JP5028197B2 - Pellet manufacturing method and pellet manufacturing apparatus - Google Patents

Description

  TECHNICAL FIELD The present invention relates to a pellet manufacturing method and a pellet manufacturing apparatus for manufacturing pellets of resin mixed with aluminum foil pieces having a low water content.

  Conventionally, film scraps (ear loss products) generated during the process of manufacturing plastic film products such as packaging bags by processing multilayer films containing aluminum foil (Al foil), plastic film products that are no longer needed, etc. are landfilled as they are Or incinerated in a special incinerator that is environmentally friendly. In particular, plastic films for packaging containing aluminum foil are manufactured by firmly laminating thin layers of different materials of about several tens of μm, so it is difficult to separate the materials and process them, and they are either landfilled or incinerated. There were many cases.

  In order to improve the recycling rate of the aluminum foil-containing multilayer film, the present inventors directly repelletize the aluminum foil-containing multilayer film by breaking and kneading in the extruder without separating the aluminum foil and the film. A technology has been proposed (see Patent Document 1).

  Conventionally, as a method of producing pellets by cutting a strand extruded from an extruder, a watering cut method in which the strand is immediately cut on the die of the extruder while being cooled with water, and the strand is air-cooled on a conveyor or in a water tank. A strand cut method is known that cuts after cooling with water. Since the strand including the aluminum foil piece has low strength, the strand cutting method tends to cause strand breakage before reaching the cutter. For this reason, the watering cut method is preferable.

In Patent Document 2, the strand cutting step is performed in a water atmosphere sprayed with mist-like water, and the obtained pellets are cooled in running water and then separated using a centrifugal dehydrator or the like. It is described.
In Patent Document 3, a synthetic resin compound strand is cooled by spraying cooling water in a watering hot cut unit, and then the cooled synthetic resin compound strand is cut and granulated into pellets. A continuous drying method of pellets that is sequentially processed by a flow rate vibration device and a dryer is described.
In Patent Document 4, the melt-regenerated synthetic resin strand extruded from the extruder is cut into pellets, and a coolant is sprayed toward the small hole of the die so as to contact the outer surface of the strand. After the outer surface of the strand is rapidly cooled and solidified, there is a method for producing a recycled synthetic resin pellet in which the cut inside is cooled and solidified by the air flow generated around the small holes and the movable cutter while being cooled and solidified. Are listed.
JP 2006-192748 A Japanese Patent Laid-Open No. 2003-200422 JP 2003-311738 A JP 7-214548 A

  In the resin mixed with aluminum foil pieces, the aluminum foil pieces are generally foreign matters for the resin. When irregularities and cavities are formed on the cut surface of the strand, moisture enters the irregularities and cavities, and the moisture content of the pellets is high. Tend to be. A pellet having a high water content (for example, close to 1%) has a problem that when remelted, water vapor is generated and the molded product is foamed.

  This invention is made | formed in view of the said situation, and it aims at providing the manufacturing method and pellet manufacturing apparatus of a pellet for manufacturing the pellet of aluminum foil piece mixing resin with a moisture content of 0.1% or less. To do.

In order to solve the above problems, the present invention provides:
A. The extruder does not contain a synthetic resin blend containing aluminum foil pieces and / or a laminate of synthetic resin containing aluminum foil, and if necessary, a synthetic resin blend and / or aluminum foil containing no aluminum foil pieces. While supplying a laminate of synthetic resin, kneading while crushing aluminum foil in the extruder to knead the aluminum foil piece and the resin kneaded product,
B. The obtained kneaded product is fed into the cut unit as a molten strand from a die hole provided at the tip of the extruder, and the mist generated while supplying hot water for cooling in the cut unit A granulation step of cutting a melted strand with a cutter while bringing the strand into contact with each other to form a pellet having residual heat inside,
C. The dehydration step of dehydrating the pellets while discharging the pellets having the residual heat from the cut unit together with the hot water, sending the pellets into a cylindrical screen, and conveying the pellets from below to above.
D. A moisture removal step of removing moisture from the pellets while rotating the pellets dehydrated in a cylinder together with air and transporting the pellets downward,
E. A sieving step of feeding the pellets from which moisture has been removed to a sieving device having a sieve on at least the top surface, and sieving only the pellets;
F. The pellets that have been sieved are transferred to a stirrer using air, and the drying step of drying the pellets by stirring while blowing air in the stirrer,
A pellet manufacturing method characterized by manufacturing pellets of resin mixed with aluminum foil pieces having a water content of 0.1% or less by having A to F in the order.

