distribution device 14 shown in FIG. 1, the configuration (shape) of the supply cylinder 57, and the lower end of the supply cylinder 57. Except for the shock-absorbing members (the shock-absorbing net 55 and the shock-absorbing plate 56), it has the same configuration in its basic device configuration, and a detailed description of the same configuration is omitted. Mainly, the different parts will be described in detail.
  • the powder and granular material distribution device 50 has a bottomed cylinder having a ceiling 51 c having a circular opening at the upper center and a hollow cylindrical outer peripheral wall 51 d.
  • a conical distribution table 5 2 is installed coaxially on the bottom surface of the Above the table 52, a hollow cylindrical distribution cylinder 53 is coaxially arranged, and the distribution table 52 and the distribution cylinder 53 form a storage chamber 54 into which the granular material is introduced.
  • the upper end of the distribution tube 53 is formed in a waveform, that is, a plurality of notches of a waveform are formed in the upper end, and a gap is formed between the entire circumference of the lower end of the distribution tube 53 and the distribution table 52.
  • a slit 60 for discharging the powder is provided.
  • a supply cylinder 57 for introducing the powder into the storage chamber 54 is arranged coaxially with the distribution cylinder 53. It is inserted into the circular opening of the ceiling 51c and is attached or fixed to its edge.
  • the supply cylinder 57 is formed by a cylindrical guide cylinder 58 at the upper part of the circular opening of the ceiling part 51 c and a reduced diameter part 51 e at the lower part.
  • An impact buffer plate 56 which is one of the impact buffer members of the present invention, is horizontally attached to the lower end of the supply cylinder 57.
  • the ceiling part 51 c of the casing 51, the reduced diameter part 51 e at the lower part of the supply cylinder 57, and the shock absorbing plate 56 are integrally formed. It is not limited to.
  • the lower end of the supply cylinder 57 is similar to the supply cylinder 24 and the distribution cylinder 22 shown in FIG. , That is, at or below the upper end of the distribution tube 53.
  • the supply cylinder 57 and the distribution cylinder 57 are positioned so that the lower end (impact buffer plate 56) of the supply cylinder 57 is located between the upper end and the lower end of the waveform cutout of the distribution cylinder 53.
  • Tube 53 is arranged.
  • the shock absorbing plate 56 is horizontally disposed at the lower end of the supply cylinder 57, and the shock absorbing net 55 is further provided a predetermined distance above the shock absorbing plate 56.
  • the shock absorbing plate 56 is arranged in a position away from the shock absorbing plate 56.
  • the shock absorbing net 55 and the shock absorbing plate 56 are located anywhere in the lower end portion of the supply cylinder 57, between the supply cylinder and the storage room composed of the distribution cylinder and the distribution stand. Although it may be installed anywhere, it is preferably disposed between the upper end of the distribution tube 53 (the upper end of the cutout of the waveform) and the lower end of the cutout. Only one may be arranged between the upper end and the lower end of the cutout of the waveform.
  • shock-absorbing nets 55 and a shock-absorbing plate 56 are attached as impact-absorbing members, but the present invention is not limited to this, and only one of them is attached. There may be. Also in this case, it is preferable that the shock absorbing member is arranged between the upper end and the lower end of the cutout of the waveform at the upper end of the distribution cylinder 53.
  • an impact absorbing net 55 or an impact absorbing plate 56 is preferable, but not limited thereto.
  • the shock absorbing net 55 has a net portion 55 b stretched in an annular frame 55 a, and an outer peripheral portion of the frame 55 a is a ceiling of the casing 51. It is fastened and fixed by screws 59 while being clamped between the flange 51b projecting from the inner periphery of the central opening of the part 51c and having its diameter reduced and its holding flange 51a. I have.
  • the size (outer diameter) of the mesh portion 55 b of the shock absorbing net 55 is such that all the particles from the guide cylinder 58 of the main cylinder 57 are formed by the net portion 55 b of the shock absorbing net 55. The larger the better, the smaller the inner diameter of the distribution cylinder 53 is.
  • the size of the net 55b of the shock absorbing net 55 will be distributed.
  • the inner diameter of the cylinder 53 must be smaller than that of the cylinder 53, and the shock absorbing net 55 needs to be located inside the distribution cylinder 53.
  • 55 c indicates a screw hole used when attaching the shock absorbing net 55.
  • the shock absorbing network is preferably an example shown in the figure, but is not limited to this example in the present invention, and various types may be used according to the type of the granular material, the processing amount, the processing speed, the device configuration, and the like. good.
  • the shock absorbing plate 56 has a large-diameter hole 56a formed in the center thereof, penetrating the front and back, and a large-diameter hole 56a penetrating the front and back in the outer periphery.
  • a large number of elongated holes 56 b are formed, which are inclined in the radial direction around the center, and a small-diameter hole 56 c that penetrates the front and back surfaces between the large-diameter hole 56 a and the long hole 56 b. are formed circumferentially.
  • the size of the shock-absorbing plate 56 that is, the diameter of the outer envelope circle of the long hole 56b is the same as the diameter of the guide cylinder 58 of the supply cylinder 57
  • the shock absorbing plate 56 is horizontally mounted on the lower end of the supply cylinder 57, and the shock absorbing net 55 and the shock absorbing plate 56 are arranged vertically in parallel,
  • the size of the shock absorbing plate 56 must be smaller than the inner diameter of the distribution cylinder 53. However, it must be located inside the distribution tube 53.
  • the shock absorbing net 55 and the shock absorbing plate 56 are arranged in an overlapping manner, it is preferable that the shock absorbing net 55 be located inside the distribution tube 53, but this is not a limitation. Absent.
  • the shock absorbing plate 56 is integrated with the ceiling 51 c of the casing 51 and the reduced diameter portion 51 e of the lower part of the supply cylinder 57 as shown in FIG. Although these parts are formed separately, these parts may be formed separately and fixed with fixing members such as screws.
  • shock absorbing plate is preferably an example shown in the drawings, but is not limited to this example in the present invention, and various types may be used according to the type of the granular material, the processing amount, the processing speed, the device configuration, and the like. .
  • the outer peripheral wall 5 1d of the casing 51 has four outlets 6 1 for the powder and granules corresponding to the four equally distributed groups, respectively.
  • a hollow arm 62 having a predetermined inclination angle is connected to transfer the evenly distributed powder to the powder / particle supply port of the shift main body 65 through the hollow member 63.
  • reference numeral 64 denotes a table on which the powdery and granular material distribution device 50 is installed.
  • the powder material distribution device 50 is configured as described above, when the powder material is introduced into the storage chamber 54 from the supply cylinder 57, the powder material is first subjected to the shock absorbing net 55 After passing through the mesh, it collides with the shock absorbing plate 56, passes through the large-diameter hole 56a, the long hole 56b, and the small-diameter hole 56c, and is introduced into the storage chamber 54. You.
  • FIG. 7 shows the result of distributing powders and granules into four groups using the powder and granules distributor 50.
  • the abscissa represents the supply speed of the granular material, and the ordinate represents the distribution ratio to the four groups.
  • indicates that only the shock-absorbing plate 56 is provided, and ⁇ indicates that only the shock-absorbing network 55 is provided.
  • the lower end of the supply tube is set to be equal to or lower than the upper end of the distribution tube. Or at a high mass velocity because an impact buffering member is provided between the supply cylinder and the storage chamber composed of the distribution cylinder and the distribution table (at the lower end of the supply cylinder). Even when the mass velocity of the powder is largely fluctuated, the powder can be equally distributed with high precision.
  • the structure of the granular material distribution device of the present invention is simple.
  • the vibration generating means of the powder and particle distributing apparatus and the vibration generating means of the shifter main body can be used in common. Is also inexpensive.

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  • Chemical Kinetics & Catalysis (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Abstract

This powder particle distributing device (14) comprises a disk-shaped or conical distribution block (18), a distribution sleeve (22) coaxially disposed above the distribution block and cooperate with the distribution block to define a reservoir chamber (20) for powder particles, a feed sleeve (24) whose outer diameter is smaller than the inner diameter of the distribution sleeve, and that is disposed coaxial with the distribution sleeve to position its lower end within the distribution sleeve, and adapted to introduce the powder particles into the reservoir chamber, and an outer peripheral wall (26) formed with a plurality of discharge ports (32) for individually discharging the powder particles, which have passed through the distribution sleeve from the reservoir chamber, into the outside from distribution block, the outer peripheral wall (26) covering the outer periphery of the distribution block and distribution sleeve. A shifter (10) comprises the powder particle distribution device (14). As a result, the distribution device and the shifter are simple in construction and even when the mass velocity of the powder particles being fed at a high mass velocity varies greatly, particularly at a high mass velocity, it is possible to evenly and accurately distribute the powder particles.

Description

 Light
粉粒体分配装置およびシフタ、 Granular material distribution device and shifter,
技術分野 本発明は、 粉粒体、 例えば小麦粉等のような粉粒体を複数のグループに均等分 配する粉粒体分配装置およびこれを用糸いたシフタ一に関するものである。 TECHNICAL FIELD The present invention relates to a powder / particle distributing apparatus for evenly distributing powder, such as flour, into a plurality of groups, and a shifter using the same.
