JP5124378B2 - Powder material supply apparatus, powder material supply system including the same, and powder material supply method using the supply apparatus - Google Patents

Description

  TECHNICAL FIELD The present invention relates to a granular material supply device, a granular material supply system including the same, and a granular material supply method using the supply device, and more specifically, includes a cyclone type collector. The present invention relates to a granular material supply apparatus, a granular material supply system including the same, and a granular material supply method using the supply apparatus.

Conventionally, there is a known powder material supply device that collects air-carrying granular material with a cyclone-type collector, discharges it from the discharge port at the lower end, and supplies it for the next processing step. It has been.
According to the supply device that collects the granular material that is air-transported by such a cyclone type collector, the air and the granular material are separated and collected by an air filter such as a bag filter. Since clogging of the filter and the like are reduced as compared with the above, the pressure loss of the transport air is small, and the particulate material can be collected stably.
By the way, the particle material as described above may not have a uniform particle size, and may contain fine powder or the like. In such a case, in the cyclone-type collector, the granular material larger than a predetermined particle size or specific gravity (hereinafter abbreviated as particle size) is separated from air by the cyclone action in the collector. Along the inner peripheral wall of the collector, it falls (falls) downward while swirling and is collected, but it is collected, but it is a granular material or fine powder (hereinafter referred to as fine powder, etc.) smaller than the predetermined particle size etc. Has a problem that it is discharged from the collector together with the air without being separated from the air.

In order to solve the above problems, a cyclone type collector is connected in series to form a multi-stage configuration, and a relatively large granular material such as a particle size is collected by the upstream collector. However, it is conceivable to collect the particulate material, fine powder, and the like that have not been collected on the front side by the rear side collector.
For example, Patent Document 1 below proposes a powder supply apparatus in which a plurality of cyclones are provided in series in a multistage manner.
This powder supply apparatus is configured to suck and collect the powder accumulated at the bottom of the processing chamber through a plurality of cyclones by a wind exhausting action by a wind exhauster and feed it to the reserve chamber. The plurality of cyclones are attached to the upper portion of the reserve chamber so that the lower portion is accommodated in the box-shaped reserve chamber. According to the above-described powder supply apparatus, since the exhaust air mixed with the powder to be collected is simultaneously passed through a plurality of cyclones, the powder is sequentially collected at each step portion, and the powder collection efficiency is increased. It is explained that it can.
JP-A-6-114737 (see FIG. 1)

However, in the powder supply apparatus described in the above-mentioned Patent Document 1, although the powder collection efficiency is improved, as described above, the reserve chamber has a structure in which lower portions of a plurality of cyclones are accommodated. There is a problem that the reserve chamber needs to be enlarged and the entire apparatus becomes large.
Moreover, in the powder material supply apparatus as described above, for example, two kinds of materials such as a virgin material and a pulverized material, and a main material and a secondary material are collected and mixed for the next processing step. However, in the powder supply apparatus described in Patent Document 1, one kind of powder accumulated at the bottom of the processing chamber is fed into the reserve chamber. Therefore, further improvement was desired.

  The present invention has been made in view of the above circumstances, and the purpose thereof is a cyclone type capable of efficiently collecting and mixing two kinds of granular materials that are pneumatically transported without increasing the size of the apparatus. It is providing the granular material material supply apparatus provided with this collector, the granular material material supply system provided with the same, and the granular material material supply method using this supply apparatus.

  In order to achieve the above-mentioned object, the granular material supply device according to the present invention comprises a plurality of cyclone-type collectors connected in series and introduced from the first-stage collector. , Two-stage cyclone collecting means for classifying and collecting, two material inlets provided in the first-stage collector, respectively connected to two material air transport paths, and the upper end Connected to the discharge port of the first-stage collector, provided a material discharge port at the lower end, and provided a branch connection part in the middle, and each of the collectors of the second and subsequent stages in the branch connection part A material storage and merging pipe connected to a branch pipe communicated with the discharge port, and a material material provided in the material storage and merging pipe, introducing pressurized air into the material storage and merging pipe, and in the material storage and merging pipe A compressed air inlet for mixing the powder material and the granular material stored in the material storage merging pipe Is discharged from the material discharge port, the reservoir level, characterized in that it comprises a sensor means for detecting that was above the predetermined level than the pressurized air inlet.

Here, the above-mentioned granular material refers to a powder / granular material, but is not limited to this, and includes a fine flake shape, a short fiber piece shape, a sliver-like material, and the like.
Moreover, although the said material mainly points out resin pellets, such as a synthetic resin material, a resin fiber piece, etc., it is not restricted to this, A metal material, a woody material, a chemical material, a food material, etc. may be sufficient.

In the granular material supply apparatus of the present invention, the sensor means may be a level meter provided at a position above the pressurized air inlet.
In the granular material supply apparatus of the present invention, the pressurized air inlet may be provided at a position higher than the branch connection portion.

Moreover, in this invention, in order to achieve the said objective, the granular material material supply system provided with one of the said granular material material supply apparatuses is provided.
That is, the particulate material supply system of the present invention includes any one of the particulate material supply devices, a supply source of the particulate material, and a pulverizer that pulverizes the molding by-product from the molding machine, A material air transport path for transporting the granular material from the supply source is connected to one material inlet of the first stage collector, and the other material inlet is connected to the material from the pulverizer. When the sensor means detects the predetermined level, a predetermined amount of one of the powder material and the pulverized material is replenished. A step of introducing pressurized air from the pressurized air introduction port to mix the material in the material storage and merging pipe; and after the step, when the sensor means detects the predetermined level, Replenish the other of the material and the pulverized material with a predetermined amount. Characterized in that it comprises a control means for controlling so as to repeat the steps of mixing the material of the material reservoir confluence pipe by introducing compressed air from said compressed air inlet.

Furthermore, in order to achieve the object, the present invention provides a powder material supply method performed using any of the powder material supply apparatuses.
That is, in the powder material supply method of the present invention, when the sensor means detects the predetermined level, a predetermined amount of one of the materials that are pneumatically transported through the two systems of material air transport paths is replenished. A step of introducing pressurized air from the pressurized air introduction port to mix the material in the material storage and merging pipe; and after the step, when the sensor means detects the predetermined level, the two systems Supplying a predetermined amount of the other of the materials that are pneumatically transported through the material air transportation path, and introducing the pressurized air from the pressurized air introduction port to mix the materials in the material storage junction pipe And repeating the above.

  Here, the pneumatic transportation of the particulate material may be suction transportation in which the particulate material is sucked and transported by suction means or the like, or compressed air is introduced by compressed air introduction means or the like. It is good also as a pressure feed which conveys a body material, and what kind of thing may be used as long as a granular material can be pneumatically conveyed.

  The granular material supply device according to the present invention is configured to classify and collect the granular material introduced from the first-stage collector by connecting a plurality of cyclone-type collectors in series. Multistage cyclone collecting means is provided. Therefore, among the granular material introduced by air transportation to the first stage collector, the material having a relatively large particle size is collected by the first stage collector, Fine powder or the like that has not been collected by the first-stage collector is collected by the latter-stage collector. Thereby, the granular material conveyed by air can be collected efficiently. That is, since it is equipped with a multistage cyclone collection means, it can be classified and collected in each collector, for example, when a dust collection means such as a filter is provided at the downstream exhaust port, suction pipe, etc. Compared with a one-stage collector, the clogging or the like is reduced, or a configuration without a filter or the like is possible. Therefore, the pressure loss of the transport air is small, and the particulate material can be collected stably.