In the manufacturing method of the pellet of this invention, it is preferable that the temperature of the said warm water for cooling in the said granulation process is 35-55 degreeC.
It is preferable that the supply amount of the warm water for cooling in the granulation step is a rate of 1 to 10 m ³ / hour with respect to the extrusion amount of 100 kg / hour from the die.
It is preferable that the temperature of the air in the drying step is 60 to 70 ° C.

  The present invention is also a pellet manufacturing apparatus for manufacturing pellets of aluminum foil piece-mixed resin having a water content of 0.1% or less by the above-described pellet manufacturing method, the twin-screw extruder having a vent from which the screen mesh is removed A die that is oriented in the same direction as the twin-screw extruder and provided at the tip of the extruder, a water supply port that supplies hot water for cooling to a strand that is extruded from a hole provided in the die, and a molten state A cutting unit having a cutter that cuts the strands into pellets, a supply port for supplying pellets at the bottom, a discharge port for discharging the pellets at the top, a cylindrical screen, and an upper part of the screen A centrifugal dehydrator equipped with a shower for washing the screen, and pellets dehydrated by the centrifugal dehydrator are supplied from above to use air. A cyclone that removes moisture from the pellets while being transported downward while rotating inside the cylinder, a sieving device having a sieve on at least the top surface, and stirring the pellets while blowing air into the sieved pellets. There is provided a pellet manufacturing apparatus having a stirrer for drying.

The pellet manufacturing apparatus of the present invention preferably further includes a tumbler that stirs the pellets dried by the stirrer in a sealed container and uniformly disperses pellets having different specific gravities.
The tumbler preferably has an intake port and an exhaust port for circulating air.

  According to the present invention, in the granulation step, the melted strand is cut with a cutter to form a pellet having residual heat inside, so that the cut surface of the strand has no unevenness or cavities, or has occurred. Since the irregularities and the cavities are blocked by the flow of the molten resin, it is possible to reduce moisture intrusion into the pellets. This makes it possible to produce pellets of resin containing aluminum foil pieces with a moisture content of 0.1% or less, even if it is a material that is difficult to produce pellets with a low moisture content, which is a resin containing aluminum foil pieces. It becomes possible to do.

The present invention will be described below with reference to the drawings based on the best mode.
FIG. 1 is a schematic configuration diagram showing an example of a pellet manufacturing apparatus used in the present invention. FIG. 2 is a schematic configuration diagram illustrating an example of a cut unit. FIG. 3 is a schematic configuration diagram illustrating an example of a centrifugal dehydrator and a cyclone.

  The pellet manufacturing apparatus 1 shown in FIG. 1 and FIG. 2 is provided at the front end of a twin screw extruder 10 provided with a vent 11 from which a screen mesh is removed, and in the same direction as the twin screw extruder 10. A cutting unit 20 including a die 13, a water supply port 21 for supplying hot water for cooling to a strand extruded from a hole 14 provided in the die 13, and a cutter 23 for cutting the molten strand into pellets; A centrifugal dehydration apparatus is provided with a supply port 31 for supplying pellets, a discharge port 32 for discharging pellets at the top, and a cylindrical screen 33 and a shower 34 for cleaning the screen 33 from above the screen 33 30 and the pellets dehydrated by the centrifugal dehydrator 30 are supplied from above and rotated in the cylinder 41 using air. A cyclone 40 that removes moisture from the pellets while being transported, a sieving device 50 having at least a sieve on the top surface, and a stirrer 63 that agitates and blows air into the sieved pellets to dry the pellets. A drying device 60.

