The present disclosure relates to an extrusion device, an extrusion molding die, a monitoring device and a monitoring program, a strand manufacturing method, and a strand diameter adjustment method, and more specifically to a technique for uniformizing a diameter of molten resin (strand) ejected from an extrusion device.
Pellets made of a resin raw material may be used when a thermoplastic resin molded article is manufactured. As one method for molding pellets, a strand cutting method is known. Japanese Patent Laying-Open No. 2018-001649 (PTL 1) discloses a method for reducing variations in strand diameter in the strand cutting method.
Japanese Patent Laying-Open No. 2018-001649 (PTL 1) discloses a configuration of an extruder to uniformize a strand diameter by differentiating, in a flow path width direction, a length of a crown disposed between a die and a die holder in a flow path direction.
In the configuration disclosed in PTL 1, the strand diameter is uniformized by changing the shape of a flow path member through which the resin raw material passes. On the other hand, there are increasing needs to realize a further uniformized strand diameter by enabling adjustment of the strand diameter even during an operation of the extrusion device.
The present disclosure was made in order to solve such a problem, and an object thereof is to uniformize a strand diameter by enabling adjustment of the strand diameter during an operation of an extrusion device in the extrusion device that is used to manufacture a thermoplastic resin molded article.
An extrusion device according to the present disclosure is configured such that ejection amounts of strands ejected from a plurality of through-holes can be individually adjusted by adjustment mechanisms.
According to the extrusion device of the present disclosure, it is possible to adjust the strand diameters by the adjustment mechanisms even during an operation of the extrusion device and thereby to uniformize the strand diameters.
Hereinafter, an embodiment of the present disclosure will be described in detail with reference to the drawings. Note that the same reference signs will be applied to the same or corresponding parts in the drawings and the description thereof will not be repeated.
[Configuration of Pellet Manufacturing Apparatus]
Extrusion device 100 is a manufacturing device for strands 160. Extrusion device 100 includes a driving unit 110, a cylinder 120, a feeder 140, and a die 150. Note that in
Driving unit 110 is configured to include, for example, a motor and a decelerator. Driving unit 110 is disposed at one end of cylinder 120 extending in the X-axis direction in
Cylinder 120 is a tubular member with a hollow inside and accommodates one or two screws 130 therein. An inlet port 121 (raw material feed port) is formed in cylinder 120 for putting the raw materials as pellets supplied from feeder 140 into the cylinder. Also, a heater 122 for heating the inside of cylinder 120 is disposed on the outer circumference of cylinder 120. The raw materials put into the cylinder 120 are melted through kneading with heat from heater 122 and rotation of screw 130. Then, the molten raw materials are transferred to the other end of cylinder 120 on the side opposite to driving unit 110 through the rotation of screw 130.
Die 150 is connected to the other end of cylinder 120 via a die holder 155. As will be described later in
Strands 160 ejected from die 150 are guided to cooling tank 20, and cooled and solidified by a coolant 21 stored in cooling tank 20. Cooled strands 160 are fed to strand cutter 30. Strand cutter 30 cuts strands 160 into a predetermined length, and pellets 50 are thereby formed.
[Configuration of Die]
Next, a detailed configuration of die 150 will be described by using
Referring to
Flow-out portion 158 is formed at an end portion of die holder 155 in a positive direction of the X axis. Die 150 is connected to flow-out portion 158. The molten resin flowed into flow-in portion 156 passes through flow path portion 157 and is then guided to a recessed portion 153 of die 150.
Plurality of through-holes 152 are formed in the Y-axis direction in die 150, the through-holes 152 establishing communication between recessed portion 153 and the outside. The molten resin passed through die holder 155 and flowed into recessed portion 153 of die 150 is extruded from through-holes 152 and is ejected as string-shaped strands 160.
Also, die 150 according to the present embodiment is provided with adjustment mechanisms 154 for adjusting strand diameters by changing minimum sectional areas of through-holes 152 for each of through-holes 152. In the example in
Note that adjustment mechanisms 154 are not limited to the bolt members as in the above example as long as they have a configuration including mechanisms to change the amounts of projection into through-holes 152. Other examples of adjustment mechanisms 154 include pins, slide mechanisms, cylinders, and the like. Alternatively, adjustment mechanisms 154 may be flow amount adjustment valves attached to through-holes 152 or mechanisms for changing a flow path resistance such as balloon catheters.
In manufacturing of pellets by using a so-called strand cutting method as described above, variations in strand diameters may cause variations in weight of each completed pellet. If weights of the pellets vary in manufacturing of a thermoplastic resin molded article, there may be a case where scaling accuracy of the resin raw material is degraded and this leads to a problem in operation of an injection molding machine. According to the extrusion device in the present embodiment, it is possible to individually adjust each strand diameter as needed even during an operation of the extrusion device, by the adjustment mechanisms provided in the die. It is thus possible to uniformize the diameters of the strands ejected from the extrusion device.