Moreover, since the said powder material supply apparatus is provided with the two material introduction ports respectively connected by the said 2nd material air conveyance path to the said 1st stage collector, two types of materials can be used. The material can be collected by the multistage cyclone collecting means via the material air transportation path.
Further, the powder material supply device has an upper end connected to the discharge port of the first stage collector, a material discharge port provided at the lower end, and a branch connection part provided in the middle, The connection part is provided with a material storage junction pipe connected to a branch pipe communicated with the discharge port of each collector in the second and subsequent stages. Therefore, the particulate material collected in each collector of the above-described collection means having a multi-stage configuration is directly charged into the material storage and merge pipe, and the material storage and merge by a branch pipe connected to the material storage and merge pipe The material is joined to a pipe and stored in the material storage joint pipe. Thereby, the granular material collected in each collector can be supplied toward the next processing step without increasing the size of the apparatus.

Furthermore, the particulate material supply device introduces pressurized air into the material storage merging tube, and has a pressurized air inlet for mixing the granular material in the material storage merging tube. The particulate material provided in the junction pipe and stored in the material storage junction pipe is discharged from the material discharge port, and the storage level is set to a predetermined level above the pressurized air introduction port. The sensor means for detecting that it has become is provided.
Accordingly, the replenishment of the particulate material by pneumatic transportation to the first stage collector can be controlled based on the detection signal of the sensor means. Thereby, as described above, the storage level of the material stored in the main material storage junction pipe connected to the discharge port of the first-stage collector is set to a predetermined level above the pressurized air introduction port. When this happens, the first stage collector can be replenished. In this way, after the replenishment of a predetermined amount from the vicinity of the predetermined level, the pressurized air in the material storage merging pipe is supplied before the replenishment is performed by introducing the pressurized air from the pressurized air introduction port. The material stored from the level of the air inlet to the vicinity of the predetermined level can be mixed with the newly replenished material.

  Thus, for example, by replenishing a predetermined amount of one of the two types of materials that are pneumatically transported via the above-mentioned two systems of material pneumatic transport paths and introducing pressurized air, the supplemented materials And mixing with the material stored up to a predetermined level before the replenishment is made possible. After that, when the storage level is lowered and the predetermined level is detected, the other material is replenished by a predetermined amount, and pressurized air is introduced to supply the replenished material and the replenishment. Mixing with materials previously stored to near the predetermined level is possible. In this way, when a predetermined level is detected, one material is replenished and mixed. When a predetermined level is detected, the other material is replenished, mixed and repeated. it can.

  In the granular material supply apparatus according to the present invention, if the sensor means is a level meter provided at a position higher than the pressurized air inlet, the granular material is stored in the material storage / merging pipe. The structure of the sensor means for detecting that the level has reached a predetermined level above the pressurized air inlet can be made simpler than that of, for example, another weight sensor.

  In the granular material supply apparatus according to the present invention, if the pressurized air inlet is provided at a position higher than the branch connection portion, the compressed air introduction port is stored in the branch pipe, and the material storage and merging from the branch connection portion. It can be reduced that fine powder or the like that has flowed into the pipe is blown up by pressurized air introduced from a pressurized air inlet for mixing and then transferred again to a subsequent collector. As a result, the two materials can be mixed as described above without hindering the flow and merging from the branch pipe of fine powder or the like collected in the subsequent collector to the material storage merging pipe.

  Further, the powder material supply system according to the present invention including any one of the powder material supply devices described above includes a supply source of the powder material and a pulverizer for pulverizing a molding by-product from the molding machine. A material air transport path for transporting the granular material from the supply source is connected to one material inlet of the first stage collector, and the other material inlet is connected to the material inlet A pulverized material air transport path for transporting the pulverized material from the pulverizer is connected. Therefore, almost the entire amount of the granular material that is pneumatically transported from the supply source is used for molding a molded product. That is, the granular material from the supply source is supplied to a molding machine, and is molded in the molding machine to become a molded product. Also, a molding by-product other than the molded product separated from the molded product (for example, a resin molded product). If this is the case, the sprue, runner, etc.) are pulverized in a pulverizer, pneumatically transported as a pulverized material toward the multistage cyclone collecting means, and supplied again to the molding machine. In addition, fine powder contained in the powder material and pulverized material and not collected by the first-stage collector is also collected by the latter-stage collector, and as described above, the branch pipe To the material storage junction pipe and supplied to the molding machine. Thereby, not only the pulverized material but also the fine particle material and the fine powder contained in the pulverized material can be used for molding a molded product, and resource saving can be achieved.

When the sensor means detects the predetermined level, the granular material supply system replenishes a predetermined amount of one of the granular material and the pulverized material, and the pressurized air inlet A step of introducing more pressurized air to mix the materials in the material storage and merge pipe, and after the step, when the sensor means detects the predetermined level, the powder material, the pulverized material, And a control means for controlling to repeat a step of replenishing the other by a predetermined amount and introducing the pressurized air from the pressurized air introduction port to mix the material in the material storing and joining pipe.
Thereby, by collecting the granular material from the supply source collected by the multistage cyclone collecting means and stored in the material storage merging pipe, and the pulverized material from the pulverizer, by introducing pressurized air, Can be mixed as described above.

  Further, the powder material supply method according to the present invention performed using any one of the powder material supply devices described above is configured such that when the sensor means detects the predetermined level, the two material air transportation paths are used. Replenishing a predetermined amount of one of the materials to be pneumatically transported, introducing the pressurized air from the pressurized air introduction port and mixing the material in the material storage and merging pipe, and after the step, When the sensor means detects the predetermined level, the other of the materials that are pneumatically transported through the two systems of material air transport paths is replenished by a predetermined amount, and pressurized air is supplied from the pressurized air inlet. And the step of mixing the material in the material storage junction pipe is repeated. Therefore, two types of materials can be mixed as in the above-described supply system.

The best mode for carrying out the present invention will be described below with reference to the drawings.
1 (a) and 1 (b) both schematically show an example of a granular material supply apparatus according to the present embodiment, (a) is a partially broken schematic front view, and (b) is a schematic view. FIG. 2A and FIG. 2B are explanatory views for explaining the collection mode of the material that is pneumatically transported to the supply device, and are respectively XX lines in FIG. FIG.
FIG. 3 is a schematic system diagram schematically showing an example of a granular material supply system provided with the supply device, FIG. 4 is a block diagram of the main part of the system, and FIG. 5 is an example of operation in the system. FIGS. 6 (a) to 6 (d) and FIGS. 7 (a) to 7 (d) are part of the operation time charts for explaining an example of material transport and mixing control in the system. It is a fracture | rupture schematic longitudinal cross-sectional view.

In addition, in this embodiment, although the synthetic resin pellet is collected as a granular material, the granular material material supply apparatus for synthetic resin pellets for supplying it for the next processing process is illustrated, It can also be applied to other materials.
Moreover, in this embodiment, although the supply destination of the granular material material supply apparatus has illustrated the granular material material supply system which used the resin molding machine for shaping | molding of a resin molded product, it is not a resin molding machine and other A processing machine or the like for the material may be a supply destination.

