JP2006289781A - Temperature control device and temperature control method for injection molding machine - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a temperature control method for a heating cylinder which can reduce the overshooting or undershooting phenomenon of temperature at the time of continuous automatic molding and restrain the periodic temperature changes of a nozzle of the molding controlling cycle. <P>SOLUTION: This temperature control method for an injection molding machine comprises the step wherein the FF memorizing/learning part 13 calculates the FF memory value that negates the deviation e and memorizes it, the step wherein the FF output part 14 outputs the FF memory value as the FF output value that is advanced by the heater dead time L, namely a lag time mounting from when the heater 9 is switched on until the thermocouple 2 begins to detect the temperature rise, and the step wherein the value obtained by adding the FF output value to the control output MV value, which is the output value from the PID control part 20, is inputted to PWM7. The heater 9 is controlled in temperature by the value obtained by adding the FF output value to the control output MV value. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a temperature control device and a temperature control method for an injection molding machine.

  Conventionally, PID (proportional, integral, derivative) control is used for temperature control of the heating cylinder of the injection molding machine and the extrusion molding machine. FIG. 6 shows a configuration diagram of an example of a conventional PID temperature control device for a heating cylinder.

  The temperature PV value detected by the thermocouple 102 inserted in the heating cylinder 101 is amplified by the amplifier 103 and compared with the set temperature SV value. The compared value is input as a deviation e to the proportional controller (P) 104, the integral controller (I) 105, and the derivative controller (D) 106, and PID control calculation is performed. Each control output MV obtained here is input to the heater 109 via the PWM 107 (pulse width modulator) and the SSR 108 (semiconductor), and the heater temperature of the heating cylinder 101 is controlled.

In addition, as an apparatus for heating cylinder temperature control used in an injection molding machine and an extrusion molding machine, only integral control of PID control is stopped for a predetermined time, and a predetermined set value is added to the operation amount during this period. A technique and a technique for performing temperature control of an integral value and an offset value corresponding to a plurality of temperature control periods are also disclosed (see Patent Document 1 and Patent Document 2).
Japanese Patent Laid-Open No. 10-100188 JP 2003-25404 A

  However, since these conventional techniques are temperature control within a certain period obtained in advance, the temperature change due to the influence of disturbance heat during actual continuous automatic operation and shear heat due to the injection speed, so-called molding control periodic temperature There was a problem with the stability of the change.

  In particular, precision molded products such as DVDs (Digital Versatile Discs) have caused defective molded products.

  As general characteristics of the PID control method, there are a target value tracking characteristic and a disturbance suppression characteristic. The target value tracking type literally becomes a characteristic that makes the detected temperature the same as the set temperature that changes, and the disturbance suppression type is so-called It is a characteristic that suppresses temperature fluctuation due to disturbance. However, it has been said that both of these characteristics cannot be optimized simultaneously.

  In general, injection machine manufacturers ship PID control constants obtained in advance by experiments and tests in their machines. However, in addition to the user's factory environment, the resin used, mold temperature, set temperature of the heating cylinder, etc. Therefore, in the PID control constant obtained in advance, overshoot and undershoot with respect to the set temperature are generated. In view of such a situation, an injection machine manufacturer takes a countermeasure by incorporating a so-called auto-tuning function capable of arbitrarily controlling PID control. However, depending on the use environment, the above-described overshoot or the like may occur due to auto-tuning, and so-called resin burning may occur.

In particular, the following points are given as specific problems.
(1) Responsiveness of heater control depends on the PID constant value. For this reason, the user may change the setting value of the injection machine manufacturer in order to adapt it to the usage environment and the resin. As a result, the actually measured value becomes an undershoot or overshoot phenomenon with respect to the set value, resulting in molding defects.
(2) During the injection process in the molding cycle, as shown in FIG. 7, a periodic temperature change (waviness curve α value) corresponding to the molding cycle occurred in the nozzle portion (LNH). Further, the shear heat generation of the resin due to the injection speed causes the above-described overshoot phenomenon, and the molded product is burnt or yellowed.

  Therefore, the present invention relates to a temperature control device and a temperature control method for an injection molding machine that can reduce the temperature overshoot and undershoot phenomenon during continuous automatic molding and can suppress the periodic temperature change of the nozzle part. The purpose is to provide.