(Kneading process)
The twin screw extruder 10 is supplied with an aluminum foil or a material containing an aluminum foil piece as at least a part of the pellet raw material. Examples of the aluminum foil or the material containing the aluminum foil piece include a synthetic resin mixture containing the aluminum foil piece, a synthetic resin laminate containing the aluminum foil, or both. Further, if necessary, as a material not containing aluminum foil and aluminum foil pieces, a synthetic resin mixture not containing aluminum foil pieces, a laminate of synthetic resins not containing aluminum foil, or both, the aluminum foil or It can be supplied together with materials including aluminum foil pieces. The laminated body of synthetic resin including aluminum foil includes, for example, a laminated film in which one or more films are laminated on one or both sides of aluminum foil, ear loss or punching waste. Moreover, the synthetic resin mixture containing an aluminum foil piece includes a synthetic resin molded article containing an aluminum foil piece, or a product crushed as a fragment of a desired size.

  Here, the plastic constituting the plastic layer is not particularly limited, but low-density polyethylene (LDPE), linear low-density polyethylene (LLDPE), high-density polyethylene (HDPE), and polypropylene (PP ), Polyolefin resins such as those modified with carboxyl groups, polyester resins such as polyethylene terephthalate (PET), polyamide resins such as nylon (Ny), ethylene-vinyl alcohol (EVOH), etc. Can do. The number of plastic layers is not particularly limited, and may be one layer or a plurality of layers, and may have an adhesive layer made of an adhesive such as urethane, epoxy, or the like.

  The thickness of the aluminum foil in the material is preferably 3 to 40 μm. The Al content in the aluminum foil-containing multilayer film is preferably 2 to 25%. From the viewpoint of pelletization and moldability, the range of 2 to 10% is more preferable. An aluminum foil and a material that does not include an aluminum foil piece may be used together for adjusting the Al content by using an aluminum foil or a material that includes an aluminum foil piece. Moreover, the dispersibility of the aluminum foil pieces in the resin is improved by adding 5 to 30% of the olefin resin as a dispersant, separately from the olefin resin contained in the material, and the pellet surface Unevenness and voids are less likely to occur, and moisture can be less likely to adhere to the pellet surface.

  The material may be supplied after being crushed into pieces, or may be supplied as it is without being crushed. In that case, the width of the material is not particularly limited as long as it can be charged into the extruder, and for example, it is possible to process even an ear loss having a width of several mm or a film having a width of 1200 mm. When the material is put in a long length without being crushed, the film is naturally drawn into the barrel as the screw rotates, so there is no need for a forced feeder, and aluminum foil The step of pulverizing the multilayered film can be omitted, and a tank for storing the pulverized product is not required, so that the equipment and the process can be simplified.

  As the extruder 10, a twin-screw extruder in which two screws are rotatably provided while meshing with each other inside the barrel is used. Since the twin screw extruder is excellent in kneadability, the above material is charged from the hopper 12 and the two screws are rotated while heating the material in the barrel, thereby giving a strong shear force and crushing the aluminum foil. Can be kneaded with resin. Thereby, the kneaded material of an aluminum foil piece and resin is obtained. The temperature of the molten resin is preferably about 230 ° C.

  The barrel of the extruder 10 preferably has a vent 11 at one or a plurality of locations in order to discharge moisture contained in the material as much as possible during kneading. Further, it is desirable to remove the screen mesh between the barrel and the die so that only the breaker plate is provided in the molten resin flow path to avoid clogging by the mesh.