As shown in FIG. 1 (a), the granular material supply apparatus 1 according to the present embodiment generally includes a multistage cyclone collecting means 10 that collects air-transported granular material, A material storage merging pipe 11 and a control panel 9 are provided for storing the granular material collected by the multistage cyclone collecting means 10 and supplying it for the next processing step.
The control panel 9 is connected to each part of a granular material supply system A (see FIG. 3) to be described later by a signal line, and functions as a control part for controlling each part.

In the present embodiment, the multistage cyclone collecting means 10 includes two cyclone collectors connected in series, and the first collector 20 on the front stage side (first stage) and the rear stage side. (Final stage) second collector 30.
The first collector 20 is provided with two materials that are connected to a hollow cylindrical cyclone main body 21 and a material air transport pipe or the like that is connected to the upper end of the side wall and pneumatically transports the granular material. The pipes 22 and 23 and the exhaust pipe 25 provided in the upper end part are provided.
The cyclone main body 21 includes a hollow cylindrical portion 21a, an inverted conical conical portion 21b coupled to the lower end of the hollow cylindrical portion 21a, and a short tube portion 21c coupled to the lower end of the conical portion 21b. The lower end opening of the short tube portion 21c constitutes a discharge port 24 for discharging the particulate material collected by the first collector 20.

The two material introduction pipes 22, 23 are connected to the hollow cylindrical portion 21a so that the granular material to be transported by air is introduced into the hollow cylindrical portion 21a in a tangential direction in a plan view. (See FIG. 1 (b) and FIG. 2).
In these material introduction pipes 22, 23, the upstream side part into which the particulate material is introduced has a circular cross section, and the downstream side part thereof is gradually expanded up and down toward the connection part with the hollow cylindrical part 21a, In the vicinity of the connecting portion, the cross section is rectangular. Moreover, the connection part side opening opened in the hollow cylindrical part 21a of these material introduction pipes 22 and 23 comprises material introduction ports 21d and 21e.
The exhaust pipe 25 is concentrically housed in the hollow cylindrical portion 21a, and is arranged so that the lower end opening is positioned below the material introduction ports 21d and 21e. Moreover, the upper end part of this exhaust pipe 25 is connected to the connection pipe 35 with the 2nd collector 30 mentioned later.
A punching metal or the like may be disposed in the exhaust pipe 25.

The second collector 30 is composed of a cyclone main body 31 composed of a hollow cylindrical portion 31a, a conical portion 31b, and a short pipe portion 31c having a discharge port 32 at the lower end, and the same as the above-described inside. An exhaust pipe 33 and a cartridge type dust collecting filter 34 detachably disposed at the upper end of the cyclone main body 31 are provided.
The inner diameter (cyclone diameter) of the hollow cylindrical portion 31 a of the second collector 30 is formed to be substantially the same or smaller than the inner diameter of the hollow cylindrical portion 21 a of the first collector 20.
Further, the second collector 30 and the first collector 20 are connected by a connecting pipe 35. That is, the first collector 20 and the second collector 30 are connected in series by the connecting pipe 35. The connecting pipe 35 is connected to the exhaust pipe 25 of the first collector 20, and the granular material that is erected upward from the connecting portion and pneumatically transported is the same as that of the second collector 30. The hollow cylindrical portion 31a is bent and connected to the hollow cylindrical portion 31a so as to be introduced in a tangential direction in plan view. A connecting portion side opening that opens into the hollow cylindrical portion 31a of the connecting pipe 35 is a material introduction port 31d (see FIG. 2).

In addition, the internal diameter and shape of each cyclone main-body parts 21 and 31 of the said 1st collector 20 and the 2nd collector 30 are the average particle diameter etc. of the granular material introduced by air transportation, fluidity | liquidity, etc. Depending on the above, it can be appropriately designed so that it can be classified and collected.
In the present embodiment, the multistage cyclone collecting means 10 that collects the powder material to be pumped is illustrated, but it may be configured to collect the powder material to be sucked and transported. In this case, for example, an air suction pipe connected to suction means such as a suction blower or a suction pump may be connected to the exhaust pipe 33 of the second collector 30.

The material storage merging pipe 11 includes a short pipe part 12 connected to the discharge port 24 of the first collector 20, a material detection part 13 connected to the lower end of the short pipe part 12, and the material detection part. 13 is provided with a storage merging portion 14 provided continuously with the lower end of 13. The short pipe part 12, the material detection part 13, and the storage merging part 14 are each arranged concentrically with the hollow cylindrical part 21a of the first collector 20, and the granular material in which the lower end opening is stored. The material discharge port 15 is configured to supply for the next processing step.
The material detection unit 13 includes an upper transparent glass tube portion and a lower base portion. The transparent glass tube portion detects the storage level of the granular material stored in the material storage junction tube 11. An electrostatic capacity type level meter (proximity sensor) 19 is attached.
In the level meter 19, the granular material stored in the material storage merging pipe 11 is sequentially discharged from the material discharge port 15, and the storage level is higher than that of the pressurized air introduction port 14c described later. Sensor means for detecting that the predetermined level (replenishment start level) LLV is reached.

The level meter 19 may be provided at an appropriate position above the pressurized air inlet 14c according to the predetermined level LLV.
Here, the predetermined level LLV is the level of the material supplied to the full level FLV or a predetermined amount after the storage level is lower than the predetermined level LLV, and the level of the pressurized air inlet 14c before the replenishment is performed. It is good also as a level which can be mixed with the pressurized air introduced from the pressurized air inlet 14c with the material stored upwards.
The predetermined level LLV is appropriately determined according to the time lag of the transportation of the granular material made based on the detection signal of the level meter 19, the discharge mode and the discharge amount of the granular material from the material discharge port 15. You may make it set.

The setting of the predetermined level LLV as described above is performed when the material transport control is performed so that two kinds of materials are alternately and repeatedly supplied in the supply system A described later, and the desired homogeneity (material storage) of the mixed materials is set. You may make it set suitably according to the transport frequency desired for the ratio of the ratio of each material contained in the mixed material discharged | emitted from the discharge port 15 of the confluence | merging pipe | tube 11, and a desired transportation frequency. For example, when it is desired to increase the homogeneity of the mixed material, the storage amount (residual amount) of the material stored above the level of the pressurized air inlet 14c before replenishment is increased. Further, the predetermined level LLV may be set so that the replenishment amount of the material to be replenished to the full level FLV after the storage level falls below the predetermined level LLV is reduced. Alternatively, when it is desired to reduce the transportation frequency, the predetermined level LLV may be set so that the remaining amount decreases and the replenishment amount increases.
For example, the amount of material stored from the level of the pressurized air inlet 14c to the detection level of the level meter 19 so that the remaining amount and the replenishment amount are substantially equal to the predetermined level LLV, and the level You may make it provide the said level meter 19 in the position where the storage amount of the material stored from the detection level of the total 19 to the full level FLV becomes substantially the same amount. As a result, the two types of mixed materials can be made relatively homogeneous while the transportation frequency is relatively low.
In FIG. 1, only the single full level FLV is shown in correspondence with the full level FLV corresponding to the case where the replenishment amounts of the two types of materials are substantially the same. If the replenishment amount is different from the replenishment amount of the other material, two different full levels FLV exist.