 Rice field
背景技術 . 粉粒体を多量に処理する場合、 装置の一部に過重な負担がかかるのを防止する ために、 予め粉粒体を均等分配して次工程に供給する必要がある。 例えば、 篩分け処理では、 多量の粉粒体を篩分けする場合、 複数のセクションを有す るシフ夕一 (篩機) が用いられる。 従って、 これら複数のセクションの一部にの み過重な負担がかからないように、 あらかじめ粉粒体分配装置により粉粒体が均 等分配され、 均等分配された粉粒体が各々のセクションに供給される。 このような目的で提案された従来の粉粒体分配装置としては、 例えば、 本出願人に係る特公平 3— 6 0 9 2号公報に開示の粉粒体等分配装置や、 特開平 1 1一 2 0 8 8 5 6号公報に開示の粉粒体分配機等がある。 . まず、 特公平 3— 6 0 9 2号公報に開示の粉粒体等分配装置は、 上方に粉体供 給口を有するとともに水平底を有する粉粒体中央集積室と、 この中央集積室から 外周方向に延出し次の処理工程に粉粒体を供給するためのそれぞれ粉粒体排出口 を有する少なくとも 4個のシュートと、 中央集積室から各シュートへの水平な遷 移区域のそれぞれ各シュートに対応する位置であって、 これらの位置が中央集積 室を中心とする正多角形のほぼ頂点または中心に対してほぼ均等かつ中心を通る 少なくとも 2本の対称軸に対してほぼ対称となるような位置に設けられ、 中央集 積室から各シュ一トに向けて等量の粉粒体を水平方向に分割分配するための水平 方向の開口度が調整可能なゲートと、 中央集積室一シュ一ト組立体に揺動あるい は振動運動を与えるための運動付与手段とを備え、 粉粒体供給口より中央集積室 内に供給された粉粒体が運動付与手段により定レベルにならされて所定の等開口 度に調整された各ゲー卜より各シユートに等量に水平方向に分割分配されるよう 構成したものである。 BACKGROUND ART When treating a large amount of powders and granules, it is necessary to distribute the powders and granules equally in advance and supply them to the next process in order to prevent an excessive burden on a part of the apparatus. For example, in the sieving process, a sifter having a plurality of sections (a sifter) is used when sifting a large amount of granules. Therefore, the granules are distributed evenly in advance by the granule distribution device so that only a part of these sections is not overloaded, and the evenly distributed granules are supplied to each section. You. Examples of the conventional powder and particle distribution apparatus proposed for such a purpose include, for example, a powder and particle distribution apparatus disclosed in Japanese Patent Publication No. 3-6092 of the present applicant, Japanese Patent Application Publication No. 2008-856 discloses a powder and particle distributor. First, the apparatus for distributing powder and the like disclosed in Japanese Patent Publication No. Hei 3-69092 has a powder and particle central accumulation chamber having a powder supply port above and a horizontal bottom, and a central accumulation chamber. At least four chutes each extending from the central area to each chute and extending in the outer circumferential direction to supply the granules to the next processing step, each having a granule discharge port. Positions corresponding to each of the chutes in the transfer area, these positions being approximately equal to the apexes or the center of the regular polygon centered on the central accumulation chamber, and at least two symmetry axes passing through the center. A gate that can be adjusted in the horizontal direction to divide and distribute an equal amount of powder and granules in the horizontal direction from the central stacking chamber to each shout. A motion imparting means for imparting a swinging or vibrating motion to the central stacking chamber one-piece assembly, wherein the granular material supplied into the central accumulating chamber from the granular material supply port is provided with the motion imparting means. Thus, each gate is divided and distributed equally in the horizontal direction from each gate adjusted to a constant level and adjusted to a predetermined equal aperture.
しかし、 同公報に開示の粉粒体等分配装置では、 ゲートにより粉粒体の流量比 を決定しているため、 粉粒体の全質量速度が変動した場合に、 その分配比が変動 しゃすいという問題があつた。  However, in the apparatus for distributing powders and the like disclosed in the same publication, the flow rate ratio of the powders and granules is determined by the gate. Therefore, when the total mass velocity of the powders and granules changes, the distribution ratio fluctuates. There was a problem.
また、 特開平 1 1— 2 0 8 8 5 6号公報に開示の粉粒体分配機は、 環状の外周 壁で囲まれた円錐形の上面を有する分配台と、 分配台に振動を付与する振動発生 体とを備え、 外周壁には周方向に等間隔をおいて複数の排出口を設け、 分配台の 頂部と外周壁との間には、 頂部を中心として径が異なる複数の環状せき板を立設 すると共に各せき板の高さを外周壁側に行くに従い順次低くなるように形成する ことにより、 分配台頂部を含む第 1段目の貯溜槽から順次せき止め高さが低くな る環状の貯溜槽を形成し、 最も外周側のせき板と外周壁の間には、 周方向に等間 隔をおいて排出口と同数の仕切り板を設け、 第 1段目の貯溜槽に連続的に供給さ れる粉粒体を、 振動によって均しながら順次外方側の貯溜槽にオーバーフローさ せ、 各排出口に均等分配するようにしたものである。 しかし、 同公報に開示の粉粒体分配機では、 複数の環状せき板が必要であり、. 分配台の構成が複雑になつてコストが上昇するという問題があつた。 Further, the powder and particle dispenser disclosed in Japanese Patent Application Laid-Open No. H11-208856 is a distributing table having a conical upper surface surrounded by an annular outer peripheral wall, and applying vibration to the distributing table. A plurality of discharge ports are provided on the outer peripheral wall at equal intervals in the circumferential direction, and a plurality of annular dams having different diameters around the top are provided between the top of the distribution table and the outer peripheral wall. The height of each dam is gradually reduced from the first storage tank, including the top of the distribution table, by erecting the plates and making the height of each dam gradually lower toward the outer peripheral wall. An annular storage tank is formed, and the same number of partitions as the number of outlets are provided at equal intervals in the circumferential direction between the outermost weir and the outer peripheral wall. The granules supplied in a continuous manner are overflowed into the outer storage tank while being equalized by vibration. It is obtained so as to evenly distribute. However, the powder and particle distributor disclosed in the publication requires a plurality of annular dams, and there is a problem in that the configuration of the distribution table becomes complicated and the cost increases.
また、 同公報に開示の粉粒体分配機では、 粉粒体の投入口と最も内周側のせき 板との間に空間があるため、 投入口から供給された粉粒体が第 1段目の貯溜槽内 に貯溜されず、 第 2段目以降の貯溜槽へ直接供給される場合があり、 粉粒体の分 配比のばらつきが大きいという問題があつた。 発明の開示  In addition, in the powder and particle distributor disclosed in the same gazette, since there is a space between the input port for the powder and the innermost crevice plate, the powder supplied from the input port is in the first stage. In some cases, the powder was not stored in the first storage tank, but was directly supplied to the second and subsequent storage tanks, and the distribution ratio of the powder particles was large. Disclosure of the invention
本発明の目的は、 前記従来技術に基づく問題点を解消し、 より簡単な構造で、 特に、 大質量速度で供給される粉粒体の質量速度が大幅に変動した場合であって も、 粉粒体を高精度に等分配することができる粉粒体分配装置およびシフ夕一を 提供することにある。  SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems based on the prior art, and to achieve a simpler structure, especially when the mass velocity of the granular material supplied at a large mass velocity fluctuates greatly. An object of the present invention is to provide a powder and particle distributing apparatus and a shifter which can distribute particles equally with high precision.
上記目的を達成するために、 本発明は、 円盤状または円錐状の分配台と、 この 分配台の上部に同軸状に配置され、 前記分配台とともに粉粒体の貯留室を形成す る分配筒と、 その外径が前記分配筒の内径よりも小さく設定され、 その下端部が 前記分配筒内に位置するように前記分配筒と同軸状に配置され、 前記粉粒体を前 記貯留室内に導入する供給筒と、 前記貯留室から前記分配筒を通り抜けた前記粉 粒体を前記分配台より外部へ個別に排出する複数の排出口が形成され、 前記分配 台および前記分配筒の外周を覆う外周壁と、 を備えることを特徴とする粉粒体分 配装置を提供するものである。  In order to achieve the above object, the present invention provides a disk-shaped or conical distribution table, and a distribution cylinder which is coaxially disposed on an upper part of the distribution table and forms a storage chamber for powder and granules together with the distribution table. The outer diameter is set smaller than the inner diameter of the distribution cylinder, and the lower end portion is disposed coaxially with the distribution cylinder so that the lower end is located in the distribution cylinder. A supply tube to be introduced, and a plurality of discharge ports for individually discharging the particles passing through the distribution tube from the storage chamber to the outside from the distribution table are formed, and cover an outer periphery of the distribution table and the distribution tube. The present invention provides a powdery and granular material distribution device comprising: an outer peripheral wall;
ここで、 .前記分配筒の上端部に、 周方向において複数の切り欠きが形成された のが好ましく、 また、 複数の切り欠きの各々が、 上方にいくに従って幅広に形成 されるのが好ましい。 Here, it is preferable that a plurality of notches are formed in a circumferential direction at an upper end portion of the distribution cylinder, and each of the plurality of notches is formed so as to become wider as going upward. Preferably.
また、 前記供給筒の下端部は、 前記分配筒の上端部と前記複数の切り欠きの下 端部との間の位置に配置されるものであるのが好ましい。  Further, it is preferable that the lower end of the supply tube is disposed at a position between the upper end of the distribution tube and the lower end of the plurality of cutouts.
また、 上記各粉粒体分配装置は、 さらに、 前記外周壁の上端部に設けられる、 中心に円形開口部を持つ円板状の天井部を有し、 前記供給筒は、 前記外周壁の天 井部に前記円形開口部を貫通するように取り付けられるのが好ましい。  In addition, each of the powder and particle distribution devices further includes a disc-shaped ceiling provided at an upper end portion of the outer peripheral wall and having a circular opening at the center. Preferably, the well is attached so as to pass through the circular opening.
また、 上記各粉粒体分配装置は、 さらに、 前記供給筒の下端部を前記分配筒内 に位置させ、 しかも前記供給筒の下端部の高さを調整する高さ調整手段を備える のが好ましい。 .  In addition, it is preferable that each of the powder and particle distribution apparatuses further includes height adjusting means for positioning a lower end of the supply cylinder in the distribution cylinder and adjusting a height of the lower end of the supply cylinder. . .
また、 上記各粉粒体分配装置は、 さらに、 前記供給筒の下端部に取り付けられ た複数の貫通孔を有する衝撃緩衝部材を備えるのが好ましい。  Further, it is preferable that each of the powder and particle distribution apparatuses further includes an impact buffering member having a plurality of through holes attached to a lower end of the supply cylinder.
また、 前記衝撃緩衝部材は、 前記供給筒の下端部を覆うように取り付けられる のが好ましい。  Further, it is preferable that the shock absorbing member is attached so as to cover a lower end portion of the supply cylinder.
また、 前記衝撃緩衝部材は、 網目状に形成された衝撃緩衝網を含むのが好まし い。  Further, it is preferable that the shock absorbing member includes a shock absorbing net formed in a mesh shape.
また、 前記衝撃緩衝部材は、 前記複数の貫通孔として、 中心開口部、 複数の円 状貫通孔およびその中心から放射方向に傾斜する複数の傾斜貫通長孔を有する衝 撃緩衝板を含むのが好ましい。  Further, the shock absorbing member preferably includes, as the plurality of through holes, an impact buffer plate having a central opening, a plurality of circular through holes, and a plurality of oblique through-holes inclined radially from the center thereof. preferable.