  In order to achieve the above object, the temperature control apparatus for an injection molding machine of the present invention receives a deviation e, which is a temperature difference between the temperature set by the temperature setting unit and the temperature of the heating cylinder measured by the thermocouple. A PID control unit including a proportional controller, an integral controller, and a derivative controller, and a control output MV value, which is an output value from the PID control unit, is converted into a pulse width modulator PWM and a semiconductor SSR. In the temperature control apparatus for an injection molding machine that controls the temperature of the heater that heats the heating cylinder by inputting to the heater via the FF storage / learning unit that calculates and stores the FF stored value that cancels the deviation e, and FF output unit that outputs the FF memory value as an FF output value that is postponed by heater waste time L, which is a delay time from when the heater is turned on until the thermocouple starts to detect a temperature rise The a, the PWM, characterized in that the value obtained by adding the FF output value to the control output MV value is an output value from the PID controller is input.

  The temperature control device for an injection molding machine according to the present invention as described above calculates an FF memory value that cancels the deviation e between the set temperature and the actually measured temperature in the heating cylinder in the FF memory / learning unit, and this FF memory The FF output value obtained by adding the heater waste time L to the value is output from the FF output unit. And a heater is controlled by the value which added this FF output value to the control output MV value which is an output value from the PID control part of a prior art. That is, by controlling the heater by feedforward control using a value obtained by adding the FF output value to the control output MV value obtained by the conventional PID control, for example, due to the deviation e caused by the molding cycle, which occurred in the conventional PID control It is possible to cancel the periodic undulation of the molding temperature.

  Further, the temperature control device for an injection molding machine according to the present invention includes a cycle start timing ST which is an automatic start signal for each molding shot output after a predetermined number of molding shots, and a correction value of a temperature error according to the number of learnings. The learning intensity coefficient Ti, which is a weighting coefficient for changing the weighting, and the heater gain K, which is a proportional coefficient between the control output MV value and the set temperature, are output to the FF storage / learning unit, and the heater waste time L is output to the FF output unit. It may have a set value output unit for outputting to it.

Further, in the temperature control device for an injection molding machine of the present invention, the calculation of the FF memory value in the FF memory / learning unit is performed when the cycle time during which the heater is controlled is set to the control cycle second.
FF memory value = − (previous FF memory value + deviation e × heater gain K × control cycle seconds / learning strength coefficient Ti)
It may be calculated by the following formula.

  The temperature control method for an injection molding machine according to the present invention includes a proportional controller and an integral control in which a deviation e, which is a temperature difference between a temperature set by a temperature setting unit and a temperature of a heating cylinder measured by a thermocouple, is input. A heater that heats a heating cylinder by inputting a control output MV value, which is an output value from a PID control unit including a detector and a differential controller, to the heater via a PWM that is a pulse width modulator and an SSR that is a semiconductor In the temperature control method of the injection molding machine that performs temperature control of the FF, the FF storage / learning unit calculates and stores the FF stored value that cancels the deviation e, and the FF output unit turns on the FF stored value and the heater Output as an FF output value that is postponed by a heater waste time L, which is a delay time from when the thermocouple starts to detect a temperature rise, and PID control in PWM Comprise the steps of: inputting a value obtained by adding the FF output value to the output value is the control output MV value from characterized.

  The temperature control method for the injection molding machine according to the present invention also includes a cycle start timing ST that is an automatic start signal for each molding shot that is output after a predetermined number of molding shots from the set value output unit to the FF storage / learning unit. And a step of outputting a learning intensity coefficient Ti that is a weighting coefficient and a heater gain K that is a proportional coefficient between the control output MV value and the set temperature, in which the weighting of the temperature error correction value is changed according to the number of learning times. And a step of outputting the heater waste time L from the set value output unit to the FF output unit.

Further, the temperature control method of the injection molding machine of the present invention is such that when the cycle time during which the heater is controlled is the control cycle second, the FF storage / learning unit
FF memory value = − (previous FF memory value + deviation e × heater gain K × control cycle seconds / learning strength coefficient Ti)
The step of calculating the FF stored value may be included.

  According to the present invention, it is possible to reduce the temperature overshoot and undershoot phenomenon during continuous automatic molding and eliminate the temperature undulation of the molding control cycle, thereby reducing the burn and yellowing of the molded product, and consequently It is possible to reduce the variation in the weight of the molded product.