The storage junction 14 is provided with a branch connection portion 14a to which a branch pipe 16 is connected. The branch pipe 16 is provided to extend obliquely upward from the branch connection portion 14a.
Further, a ball vibrator (air vibrator) 18 is attached to the vicinity of the branch connection portion 14 a of the storage junction 14 (in the illustrated example, the opposite outer surface).
The ball vibrator 18 has a built-in steel ball, and constitutes a vibration generating source that generates vibration by rotating the steel ball at high speed by compressed air introduced into the vibrator main body via the tube connector 18a. To do. Further, the air introduced into the main body is exhausted to the outside from the muffler 18b.
By providing the ball vibrator 18 constituting such a vibration generating source in the vicinity of the branch connection portion 14a, fine powder or the like stored in the branch pipe 16 described later smoothly flows into the branch connection portion 14a in the branch pipe 16. In addition, the fine powder in the branch pipe 16 can be smoothly introduced and merged toward the material storage merging pipe 11.

In addition, instead of the ball vibrator 18, another vibration generation source may be applied as a vibration generation source that vibrates the storage junction 14 and the branch pipe 16. Further, the location of such a vibration generating source is not limited to the location shown in the figure, and may be arranged in the vicinity of the base end portion of the branch pipe 16 (connection end portion with the branch connection portion 14a). Good.
Further, as means for facilitating the flow of fine powder or the like from the branch pipe 16 to the material storage / merging pipe 11, instead of or in addition to the above vibration generation source, the base end portion of the branch pipe 16 is joined to the material storage / merging joint You may make it provide the injection | throwing-in guide part extended so that it might face in a pipe | tube from the inner wall of the pipe | tube 11. FIG.

Further, the storage / merging portion 14 is provided with a pressurized air introduction port 14c for introducing pressurized air into the material storage / merging tube 11 and mixing the granular material in the material storage / merging tube 11. It has been. In the present embodiment, the pressurized air inlet 14c is provided at a position above the branch connecting portion 14a.
Thus, by providing the pressurized air introduction port 14c at a position above the branch connection portion 14a, the compressed air introduction port 14c is stored in the branch pipe 16 as described later, and flows into the material storage junction pipe 11 from the branch connection portion 14a. It can be reduced that the fine powder or the like blown up by the pressurized air introduced from the pressurized air introduction port 14c for mixing and transferred to the second collector 30 at the subsequent stage again. As a result, the two materials can be mixed as described above without hindering the flow and merging of the fine powder or the like collected in the second collector 30 from the branch pipe 16 to the material storage merging pipe 11.

The pressurized air introduction port 14c is provided with a tube joint 14b attached to the side wall of the storage junction 14, and pressurized air is introduced via a pressurized air introduction pipe connected to the tube joint 14b. Is introduced into the material storage merging pipe 11 so that the material stored above the level where the pressurized air inlet 14c is located is blown up and allowed to flow, thereby mixing the materials. .
The number of pressurized air inlets 14c is not limited to one as shown in the figure, and a plurality of pressurized air inlets 14c may be provided. Moreover, it is not restricted to the aspect which blows off pressurized air substantially horizontally with respect to the material storage confluence | merging pipe 11, It is good also as an aspect which blows off pressurized air toward diagonally upward.

The branch pipe 16 allows the material storage / merging pipe 11 and the discharge port 32 of the second collector 30 to communicate with each other, and the base end thereof is connected to the branch connection part 14 a of the material storage / merging pipe 11. A cap 16a for closing the opening is detachably attached to the end of the branch pipe 16. By removing the cap 16a, for example, a purge material for purifying the inside of the resin molding machine can be introduced.
The inclination angle of the branch pipe 16 is such that the fine powder and the like collected by the second collector 30 can move toward the branch connection portion 14a at the base end, and the fluidity, repose angle, fine powder, etc. It is appropriately set according to the presence or absence of means such as a vibration generation source for facilitating movement.

Further, a branch portion 16b coupled upward is provided in the vicinity of the terminal portion of the branch pipe 16, and the second collector 30 is connected to the branch portion 16b via a flexible hose 17. The discharge port 32 is communicated.
The flexible hose 17 is detachable as shown by the two-dot chain line in the figure at the connecting portion with the branch portion 16b at the lower end. In this way, by making the flexible hose 17 detachable, if it is not desired to join the fine powder collected by the second collector 30 to the material storage merging pipe 11, it is detached from the connecting portion. For example, it can be connected to a fine powder collection box or the like. Instead of such a mode, a valve or the like for blocking the supply of fine powder or the like to the material storage junction pipe 11 may be provided on the branch pipe 16 or the like.

Next, the collection mode of the granular material in the granular material supply apparatus 1 having the above-described configuration will be described with reference to FIG.
FIG. 2A shows a case where a granular material (in the example shown, a virgin material (main material) vp) introduced through one of the two material introduction pipes 22 and 23 is multi-staged. The aspect which collects by the type | formula cyclone collection means 10 is shown.
The virgin material vp pneumatically transported to the material introduction pipe 22 through the material air transportation path or the like is introduced into the hollow cylindrical portion 21a of the first collector 20 from the material introduction port 21d. The virgin material vp introduced into the hollow cylindrical portion 21a is separated from transport air and fine powder by centrifugal force due to the cyclone action, swirls along the inner wall surface of the cyclone main body portion 21, and gradually descends to the first catch. It is collected in the collector 20.
The virgin material vp collected by the first collector 20 is discharged from the discharge port 24 at the lower end toward the material storage merging pipe 11 and is stored in the material storage merging pipe 11. The material is sequentially discharged from the material discharge port 15 at the lower end of the junction pipe 11 and supplied to the next processing step (see FIG. 1).

Moreover, fine powder or the like sp that has not been collected by the first collector 20 is introduced into the hollow cylindrical portion 31a of the second collector 30 through the exhaust pipe 25 and the connecting pipe 35 together with the transport air. . The fine powder sp and the like introduced into the hollow cylindrical portion 31a is swung along the inner wall surface of the cyclone main body 31 and gradually descends and is collected by the second collector 30 as described above. In addition, a part of the fine powder not collected by the second collector 30 is separated from the transport air by the dust collecting filter 34 (see FIG. 1) through the exhaust pipe 33 and captured. .
Fine powder or the like sp collected by the second collector 30 is discharged from the discharge port 32 at the lower end toward the flexible hose 17 and is stored in the branch pipe 16 via the flexible hose 17 and the branch portion 16b. (See FIG. 1). The fine powder sp and the like stored in the branch pipe 16 flows down and is stored in the material storage junction pipe 11 from the branch connection portion 14a, and is sequentially discharged from the material discharge port 15 at the lower end of the material storage junction pipe 11 as described above. Then, it is supplied for the next processing step (see FIG. 1).

FIG. 2B shows a mode in which the granular material (in the illustrated example, the pulverized material rp) introduced through the other material introduction tube 23 is collected by the multistage cyclone collecting means 10.
The pulverized material rp pneumatically transported to the material introduction pipe 23 via the material air transportation path or the like is introduced from the material introduction port 21e into the hollow cylindrical portion 21a of the first collector 20 and is centrifuged by the cyclone action as described above. It is separated from the transport air and fine powder by force and collected by the first collector 20.
The pulverized material rp collected by the first collector 20 is discharged from the lower discharge port 24 toward the material storage merging pipe 11 and stored in the material storage merging pipe 11, as described above. The materials are sequentially discharged from the material discharge port 15 at the lower end of the material storage and merging pipe 11 and supplied for the next processing step (see FIG. 1).
Incidentally, the fine powder sp and the like which are not collected by the first collector 20 and the extremely small fine powder as described above are collected by the second collector 30 as described above.

