WO1997012740A2 - Verfahren zur regelung des werkzeuginnendruckverlaufs an einer zyklisch arbeitenden maschine - Google Patents
Verfahren zur regelung des werkzeuginnendruckverlaufs an einer zyklisch arbeitenden maschine Download PDFInfo
- Publication number
- WO1997012740A2 WO1997012740A2 PCT/DE1996/001895 DE9601895W WO9712740A2 WO 1997012740 A2 WO1997012740 A2 WO 1997012740A2 DE 9601895 W DE9601895 W DE 9601895W WO 9712740 A2 WO9712740 A2 WO 9712740A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- pressure
- steps
- time
- pwi
- course
- Prior art date
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D17/00—Pressure die casting or injection die casting, i.e. casting in which the metal is forced into a mould under high pressure
- B22D17/20—Accessories: Details
- B22D17/32—Controlling equipment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/76—Measuring, controlling or regulating
- B29C45/77—Measuring, controlling or regulating of velocity or pressure of moulding material
Definitions
- the invention relates to a method for regulating the mold internal pressure on a cyclically operating machine according to claims 1, 8 and 14.
- the method can preferably be used in the plastics processing and metal processing industries, for example in connection with plastic injection molding machines, blow molding machines, die casting machines, aluminum die casting machines, but also in connection with presses or welding apparatus, provided that cyclical processes are carried out.
- process curve profiles are referred to in the following, they are not only understood to be directly recordable profiles, but also the predictable process curve profiles, such as e.g. Derivatives, integrals and the like.
- DE-A 30 21 978 describes a method for regulating the mold internal pressure curve on a cyclically operating machine, both the mold internal pressure curve and the hydraulic pressure curve being monitored as decision criteria for determining the switchover point.
- both the mold internal pressure curve and the hydraulic pressure curve being monitored as decision criteria for determining the switchover point.
- the present invention is based on the task of optimizing and monitoring the cycle on such machines in order to achieve high-quality parts.
- this mold cavity pressure curve is recorded during the different phases of a cycle. If one aims at an optimal switchover point between injection and hold pressure phase, the curve is checked for monotonous rise according to claim 1 or 8. If there is no monotonically increasing Course, the times to or the way to the changeover point are changed until an optimal changeover point is determined. If one aims for an optimal hold pressure time until the sprue is sealed, then the curve is checked for constant falling in the area of the hold end, that is to say that there is no kink or slope difference between adjacent points in the curve. The reprint time can also be optimized. This enables the cycle time to be optimized without loss of quality.
- Fig. 8 the process sequence on the basis of a block diagram for determining an optimal switchover time
- FIG. 9 is a schematic representation of the elements provided on a plastic injection molding machine
- Fig. 10 shows a schematic process sequence with regard to quality control
- FIG. 11 shows a representation according to FIG. 5 with a course of the derivation of the mold internal pressure after the path.
- an injection molding machine preferably an injection molding machine for processing plastic materials, such as plastics or powder materials.
- plastic materials such as plastics or powder materials.
- the process can also be used without problems in other areas in which cyclical processes are used for the production (master shaping) or processing (shaping) of products.
- the method is used to control the mold cavity pressure curve on a cyclically operating machine. This is due to the fact that it has been found that the internal mold pressure Pwi is most suitable for indicating inconsistencies when it comes to producing optimally high quality products. With these machines, the manufacturing process for the products is roughly as described below for a plastic injection molding machine.
- An injection means 31 of an injection molding unit such as a screw conveyor or an injection piston, inject material into a mold cavity 32 of an injection mold 34 in a tool closing unit 33.
- the device has sensor means such as an internal mold pressure sensor 11 and a temperature sensor 12 in the area of the injection molding unit.
- the conveying means moves, the mold cavity is first gradually filled, the internal mold pressure initially increasing very gradually according to FIG. 1. If the mold cavity pressure sensor is not arranged close to the gate, the process curve profile may also be started too late, as shown in FIGS. 5 and 6 is shown. However, an arrangement close to the sprue of the cavity pressure sensor 11 is preferred, since otherwise problems arise with regard to the detection of the cavity pressure Pwi, at least in the case of thin-walled parts can.