また、 前記衝撃緩衝部材は、 網目状に形成された衝撃緩衝網と、 前記複数の貫 通孔として、 中心開口部、 複数の円状貫通孔およびその中心から放射方向に傾斜 する複数の傾斜貫通長孔を有する衝撃緩衝板とを含み、 前記衝撃緩衝板は、 前記 衝撃緩衝網より下方に配置されるるのが好ましい。 また、 前記衝撃緩衝板は、 前記分配筒内に位置するのが好ましい。 In addition, the shock-absorbing member includes a mesh-shaped shock-absorbing net, a plurality of through-holes, a central opening, a plurality of circular through-holes, and a plurality of inclined through-holes that are inclined radially from the center thereof. And a shock-absorbing plate having a long hole, wherein the shock-absorbing plate is preferably disposed below the shock-absorbing net. Further, it is preferable that the shock absorbing plate is located in the distribution cylinder.
また、 前記分配筒の上端部に、 周方向において複数の切り欠きが形成されてい る時、 前記衝撃緩衝板は、 前記分配筒の上端部と前記複数の切り欠きの下端部と の間の位置に配置されるものであるのが好ましい。  Further, when a plurality of notches are formed in a circumferential direction at an upper end portion of the distribution tube, the shock absorbing plate is positioned between an upper end portion of the distribution tube and a lower end portion of the plurality of notches. It is preferred that they are arranged in
また、 上記各粉粒体分配装置は、 さらに前記分配筒の下端部と前記分配台との 間に、 前記分配筒の下端部全周に亘つて設けられたスリツトを備えるのが好まし い。  In addition, it is preferable that each of the powder and particle distributing apparatuses further includes a slit provided between the lower end of the distribution tube and the distributing table over the entire periphery of the lower end of the distribution tube.
また、 前記分配筒の下端部と前記分配台との間の前記スリツ卜の寸法は、 The dimensions of the slit between the lower end of the distribution cylinder and the distribution table are as follows:
4〜3 O mmであるのが好ましい。 It is preferably between 4 and 3 O mm.
また、 上記の各粉粒体分配装置は、 さらに、 当該粉粒体分配装置を振動させる 振動発生手段を備えるのが好ましい。  Further, it is preferable that each of the above-mentioned granular material distribution devices further includes a vibration generating unit that vibrates the granular material distribution device.
また、 本発明は、 複数のグループに分配された粉粒体を同時に篩分けする シフタ一本体と、 このシフ夕一本体を振動させる振動発生手段と、 前記シフ夕一 本体の上面部に設置され、 前記振動発生手段によって前記シフ夕一本体が振動さ れると同時に振動され、 前記粉粒体を前記複数のグループに分配して前記 シフタ一本体に供給する請求項 1〜 2 0のいずれかに記載の粉粒体分配装置とを 具備したことを特徴とするシフ夕一を提供するものである。  The present invention also provides a shifter body for simultaneously sieving the powders and granules distributed to a plurality of groups, vibration generating means for vibrating the shift body, and a shifter installed on an upper surface of the shift body. The method according to any one of claims 1 to 20, wherein the shift main body is vibrated at the same time as the main body is vibrated by the vibration generating means, and the granular material is distributed to the plurality of groups and supplied to the shifter main body. The present invention also provides a shifter characterized by comprising the above-described powder and particle distribution apparatus.
なお、 本発明でいう 「振動」 とは、 垂直 (鉛直) 方向、 水平方向の振動は もちろん、 略円状を描く回転運動をも含むものである。  The “vibration” referred to in the present invention includes not only vertical (vertical) and horizontal vibrations, but also rotational movements in a substantially circular shape.
また、 本発明において、 分配筒は、 堰板として機能するものをいう。 図面の簡単な説明 図 1は、 本発明のシフ夕一の一実施例の側断面図である。 Further, in the present invention, the distribution cylinder refers to one that functions as a weir plate. BRIEF DESCRIPTION OF THE FIGURES FIG. 1 is a side sectional view of an embodiment of the present invention.
図 2は、 図 1に示すシフターで用いられている本発明の粉粒体分配装置の一実 施例の上断面図である。  FIG. 2 is a top cross-sectional view of one embodiment of the granular material distribution device of the present invention used in the shifter shown in FIG.
図 3は、 図 2に示す粉粒体分配装置において、 分配筒と仕切り板の位置関係を 表す一実施例の斜視概略図である。  FIG. 3 is a schematic perspective view of one embodiment showing a positional relationship between a distribution cylinder and a partition plate in the granular material distribution device shown in FIG.
図 4は、 本発明のシフタ一の他の実施例の側断面図である。  FIG. 4 is a side sectional view of another embodiment of the shifter of the present invention.
図 5は、 図 4に示す衝撃緩衝網の一実施例の平面図である。  FIG. 5 is a plan view of an embodiment of the shock absorbing net shown in FIG.
図 6は、 図 4に示す衝撃緩衝板の一実施例の平面図である。  FIG. 6 is a plan view of one embodiment of the shock absorbing plate shown in FIG.
図 7は、 本発明の粉粒体分配装置を用いて粉粒体を 4つのグループに分配した 結果を表す他の実施例の特性図である。 発明を実施するための最良の形態  FIG. 7 is a characteristic diagram of another example showing a result of distributing powders and granules into four groups using the powder and granules distribution apparatus of the present invention. BEST MODE FOR CARRYING OUT THE INVENTION
本発明に係る粉粒体分配装置およびシフターを添付の図面に示す好適実施例に 基づいて以下に詳細に説明する。  DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A granular material distribution device and a shifter according to the present invention will be described in detail below based on preferred embodiments shown in the accompanying drawings.
図 1は、 本発明のシフ夕一の一実施例の側断面図である。 また、 図 2は、 図 1 に示すシフタ一で用いられている本発明の粉粒体分配装置の一実施例の上断面図 である。 なお、 図 1に示す粉粒体分配装置は、 図 2に示す粉粒体分配装置の A - A線における側断面図を示すものである。  FIG. 1 is a side sectional view of an embodiment of the present invention. FIG. 2 is a top cross-sectional view of one embodiment of the granular material distribution apparatus of the present invention used in the shifter shown in FIG. Note that the granular material distribution device shown in FIG. 1 is a side sectional view taken along line AA of the granular material distribution device shown in FIG.
これらの図に示すシフ夕一 1 0は、 例えば小麦粉等のような粉粒体を均等に分 配、 本実施例の場合には粉粒体を 3つのグループに均等分配し、 これらの 3つの グループに分配された粉粒体を同時に篩分けするもので、 篩分けを行うシフタ一 本体 1 2と、 このシフタ一本体を振動させる振動発生手段 (図示省略) と、 粉粒 PC画 2/10339 The shifts 10 shown in these figures are obtained by uniformly distributing particles such as flour, and in the case of this embodiment, distributing the particles equally into three groups. A sifter body 12 for sieving the powders and granules distributed to the group at the same time, a vibration generating means (not shown) for vibrating the shifter body, PC drawing 2/10339
7  7
体を 3つのグループに均等分配してシフター本体 1 2に供給する粉粒体分配装置 1 4とを備えている。  And a powder / particle distributing device 14 for evenly distributing the bodies into three groups and supplying the same to the shifter body 12.
同図に示すシフタ一 1 0において、 まず、 粉粒体分配装置 1 4は、 図示例の場 In the shifter 10 shown in the figure, first, the powder material distribution device 14
.合、 振動発生手段によってシフタ一本体 1 2が振動される時同時に振動され、 粉 粒体を 3つのグループに分配してシフター本体 1 2の各セクションの粉粒体の供 給口に供給するもので、 シフタ一本体 1 2の上面部に設置台 1 6を配置し、 この 設置台 1 6の上に設置されている。 なお、 設置台 1 6は、 粉粒体分配装置 1 4と 分離型に構成しても一体型に構成してもよい。 When the shifter main body 12 is vibrated by the vibration generating means, it is vibrated at the same time, and the powder is distributed into three groups and supplied to the supply port of the powder in each section of the shifter main body 12. An installation table 16 is arranged on the upper surface of the shifter body 12, and is installed on the installation table 16. In addition, the installation table 16 may be configured to be separated from or integrated with the powder material distribution device 14.
粉粒体分配装置 1 4は、 基本的に、 円錐状の分配台 1 8と、 この分配台 1 8の The granular material distribution device 14 basically includes a conical distribution table 18 and a distribution table 18.
, 中心を中心として、 すなわち同軸状に分配台 1 8の上部に配置され、 分配台 1 8 と共に粉粒体の貯留室 2 0を形成するとともに堰板として機能する中空円筒状の 分配筒 2 2と、 分配台 1 8の中心を中心として、 すなわち同軸状に分配台 1 8の 上部に配置され、 粉粒体を貯留室 2 0内に導入するための中空円筒状の供給筒 2 4と、 分配台 1 8、 分配筒 2 2および供給筒 2 4の外周を覆う中空円筒状の外周 壁 2 6とを備えている。 , A hollow cylindrical distribution tube 2 2 which is arranged around the center, that is, coaxially above the distribution table 18, forms a storage room 20 for the powder and granules together with the distribution table 18, and functions as a weir plate. A hollow cylindrical supply cylinder 24 arranged around the center of the distribution table 18, that is, coaxially at the top of the distribution table 18, for introducing the granular material into the storage chamber 20; A hollow cylindrical outer peripheral wall 26 covering the outer circumferences of the distribution table 18, the distribution cylinder 22 and the supply cylinder 24 is provided.
ここで、 分配台 1 8は、 図示例では円錐状のものであるが、 円盤状のものでも よい。 なお、 円盤状の分配台よりも円錐状の分配台の方が、 粉粒体が外周壁 2 6 側へ付勢され、 速やかに排出されるため、 好ましい形状と言える。  Here, the distribution table 18 has a conical shape in the illustrated example, but may have a disk shape. It should be noted that the cone-shaped distribution table is more preferable than the disk-shaped distribution table because the powders are urged toward the outer peripheral wall 26 and are discharged quickly.