As described above, the particulate material supply apparatus 1 according to the present embodiment allows the cyclone-type first collector 20 and the second collector 30 to communicate in series and is introduced from the first collector 20. A multistage cyclone collecting means 10 is provided for classifying and collecting the collected granular material. Accordingly, as described above, the materials vp and rp having a relatively large particle size and the like are collected by the first collector 20, and the fine powder and the like sp that are not collected by the first collector 20 Are collected by the second collector 30. Thereby, the granular material conveyed by air can be collected efficiently. That is, since the multistage cyclone collecting means 10 is provided, it can be classified and collected in each of the collectors 20 and 30, and even when the dust collector 34 is provided as in this embodiment. The clogging of the dust collection filter 34 and the like are reduced as compared with the one collected by a single-stage collector. Therefore, the pressure loss of the transport air is small, and the particulate material can be collected stably.
Moreover, in the said granular material material supply apparatus 1, as mentioned above, the granular material collected in each collector 20 and 30 of the said collection means 10 made into the multistage structure is the material storage merging pipe. 11 and is joined to the material storing and joining pipe 11 by the branch pipe 16 connected thereto, and supplied to the next processing step. Thereby, the granular material collected in each collector 20 and 30 can be supplied toward the next process, without enlarging an apparatus.

  Furthermore, since the said granular material supply apparatus 1 is provided with the said level meter 19, based on the detection signal of this level meter 19, of the granular material by the pneumatic transport to the said 1st collector 20 is carried out. Control replenishment. Thereby, as above-mentioned, the storage level of the material stored in the main material storage confluence | merging pipe | tube 11 connected to the discharge port 24 of the 1st collector 20 is higher than the pressurized air introduction port 14c. When the predetermined level LLV is reached, the first collector 20 can be replenished. Further, in this way, after a predetermined amount is newly replenished from the vicinity of the predetermined level LLV, by introducing the pressurized air from the pressurized air introduction port 14c, the material storage junction pipe 11 is supplied before the replenishment is performed. The material stored from the level of the pressurized air inlet 14c to the vicinity of the predetermined level LLV can be mixed with the newly supplied material.

  In particular, as in the present embodiment, by applying the powder material supply device 1 as a supply device for supplying synthetic resin pellets for the next processing step, conventionally, on the quality of the molded product Only materials that are pneumatically transported from the viewpoint and separated from transport air and fine powder, etc. are supplied to the molding machine and used, and the separated fine powder is stored in the dust collection box of the dust collector and discarded. However, according to the present embodiment, the fine powder can be easily used for molding with a simple configuration.

In addition, in the granular material supply apparatus 1 which concerns on this embodiment, the material discharge port 15 of the material storage confluence | merging pipe | tube 11 is opened below, and the stored granular material is successively carried out by the dead weight from the opening sequentially. Although the aspect supplied toward the process of this is illustrated, it is not restricted to such an aspect. For example, a material quantitative cutout device such as a rotary valve, cutout damper, screw feeder, and vibration feeder may be further provided below the material storage junction pipe 11.
Moreover, as a storage part which stores the granular material collected by the 1st collector 20, not only the material storage merging pipe 11, but the cyclone main-body part 21 of the 1st collector 20 is also used as a storage part. You may make it grasp. Similarly, the reservoir for storing fine powder collected by the second collector 30 is not limited to the branch pipe 16, and the cyclone main body 31 and the flexible hose 17 of the second collector 30 are also included. You may make it grasp | ascertain as a storage part. Further, the storage section is not limited to the pipe-shaped material storage junction pipe 11 and the branch pipe 16 as shown in the figure, but instead of or in addition to these, a tank-shaped (hopper-shaped) one is provided. May be.

Furthermore, in the present embodiment, as the sensor means for detecting that the storage level of the granular material stored in the material storage merging pipe 11 has reached a predetermined level (replenishment start level) LLV, Although the capacity type level meter 19 is illustrated, the present invention is not limited to this. For example, it is possible to detect that the storage level of the particulate material stored in the material storage merging pipe 11 such as a weight sensor such as a load cell or other optical sensor has reached a predetermined level (replenishment start level) LLV. Any sensor means may be used.
Furthermore, in the present embodiment, a ball vibrator 18 is provided in order to more smoothly join fine powder stored in the branch pipe 16 to the material storage merging pipe 11, and air pollution due to external dispersion of fine powder is taken into consideration. And although the dust collection filter 34 is provided in the 2nd collector 30 of a back | latter stage, you may make it not provide these.

Next, the granular material material supply system A provided with the granular material material supply device 1 having the above-described configuration will be described with reference to FIGS.
As shown in FIG. 3, the granular material supply system A according to the present embodiment is roughly configured by the above granular material supply apparatus 1, the granular material supply source 2, and the molding machine 4. Virgin material air for air transporting the virgin material from the pulverizer 3 for pulverizing the pulverized material, the air units 5 and 6 as the compressed air introduction means, and the supply source 2 toward the powder material supply device A transport path 7 and a pulverized material air transport path 8 for pneumatically transporting the pulverized material from the pulverizer 3 toward the powder material supply apparatus 1 are provided.

The powder material supply source 2 includes a material tank 2a for storing virgin material such as synthetic resin pellets, a drying device 2b for drying the virgin material to a predetermined moisture content, a suction blower, a suction pump, and the like. And a suction means 2c provided.
The virgin material stored in the material tank 2a is transported to the collection hopper of the drying device 2b by suction by the suction means 2c, and is heated and dried by hot air that is put into the drying hopper and heated by a heat source such as a heater. The
The pulverizer 3 includes an inlet 3a into which a molding by-product such as a sprue and a runner taken out from a molding machine and separated from the molded product is crushed and pulverized the molding by-product into a granular form. A crushing portion 3b including a rotary blade, a fixed blade, a crushing blade, and the like.

The air unit 5 incorporates compressed air generating means such as an air compressor, and includes a booster nozzle 7a provided at the upstream end of the virgin air transport path 7, a vibrator line 5c connected to the ball vibrator 18, and Compressed air is introduced into the mixed air line 5f connected to the tube joint 14b of the pressurized air inlet 14c. The introduction of these compressed air is controlled by opening / closing virgin material transport valves 5a, vibrator valves 5b, and mixed air valves 5e such as solenoid valves provided in the respective air lines. In the figure, reference numerals 5d and 5g denote flow rate adjusting means (speed controllers) for adjusting the flow rates of the compressed air in the vibrator line 5c and the mixed air line 5f, respectively.
Similarly, the air unit 6 incorporates an air compressor or the like, and introduces compressed air into a booster nozzle 8 a provided at the upstream end of the pulverized material air transport path 8. The introduction of the compressed air is controlled by opening and closing the pulverized material transport valve 6a as described above.

The virgin material air transport path 7 has a booster nozzle 7a provided at an upstream end thereof inserted into the virgin material of the material discharge portion of the drying device 2b. The air is drawn into the booster nozzle 7a by the suction action by the negative pressure of the compressed air introduced into the pipe of the nozzle 7a, and is sent to the downstream side by pressurization of the compressed air. Further, the downstream end 7 b of the virgin material air transport path 7 is connected to one material introduction pipe 22 of the powder material supply apparatus 1.
Further, in the same manner as described above, the pulverized material air transport path 8 has a booster nozzle 8a provided at the upstream end thereof inserted into the pulverized material of the material discharge portion of the pulverizer 3, and the material discharge portion is pulverized. Similarly to the above, the material is drawn into the booster nozzle 8a and is pumped toward the downstream side. Further, the downstream end portion 8 b of the pulverized material air transport path 8 is connected to the other material introduction pipe 23.