- the mold cavity is now filled at the height of the kink K in the mold cavity pressure curve Pwi.
- the funding continues to press even more material into the mold cavity in a compression phase.
- the conveying means 31 comes to a point at which a further forward movement in the direction of the mold cavity is no longer possible, so that distance or speed control can no longer take place.
- t um a switch is made to a pressure control and a hold pressure control begins, roughly equivalent to area C in FIG. 5.
- the time of the switchover set on a machine determines, for example, when the changeover is made from speed-controlled injection to the pressure-controlled holding pressure range.
- the switchover point should match the volumetric filling of the mold cavity 32 as much as possible, since the mold cavity is to be filled at a defined speed, but the shrinkage occurring in the post-pressure phase must be compensated for by a predetermined pressure profile.
- pressure fluctuations and pressure peaks must be avoided at the switchover point, if possible, so that there is a steady and harmonious transition between the injection phase and the holding pressure phase, so that no negative influences can impair the quality of the molded part.
- a maximum Max (Pwi) of the mold internal pressure Pwi then also occurs in the area C of the holding pressure. After the maximum is exceeded, the pressure gradually drops as the molded part cools. It is now crucial to determine when the molded part is sealed in the mold. This point in time is to be equated with an optimal holding time. If the hold pressure time is set too long, it can become the variable determining the cycle time and thus reduce the productivity and economy of the process. However, if it is too short, the molded part is not sealed and melt emerges from the tool. This loss of mass affects the quality of the parts and their reproducibility.
- the figures 1 and 2 differ from FIGS. 3 and 4 in that in FIGS. 3 and 4 an amorphous material is processed, while in FIGS. 1 and 2 semi-crystalline material is processed. Since the amorphous material takes a long time to form the product, the mold internal pressure Pwi must also be maintained there for a long time.
- Figs. 1-4 the hydraulic pressure Phy is also plotted. It goes without saying that this hydraulic pressure on a hydraulic machine can be used as a manipulated variable for the mold cavity pressure, but a similar picture emerges when other drives are used, e.g. in the case of electromechanical drives, the hydraulic pressure Phy then being replaced by a force curve.
- the hydraulic pressure is high at the beginning of the filling phase in order to achieve filling of the mold cavity 31 as quickly as possible.
- the hydraulic pressure is then at a level Pl, from which it drops to a level P2 at the end of the holding pressure time.
- step S4 the process curve profiles, but essentially differentiates the mold internal pressure profile according to time t or path s.
- step S6 The aim of this is to avoid the drop in the mold cavity pressure resulting from the premature reduction in the holding pressure due to material escaping during the next injection cycle (step S6).
- the next injection cycle is then carried out with the changed hold pressure time tn and, if an optimum already results, only steps S1 to S4 are carried out in the following.
- the hold pressure time is reduced and the next injection cycle is carried out. This reduction in hold pressure time continues until there is no constant rise again. If the holding pressure time is increased slightly, an optimal holding time tn results.
- This regulation of the hold pressure time tn can first be carried out by checking a large number of points along the mold internal pressure curve and, if no constant slope occurs in a closed control loop, the hold pressure time tn is regulated to a value at which a constant slope no longer occurs.
- the mold internal pressure curve Pwi is differentiated once over time t and the value Sl of the slope is determined in an area Bl before the point tn and the value S2 in an area B2 after the point. If the value S1 is divided by the value S2 by a value of approximately 1, then there is continuity.
- the search algorithm for finding a kink Un can, however, be accelerated if the check is carried out, for example, starting from the point at which the digital signal "reprint end" 10 in FIG. 2 results.
- the digital signal "reprint end” one can also use the negative edge in the hydraulic pressure Phy at the reprint end.
- the hydraulic pressure Phy drops at the holding pressure end from a high pressure level Pl to a lower level P2.
- the disadvantage of this procedure is that both pressure levels depend on the settings and the machine and are therefore more difficult to evaluate.
- the digital signal "reprint end” can be determined by the digital signal "open tool” and the value of the machine setting variable "remaining cooling time", since the time at which the reprint ends corresponds to the time "open tool” minus the remaining cooling time.