Next, embodiments of the present invention will be described with reference to the drawings.
[Heater temperature control device]
FIG. 1 is a block diagram showing a heater temperature control device for an injection molding machine according to an embodiment of the present invention.

  In the figure, the heater temperature control shows only one zone, but the same applies to the other heater zones.

  The temperature control device for an injection molding machine of this embodiment performs temperature control of the heater 9 attached to the heating cylinder 1. A screw (not shown) is rotatably incorporated in the heating cylinder 1 and plasticizes a resin material supplied from the outside by kneading.

  The temperature control device of the present embodiment includes a thermocouple 2 that measures the internal temperature of the heating cylinder 1, an amplifier 3 that amplifies the output signal of the thermocouple 2, a temperature setting unit 17 that sets a molding temperature, and PID control. A PID control unit 20 including a proportional controller (P) 4, an integral controller (I) 5 and a differential controller (D) 6, a PWM (Pulse Width Modulation) 7 that is a pulse width modulator, and a semiconductor. An SSR (Solid State Relay) 8, a set value output unit 16 for setting various set values, an FF (feed forward) storage / learning unit 13 for calculating and storing an FF stored value, which will be described later, and performing feedforward control; The FF output unit 14 outputs an FF output value that is a value obtained by adding the heater waste time L to the FF stored value calculated by the FF storing / learning unit 13. Having.

A screw (not shown) is rotatably incorporated in the heating cylinder 1 and plasticizes a resin material supplied from the outside by kneading.
[Control action]
Next, the operation of the heating cylinder temperature control by the heater temperature control device of the present embodiment will be described with reference to FIGS.

  First, an automatic start signal for each molding shot output from a controller (not shown) provided as a standard of the injection molding machine is input to the set value output unit 16 as the cycle start timing ST. The temperature control of this embodiment starts with molding of a molded product based on normal molding conditions by obtaining each control output MV value by PID control of the prior art and after the molded product is stably molded. Is done. Therefore, for example, if the molded product is stably molded by molding 20 shots from the start of molding, the cycle start timing ST which is an automatic start signal after 20 shots from the molding start is sent to the FF storage / learning unit 13. Set to output.

  When the cycle start timing ST is input to the FF storage / learning unit 13, the temperature control of the present embodiment is started, and the deviation e at the time of continuous automatic molding is input to the FF storage / learning unit 13. Here, the deviation e is a temperature difference between the temperature set by the temperature setting unit 17 and the temperature measured by the thermocouple 2. That is, the temperature of the superheated cylinder 1 differs from the set temperature due to environmental disturbance during continuous automatic molding and shearing heat generation under molding conditions. This temperature difference is defined as a deviation e.

  The FF storage / learning unit 13 obtains and stores the FF storage value for each time by, for example, the following calculation formula (1).

FF memory value = − (previous FF memory value + deviation e × heater gain K × control cycle (seconds) / learning strength coefficient Ti) (1)
The heater gain K is a proportional coefficient between the actual control output MV value and the set temperature. For example, after obtaining an approximate linear function by the least square method from the relationship between the control output MV value and the set temperature SV as shown in FIG. The heater gain K is calculated from this approximate expression and stored in the set value output unit 16. The set value output unit 16 outputs the heater gain K to the FF storage / learning unit 13 when the FF storage / learning unit 13 calculates the FF stored value.

  As the control cycle (seconds), a cycle time in which the heater is controlled by a controller provided as standard in the injection molding machine is used. For example, [1 (second) or 3 (second)] is used as the control cycle (second). The controller outputs the control cycle (seconds) to the FF storage / learning unit 13 when the FF storage / learning unit 13 calculates the FF stored value.

  The learning intensity coefficient Ti value is a weighting coefficient that changes the weighting of the temperature error correction value according to the number of learnings. In other words, the learning intensity coefficient Ti value is the rate at which the correction value of temperature error (deviation e × heater gain K × control cycle (seconds)) is reflected in the current FF stored value in the calculation formula (1). If the coefficient is large, the correction value of the temperature error is greatly reflected in the current FF stored value with a small number of learning times. In other words, the learning intensity coefficient Ti value means response sensitivity for correcting the waviness curve α (FIG. 7) generated by the molding control cycle. Here, the learning number means the number of times the FF stored value is calculated and the FF stored value is stored.