The said granular material material supply system A is controlled by CPU90 as a control means incorporated in the control board 9 with which the granular material material supply apparatus 1 is provided, as shown in FIG.
That is, under the control of the CPU 90, the valves 5a, 5b, 5e, and 6a are opened and closed as described later according to a program stored in the storage unit 91.

Next, an example of the operation in the granular material supply system A configured as described above, and the transport and mixing control of each material will be described with reference to FIGS.
First, as shown in FIG. 5 and FIG. 6A, the storage level of the granular material (in the example shown, the virgin material vp) stored in the material storage merging pipe 11 changes from the full level FLV to the replenishment start level. Up to LLV, the virgin material transport valve 5a and the pulverized material transport valve 6a are closed, and neither material is transported. The mixed air valve 5e is also closed.
Further, the virgin material vp and fine powder sp stored in the material storage merging pipe 11 are sequentially discharged from the material discharge port 15 and supplied to the molding machine 4 and supplied to the molding machine 4. As shown in FIG. 5, the vibrator valve 5 b is always open, and the ball vibrator 18 applies vibrations to the material storage / merging pipe 11 and the branch pipe 16.
In the above state, the fine powder sp collected by the second collector 30 during the previous transportation is stored in the branch pipe 16, and this fine powder sp is promoted by the vibration action of the ball vibrator 18 and the like. However, it gradually flows down toward the material storage junction pipe 11.

Next, as shown in FIG. 6B, the virgin material vp and the fine powder sp are sequentially discharged from the material discharge port 15, and the storage level of the virgin material vp and the fine powder sp in the material storage junction pipe 11 is lowered. The supply start level LLV is reached.
When the storage level reaches the replenishment start level LLV, as shown in FIG. 5, the level meter 19 issues a material replenishment start signal (no material signal), and the pulverized material transport valve 6a is opened for a predetermined time.
When the pulverized material transport valve 6a is opened, the pulverized material rp from the pulverizer 3 is turned into a granular material until the storage level reaches the full level FLV as shown in FIG. The feed device 1 is pumped toward the multistage cyclone collecting means 10.

After the pulverized material rp is replenished until the storage level reaches the full level FLV as described above, the mixed air valve 5e is opened for a predetermined time as shown in FIG. 5 and FIG. 6 (d). Pressurized air is introduced from the pressurized air inlet 14c.
By the introduction of the pressurized air, before the replenishment is performed, the virgin material vp stored from the level of the pressurized air introduction port 14c to the vicinity of the replenishment start level LLV and the replenished pulverized material rp are mixed. The
The predetermined time for opening the mixed air valve 5e is that the mixing of the materials depends on the fluidity of each material, the inner diameter of the material storage / merging pipe 11, the storage amount of the material stored therein, and the like. It should be sufficient time. Further, the introduction of the pressurized air is performed in place of the continuous opening for a predetermined time as shown in the time chart of FIG. 5, and the pulverized material rp until the storage level reaches the full level FLV as described above. After the replenishment, the mixed air valve 5e may be opened and closed intermittently for a predetermined time to introduce the pressurized air intermittently. Alternatively, a mode in which pulsating air generating means or the like is further provided in the air unit 5 and the pressurized air is pulsated and introduced may be adopted.

Next, as shown in FIG. 7A, the storage level of the mixed virgin material vp, pulverized material rp, and fine powder sp stored in the material storage merging pipe 11 is lowered, and again reaches the replenishment start level LLV. When it reaches, as shown in FIG. 5, the level meter 19 issues a material replenishment start signal, and the virgin material transport valve 5a is opened for a predetermined time.
When the virgin material transport valve 5a is opened, the virgin material vp from the supply source 2 is a granular material until the storage level reaches the full level FLV as shown in FIG. The feed device 1 is pumped toward the multistage cyclone collecting means 10.
After the virgin material vp is replenished until the storage level reaches the full level FLV as described above, as shown in FIGS. 5 and 7C, the mixed air valve 5e is opened again for a predetermined time, Pressurized air is introduced from the pressurized air inlet 14c.
By the introduction of the pressurized air, the mixed virgin material vp and the pulverized material rp stored from the level of the pressurized air introduction port 14c to the vicinity of the replenishment start level LLV and the replenished virgin before the replenishment is performed. Mixing with the material vp is made.
Further, from the above state, when the storage level decreases as shown in FIG. 7D and reaches the replenishment start level LLV again, the virgin material vp is replenished as shown in FIGS. 5 and 6C. As above, mixing is performed by introducing pressurized air. Thereafter, the above operation is repeated.

  As described above, according to the granular material supply system A according to the present embodiment, substantially the entire amount of the virgin material vp pneumatically transported from the supply source 2 is used for molding a molded product. That is, the virgin material vp from the supply source 2 is supplied to the molding machine 4 and is molded in the molding machine 4 to form a molded product, and molding by-products other than the molded product separated from the molded product are pulverized. 3 is pulverized and pneumatically transported as a pulverized material rp toward the multistage cyclone collecting means 10 and supplied to the molding machine 4 again. In addition, the fine powder sp and the like contained in the virgin material vp and the pulverized material rp and not collected by the first collector 20 are also collected by the second collector 30 and branched as described above. The material is merged from the tube 16 to the material storage merging tube 11 and supplied to the molding machine 4. As a result, not only the pulverized material rp but also the virgin material vp and the fine powder sp included in the pulverized material rp, which have been disposed of in the past, can be used for molding molded products, thereby saving resources. it can.

  In addition, when the storage level of the particulate material supply system A decreases with supply to the molding machine 4 and the level meter 19 detects the replenishment start level LLV, the virgin material vp and the pulverized material rp One of them is replenished until it reaches the full level FLV, the pressurized air is introduced from the pressurized air introduction port 14c, and the material in the material storage merging pipe 11 is mixed. When the meter 19 detects the replenishment start level LLV, the other of the virgin material vp and the pulverized material rp is replenished until the full level FLV is reached, and the pressurized air is introduced from the pressurized air inlet 14c. And the step of mixing the materials in the storage junction pipe 11 are repeated. Thereby, the virgin material vp from the supply source 2 collected by the multistage cyclone collecting means 10 and stored in the material storage merging pipe 11 and the pulverized material rp from the pulverizer 3 are mixed as described above. it can.

In the granular material supply system A, when the level meter 19 detects the supply start level LLV, the materials vp and rp are supplied by timer control until the full level FLV is reached. For example, an upper limit sensor for detecting the full level FLV may be provided in the material storage merging pipe 11 or the first collector 20.
Moreover, in the said granular material material supply system A, although the said each material vp and rp are each illustrating the aspect which replenishes substantially the same amount each time the said level meter 19 detects the replenishment start level LLV, For example, the replenishment amount of the virgin material vp may be different from the replenishment amount of the pulverized material rp.