(Granulation process)
In the granulation step, the aluminum foil pieces and the resin kneaded product obtained in the kneading step are each of the holes 14 of the die 13 including a plurality of holes 14 provided at the tip of the extruder 10 as shown in FIG. A strand that is fed out as a molten strand (not shown) into the cut unit 20 and is extruded in a molten state while the strand is brought into contact with the mist generated by spraying hot water 22 for cooling in the cut unit 20. Only the surface layer is solidified, and sequentially cut with a cutter 23 to obtain pellets having residual heat inside.

  In the example shown in FIG. 2, the cutter 23 is provided in contact with the plate surface of the die 13 so that the two blades are point-symmetric with respect to the rotation center of the shaft 24, and is connected via the shaft 24. It is driven to slide and rotate on the plate surface by a motor (not shown). Thereby, until the cutter 23 circulates, only the surface layer of the strand extruded in the molten state from the hole 14 of the die 13 is solidified and cut by the cutter 23. Therefore, since the inside of the cut unit 20 is not routed as a strand, it is possible to prevent the strand of the resin containing foreign matter called an aluminum foil piece from being cut. The cutter 23 is preferably provided so that the two blades are point-symmetric with respect to the rotation center of the shaft 24. However, one blade may be provided, or three or more blades may be equal. It may be provided at any angle.

  Moreover, the water supply port 21 which is provided in the inner wall of the cut unit 20 on the same side as the die 13 and ejects the hot water 22 for cooling is away from the dice 13 so that the hot water 22 does not directly touch the dice 13 and the strand (see FIG. 2 is directed so as to eject the hot water 22 for cooling. Specifically, the hot water 22 is jetted obliquely so as to be provided on the outer side in the radial direction (the vertical direction in FIG. 2) of the die 13 and the cutter 23 and to be on the inner side in the radial direction of the die 13 and the cutter 23. The direction in which the hot water 22 is ejected from the water supply port 21 is preferably about 30 to 60 ° as an angle θ with respect to the direction in which the molten resin is extruded from the die 13 (rightward in FIG. 2). With this configuration, a large amount of hot water can be supplied as will be described later, and the hot water 22 ejected from the water supply port 21 collides with the opposite wall of the cut unit 20 and the shaft 24 of the cutter 23. As a result, fine water droplets in the form of mist or mist (hereinafter sometimes referred to as mist) are formed.

  In the present invention, the hot water 22 becomes mist when water is supplied, and the mist fills the cut unit 20. Since the hot water 22 does not directly touch the die 13 or the strand, a decrease in the temperature inside the tip portion (head) 15 of the extruder 10 or inside the pellet is suppressed. For this reason, an increase in the extrusion pressure of the extruder 10 can be suppressed, and clogging of the kneaded material in the molten resin flow path 16 in the head 15 and damage to the drive motor and screw of the extruder 10 can be prevented. By obtaining the pellets as pellets having residual heat in the interior, it becomes easy for moisture to fly as steam in the steps after the dehydration step. The temperature of the hot water 22 for cooling in the granulation step is a temperature when supplied into the cut unit 20, and is preferably 35 to 55 ° C. More preferably, it is 40-45 degreeC. In this embodiment, the molten resin flow path 16 extends conically around a cone 17 whose diameter increases in a tapered shape toward the tip in the head 15, and a plurality of holes 14 are provided along the circumference. Yes.

In addition, while the conventional common sense is that if the pellet temperature after cutting is high, fusion between the pellets occurs and satisfactory granulation is not possible, in the present invention, while setting the temperature of the hot water high By increasing the amount of hot water supplied, fusion between the pellets was avoided. Specifically, the hot water 22 is supplied into the cut unit 20 at a rate that the supply amount of the hot water 22 for cooling is 1 to 10 m ³ / hour with respect to the extrusion rate of 100 kg / hour of the kneaded material from the die. preferable. Here, the ratio of the hot water supply amount to the extrusion amount means that the supply amount of the hot water 22 is 2 to 20 m ³ / hour when the extrusion amount of the kneaded material from the die is 200 kg / hour, for example. In this way, the pellet immediately after cutting is placed in a relatively high temperature mist or mist atmosphere, and the temperature inside the pellet is maintained at a high temperature, so that in the steps after the dehydration step, the pellet surface has a recess or void inside. Residual moisture can be avoided. In addition, the unevenness and cavities generated on the surface or inside of the pellet are blocked or reduced by the flow of the resin in a molten or softened state, so that the intrusion and adhesion of moisture to the pellet can be suppressed.