[Monitoring Device]
Next, a monitoring device that detects strand diameters during an operation of the extrusion device will be described. It is possible to quickly adjust strand diameters in a case where the strand diameters have changed due to a change in manufacturing conditions, for example, by detecting the strand diameters during the operation in real time, which is useful for preventing variations in strand diameters.
Control device 300 is typically a personal computer and incorporates a central processing unit (CPU) 301 and a memory 302. CPU 301 and memory 302 are connected to a common bus 303, and various kinds of processing is realized by CPU 301 executing a program stored in memory 302. Control device 300 performs binarization processing on the image acquired from imaging device 200 and calculates a strand diameter (strand width) of each strand 160. Note that control device 300 may be a programmable logic controller (PLC), a micro-computer, a micro-computer board, or the like.
Display device 305 is composed of, for example, a liquid crystal diode (LCD) panel or an organic electronic luminescence (EL) panel, and displays the image acquired by imaging device 200 and the strand diameter computed by control device 300. In the example in
The user determines a degree of variations in strand diameters on the basis of the deviation of the strand diameters from the average value and the standard deviation or dispersion displayed on display device 305. In a case where the variations are large, the user adjusts adjustment mechanisms 154 of die 150 with the strand diameters with large deviations from the average value and performs adjustment such that the variations in strand diameters fall within the predetermined range.
It is possible for the user to easily detect the strand diameters during an operation of the extrusion device by providing such a monitoring device, and thereby to quickly adjust the strand diameters even in a case where variations in strand diameters are large.
Note that in the first example, “imaging device 200”, “control device 300”, and “display device 305” correspond to an “imaging unit”, a “detection unit”, and an “output unit” in the present disclosure, respectively.
Next, a configuration of a second example of the monitoring device that can be applied to extrusion device 100 according to the embodiment will be described by using
Referring to
Once the user executes the application for monitoring strands on mobile terminal 250, a camera incorporated in mobile terminal 250 is activated. When the user places mobile terminal 250 such that strands 160 are located within the field of view of the camera, strands 160 imaged by the camera are displayed on a display 251 of mobile terminal 250 as illustrated in
As in the second example, it is possible to detect the strand diameters during an operation without using a dedicated device as in the first example by installing the monitoring application on the user's mobile terminal. Also, it is possible to reduce variations in strand diameters by adjusting the adjustment mechanisms as needed on the basis of the detected strand diameters.
Note that in the second example, the “camera”, the “CPU”, and “display 251” mounted on mobile terminal 250 correspond to the “imaging unit”, the “detection unit”, and the “output unit” in the present disclosure, respectively.
Referring to
The user can easily detect the strand diameters and variations in strand diameters during an operation of the extrusion device by executing such processing. It is possible to reduce variations in strand diameters and to uniformize the strand diameters by the user adjusting adjustment mechanisms 154 of die 150 during an operation of the extrusion device in a case where the detected variations in strand diameters are large.
Note that although the example in which the strand diameters are detected by processing the image captured by the imaging device has been described in the above example, the strand diameters may be detected by another method. For example, instead of the imaging device, the strand diameter of each strand may be detected by using a non-contact-type sensor such as a photoelectric sensor, a spectroscopy/optical interference-type thickness gauge, an infrared film thickness gauge, a laser thickness gauge, an ultrasonic film thickness gauge, a fluorescent X-ray film thickness gauge, an eddy current-type film thickness gauge, an electromagnetic-type film thickness gauge, or an electrical resistance-type film thickness gauge.
[Automatic Adjustment System]
In the aforementioned example, a case where the adjustment of the strand diameters is performed by a user's manual operation has been described. However, a configuration in which the adjustment mechanisms are automatically adjusted on the basis of the detected strand diameters by using the monitoring device as illustrated in the first example in
Moving units 410 are allowed to project into through-holes 152 of die 150 similarly to the bolt members in
Driving units 400 are actuators of a pneumatic type, a hydraulic type, or an electric type and are composed of, for example, cylinders, motors, ball screws, or the like. Driving units 400 drive moving units 410 on the basis of a signal from control device 300.
Next, the automatic adjustment function of control device 300 will be described by using
Image acquisition unit 310 receives image data captured by imaging device 200. Image processing unit 320 processes the image acquired by image acquisition unit 310 and specifies strands 160 in the image data. Strand diameter computing unit 330 computes the strand diameter of each strand 160 from the image of the specified strands.
Variation determination unit 340 computes an average value of the strand diameters or a parameter (dispersion, a standard deviation, or the like) indicating variations by using the data of the calculated strand diameters, determines whether or not there are variations, and outputs a determination result to driving control unit 350. Driving control unit 350 generates a control signal for driving corresponding to each strand 160 on the basis of the determination result from variation determination unit 340 and controls driving units 400 in accordance with the driving signal.
Referring to
Next, CPU 301 calculates the strand diameter of each detected strand 160 (S120) and computes a parameter (dispersion, a standard deviation, or the like) indicating variations in the calculated strand diameters (S130).
In S140, CPU 301 determines whether the obtained standard deviation is greater than a predetermined threshold value a. In a case where the standard deviation is predetermined threshold value a or less, that is, in a case where variations in strand diameters are small (NO in S140), following steps S150 and S160 are skipped, and the processing is returned to the main routine.