  The learning intensity coefficient Ti can be arbitrarily input to the set value output unit 16 by an operator (molding engineer). However, if the learning intensity coefficient Ti is too large, the correction of the temperature error is converted to the FF stored value. It will be reflected excessively, which leads to the possibility that the control will be disturbed. For this reason, a value within a range in which the temperature control is not disturbed is input as the learning intensity coefficient Ti. In the present embodiment, the learning intensity coefficient Ti is a value within a range in which the temperature control is not disturbed and is a value at which the learning intensity is strongest. That is, in the present embodiment, the learning intensity coefficient Ti is set to a value that reflects the correction of the temperature error in the FF stored value with the smallest possible number of learning. The set value output unit 16 outputs the learning intensity coefficient Ti as described above to the FF storage / learning unit 13 when the FF storage / learning unit 13 calculates the FF stored value.

  The FF stored value is obtained by the above formula (1) and stored in the FF storage / learning unit 13 in time series for each time. The FF stored value obtained here becomes a minus signal for canceling the deviation e of the actual measurement value. FIG. 3 shows the relationship between the deviation e and the FF stored value. FIG. 3 shows data (solid line) for a half cycle of the deviation e that periodically varies. The deviation e is [+ 0.1 ° C.] when [5 sec]. As a value for canceling this, [−0.1 ° C.] is calculated and stored as the FF storage value (two-dot chain line) at [5 sec]. In other words, the periodic fluctuation is canceled by canceling the deviation e with the FF stored value.

  The FF storage value calculated by the FF storage / learning unit 13 using the calculation formula (1) and stored in time series is output to the FF output unit 14. The FF output unit 14 outputs the FF stored value input from the FF storage / learning unit 13 in time series as an FF output value that is advanced by the heater waste time L at the cycle start timing. Here, the heater waste time L is a delay time from when the heater 9 is turned on until the thermocouple 2 starts to detect a temperature rise, as shown in FIG.

  The FF output value output from the FF output unit 14 is added to the control output MV value obtained by the PID control unit 20 and input to the PWM 7. A value obtained by adding the FF output value and the control output MV value is input to the heater 9 via the PWM 7 and the SSR 8. The FF output value is a value including the FF stored value and cancels the deviation e. Therefore, periodic temperature fluctuations in the heating cylinder 1 can be suppressed by controlling the temperature of the heater 9 with this FF output value.

As described above, according to the temperature control device and the temperature control method of the present embodiment, it is possible to reduce the temperature overshoot and undershoot phenomenon during continuous automatic molding and to eliminate the temperature undulation of the molding control cycle. As a result, it is possible to reduce the burn and yellowing of the molded product and to reduce the weight variation of the molded product.
[Example]
The example shown in FIG. 7 is a measured value of the temperature of the heating cylinder by conventional PID control, and the molded product shows a temperature waveform when two connectors called precision molded products are taken.

  The graph shown in FIG. 7 is based on the stable data 1 hour after the start of molding, and the temperature fluctuation of the nozzle portion (LNH) measured at a control cycle of about 1 ° C. (in FIG. 7, swell curve α value). As a result, the short shot defect of the molded product was incurred.

  On the other hand, the result of controlling by the control method of the present embodiment under the same conditions is shown in FIG.

  In the control method of the present embodiment, an FF memory value that cancels the deviation e is calculated, and the FF output value calculated by adding the heater waste time L to the FF memory value is added to the control output MV value output from the PID control unit. The heater temperature is controlled according to the value obtained. Thereby, as shown in FIG. 5, the temperature waveform of the nozzle part (LNH) becomes a temperature waveform when a molded product can be stably taken out without causing undulation. As described above, according to the present embodiment, the temperature overshoot and undershoot phenomenon during continuous automatic molding can be reduced, and the temperature fluctuation of the molding control cycle can be eliminated. And weight variation of molded products could be reduced.