Furthermore, in the present embodiment, the supply source 2 included in the particulate material supply system A is exemplified by the one provided with the material tank 2a, the drying device 2b, and the suction means 2c. However, the supply source 2 is not limited thereto. For example, it may be composed only of a material tank.
Furthermore, the particulate material supply system A includes a supply source 2 and a pulverizer 3, from which a virgin material vp and a pulverized material rp are pneumatically transported toward the particulate material supply device 1. Although shown, other configurations are possible. For example, without providing the pulverizer 3, a supply system for supplying two types of powder material and supplying two types of powder material to the powder material supply device 1 by air is supplied to the supply system. The granular material supply device 1 may be applied.

Next, a modification of the particulate material supply device according to the present embodiment will be described with reference to FIG.
FIG. 8 is a view corresponding to FIG. 1A, showing a powder material supply apparatus according to a first modification.
In addition, the difference with the granular material material supply apparatus 1 of an above-described example is mainly the structure of a multistage cyclone collection means and a branch pipe, About the same structure, the same code | symbol is attached | subjected, The description will be omitted or briefly described.
Moreover, the granular material material supply apparatus 1A according to the present modification is also applicable to the granular material material supply system A described with reference to FIGS. 3 to 7 in the same manner as the granular material material supply apparatus 1 of the above example. .

The multistage cyclone collection means 10A provided in the granular material material supply apparatus 1A according to this modification has three cyclone collectors connected in series, and the first collector 20 of the first stage. And a second collector 40 located in the middle stage on the subsequent stage side, and a third collector 30A in the final stage.
The first collector 20 and the second collector 40 are communicated with each other by a connecting pipe 45 having a configuration substantially similar to that of the connecting pipe 35, and the second collector 40 and the third collector 40 are connected to each other. The collector 30 </ b> A communicates with the connecting pipe 35.

The second collector 40 is composed of a cyclone main body 41 composed of a hollow cylindrical portion 41a, a conical portion 41b, and a short pipe portion 41c having a discharge port 42 at the lower end, and the same as the above-described in the above. The exhaust pipe 43 and the connection pipe 45 connected to the upper end of the side wall of the cyclone main body 41 are provided.
The inner diameter (cyclone diameter) of the hollow cylindrical portion 41a of the second collector 40 is formed to be substantially the same or smaller than the inner diameter of the hollow cylindrical portion 21a of the first collector 20.
Further, the connecting pipe 45 is connected to the exhaust pipe 25 of the first collector 20 as described above, and the granular material that is erected upward from the connecting portion and pneumatically transported is the same as described above. The hollow cylindrical portion 41a of the collector 40 is bent and connected to the hollow cylindrical portion 41a so as to be introduced in a tangential direction in plan view. The connection portion side opening that opens into the hollow cylindrical portion 41a of the connecting tube 45 is the same material inlet as described above.

The third collector 30A has substantially the same configuration as the second collector 30 in the above-described example, and the second collector 30A is connected to the exhaust pipe 43 of the second collector 40 by the connecting pipe 35. The collector 40 is in communication.
In the present modification, the third collector 30 </ b> A has a cyclone diameter smaller than that of the first collector 20 and the second collector 40.
In this modification, the branch pipe 16A for joining the material collected by the second collector 40 and the third collector 30A to the material storage junction pipe 11 is more than the branch pipe 16 of the above example. The length of the third collector 30A is increased, and two branch portions 16b and 16b are provided.
The outlets 32 and 42 at the lower ends of the third collector 30A and the second collector 40 are respectively connected to the branch portions 16b and 16b of the branch pipe 16A by the same flexible hoses 17 and 17A. Yes.

In the granular material supply apparatus 1A according to the present modification, each material that is pneumatically transported via a material pneumatic transport pipe or the like is sent from the material introduction pipes 22 and 23 of the first collector 20 to the first collector 20. It is introduced into the inside, collected, and discharged from the discharge port 21 at the lower end toward the material storage junction pipe 11.
In addition, the material not collected in the first collector 20 is introduced into the second collector 40 through the exhaust pipe 25 and the connecting pipe 45, collected, and discharged from the lower discharge port 42. It is discharged toward the branch pipe 16A.
Further, the material that has not been collected in the second collector 40 is introduced into the third collector 30A through the exhaust pipe 43 and the connecting pipe 35, collected, and discharged from the lower discharge port 32. It is discharged toward the branch pipe 16A. Further, a part of the tiny fine powder that has not been collected by the third collector 30A is separated from the transported air by the dust collecting filter 34 through the exhaust pipe 33 and captured.

Further, the material such as fine powder stored in the branch pipe 16A as described above gradually flows down toward the material storage junction pipe 11 as described above, and joins with the mixed material as described above. Is supplied for the processing step.
As described above, according to the granular material supply device 1A according to this modification, as in the above example, the granular material collected in each of the collectors 20, 40, and 30A without increasing the size of the device. The material can be smoothly supplied for the next processing step.
In this modification, the number of stages of the collector is increased from the above example, and the collector on the rear stage (the last stage in this modification) is assumed to have a smaller cyclone diameter than the collector on the front stage. Therefore, as compared with the above-described example, the particulate material that is pneumatically transported can be collected more efficiently by the multistage cyclone collecting means 10A.
In addition, in this modification, it is set as the three-stage cyclone collection means 10A which connected three cyclone type collectors in series, However, Four or more cyclone type collectors were connected in series. It may be a thing.

Next, a modification of the granular material supply device according to the present embodiment will be described with reference to FIGS. 9 and 10.
FIG. 9 and FIG. 10 both show a granular material supply device according to a second modification, for explaining an example of material transport and mixing control in the granular material supply system provided with the supply device. It is a partially broken schematic longitudinal cross-sectional view.
In addition, the difference with the granular material supply apparatus 1 and granular material supply system A of an above-described example is mainly the structure of a material storage confluence | merging pipe and the branch pipe connected to this, The same structure Are given the same reference numerals, and explanations thereof are omitted or simplified. Also, description of similar operations will be omitted or briefly described.

As shown in FIGS. 9 and 10, the material storage and merging pipe 11 </ b> A provided in the granular material material supply apparatus 1 </ b> B according to the present modification adds a branch connection part 14 </ b> Aa that is a connection part to the branch pipe 16 </ b> B. The pressure air inlet 14 c and the level meter 19 are provided so as to be located above the level air inlet 14 c and the level meter 19.
That is, in the present modification, the level meter 19 is provided at a position below the branch connection portion 14Aa, so the supply start level LLV is at a position below the level of the branch connection portion 14Aa.

Next, an example of material transport and mixing control in the powder material supply system A including the powder material supply device 1B according to the present modification will be described.
When the storage level of the virgin material vp stored in the material storage junction pipe 11A is the full level FLV shown in FIG. 9A, the fine powder sp stored in the branch pipe 16B is vibrated by the ball vibrator 18. The material gradually flows down into the material storing and joining pipe 11A while being promoted by the action.
Here, the fine powder or the like sp collected in the second collector 30 at the subsequent stage may have a lower fluidity than the virgin material vp collected in the first collector 20. In such a case, flow of fine powder or the like from the branch pipe 16B to the material storage joint pipe 11A is hindered by the material with good fluidity stored in the material storage joint pipe 11A, and the fine powder in the branch pipe 16B In some cases, sp is retained. In addition, when the type of material (particularly, a material having poor fluidity) or a long-term stay continues, it is conceivable that fine powder or the like sp is blocked in the branch pipe 16B. According to this, such a thing can be prevented as follows.