中空円筒状の外周壁 2 6には、 上部中央部に円形に開口した開口部を持つ天井 部 2 7 aが取り付けられ、 外周壁 2 6および天井部 2 7 aは、 有底円筒形の ケ一シング 2 7を構成し、 この有底円筒形のケーシング 2 7内の底面上に円錐状 の分配台 1 8が同軸状に設置され、 この分配台 1 8の上方に中空円筒状の分配筒 2 2が同軸状に配置されている。 分配台 1 8の上方には、 粉粒体を貯留室 2 0内 に導入するための供給筒 2 4が、 分配筒 2 2に同軸状に配置されるように、 ケーシング 2 7の天井部 2 7 aの円形開口部に揷入されて、 好ましくは上下動可 能に天井部 2 7 aに取り付けられている。 The hollow cylindrical outer peripheral wall 26 is provided with a ceiling part 27a having a circular opening at the center of the upper part, and the outer peripheral wall 26 and the ceiling part 27a are provided with a bottomed cylindrical casing. A conical distribution table 18 is installed coaxially on the bottom surface of the bottomed cylindrical casing 27, and a hollow cylindrical distribution cylinder is provided above the distribution table 18. 22 are arranged coaxially. Above the distribution table 18, the supply cylinder 24 for introducing the granular material into the storage chamber 20 is arranged so that the supply cylinder 24 is coaxially arranged with the distribution cylinder 22 so that the ceiling 2 of the casing 2 7 is disposed. It is inserted into the circular opening of 7a, and is preferably attached to the ceiling 27a so as to be vertically movable.
供給筒 2 4の上端部は、 ケ一シング 2 7の外部、 すなわち外周壁 2 6に取り付 けられている天井部 2 7 aの上方に延在しており、 振動による振れを吸収する可 撓性の中空部材を介して、 例えばホッパーやスクリユーフィーダ一等の粉粒体の 排出口に接続される。 これらのホッパーに貯留される粉粒体やスクリュ一 フィーダ一により搬送される粉粒体が供給筒 2 4を介して粉粒体分配装置 1 4の 貯留室 2 0内へ導入される。 なお、 貯留室 2 0は、 粉粒体を一時的に貯留する空 間であり、 分配台 1 8の上面をその底面とし、 堰として機能する分配筒 2 2の内 壁をその内壁として構成される。  The upper end of the supply tube 24 extends outside the casing 27, that is, above the ceiling portion 27a attached to the outer peripheral wall 26, and can absorb vibration caused by vibration. Through a flexible hollow member, for example, it is connected to a discharge port of a granular material such as a hopper or a screw feeder. The powder stored in the hopper and the powder transported by the screw feeder are introduced into the storage chamber 20 of the powder distributor 14 via the supply tube 24. The storage room 20 is a space for temporarily storing the powder and granules, the upper surface of the distribution table 18 being the bottom surface, and the inner wall of the distribution cylinder 22 functioning as a weir as the inner wall. You.
また、 供給筒 2 4の外径は、 分配筒 2 2の内径よりも小径であり、 供給筒 2 4 の下端部は、 分配台 1 8よりも高く、 なおかつ、 分配筒 2 2の上端部以下の位置 (分配筒 2 2の上端部の位置、 またはそれよりも低い位置) に設定される。 すな わち、 供給筒 2 4の下端部は、 分配筒 2 2内に配置されている。 これにより、 貯 留室 2 0内に落下した粉粒体は、 供給筒 2 4の下端部に接触されることになり、 この状態で、 粉粒体分配装置 1 4を振動させれば、 粉粒体を貯留室 2 0内でより 効果的に均すことができるようになる。 つまり、 大質量流量で粉粒体が偏心して 落下してきてもその勢いで特定の方向に粉粒体が多く流れるという現象が抑制さ れ、 全周排出の均等性が維持される。 このため、 本発明の粉粒体分配装置 1 4で は、 特開平 1 1— 2 0 8 8 5 6号公報に開示の粉粒体分配機のような複数の環状 せき板は不要である。 Also, the outer diameter of the supply cylinder 24 is smaller than the inner diameter of the distribution cylinder 22, and the lower end of the supply cylinder 24 is higher than the distribution table 18, and is equal to or less than the upper end of the distribution cylinder 22. (The position of the upper end of the distribution tube 22 or a position lower than it). That is, the lower end of the supply tube 24 is disposed in the distribution tube 22. As a result, the granular material that has fallen into the storage chamber 20 comes into contact with the lower end of the supply cylinder 24. In this state, if the granular material distribution device 14 is vibrated, Granules can be more effectively leveled in the storage chamber 20. In other words, even if the granular material drops eccentrically at a large mass flow rate, the phenomenon that a large amount of the granular material flows in a specific direction by the momentum is suppressed, and the uniformity of the discharge around the entire circumference is maintained. For this reason, in the granular material distribution device 14 of the present invention, a plurality of annular materials such as the granular material distribution machine disclosed in Japanese Patent Application Laid-Open No. 11-208856 No dams are required.
また、 図示例の場合には、 好ましい実施形態として供給筒 2 4の下端部 の高さを調整するための調整手段 2 8を備えている。 この調整手段 2 8を ケ一シング 2 7の天井部 2 7 aに設けることにより、 粉粒体の種類や流量等に応 じて供給筒 2 4の下端部の高さを適宜調整し、 粉粒体の分配精度を最適化するこ とができるという利点がある。 なお、 もちろん、 この調整手段 2 8を設けること なく、 供給筒 2 4をケ一シング 2 7の天井部 2 7 aに取り付けて、 供給筒 2 4の 下端部の高さを上記範囲内の所定位置に固定するようにしてもよい。  In the case of the illustrated example, an adjusting means 28 for adjusting the height of the lower end of the supply tube 24 is provided as a preferred embodiment. By providing the adjusting means 28 on the ceiling 27 a of the casing 27, the height of the lower end of the supply cylinder 24 is appropriately adjusted according to the type and flow rate of the powder and the like, and There is an advantage that the distribution accuracy of the granules can be optimized. Of course, without providing the adjusting means 28, the supply cylinder 24 is attached to the ceiling 27a of the casing 27, and the height of the lower end of the supply cylinder 24 is set within the above range. You may make it fix to a position.
分配筒 2 2の上端部は、 波形に成形されており、 複数の波形の切り欠きが均等 に形成されているのが好ましい。 ここで、 供給筒 2 4の下端部は、 この分配 筒 2 2の上端部の波形の切り欠きの下端部より上方にあるのが好ましい、 すなわ ち分配筒 2 2の上端部 (切り欠きの上端部) と切り欠きの下端部との間に位置さ せるのが好ましい。 こうすることにより、 分配筒 2 2の上端部に形成された複数 の波形の切り欠きから、 貯留室に貯留された粉粒体を均等排出することが できる。  It is preferable that the upper end of the distribution cylinder 22 is formed in a corrugated shape, and the notches of the plurality of corrugations are formed uniformly. Here, the lower end of the supply tube 24 is preferably located above the lower end of the cutout of the waveform at the upper end of the distribution tube 22, that is, the upper end of the distribution tube 22 (notch Preferably, it is located between the upper end) and the lower end of the notch. By doing so, the powder particles stored in the storage chamber can be uniformly discharged from the plurality of corrugated notches formed at the upper end of the distribution cylinder 22.
また、 図示例のように、 分配筒 2 2の下端部は、 分配台 1 8から所定間隔離さ れており、 分配台 1 8との間に分配筒 2 2の下端部全周にわたるスリット 3 0が 設けられているのが好ましい。  Further, as shown in the illustrated example, the lower end of the distribution tube 22 is separated from the distribution table 18 by a predetermined distance, and a slit 30 extending over the entire lower end of the distribution tube 22 between the distribution table 18 and the distribution table 18. Is preferably provided.
なお、 分配筒 2 2の上端部の形状は、 図示例の波形に限定されず、 どのような 形状でも良く、 スリット状の切り欠きのない平坦なものであっても良いが、 複数 の切り欠きが形成されているのが好ましい。 切り欠きとしては、 例えば、 図示例 の波形切り欠きや V字型切り欠きのように、 上方になるほど幅広の切り欠きが複 数設けてあるのがより好ましい。 このように、 分配筒 2 2の上端部に、 上方にな るほど幅広の切り欠きを複数設けることによって、 大質量流量時に、 供給筒 2 4 と分配筒 2 2との間の粉面高さが上昇した場合であっても粉粒体流出のための実 質的な開口面積が増大し、 全周排出の均等性を確保したまま、 全質量排出速度を 増加させることができる。 The shape of the upper end of the distribution cylinder 22 is not limited to the waveform shown in the illustrated example, and may be any shape, and may be a flat shape without a slit-shaped notch. Is preferably formed. As the notch, for example, a notch that is wider toward the top, such as a waveform notch or a V-shaped notch in the illustrated example, More preferably, a number is provided. In this manner, by providing a plurality of notches wider at the upper end of the distribution cylinder 22 at the top, the powder surface height between the supply cylinder 24 and the distribution cylinder 22 at a large mass flow rate Even if the water level rises, the actual opening area for powder outflow increases, and the total mass discharge speed can be increased while ensuring uniform discharge around the entire circumference.
また、 分配台 1 8と分配筒 2 2との間のスリットの所定間隔は粉粒体の種類に 応じて適宜決定すればよいが、 通常、 4〜 3 O mm程度であるのが好ましい。 こ のように、 分配台 1 8と分配筒 2 2の下端部との間に全周に亘るスリットを設け ることによって、 粉粒体の分配時に、 貯留室 2 0の底部に粉粒体が留まるのを防 止すると共に、 大質量速度の粉粒体の供給終了後、 速やかに装置より全量排出す ることができるという利点がある。  Further, the predetermined interval of the slit between the distribution table 18 and the distribution tube 22 may be appropriately determined according to the type of the granular material, but is usually preferably about 4 to 3 Omm. In this way, by providing a slit over the entire circumference between the distribution table 18 and the lower end of the distribution tube 22, at the time of the distribution of the powder, the powder is placed at the bottom of the storage chamber 20. This has the advantage that it can be prevented from staying and that the entire amount can be discharged from the device immediately after the supply of the large-mass-rate granular material.
外周壁 2 6の側面部には、 均等分配される 3つのグループに各々対応する 3つ の粉粒体の排出口 3 2が設けられており、 これらの排出口 3 2には、 それぞれ均 等分配された後の粉粒体をシフタ一本体 1 2の粉粒体の供給口へ搬送するための 所定傾斜角を持つ中空のアーム 3 4が接続されている。 そして、 これらのアーム 3 4の開口部とシフター本体 1 2の供給口との間は、 可撓性の中空部材 3 6によ り接続されている。  On the side surface of the outer peripheral wall 26, there are provided three outlets 32 for the powder and granules corresponding to the three equally distributed groups, respectively. A hollow arm 34 having a predetermined angle of inclination is connected to transport the powdery material after being distributed to the supply port of the powdery material of the shifter main body 12. The openings of the arms 34 and the supply ports of the shifter body 12 are connected by a flexible hollow member 36.