(Dehydration process)
After the granulation step, the pellets having the remaining heat are discharged from the cut unit 20 together with the hot water used for cooling and sent into the cylindrical screen 33, and the wing member 36 provided inside the cylindrical screen 33 is attached in a spiral shape. The cylindrical body 35 thus rotated is rotated, and the pellets are dehydrated while being conveyed from below to above. As shown in FIG. 2, a pellet discharge port 25 is provided on the side surface of the lower part of the cut unit 20 (the front side of FIG. 2, the direction corresponding to the lower side of FIG. 1), and the granulated pellet transfer tube 26. The pellets and the hot water are transferred through and are introduced into the centrifugal dehydrator 30 through the supply port 31 provided at the lower part of the centrifugal dehydrator 30 shown in FIG. In the present invention, since a sufficient amount of hot water is supplied, only the hot water used for cooling is sufficient for the transfer, but hot water for transfer may be added.

  Inside the centrifugal dehydrator 30 is provided a cylindrical screen 33 having a rotatable cylinder 35 with a wing member 36 attached in a spiral shape. A plurality of wing members 36 are spirally attached to the peripheral surface of the cylindrical body 35, and are supported by a rotating shaft (not shown) so as to be rotatable around a central axis 35a. When the cylinder 35 is rotated by a drive motor or the like (not shown) in the stationary screen 33, an ascending air current is generated with the rotation of the wing member 36 attached to the cylinder 35, and the pellets are formed on the screen 33. It is conveyed from the lower side to the upper side through the space between the cylindrical body 35 inside. The hot water supplied together with the pellets in the centrifugal dehydrator 30 is discharged from a drain port (not shown) provided at the lower part of the centrifugal dehydrator 30. Further, since the screen 33 has a mesh shape that does not allow the pellets to pass through, moisture adhering to the pellets passes through the outside of the screen 33 due to centrifugal force and is separated from the pellets. The pellets conveyed upward in the centrifugal dewatering device 30 are discharged from a discharge port 32 provided in the upper part of the centrifugal dewatering device 30.

  Further, the centrifugal dehydrator 30 is provided with a shower 34 for supplying water from the upper part of the screen 33 to wash the screen 33. During the pellet production, the screen 33 is periodically cooled (for example, every hour) with cold water or By spraying warm water from the outside and washing it, pellets broken into smaller grains can be removed to prevent clogging of the screen 33 and continuous production can be easily performed.

(Moisture removal process)
The pellets dehydrated in the dehydration step are rotated in the cylinder 41 together with air and removed from the pellets while being conveyed downward.
The pellet manufacturing apparatus 1 of the present embodiment supplies the pellets dehydrated by the centrifugal dehydration apparatus 30 from above and transports the pellets downward while rotating in the cylinder 41 using air, and removes moisture from the pellets. 40, and the pellets are discharged from a pellet discharge port 42 provided in the lower part of the cyclone 40. In addition, water containing water vapor or moisture generated by evaporating the moisture on the surface of the pellets by heat stored in the pellets is discharged from an exhaust port 43 provided in the upper part of the cyclone 40. In the present invention, the top surface of the cyclone 40 is opened, and a cylinder made of mesh is attached. With this cylindrical body, the pellets are efficiently separated from water vapor and moisture without jumping out of the cyclone 40, and the moisture in the pellets is removed. In the present invention, since the moisture on the surface of the pellet evaporates due to the heat stored inside the pellet, normal air can be used, but heated air may also be used.