As shown in FIG. 9B, the storage level of the virgin material vp stored in the material storage junction pipe 11A decreases, reaches a level in the vicinity of the branch connection portion 14Aa, and a new material is introduced from this state. Until the storage level reaches the replenishment start level LLV, as shown in FIG. 9 (c), the fine powder or the like sp stored in the branch pipe 16B is affected by the block or the like by the virgin material vp. Without any problem, the material smoothly flows down from the branch pipe 16B into the material storage joint pipe 11A.
That is, almost all of the fine powder sp and the like stored in the branch pipe 16B flows down into the material storage junction pipe 11A, and no new material is supplied until the storage level reaches the supply start level LLV. Therefore, the abnormal retention of sp, such as fine powder, in the branch pipe 16B as described above can be prevented.

As described above, when the storage level reaches the replenishment start level LLV, as shown in FIG. 10A, the pulverized material rp is replenished until it reaches the full level FLV by timer control, as in the above example.
Next, as in the above-described example, as shown in FIG. 10B, pressurized air is introduced from the pressurized air introduction port 14c, and the material in the material storage merging pipe 11A is mixed. At this time, as described above, the fine powder or the like sp that has almost flowed down into the material storage / merging pipe 11A is mixed with the virgin material vp and the pulverized material rp in the material storage / merging pipe 11A, and a part thereof. Is blown up by introduction of pressurized air, transferred again to the second collector 30 and stored again in the branch pipe 16B, but gradually flows down into the material storage junction pipe 11A as described above. That is, by mixing in this way, as shown in FIG. 10 (a), it is possible to reduce the bias of fine powder and the like sp stored in the material storage / merging pipe 11A, and the homogeneous material is directed to the next processing step. Can supply.
Further, with the discharge from the material discharge port 15, the storage level of the material in the material storage junction pipe 11 </ b> A decreases, and as shown in FIG. 10C, when the storage level is lower than the vicinity of the branch connection portion 14 </ b> Aa, Similarly to the above, the fine powder sp in the branch pipe 16B smoothly flows down into the material storage junction pipe 11A. Further, when the storage level is further lowered and the supply start level LLV is reached, the virgin material vp is replenished and pressurized air is introduced and mixed as in the above example (see FIGS. 7B and 7C). . Thereafter, the above operation is repeated.

As described above, according to the powder material supply apparatus 1B and the supply system A including the powder material supply apparatus 1B according to this modification, in addition to the effects described in the above example, the fine powder sp in the branch pipe 16B Abnormal stagnation can be prevented.
Note that the multistage cyclone collection means 10A described in the first modification may be applied instead of the multistage cyclone collection means 10 of the granular material material supply apparatus 1B according to the present modification.

(A), (b) shows typically one Embodiment of the granular material material supply apparatus which concerns on this invention, (a) is a partially broken schematic front view, (b) is a schematic plane. FIG. (A), (b) is explanatory drawing for demonstrating the collection aspect of the material pneumatically transported to the supply apparatus, respectively, respectively, and each XX arrow partial fracture | rupture in Fig.1 (a) It is a schematic cross-sectional view. It is a schematic system diagram which shows typically an example of the granular material material supply system provided with the supply device. It is a principal part block diagram of the system. It is an operation time chart for explaining an example of operation in the system. (A)-(d) is a partially broken schematic longitudinal cross-sectional view for demonstrating an example of the conveyance of the material in this system, and mixing control. (A)-(d) is a partially broken schematic longitudinal cross-sectional view for demonstrating an example of the conveyance of the material in this system, and mixing control. It is the figure which showed the modification of the granular material material supply apparatus, and was made to respond | correspond to Fig.1 (a). (A)-(c) all show one modification of the granular material supply device, and explain an example of material transport and mixing control in the granular material supply system including the supply device. It is a partially broken schematic longitudinal cross-sectional view. (A)-(c) is a partially broken schematic longitudinal cross-sectional view for demonstrating an example of the conveyance of the material in this system, and mixing control.

Explanation of symbols

1, 1A, 1B Granule material supply device 2 Powder material supply source 3 Crusher 7 Virgin material air transport path (material air transport path)
8 Pulverized material air transportation path (material air transportation path)
DESCRIPTION OF SYMBOLS 10,10A Multistage cyclone collection means 11, 11A Material storage merging pipe 14a, 14Aa Branch connection part 14c Pressurized air inlet 15 Material discharge port 16, 16A, 16B Branch pipe 19 Level meter (sensor means)
20 1st collector (1st stage collector)
21d, 21e Material introduction port 24 discharge port (discharge port of the first stage collector)
30 Second collector (final collector)
30A 3rd collector (final collector)
32, 42 outlet (exhaust outlet of the second and subsequent collectors)
40 Second collector 90 CPU (control means)
A powder material supply system vp virgin material (particle material with relatively large particle size or specific gravity)
rp pulverized material (particulate material with relatively large particle size or specific gravity)
sp Fine powder, etc. (powder material with relatively small particle size or specific gravity, fine powder)
LLV supply start level (predetermined level)

Claims (5)

A multi-stage cyclone collecting means for classifying and collecting the particulate material introduced from the first-stage collector by connecting a plurality of cyclone-type collectors in series.
Two material inlets provided in the first stage collector and respectively connected to two systems of material air transport paths;
The upper end is connected to the discharge port of the first-stage collector, the material discharge port is provided at the lower end, and a branch connection part is provided in the middle. A material storage and merging pipe connected to a branch pipe communicating with the collector outlet;
Provided in the material storage merging pipe, introduced pressurized air into the material storage merging pipe, and a pressurized air inlet for mixing the granular material in the material storage merging pipe;
In order to detect that the granular material material stored in the material storage junction tube is discharged from the material discharge port, and the storage level becomes a predetermined level above the pressurized air introduction port. And a granular material supply device. In claim 1,
The powder material supply apparatus, wherein the sensor means is a level meter provided at a position above the pressurized air inlet. In claim 1 or 2,
The granular air material supply device, wherein the pressurized air introduction port is provided at a position above the branch connection portion. A powder material supply device according to any one of claims 1 to 3, a supply source of the powder material, and a pulverizer for pulverizing a molding byproduct from the molding machine,
A material air transport path for transporting the granular material from the supply source is connected to one material inlet of the first stage collector, and the pulverizer is connected to the other material inlet. Pulverized material air transportation path for transporting pulverized material from
When the sensor means detects the predetermined level, a predetermined amount of one of the granular material and the pulverized material is replenished, and pressurized air is introduced from the pressurized air inlet to store the material. Mixing the material in the junction tube;
After the step, when the sensor means detects the predetermined level, a predetermined amount of the other of the granular material and the pulverized material is replenished, and pressurized air is introduced from the pressurized air inlet. And a control means for controlling to repeat the step of mixing the materials in the material storage and merging pipe. It is a granular material supply method performed using the granular material supply apparatus according to any one of claims 1 to 3,
When the sensor means detects the predetermined level, a predetermined amount of one of the materials that are pneumatically transported via the two systems of material air transport paths is replenished, and pressurized air is supplied from the pressurized air inlet. Mixing the material in the material storage merging pipe,
After the step, when the sensor means detects the predetermined level, a predetermined amount of the other material that is pneumatically transported through the two systems of material air transport paths is replenished, and the pressurized air is introduced. And a step of introducing the pressurized air from the mouth and mixing the material in the material storage and merging pipe.

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