On the other hand, in a case where the standard deviation is greater than predetermined threshold value a, that is, in a case where the variations in strand diameters are large (YES in S140), the processing proceeds to S150, and CPU 301 computes the driving amounts of driving units 400 corresponding to through-holes 152 with large deviations from the average value. Thereafter, CPU 301 drives the driving units by outputting a control command to target driving units 400 and adjusts the diameters of the strands ejected from these through-holes 152 to approach the average value in S160.
Specifically, in a case where the strand diameters are greater than the average value, CPU 301 drives driving units 400 such that the sectional areas of corresponding through-holes 152 in die 150 become smaller. Conversely, in a case where the strand diameters are smaller than the average value, CPU 301 drives driving units 400 such that the sectional areas of corresponding through-holes 152 become larger. In this manner, it is possible to reduce variations in strand diameters by driving driving units 400 and adjusting strokes of moving units 410 on the basis of the image data of strands 160 ejected from die 150 in the system illustrated in
[Modification Examples of Adjustment Mechanisms]
In the above embodiment, the configuration example of the adjustment mechanisms that adjust the strand diameters by changing the sectional areas of the through-holes in the die has been described. The following modification examples show examples of adjustment mechanisms using methods different from the above for adjusting the strand diameters.
Referring to
Blowers 450 are controlled by a control signal from control device 300 and adjust the temperatures of strands 160 by blowing hot air or cold air to ejected strands 160. Blowers 450 may be configured to switch and use hot air and cold air or may be configured to use only one of hot air or cold air.
Heaters 460 are attached to the ejection ports of through-holes 152, for example. Heaters 460 are controlled by a control signal from control device 300 and heat ejected strands 160.
Since strands 160 are softened when they are heated and their temperatures are raised, the strand diameters decrease due to a winding effect of strand cutter 30.
Conversely, since hardening of strands 160 is promoted when they are cooled, the strand diameters increase.
Note that the heating/cooling mechanism for strands 160 is not limited to the configurations disposed outside the ejection ports as illustrated in
Therefore, in a case where variations in the detected strand diameters are large, it is possible to reduce the variations in strand diameters by heating/cooling the target strands by using blowers 450 and/or heaters 460 in response to a control command from control device 300.
“Blower 450” and “heater 460” in modification example 1 correspond to a “temperature adjustment unit” in the present disclosure.
Referring to
Tensioners 470 are formed of rod-shaped members movable in the Y-axis direction, for example, and can increase the tensions of strands 160 by tensioners 470 moving to the outside. Note that a direction in which tensioners 470 apply the tensions may not be the Y-axis direction and the tensions may be increased by causing strands 160 to move in the Z-axis direction, for example. Also, tensioners 470 may be applied to all strands 160.
When the tensions applied to strands 160 are caused to increase, the strand diameters decrease due to a change in volume. In general, the molten resin ejected from die 150 has parabolic speed distribution with the center of die 150 in the Y-axis direction included as a vertex. Therefore, it is more difficult to eject the molten resin from the through-holes located closer to the end portions of die 150 in the Y-axis direction as compared with the through-holes at the center in the Y-axis direction. In order to solve this problem, a case where a measure to promote flowing of the molten resin to the end portion side in the Y-axis direction by changing the flow path shape inside die 150 may be employed. In this case, the strand diameters at the end portions are likely to be larger as compared with those at the center in the Y axis direction, and it is thus possible to reduce variations in strand diameters by disposing tensioners 470 on the end portion side in the Y-axis direction.
On the other hand, in a case where the flow path shape inside die 150 is not changed, it is likely to increase the ejection amounts at the center and to become larger in the strand diameters as compared with the strand diameters at the end portions in the Y-axis direction as described above. Therefore, it is possible to reduce variations in strand diameters by disposing tensioners 470 at the center and increasing the tensions at the strands at the center.
“Tensioner 470” in modification example 2 corresponds to a “tension adjustment unit” in the present disclosure.
Note that the adjustment mechanisms with the configuration of changing the sectional areas of through-holes 152 in die 150 as in
As described above, it is possible to adjust the strand diameters even during an operation of the extrusion device by providing the adjustment mechanisms capable of individually adjusting the strand diameters of the strands ejected from the die in the extrusion device. It is thus possible to uniformize the strand diameters. Also, it is possible to detect the strand diameters in real time during an operation of the extrusion device by providing the imaging device or the monitoring device using a displacement sensor. It is thus possible to quickly perform adjustment even in a case where the strand diameters change during an operation. Furthermore, it is possible to omit user's time and effort for adjustment and to further reduce variations in strand diameters by employing the configuration in which the adjustment mechanisms are automatically controlled by using data regarding the strand diameters detected by the monitoring device.
The embodiment disclosed herein should be considered as illustrative examples and not limitations in any sense.
Number | Date | Country | Kind |
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2021-033644 | Mar 2021 | JP | national |
Filing Document | Filing Date | Country | Kind |
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PCT/JP2021/041870 | 11/15/2021 | WO |