(Sieving process)
The pellets from which moisture has been removed in the moisture removal step are fed into a sieving device 50 having a sieve on at least the top surface, and only the pellets are sieved and stored in the sieving device 50. When the sieving device 50 has, for example, a two-layer sieve, the top side sieve of the sieving device 50 passes pellets, and the bottom side sieve of the sieving device 50 does not pass pellets. As a result, only the pellets are stored between the top-side sieve and the bottom-side sieve. And, for example, a plurality of pellets fused and coarsened are left on the top side sieve, and smaller pellets fall under the bottom side sieve and separated. Is done.

  Alternatively, in the present invention, since a sufficient amount of hot water is supplied and cooled, there are almost no grains that are fused and coarsened by a plurality of pellets. Can only be. In this case, if the top sieve of the sieving device 50 is not allowed to pass through the pellets, only the pellets remain on the top sieve, and the pellet fragments that have become smaller particles fall to the bottom, To be separated. And if a sieve is inclined so that it may become low gradually toward the downstream from an upstream, a pellet can be collect | recovered by the lower end of a sieve.

  The upper surface of the sieving device 50 is preferably opened without a cover or the like so that moisture and water vapor can be easily scattered. Moreover, in order to prevent scattering of pellets or the like, it is preferable to provide a wire mesh or the like on the upper portion of the sieving device 50. Note that a plurality of sieves may be provided and classified according to pellet size.

(Drying process)
The pellets sieved in the sieving step are stored in the sieving device 50 or blown air without being stored, transferred to the container 61 together with the air flow, exhausted in the container 61, and stirred. Accumulate in 63 and dry the pellets.

  The drying device 60 used here includes a container 61 that receives pellets transferred from the sieving device 50 through a pipe 51 to the inside through an air flow. Since the container 61 has the exhaust port 62 on the top surface, moisture is discharged out of the container 61 together with air blown as water vapor, and the pellets are coarsely dried. The pellets received in the container 61 are accumulated in the stirrer 63, and heated air is blown into the stirrer 63 and stirred for about 4 to 5 minutes. In this drying step, the air blown into the stirrer 63 may be normal air, but is preferably heated air. The temperature of the heated air is preferably 60 to 70 ° C.

(Uniform dispersion process)
Further, the pellet manufacturing apparatus 1 includes a tumbler 70 that stirs the pellets dried by the drying apparatus 60 in a sealed container 71 and uniformly disperses pellets having different specific gravities. In the aluminum foil piece-mixed resin pellets, particles with higher Al content and specific gravity are more likely to collect downward, and particles with lower Al content and specific gravity are more likely to float upward, so when subdivided into containers such as bags, There is a risk that the variation of the average Al content will increase for every time. For this reason, if it disperse | distributes uniformly by stirring using the tumbler 70, the dispersion | variation in the quality of the manufactured pellet can be suppressed. The uniformly dispersed pellets can be taken out from a pellet discharge port 74 provided on the side of the tumbler 70. When the tumbler 70 having the air inlet 72 and the air outlet 73 for circulating air is used, even when the pellets are uniformly dispersed, the normal or heated air is circulated to remove moisture from the pellets. It can be performed.

  INDUSTRIAL APPLICABILITY The present invention can be used to recycle pellets of aluminum foil-containing films such as lost products and cuts of aluminum foil-containing films produced during the manufacture of packaging bags and nonstandard packaging bags. The recycled pellets obtained by the present invention can be used for the production of various molded products such as blocks, bricks, piles and fences, plate materials, sheets, injection molded products, and multilayer containers.