ここで、 分配筒 2 2の側面部の外壁と外周壁 2 6の側面部の内壁との間には、 図 3に示すように、 互いに隣接する排出口 3 2の間に各タ仕切り板 3 8が設けら れている。 これらの仕切り板 3 8により、 分配筒 2 2と外周壁 2 6との間の空間 は、 3つの排出口 3 2の各々に対応する 3つの空間に分割される。 なお、 これら の 3つの空間において、 分配筒 2 2の上端部の波形の形状は同一形状となるよう T JP02/10339 に形成されている。 波形以外の形状に形成される場合も同様である。 Here, between the outer wall of the side wall of the distribution cylinder 22 and the inner wall of the side wall of the outer peripheral wall 26, as shown in FIG. 8 are provided. By these partition plates 38, the space between the distribution cylinder 22 and the outer peripheral wall 26 is divided into three spaces corresponding to each of the three outlets 32. In these three spaces, the shape of the waveform at the upper end of the distribution cylinder 22 should be the same. T JP02 / 10339. The same applies to the case where a shape other than the waveform is formed.
また、 分配筒 2 2は、 互いに隣接する仕切り板 3 8の間に設けられた 3つの固 定部材 4 0により、 排出口 3 2の位置を除く、 外周壁 2 6の側面部の内壁に固定 されている。  The distribution cylinder 22 is fixed to the inner wall of the side wall of the outer peripheral wall 26 except for the position of the discharge port 32 by three fixing members 40 provided between the partition plates 38 adjacent to each other. Have been.
また、 外周壁 2 6に取り付けられている天井部 2 7 a (ケーシング 2 7の上面 部) には、 外周壁 2 6および天井部 2 7 a (ケ一シング 2 7 ) によって覆われた 粉粒体分配装置 1 4の内部の様子を点検するために、 3つの排出口 3 2に各々対 応して 3つの透明な点検窓 4 2が設けられている。  The ceiling 27 a (the upper surface of the casing 27) attached to the outer peripheral wall 26 has powder particles covered by the outer peripheral wall 26 and the ceiling 27 a (casing 27). In order to inspect the inside of the body distribution device 14, three transparent inspection windows 42 are provided corresponding to the three outlets 32 respectively.
図示例のシフター 1 0においては、 シフタ一本体 1 2は、 本実施例の場合、 例 えば、 目の粗さの違う複数の篩網を有する篩枠を積み重ねて構成される 3つの篩 分セクションを備えている。 このシフ夕一本体 1 2は、 振動発生手段により振動 され、 3つの篩分セクションにより、 粉粒体分配装置 1 4から供給される 3つの グループの粉粒体を同時に篩分けする。 シフ夕一本体 1 2から排出される粉粒体 は、 例えば袋詰等の次工程に供給される。  In the shifter 10 of the illustrated example, the shifter main body 12 is, in the present embodiment, for example, a three-sieving section configured by stacking a sieve frame having a plurality of sieve nets having different meshes. It has. The shifter main body 12 is vibrated by the vibration generating means, and simultaneously sieves three groups of the granular materials supplied from the granular material distribution device 14 by three sieving sections. The powder and granules discharged from the shift main body 12 are supplied to the next process, for example, bagging.
なお、 シフタ一本体 1 2の構成は何ら限定されず、 従来公知の構成のシフ夕一 本体がいずれも適用可能である。  The configuration of the shifter main body 12 is not limited at all, and any conventionally known shifter main body can be applied.
図示例のシフタ一 1 0では、 粉粒体が供給筒 2 4を介して粉粒体分配装 置 1 4の貯留室 2 0内へ導入される。 粉粒体分配装置 1 4は、 振動発生手段 によってシフタ一本体 1 2が振動される時同時に振動され、 この振動により、 貯 留室 2 0に貯留された粉粒体は、 分配筒 2 2の上端部の波形の切り欠きおよび分 配筒 2 2と分配台 1 8との間のスリット 3 0から、 仕切り板 3 8によって区切ら れた 3つの空間へほぼ均等にこぼれ落ちる。 なお、 振動発生手段による振動は、 大質量速度の粉粒体を効率良く分配するた めに、 水平方向の回転振動であるのが好ましい。 In the shifter 10 of the illustrated example, the granular material is introduced into the storage chamber 20 of the granular material distribution device 14 via the supply cylinder 24. The granular material distribution device 14 is simultaneously vibrated when the shifter main body 12 is vibrated by the vibration generating means, and due to this vibration, the granular material stored in the storage chamber 20 is moved to the distribution cylinder 22. It spills almost evenly from the cutout of the waveform at the upper end and the slit 30 between the distribution tube 22 and the distribution table 18 into three spaces separated by the partition plate 38. The vibration generated by the vibration generating means is preferably a horizontal rotational vibration in order to efficiently distribute the powder having a large mass velocity.
仕切り板 3 8によって区切られた 3つの空間にこぼれ落ちた 3つのグループの 粉粒体は、 外周壁 2 6に設けられている 3つの排出口 3 2からアーム 3 4および 中空部材 3 6を介して、 シフタ一本体 1 2の供給口へそれぞれ供給される。 そし て、 シフ夕一本体 1 2は振動発生手段により振動され、 3つの篩分セクションに より、 粉粒体分配装置 1 4から供給される 3つのグループの粉粒体が同時に篩分 けされる。  The three groups of powder particles spilled into the three spaces separated by the partition plates 38 pass from the three outlets 32 provided on the outer peripheral wall 26 via the arms 34 and the hollow members 36. Are supplied to the supply ports of the shifter body 12 respectively. Then, the sift body 1 12 is vibrated by the vibration generating means, and the three sieving sections sift the three groups of granules supplied from the granule distributor 14 at the same time.
なお、 前記実施例では、 粉粒体を 3つのグループに均等分配して同時に篩分け する場合を示しているが、 本発明はこれに限定されず、 2つ以上のグループであ れば、 粉粒体をいくつのグループに分配するようにしてもよい。  Note that, in the above-described embodiment, a case is shown in which the powder and granules are equally distributed into three groups and sieved at the same time. However, the present invention is not limited to this. The granules may be distributed into any number of groups.
また、 シフタ一本体 1 2と粉粒体分配装置 1 4とを組み合わせたシフター 1 0 の例を挙げて説明しているが、 本発明はこれに限定されず、 粉粒体分配装置 1 4 を単体で使用してもよいし、 あるいは、 シフター本体 1 2以外の別の装置と組み 合わせて使用してもよい。 この場合、 シフタ一本体 1 2のように振動発生手段を 備えていない場合には、 別途、 粉粒体分配装置 1 4を振動させるための振動発生 手段を備える必要がある。  In addition, although an example of the shifter 10 in which the shifter main body 12 and the granular material distribution device 14 are combined is described, the present invention is not limited to this, and the granular material distribution device 14 is It may be used alone, or may be used in combination with another device other than the shifter body 12. In this case, when the vibration generating means is not provided as in the shifter main body 12, it is necessary to separately provide a vibration generating means for vibrating the powder material distribution device 14.
ここで、 本発明の粉粒体分配装置を使用して実際に粉粒体を 4つのグループに 分配した結果を表 1に示す。 表 1 Here, Table 1 shows the results of actually distributing powders and granules into four groups using the powder and granules distribution apparatus of the present invention. table 1
Figure imgf000015_0001
Figure imgf000015_0001
なお、 分配台と分配筒との間のスリットの間隔を約 1 Omm、 また、 供給筒の 下端部の位置を分配筒の上端部から 45 mm下方とした。 また、 粉粒体は、 ゆき:ォ一シヨン: フラワー (いずれも日清製粉株式会社製) = 3 : 1 : 1 の混合粉とした。 そして、 あらかじめ貯留室に粉粒体を導入している状態から、 シフ夕一への粉粒体の供給とシフタ一の稼働を同時に停止し、 その後、 両者を指 定時間だけ同時に運転して、 4つのグループに分配された粉粒体の重量を計測し た。  The interval between the slits between the distribution table and the distribution tube was about 1 Omm, and the position of the lower end of the supply tube was 45 mm below the upper end of the distribution tube. The powder was a mixed powder of Yuki: Ossion: Flower (all manufactured by Nisshin Flour Milling Co., Ltd.) = 3: 1: 1. Then, from the state where the granular material is introduced into the storage room in advance, the supply of the granular material to the shifter and the operation of the shifter are simultaneously stopped, and then both are simultaneously operated for a specified time, The weight of the granules divided into four groups was measured.
表 1に示すように、 粉粒体の供給速度を 4. 4トン Z時 (tZh) 、 供給時間 を 60秒 (s) とした場合、 取口 A, B, C, D毎の重量比が ± 1 %以内に 入っていて非常に高精度に均等分配できていることが分かる。  As shown in Table 1, when the supply speed of the granular material is 4.4 tons Z hour (tZh) and the supply time is 60 seconds (s), the weight ratio of each of the intakes A, B, C, and D becomes It can be seen that the distribution is within ± 1% and that the distribution is very accurate.
これに対し、 供給速度を 27. 0トン Z時、 供給時間を 10秒間とした場合の ように、 粉粒体の供給速度を増加した場合には、 各取口 A, B, C, Dの重量比 は ±2%前後までばらつく。 これは、 供給速度を上昇することにより、 上部から 供給筒を介して粉粒体分配装置の貯留室に導入される粉粒体が偏心していて、 そ の衝撃で落下位置に近い取口により多くの粉粒体が分配されたためであると推察 できる。 On the other hand, when the supply speed of the granular material is increased, for example, when the supply speed is 27.0 tons Z and the supply time is 10 seconds, each of the intakes A, B, C, D The weight ratio varies up to ± 2%. This is because by increasing the feed rate, It can be inferred that the granular material introduced into the storage room of the granular material distribution device via the supply cylinder was eccentric, and that the impact caused a large amount of granular material to be distributed to the intake near the drop position. .
いずれにしても、 粉粒体の分配重量比は 2 %前後以下の値であり、 本発明の粉 粒体分配装置を用いて粉粒体を分配した場合、 極めて高精度に粉粒体を均等分配 することができるということが分かる。  In any case, the distribution weight ratio of the granular material is about 2% or less, and when the granular material is distributed using the granular material distribution device of the present invention, the granular material is evenly distributed with extremely high accuracy. You can see that they can be distributed.