- the hold pressure time can thus be regulated according to the controller equation:
- ⁇ tn - ((Sl / S2) setpoint) x gain factor.
- FIGS. 5, 6 and 8 A regulation of the switchover point is also possible with a similar algorithm, for which reference is now made to FIGS. 5, 6 and 8.
- FIGS. 5, 6 and 8 the internal tool pressure Pwi and, on the other hand, its second-degree derivative are plotted over time. Since the internal pressure Pwi can also be derived via the path covered by the conveying means 31, a representation comparable to FIG. 5 is shown in FIG. 11.
- the control algorithm which is otherwise identical, is shown below on the basis of the time-dependent differentiation.
- FIG. 5 shows a correct switchover, in which the course of the mold cavity pressure curve increases in the area of the switchover point t by a monotonous or strictly monotonous curve.
- FIG. 6 shows a pressure drop occurs, which is noticeable in extreme values, ie maxima or minima of the derivatives.
- both a pronounced local maximum and an associated local mini mum the second derivative of the internal pressure.
- the criterion is whether the second degree derivative has an extreme value. Control is based on a state of the switchover that is not quite perfect. A slightly too early switch error is required, otherwise there is no criteria to determine if the switch is too late.
- step S8 A check is carried out in step S8 if no optimum has previously been achieved, which can only be determined by comparing after at least two injection cycles
- the changeover time t urn is increased by cft according to step S10.
- the switchover time can now be reduced by cft in order to find out the point in time at which there is an optimal switchover time, which is not only contributes to the production of a high quality part, but also helps to shorten the cycle time.
- the aim is to achieve regulation in such a way that the changeover time t urn is where an extreme value of the derivative of the second degree no longer occurs.
- the maximum or minimum that is, the extreme value Max (dPwi / dt) 2 , namely, the search is made between the changeover time t urn set on the machine and the time tm at which the first maximum Max (Pwi) of the mold cavity pressure occurs in the holding pressure phase C.
- a threshold value of a screw position or a fixed point in time is usually specified as the search criterion from which the search can start.
- a criterion can also be a mold cavity pressure or hydraulic pressure threshold value. This results in a controller equation either as a function of the time t or the screw position as follows:
- the S. factor is the scaling factor and is used to adapt to the value scale that is available in the machine as a setting variable, e.g. Screw path, spray volume or time.
- the value s can assume very large values, so that it cannot be used directly as a manipulated variable. Only the sign of the determined value is used and multiplied by a fixed, small adjustment unit in order to obtain a meaningful adjustment.
- Repressurization time regulator and switchover point regulator can be part of a multivariable regulator for regulating the quality of the features produced, as is explained in the older German patent application P 44 34 653.0 and the associated PCT application PCT / DE 95/01345 filed on September 28, 1995.
- the disclosure content of these applications is hereby expressly made the disclosure content of the present application. A summary of this can be found in FIGS. 9 and 10.
- a multitude of process parameters are ascertained during each process by means of sensors such as an internal mold pressure sensor 11 and a temperature sensor 12. However, this determination is initially carried out in a test phase T in which the machine setting variables MG are changed systematically. With every change the Quality characteristics QM of the manufactured products are recorded as well as the machine setting variables set here (steps S1 ', S2', S3 '). Process curve profiles PKV are recorded during a process via means 13. The quality features QM, which can be determined by conventional methods, but also directly by the machine, can also be input via input means 14.
- step S4 ' the process curve profiles are usually automatically broken down into process phases PPH, which are determined by the machine itself on the basis of the signal input. Different signals of different process curve profiles can be connected to each other in order to determine sensible process phases PPH. Within these process phases, process indicators PKZ characterizing the process phases are then formed (step S5 '). A connection between the machine setting variable and the quality characteristic QM can then be determined using these process key figures. Corresponding equations are shown in step S6 '. These relationships are determined by means 15. In most cases, neither the quality features nor the machine settings are linearly independent of one another. In step S10 ', target values QMsol1 »MGs 0 ⁇ are specified for the quality features QM and the machine setting variables MG.