It is a schematic block diagram which shows an example of the pellet manufacturing apparatus used by this invention. It is a schematic block diagram which shows an example of a cut unit. It is a schematic block diagram which shows an example of a centrifugal dehydration apparatus and a cyclone.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 ... Pellet manufacturing apparatus, 10 ... Twin screw extruder, 11 ... Vent, 12 ... Hopper, 13 ... Dies, 14 ... Hole, 20 ... Cut unit, 21 ... Water supply port, 22 ... Hot water for cooling, 23 ... Cutter, DESCRIPTION OF SYMBOLS 30 ... Centrifugal dehydrator, 31 ... Supply port, 32 ... Discharge port, 33 ... Cylindrical screen, 34 ... Shower, 35 ... Cylindrical body, 36 ... Feather member, 40 ... Cyclone, 41 ... Cylindrical body, 50 ... Sieve Device: 60 ... Drying device, 61 ... Container, 63 ... Stirrer, 70 ... Tumbler, 71 ... Container, 72 ... Intake port, 73 ... Exhaust port.

Claims (7)

A. The extruder does not contain a synthetic resin blend containing aluminum foil pieces and / or a laminate of synthetic resin containing aluminum foil, and if necessary, a synthetic resin blend and / or aluminum foil containing no aluminum foil pieces. While supplying a laminate of synthetic resin, kneading while crushing aluminum foil in the extruder to knead the aluminum foil piece and the resin kneaded product,
B. The obtained kneaded product is fed into the cut unit as a molten strand from a die hole provided at the tip of the extruder, and the mist generated while supplying hot water for cooling in the cut unit A granulation step of cutting a melted strand with a cutter while bringing the strand into contact with each other to form a pellet having residual heat inside,
C. The dehydration step of dehydrating the pellets while discharging the pellets having the residual heat from the cut unit together with the hot water, sending the pellets into a cylindrical screen, and conveying the pellets from below to above.
D. A moisture removal step of removing moisture from the pellets while rotating the pellets dehydrated in a cylinder together with air and transporting the pellets downward,
E. A sieving step of feeding the pellets from which moisture has been removed to a sieving device having a sieve on at least the top surface, and sieving only the pellets;
F. The pellets that have been sieved are transferred to a stirrer using air, and the drying step of drying the pellets by stirring while blowing air in the stirrer,
A method for producing a pellet, characterized in that a pellet of resin mixed with an aluminum foil piece having a water content of 0.1% or less is produced by having A to F in the order.   The method for producing pellets according to claim 1, wherein the temperature of the hot water for cooling in the granulation step is 35 to 55 ° C. ^3. The pellet according to claim 1, wherein the supply amount of the warm water for cooling in the granulation step is a rate of 1 to 10 m ³ / hour with respect to 100 kg / hour of extrusion from the die. Manufacturing method.   The method for producing pellets according to any one of claims 1 to 3, wherein an air temperature in the drying step is 60 to 70 ° C. A pellet manufacturing apparatus for manufacturing pellets of aluminum foil piece mixed resin having a water content of 0.1% or less by the pellet manufacturing method according to any one of claims 1 to 4,
A twin-screw extruder with a vent from which the screen mesh has been removed;
A die that is oriented in the same direction as the twin-screw extruder and provided at the tip of the extruder;
A water supply port for supplying hot water for cooling to the strand extruded from the hole provided in the die and a cutting unit including a cutter that cuts the molten strand into pellets;
A centrifugal dewatering device provided with a supply port for supplying pellets at the bottom, a discharge port for discharging the pellets at the top, a cylindrical screen and a shower for washing the screen from the top of the screen;
A cyclone that removes moisture from the pellets while transporting downward while rotating the pellets dehydrated by the centrifugal dehydrator from above and rotating in the cylinder using air,
A sieving device having a sieve on at least the top surface;
A pellet production apparatus comprising: a stirrer that dries the pellets by blowing air into the sieved pellets and drying the pellets.   The pellet manufacturing apparatus according to claim 5, further comprising a tumbler that stirs the pellets dried by the stirrer in a sealed container and uniformly disperses pellets having different specific gravities.   The pellet manufacturing apparatus according to claim 6, wherein the tumbler has an intake port and an exhaust port for circulating air.

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