以上に説明した本発明の粉粒体分配装置およびシフタ一は、 供給筒 2 4の下端 位置を分配筒 2 2の上端部より下方に、 すなわち分配筒 2 2の内部に位置させ、 好ましくは、 分配筒 2 2の上端部に複数の波形の切り欠きを形成して、 供給 筒 2 4から貯留室 2 0内に供給される粉粒体を均等に分配するものであるが、 本 発明はこの実施例に限定されず、 供給筒の下端部に衝撃緩衝部材を取り付けるこ とにより、 供給筒から貯留室内に供給される粉粒体を均等に分配するようにして も良い。  The above-described powder and granular material distribution apparatus and the shifter of the present invention are arranged such that the lower end position of the supply tube 24 is located below the upper end portion of the distribution tube 22, that is, the inside of the distribution tube 22. A plurality of corrugated notches are formed at the upper end of the distribution cylinder 22 to distribute the powder particles supplied from the supply cylinder 24 into the storage chamber 20 evenly. The present invention is not limited to the embodiment, and it is also possible to equip the lower end portion of the supply cylinder with a shock-absorbing member to evenly distribute the powder and granules supplied from the supply cylinder into the storage chamber.
このような衝撃緩衝板を備える粉粒体分配装置の一実施例を図 4に示す。 なお、 図 4に示す粉粒体分配装置 5 0は、 図 1に示す粉粒体分配装置 1 4と、 供給筒 5 7の構成 (形状) と、 この供給筒 5 7の下端部に取り付けられる衝撃緩 衝部材 (衝撃緩衝網 5 5および衝撃緩衝板 5 6 ) とを除いて、 その基本的な装置 構成において同様な構成を有するものであり、 同様な構成についての詳細な説明 は省略し、 主に、 異なる部分について詳細に説明する。 ' 同図に示すように、 粉粒体分配装置 5 0では、 上部中央部に円形に開口した開 口部を持つ天井部 5 1 cおよび中空円筒状外周壁 5 1 dとを備える有底円筒形の ケ一シング 5 1内の底面上に円錐状の分配台 5 2が同軸状に設置され、 この分配 台 5 2の上方に中空円筒状の分配筒 5 3が同軸状に配置され、 これらの分配台 5 2および分配筒 5 3によって粉粒体が導入される貯留室 5 4が形成されている。 また、 分配筒 5 3の上端部は、 波形に形成され、 すなわち上端部には複数の波形 の切り欠きが形成され、 分配筒 5 3の下端部全周と分配台 5 2との間には粉粒体 をお出するスリット 6 0が設けられている。 FIG. 4 shows an embodiment of the powder and particle distribution apparatus provided with such an impact buffer plate. In addition, the granular material distribution device 50 shown in FIG. 4 is attached to the granular material distribution device 14 shown in FIG. 1, the configuration (shape) of the supply cylinder 57, and the lower end of the supply cylinder 57. Except for the shock-absorbing members (the shock-absorbing net 55 and the shock-absorbing plate 56), it has the same configuration in its basic device configuration, and a detailed description of the same configuration is omitted. Mainly, the different parts will be described in detail. '' As shown in the figure, the powder and granular material distribution device 50 has a bottomed cylinder having a ceiling 51 c having a circular opening at the upper center and a hollow cylindrical outer peripheral wall 51 d. A conical distribution table 5 2 is installed coaxially on the bottom surface of the Above the table 52, a hollow cylindrical distribution cylinder 53 is coaxially arranged, and the distribution table 52 and the distribution cylinder 53 form a storage chamber 54 into which the granular material is introduced. Further, the upper end of the distribution tube 53 is formed in a waveform, that is, a plurality of notches of a waveform are formed in the upper end, and a gap is formed between the entire circumference of the lower end of the distribution tube 53 and the distribution table 52. A slit 60 for discharging the powder is provided.
分配台 5 2の上方には、 分配筒 5 3に同軸状に配置されるように、 粉粒体を貯 留室 5 4内に導入するための供給筒 5 7が、 ケ一シング 5 1の天井部 5 1 cの円 形開口部に挿入されてその縁部に取り付けられている、 または固定されている。 この供給筒 5 7は、 天井部 5 1 cの円形開口部の上部の円筒状ガイド筒 5 8と下 部の縮径部 5 1 eとによって形成される。  Above the distribution table 52, a supply cylinder 57 for introducing the powder into the storage chamber 54 is arranged coaxially with the distribution cylinder 53. It is inserted into the circular opening of the ceiling 51c and is attached or fixed to its edge. The supply cylinder 57 is formed by a cylindrical guide cylinder 58 at the upper part of the circular opening of the ceiling part 51 c and a reduced diameter part 51 e at the lower part.
供給筒 5 7の下端部には、 本発明の衝撃緩衝部材の 1つである衝撃緩衝板 5 6 が水平に取り付けられる。 なお、 図示例では、 ケ一シング 5 1の天井部 5 1 c、 供給筒 5 7の下部の縮径部 5 1 eおよび衝撃緩衝板 5 6は、 一体成形されている が、 本発明はこれに限定されるわけではない。  An impact buffer plate 56, which is one of the impact buffer members of the present invention, is horizontally attached to the lower end of the supply cylinder 57. In the illustrated example, the ceiling part 51 c of the casing 51, the reduced diameter part 51 e at the lower part of the supply cylinder 57, and the shock absorbing plate 56 are integrally formed. It is not limited to.
ここで、 供給筒 5 7の下端部、 従って、 ここに取り付けられている衝撃緩衝板 5 6は、 図 1に示す供給筒 2 4および分配筒 2 2の場合と同様に、 分配筒 5 3内 に位置する、 すなわち、 分配筒 5 3の上端部またはその下方に位置する。 換言す れば、 供給筒 5 7の下端部 (衝撃緩衝板 5 6 ) が、 分配筒 5 3の波形の切り欠き 上端部と下端部との間に位置するように、 供給筒 5 7および分配筒 5 3は配置さ れる。  Here, the lower end of the supply cylinder 57, and thus the shock absorbing plate 56 attached thereto, is similar to the supply cylinder 24 and the distribution cylinder 22 shown in FIG. , That is, at or below the upper end of the distribution tube 53. In other words, the supply cylinder 57 and the distribution cylinder 57 are positioned so that the lower end (impact buffer plate 56) of the supply cylinder 57 is located between the upper end and the lower end of the waveform cutout of the distribution cylinder 53. Tube 53 is arranged.
供給筒 5 7には、 上述したように、 その下端部に衝撃緩衝板 5 6が水平に配置 されるとともに、 さらに、 衝撃緩衝網 5 5が、 衝撃緩衝板 5 6より所定距離上方 に離れた位置に、 衝撃緩衝板 5 6と平行に配置される。 As described above, the shock absorbing plate 56 is horizontally disposed at the lower end of the supply cylinder 57, and the shock absorbing net 55 is further provided a predetermined distance above the shock absorbing plate 56. The shock absorbing plate 56 is arranged in a position away from the shock absorbing plate 56.
ここで、 衝撃緩衝網 5 5および衝撃緩衝板 5 6は、 供給筒と、 分配筒および分 配台で構成される貯留室との間であれば、 供給筒 5 7の下端部のどこに配置して も良いが、 どこに取り付けた場合であっても、 分配筒 5 3の上端部 (波形の切り 欠きの上端部) と切り欠きの下端部との間に配置されるのが好ましいが、 いずれ か一方のみが、 波形の切り欠きの上端部と下端部との間に配置されるようにして も良い。  Here, the shock absorbing net 55 and the shock absorbing plate 56 are located anywhere in the lower end portion of the supply cylinder 57, between the supply cylinder and the storage room composed of the distribution cylinder and the distribution stand. Although it may be installed anywhere, it is preferably disposed between the upper end of the distribution tube 53 (the upper end of the cutout of the waveform) and the lower end of the cutout. Only one may be arranged between the upper end and the lower end of the cutout of the waveform.
なお、 図示例においては、 衝撃緩衝部材として、 衝撃緩衝網 5 5および衝撃緩 衝板 5 6の 2つを取り付けているが、 本発明はこれに限定されず、 いずれか一方 のみを取り付けるものであっても良い。 この場合にも、 衝撃緩衝部材は、 分配筒 5 3の上端部の波形の切り欠きの上端部と下端部との間に配置されるようにする のが好ましい。  In the illustrated example, two shock-absorbing nets 55 and a shock-absorbing plate 56 are attached as impact-absorbing members, but the present invention is not limited to this, and only one of them is attached. There may be. Also in this case, it is preferable that the shock absorbing member is arranged between the upper end and the lower end of the cutout of the waveform at the upper end of the distribution cylinder 53.
さらに、 本発明の衝撃緩衝部材としては、 衝撃緩衝網 5 5や衝撃緩衝板 5 6が 好ましいが、 これらに限定されるわけではない。  Further, as the shock absorbing member of the present invention, an impact absorbing net 55 or an impact absorbing plate 56 is preferable, but not limited thereto.
ここで、 衝撃緩衝網 5 5は、 図 5に示すように、 環状の枠体 5 5 a内に網部 5 5 bが張設され、 枠体 5 5 aの外周部がケーシング 5 1の天井部 5 1 cの中央開 口部の内周部に縮径して突設されたフランジ 5 1 bと、 その押えフランジ 5 1 a と間に挟持された状態でねじ 5 9によって締結固定されている。 衝撃緩衝網 5 5 の網部 5 5 bの大きさ (外径) は、 供,铪筒 5 7のガイド筒 5 8からの全ての粉粒 体が衝撃緩衝網 5 5の網部 5 5 bに投入されるように、 大きい方が良いが、 分配 筒 5 3の内径より小さい方が好ましい。 なお、 衝撃緩衝網 5 5のみを供給筒 5 7 の下端部に取り付ける場合には、 衝撃緩衝網 5 5の網部 5 5 bのサイズは、 分配 筒 5 3の内径より小さくする必要があり、 衝撃緩衝網 5 5は、 分配筒 5 3の内部 に位置させる必要がある。 Here, as shown in FIG. 5, the shock absorbing net 55 has a net portion 55 b stretched in an annular frame 55 a, and an outer peripheral portion of the frame 55 a is a ceiling of the casing 51. It is fastened and fixed by screws 59 while being clamped between the flange 51b projecting from the inner periphery of the central opening of the part 51c and having its diameter reduced and its holding flange 51a. I have. The size (outer diameter) of the mesh portion 55 b of the shock absorbing net 55 is such that all the particles from the guide cylinder 58 of the main cylinder 57 are formed by the net portion 55 b of the shock absorbing net 55. The larger the better, the smaller the inner diameter of the distribution cylinder 53 is. If only the shock absorbing net 55 is attached to the lower end of the supply cylinder 57, the size of the net 55b of the shock absorbing net 55 will be distributed. The inner diameter of the cylinder 53 must be smaller than that of the cylinder 53, and the shock absorbing net 55 needs to be located inside the distribution cylinder 53.