It is a block diagram of the heater temperature control apparatus of the injection molding machine of one Example of this invention. It is a graph which shows how to obtain | require a heater gain K value. It is a graph which shows the relationship between the deviation e and FF memory | storage value. It is a graph explaining the heater waste time L. It is a graph which shows the temperature change of the nozzle part at the time of controlling with the control method by one Embodiment of this invention. It is a block diagram of an example of the conventional PID temperature control apparatus. It is a graph which shows the temperature change of the nozzle part at the time of controlling by the conventional PID temperature control.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Heating cylinder 2 Thermocouple 3 Amplifier 9 Heater 13 FF memory | learning part 14 FF output part 16 Set value output part 17 Temperature setting part 20 PID control part e Deviation K Heater gain L Heater waste time MV Control output value ST Cycle start timing SV Set temperature Value Ti Learning intensity coefficient α Waviness curve

Claims (6)

Proportional controller (4), integral control to which deviation e which is a temperature difference between the temperature set by the temperature setting unit (17) and the temperature of the heating cylinder (1) measured by the thermocouple (2) is input A PID control unit (20) comprising a voltage controller (5) and a differential controller (6), and a control output MV value, which is an output value from the PID control unit (20), is converted into a PWM (pulse width modulator). 7) and a temperature control device for an injection molding machine that controls the temperature of the heater (9) that heats the heating cylinder (1) by inputting to the heater (9) via the SSR (8) that is a semiconductor. In
An FF storage / learning unit (13) for calculating and storing an FF stored value that cancels the deviation e;
An FF output unit that outputs the FF stored value as an FF output value that is advanced by a heater waste time L, which is a delay time from when the heater (9) is turned on until the thermocouple (2) starts to detect a temperature rise. (14)
The PWM (7) is inputted with a value obtained by adding the FF output value to a control output MV value which is an output value from the PID control unit (20). apparatus.   Cycle start timing ST that is an automatic start signal for each molding shot that is output after a predetermined number of molding shots, a learning intensity coefficient Ti that is a weighting coefficient that changes the weight of the correction value of the temperature error according to the number of learning, A heater gain K, which is a proportional coefficient between the control output MV value and the set temperature, is output to the FF storage / learning unit (13), and the heater waste time L is output to the FF output unit (14). The temperature control device for an injection molding machine according to claim 1, further comprising a set value output unit (16). In the FF memory / learning unit (13), the calculation of the FF memory value is performed when a cycle time during which the heater (9) is controlled is a control cycle (seconds).
FF memory value = − (previous FF memory value + deviation e × heater gain K × control cycle (seconds) / learning strength coefficient Ti)
The temperature control device for an injection molding machine according to claim 2, which is obtained by: Proportional controller (4), integral control to which deviation e which is a temperature difference between the temperature set by the temperature setting unit (17) and the temperature of the heating cylinder (1) measured by the thermocouple (2) is input The control output MV value, which is an output value from the PID control unit (20) including the voltage controller (5) and the derivative controller (6), is converted into a PWM (7) as a pulse width modulator and an SSR (8) as a semiconductor. In the temperature control method of the injection molding machine that controls the temperature of the heater (9) that heats the heating cylinder (1) by inputting to the heater (9) via
A step of the FF storage / learning unit (13) calculating and storing an FF stored value for canceling the deviation e;
The FF output unit (14) forwards the FF stored value by a heater waste time L, which is a delay time from when the heater (9) is turned on until the thermocouple (2) starts to detect a temperature rise. Outputting as an output value;
The step of inputting to the PWM (7) a value obtained by adding the FF output value to the control output MV value that is an output value from the PID control unit (20). Control method. According to the cycle start timing ST, which is an automatic start signal for each molding shot output after a predetermined number of molding shots, from the set value output unit (16) to the FF storage / learning unit (13), and the number of learnings A step of outputting a learning intensity coefficient Ti, which is a weighting coefficient, and a heater gain K, which is a proportional coefficient between the control output MV value and the set temperature, for changing the weighting of the correction value of the temperature error;
The temperature control method for an injection molding machine according to claim 4, further comprising a step of outputting the heater waste time L from the set value output unit (16) to the FF output unit (14). When the cycle time during which the heater (9) is controlled is a control cycle (seconds), the FF storage / learning unit (13)
FF memory value = − (previous FF memory value + deviation e × heater gain K × control cycle (seconds) / learning strength coefficient Ti)
The temperature control method for an injection molding machine according to claim 5, including the step of calculating the FF stored value by means of:

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