なお、 図中、 5 5 cは、 衝撃緩衝網 5 5を取付ける際に用いるねじ孔を示す。 また、 衝撃緩衝網は、 図示例のものが好まし が、 本発明ではこれに限定され ず、 粉粒体の種類や処理量や処理速度や装置構成等に応じて種々のものを用いて も良い。 In the figure, 55 c indicates a screw hole used when attaching the shock absorbing net 55. Further, the shock absorbing network is preferably an example shown in the figure, but is not limited to this example in the present invention, and various types may be used according to the type of the granular material, the processing amount, the processing speed, the device configuration, and the like. good.
また、 衝撃緩衝板 5 6は、 図 6に示すように、 その中央部に表裏を貫通する大 径孔 5 6 aが形成され、 外周部にはその表裏を貫通し、 大径孔 5 6 aを中心とし て放射方向に傾斜する長孔 5 6 bが多数形成されるとともに、 前記大径孔 5 6 a と長孔 5 6 bとの間には、 その表裏を貫通する小径孔 5 6 cが周状に多数形成さ れている。 ここで、 衝撃緩衝板 5 6のサイズ; すなわち長孔 5 6 bの外側包絡円 の直径は、 供給筒 5 7のガイド筒 5 8カゝらの全ての粉粒体が衝撃緩衝板 5 6の大 径孔 5 6 a、 多数の長孔 5 6 bおよび多数の小径孔 5 6 c形成部分に投入される ように、 大きい方が良いが、 分配筒 5 3の内径より小さい方が好ましい。 なお、 図示例のように、 衝撃緩衝板 5 6を供給筒 5 7の下端部に水平に取り付け、 衝撃 緩衝網 5 5と衝撃緩衝板 5 6とを上下に平行に重ねて配置する場合や、 衝撃緩衝 板 5 6のみを供給筒 5 7の下端部に水平に取り付ける場合には、 衝撃緩衝板 5 6 のサイズは、 分配筒 5 3の内径より小さくする必要があり、 衝撃緩衝板 5 6は、 分配筒 5 3の内部に位置させる必要がある。 しかし、 衝撃緩衝網 5 5と衝撃緩衝 板 5 6とを重ねて配置する場合には、 衝撃緩衝網 5 5は、 分配筒 5 3の内部に位 置させるのが好ましいが、 限定されるわけではない。  As shown in FIG. 6, the shock absorbing plate 56 has a large-diameter hole 56a formed in the center thereof, penetrating the front and back, and a large-diameter hole 56a penetrating the front and back in the outer periphery. A large number of elongated holes 56 b are formed, which are inclined in the radial direction around the center, and a small-diameter hole 56 c that penetrates the front and back surfaces between the large-diameter hole 56 a and the long hole 56 b. Are formed circumferentially. Here, the size of the shock-absorbing plate 56; that is, the diameter of the outer envelope circle of the long hole 56b is the same as the diameter of the guide cylinder 58 of the supply cylinder 57 The larger the better, the smaller the inner diameter of the distribution cylinder 53 is preferable, so that the large diameter hole 56a, the many long holes 56b, and the many small holes 56c are formed. In addition, as shown in the example in the figure, the shock absorbing plate 56 is horizontally mounted on the lower end of the supply cylinder 57, and the shock absorbing net 55 and the shock absorbing plate 56 are arranged vertically in parallel, When mounting only the shock absorbing plate 56 horizontally on the lower end of the supply cylinder 57, the size of the shock absorbing plate 56 must be smaller than the inner diameter of the distribution cylinder 53. However, it must be located inside the distribution tube 53. However, when the shock absorbing net 55 and the shock absorbing plate 56 are arranged in an overlapping manner, it is preferable that the shock absorbing net 55 be located inside the distribution tube 53, but this is not a limitation. Absent.
なお、 長?し 5 6 bの傾斜方向は、 分配筒 5 3を回転振動させる場合には、 その 回転方向に一致させるとよい。 In addition, long? When the distribution cylinder 53 is rotated and vibrated, the inclination direction of It is good to match with the direction of rotation.
衝撃緩衝板 5 6は、 図 6には省略されているが、 図 4に示すように、 ケーシン グ 5 1の天井部 5 1 cおよび供給筒 5 7の下部の縮径部 5 1 eと一体に成形され ているものであるが、 これらの各部分を別体で構成し、 ねじ等の固定具で固定し ても良い。  Although not shown in FIG. 6, the shock absorbing plate 56 is integrated with the ceiling 51 c of the casing 51 and the reduced diameter portion 51 e of the lower part of the supply cylinder 57 as shown in FIG. Although these parts are formed separately, these parts may be formed separately and fixed with fixing members such as screws.
また、 衝撃緩衝板は、 図示例のものが好ましいが、 本発明ではこれに限定され ず、 粉粒体の種類や処理量や処理速度や装置構成等に応じて種々のものを用いて も良い。  In addition, the shock absorbing plate is preferably an example shown in the drawings, but is not limited to this example in the present invention, and various types may be used according to the type of the granular material, the processing amount, the processing speed, the device configuration, and the like. .
ケーシング 5 1の外周壁 5 1 dには、 均等分配される 4つのグループに各々対 応する 4つの粉粒体の排出口 6 1が設けられ、 これらの排出口 6 1には、 それぞ れ均等分配された粉粒体をシフ夕一本体 6 5の粉粒体の供給口へ中空部材 6 3を 介して搬送するための所定傾斜角を持つ中空のアーム 6 2が接続されている。 な お、 図中、 6 4は、 粉粒体分配装置 5 0の設置台を示す。  The outer peripheral wall 5 1d of the casing 51 has four outlets 6 1 for the powder and granules corresponding to the four equally distributed groups, respectively. A hollow arm 62 having a predetermined inclination angle is connected to transfer the evenly distributed powder to the powder / particle supply port of the shift main body 65 through the hollow member 63. In the drawing, reference numeral 64 denotes a table on which the powdery and granular material distribution device 50 is installed.
粉粒体分配装置 5 0は、 以上のように構成されているので、 粉状体が供給 筒 5 7より貯留室 5 4内に導入される際、 粉状体は、 先ず衝撃緩衝網 5 5に衝突 し、 網目を擦り抜けた後、 衝撃緩衝板 5 6に衝突し、 大径孔 5 6 a、 長孔 5 6 b および小径孔 5 6 cを通過して貯留室 5 4内に導入される。  Since the powder material distribution device 50 is configured as described above, when the powder material is introduced into the storage chamber 54 from the supply cylinder 57, the powder material is first subjected to the shock absorbing net 55 After passing through the mesh, it collides with the shock absorbing plate 56, passes through the large-diameter hole 56a, the long hole 56b, and the small-diameter hole 56c, and is introduced into the storage chamber 54. You.
即ち、 粉粒体が大質量速度で貯留室 5 4内に導入される場合であっても、 粉粒 体は、 衝撃緩衝網 5 5および衝撃緩衝板 5 6に衝突することで、 その質量速度が 抑制され、 しかも粉粒体は網目および孔 5 6 a〜5 6 cを通過するとき、 細かく 分散されるので、 貯留室 5 4内の粉状体に塊が生じることなく、 その流動性が促 進され、 均等分配が効果的かつ高精度に行われるようになる。 なお、 このような 効果は、 上述したように、 衝撃緩衝部材として、 衝撃緩衝網 5 5および衝撃緩衝 板 5 6のどちらか一方のみを用いた場合でも期待できる。 In other words, even when the granular material is introduced into the storage chamber 54 at a large mass velocity, the granular material collides with the impact buffer net 55 and the impact And the powder is finely dispersed when passing through the meshes and pores 56a to 56c, so that the powder in the storage chamber 54 does not form lumps and its fluidity is reduced. It will be promoted and effective distribution will be performed effectively and with high precision. In addition, such The effect can be expected even when only one of the shock absorbing network 55 and the shock absorbing plate 56 is used as the shock absorbing member as described above.
例えば、 粉粒体分配装置 5 0を使用して粉粒体を 4つのグループに分配した結 果を、 図 7に示す。  For example, FIG. 7 shows the result of distributing powders and granules into four groups using the powder and granules distributor 50.
図 7においては、 粉粒体の供給速度を横軸、 4つのグループへの分配率を縦軸 にとつている。 また、 〇は、 衝撃緩衝板 5 6のみを設けた場合、 △は、 衝撃緩衝 網 5 5のみを設けた場合、 口は、 衝撃緩衝部材がない塲合を示す。 図 7から明ら かなように、 衝撃緩衝部材を設けた場合の方が衝撃緩衝部材がない場合より均等 分配率の 2 5 %のラインに対してのばらつきが小さく、 均等分配率が向上してい ることが分かる。  In Fig. 7, the abscissa represents the supply speed of the granular material, and the ordinate represents the distribution ratio to the four groups. In addition, 〇 indicates that only the shock-absorbing plate 56 is provided, and Δ indicates that only the shock-absorbing network 55 is provided. As is evident from Fig. 7, when the shock absorbing member is provided, the dispersion for the 25% line of the uniform distribution ratio is smaller than when the shock absorbing member is not provided, and the uniform distribution ratio is improved. You can see that
以上、 本発明の粉粒体分配装置およびシフタ一について詳細に説明したが、 本 発明は前記実施例に限定されず、 本発明の主旨を逸脱しない範囲において、 種々 の改良や変更をしてもよいことは勿論である。 ' 産業上の利用可能性  As mentioned above, although the granular material distribution apparatus and the shifter of the present invention have been described in detail, the present invention is not limited to the above-described embodiment, and various improvements and changes may be made without departing from the gist of the present invention. Of course it is good. '' Industrial applicability
以上詳細に説明した様に、 本発明によれば、 供給筒の下端部を分配筒の上端部 以下としているため、 好ましくは、 さらに分配筒の上端部に複数の波形の切り欠 きを均等に設けているため、 あるいはさらに、 供給筒と、 分配筒および分配台で 構成される貯留室との間 (供給筒の下端部) に衝撃緩衝部材を設けているため、 大質量速度で供給される粉粒体の質量速度が大幅に変動した場合であっても、 粉 粒体を高精度に等分配することができる。  As described in detail above, according to the present invention, the lower end of the supply tube is set to be equal to or lower than the upper end of the distribution tube. Or at a high mass velocity because an impact buffering member is provided between the supply cylinder and the storage chamber composed of the distribution cylinder and the distribution table (at the lower end of the supply cylinder). Even when the mass velocity of the powder is largely fluctuated, the powder can be equally distributed with high precision.
また、 本発明の粉粒体分配装置はその構造が簡単であり、 特に、 これを シフ夕一本体の上面部に設置して使用する本発明のシフタ一の場合には、 粉粒体 分配装置の振動発生手段とシフ夕一本体の振動発生手段を共用することができる ため、 コストも安価であるという利点がある。 Further, the structure of the granular material distribution device of the present invention is simple. In the case of the shifter of the present invention which is used by being installed on the upper surface of the shifter main body, the vibration generating means of the powder and particle distributing apparatus and the vibration generating means of the shifter main body can be used in common. Is also inexpensive.

Claims

請求の範囲 The scope of the claims
1 . 円盤状または円錐状の分配台と、 1. A disk-shaped or conical distribution table,
この分配台の上部に同軸状に配置され、 前記分配台とともに粉粒体の貯留室を 形成する分配筒と、  A distributing cylinder disposed coaxially on an upper part of the distributing table, and forming a storage chamber for the granular material together with the distributing table;
その外径が前記分配筒の内径よりも小さく設定され、 その下端部が前記分配筒 内に位置するように前記分配筒と同軸状に配置され、 前記粉粒体を前記貯留室内 に'導入する供給筒と、  The outer diameter is set smaller than the inner diameter of the distribution tube, and the lower end portion is disposed coaxially with the distribution tube so that the lower end portion is located in the distribution tube, and the powder is introduced into the storage chamber. A supply cylinder,
前記貯留室から前記分配筒を通り抜けた前記粉粒体を前記分配台より外部へ個 別に排出する複数の排出口が形成され、 前記分配^および前記分配筒の外周を覆 う外周壁とを備えることを特徴とする粉粒体分配装置。  A plurality of outlets are formed to individually discharge the granules passing through the distribution cylinder from the storage chamber to the outside from the distribution table, and include a distribution wall and an outer peripheral wall covering an outer periphery of the distribution cylinder. A granular material distribution apparatus characterized by the above-mentioned.
2 . 前記分配筒の上端部に、 周方向において複数の切り欠きが形成されたこと を特徴とする請求項 1に記載の粉粒体分配装置。 2. The granular material distribution device according to claim 1, wherein a plurality of notches are formed in an upper end portion of the distribution cylinder in a circumferential direction.
3 . 複数の切り欠きの各々が、 上方にいくに従って幅広に形成されたことを特 徴とする請求項 2に記載の粉粒体分配装置。 3. The granular material distribution device according to claim 2, wherein each of the plurality of cutouts is formed wider as going upward.
4. 前記供給筒の下端部は、 前記分配筒の上端部と前記複数の切り欠きの下端 部との間の位置に配置されるものであることを特徴とする請求項 2または 3に記 載の粉粒体分配装置。 4. The lower end of the supply cylinder is disposed at a position between an upper end of the distribution cylinder and a lower end of the plurality of cutouts. Powder and granular material distribution device.
5 . 請求項 1〜4のいずれかに記載の粉粒体分配装置であって、 5. The powder and grain distribution device according to any one of claims 1 to 4,
さらに、 前記外周壁の上端部に設けられる、 中心に円形開口部を持つ円板状の 天井部を有し、  Further, a disk-shaped ceiling portion having a circular opening at the center is provided at an upper end portion of the outer peripheral wall,
前記供給筒は、 前記外周壁の天井部に前記円形開口部を貫通するように取り付 けられたことを特徴とする粉粒体分配装置。  The powder supply device is characterized in that the supply cylinder is attached to a ceiling of the outer peripheral wall so as to penetrate the circular opening.
6 . 請求項 1〜 5のいずれかに記載の粉粒体分配装置であって、 6. The granular material distribution apparatus according to any one of claims 1 to 5,
さらに、 前記供給筒の下端部を前記分配筒内に位置させ、 しかも、 前記供給筒 の下端部の高さを調整する高さ調整手段を備えることを特徴とする粉粒体分配装  Further, a height adjustment means for positioning the lower end of the supply cylinder in the distribution cylinder and adjusting the height of the lower end of the supply cylinder is provided.
7 . 請求項 1〜 6のいずれかに記載の粉粒体分配装置であつて、 7. The granular material distribution device according to any one of claims 1 to 6, wherein
さらに、 前記供給筒の下端部に取り付けられた複数の貫通孔を有する衝撃緩衝 部材を備えることを特徴とする粉粒体分配装置。  Further, the powder and particle distribution device is provided with an impact buffering member having a plurality of through holes attached to a lower end of the supply cylinder.
8 . 前記衝撃緩衝部材は、 前記供給筒の下端部を覆うように取り付けられたこ とを特徴とする請求項 7に記載の粉粒体分配装置。 8. The powder and granular material distribution device according to claim 7, wherein the shock absorbing member is attached so as to cover a lower end portion of the supply cylinder.
9 . 前記衝撃緩衝部材は、 網目状に形成された衝撃緩衝網を含むことを特徴と する請求項 7または 8に記載の粉粒体分配装置。 9. The apparatus according to claim 7, wherein the shock absorbing member includes a shock absorbing net formed in a mesh shape.
1 0 . 前記衝撃緩衝部材は、 前記複数の貫通孔として、 中心開口部、 複数の円 状貫通孔およびその中心から放射方向に傾斜する複数の傾斜貫通長孔を有する衝 撃緩衝板を含むことを特徴とする請求項 7または 8に記載の粉粒体分配装置。 10. The shock absorbing member includes a central opening, a plurality of circles as the plurality of through holes. 9. The granular material distribution device according to claim 7, further comprising: an impact buffer plate having a through-hole and a plurality of inclined through-holes inclined radially from the center thereof.
1 1 . 前記衝撃緩衝部材は、 網目状に形成された衝撃緩衝網と、 前記複数の貫 通孔として、 中心開口部、 複数の円状貫通孔およびその中心から放射方向に傾斜 する複数の傾斜貫通長孔を有する衝撃緩衝板とを含み、 11. The shock-absorbing member includes a mesh-shaped shock-absorbing net, a plurality of through-holes, a central opening, a plurality of circular through-holes, and a plurality of slopes inclined radially from the center thereof. A shock absorbing plate having a through-hole,
前記衝撃緩衝板は、 前記衝撃緩衝網より下方に配置されることを特徴とする請 求項 7または 8に記載の粉粒体分配装置。  9. The apparatus according to claim 7, wherein the shock absorbing plate is disposed below the shock absorbing net.
1 2 . 前記衝撃緩衝板は、 前記分配筒内に位置することを特徴とする請求 項 1 1に記載の粉粒体分配装置。 12. The granular material distribution device according to claim 11, wherein the shock absorbing plate is located in the distribution cylinder.
1 3 . 前記分配筒の上端部に、 周方向において複数の切り欠きが形成されてい る時、 前記衝撃緩衝板は、 前記分配筒の上端部と前記複数の切り欠きの下端部と の間の位置に配置されるものであることを特徴とする請求項 1 1または 1 2に記 載の粉粒体分配装置。 13. When a plurality of notches are formed in the upper end of the distribution tube in the circumferential direction, the shock absorbing plate is provided between the upper end of the distribution tube and the lower end of the plurality of notches. 13. The granular material distribution device according to claim 11, wherein the granular material distribution device is arranged at a position.
1 4. 請求項 1〜 1 3のいずれかに記載の粉粒体分配装置であって、 さらに、 前記分配筒の下端部と前記分配台との間に、 前記分配筒の下端部全周 に亘つて設けられたスリットを備えることを特徴とする粉粒体分配装置。 1 4. The powder and granular material distribution device according to any one of claims 1 to 13, further comprising: between the lower end of the distribution tube and the distribution table, around the lower end of the distribution tube. A granular material distribution device comprising a slit provided over the entire surface.
1 5 . 前記分配筒の下端部と前記分配台との間の前記スリツトの寸法は、 4〜3 0 mmであることを特徵とする請求項 1 4に記載の粉粒体分配装置。 15. The dimension of the slit between the lower end of the distribution cylinder and the distribution table is: 15. The powder and granular material distribution device according to claim 14, wherein the particle size is 4 to 30 mm.
1 6 . 請求項 1〜 1 5のいずれかに記載の粉粒体分配装置であって、 さらに、 当該粉粒体分配装置を振動させる振動発生手段を備えることを特徴と する粉粒体分配装置。 16. The granular material distribution device according to any one of claims 1 to 15, further comprising vibration generating means for causing the granular material distribution device to vibrate. .
1 7 . 複数のグループに分配された粉粒体を同時に篩分けするシフタ一本 体と、 17. A single shifter that sifts through powders distributed in multiple groups simultaneously;
このシフタ一本体を振動させる振動発生手段と、  Vibration generating means for vibrating the shifter body,
前記シフタ一本体の上面部に設置され、 前記振動発生手段によって前記 シフ夕一本体が振動されると同時に振動され、 前記粉粒体を前記複数のグループ に分配して前記シフター本体に供給する請求項 1〜 1 6のいずれかに記載の粉粒 体分配装置とを具備したことを特徴とするシフタ一。  The shifter main body is installed on an upper surface portion of the shifter main body, and is vibrated at the same time as the shift main body is vibrated by the vibration generating means, and the powder and granules are distributed to the plurality of groups and supplied to the shifter main body. Item 1. A shifter comprising the powder / particle distribution device according to any one of Items 1 to 16.
PCT/JP2002/010339 2001-10-03 2002-10-03 Powder particle distribution device and shifter WO2003031294A1 (en)

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KR102491618B1 (en) * 2018-09-21 2023-01-20 주식회사 엘지화학 Particle distributor
KR102491617B1 (en) * 2018-09-21 2023-01-20 주식회사 엘지화학 Particle distributor
KR102487734B1 (en) * 2018-09-21 2023-01-12 주식회사 엘지화학 Particle distributor
KR102491149B1 (en) * 2018-09-21 2023-01-19 주식회사 엘지화학 Particle distributor

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