- step S7 Series process curves SPKV are determined (step S7 '), these are broken down into series process phases SPPH (step S8') and identified by series process key figures SPKZ (step S9 1 ). Based on these series process key figures, the quality of the parts to be produced can be monitored and regulated in step S12 '.
- the relationship determined in the test phase was stored in storage means 16.
- the machine setting variables can then be influenced, for example, using the setting device 17, 18. If a difference value QM, PKZ, MG results in a comparator 21, this difference value can be evaluated by the controller 19 in such a way that readjustment takes place.
- 11 shows the determined internal mold pressure as well as its second differential derivative (d Pwi / ds) 2 after the path s of the conveying means, represented over time.
- the time range for an injection cycle on an injection molding machine covers approximately a range from 0.3 see before switching to approximately 0.7 see. after switching.
- a correct switchover point is shown at which the second derivative moves approximately around zero in the period under consideration.
- the switch is made too late, the second derivative receives a pronounced minimum.
- the switch is made too early, a difference to the case of the correct switch cannot be made. For this reason, it is regulated in such a way that only a slight reduction in the pressure rise occurs, corresponding to a small extreme value of the second derivative, so that the best possible switchover point is achieved.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
- Numerical Control (AREA)
- Operation Control Of Excavators (AREA)
- Constituent Portions Of Griding Lathes, Driving, Sensing And Control (AREA)
- Moulds For Moulding Plastics Or The Like (AREA)
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP96945150A EP0854778B1 (de) | 1995-10-02 | 1996-10-02 | Verfahren zur regelung des werkzeuginnendruckverlaufs an einer zyklisch arbeitenden maschine |
DE59602740T DE59602740D1 (de) | 1995-10-02 | 1996-10-02 | Verfahren zur regelung des werkzeuginnendruckverlaufs an einer zyklisch arbeitenden maschine |
US09/051,069 US5945046A (en) | 1995-10-02 | 1996-10-02 | Process for regulating the tool inner pressure curve of a cyclically working machine |
JP9513891A JPH11512665A (ja) | 1995-10-02 | 1996-10-02 | 周期的に動作する機械の工具内圧経過制御方法 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19536566A DE19536566C1 (de) | 1995-10-02 | 1995-10-02 | Verfahren zur Regelung des Werkzeuginnendrucks an einer zyklisch arbeitenden Maschine |
DE19536566.6 | 1995-10-02 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO1997012740A2 true WO1997012740A2 (de) | 1997-04-10 |
WO1997012740A3 WO1997012740A3 (de) | 1997-07-03 |
Family
ID=7773737
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/DE1996/001895 WO1997012740A2 (de) | 1995-10-02 | 1996-10-02 | Verfahren zur regelung des werkzeuginnendruckverlaufs an einer zyklisch arbeitenden maschine |
Country Status (7)
Country | Link |
---|---|
US (1) | US5945046A (de) |
EP (1) | EP0854778B1 (de) |
JP (1) | JPH11512665A (de) |
AT (1) | ATE183132T1 (de) |
CA (1) | CA2233650A1 (de) |
DE (2) | DE19536566C1 (de) |
WO (1) | WO1997012740A2 (de) |
Cited By (1)
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DE102022127260A1 (de) | 2022-10-18 | 2024-04-18 | Arburg Gmbh + Co Kg | Prozesskennzahlermittlung |
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JP2550921B2 (ja) * | 1994-08-26 | 1996-11-06 | 日本電気株式会社 | 環状バッファ制御装置 |
ATE320904T1 (de) * | 1997-08-21 | 2006-04-15 | Kistler Holding Ag | Verfahren zum regeln einer spritzgiessanlage für kunststoff-materialien |
US6309571B2 (en) * | 1998-02-27 | 2001-10-30 | The Hong Kong University Of Science & Technology | Method and apparatus for the control of injection molding |
JP3423219B2 (ja) * | 1998-06-30 | 2003-07-07 | 株式会社名機製作所 | ディスク基板の射出成形機におけるモニタ方法及び成形作動制御装置 |
US6649095B2 (en) | 2000-11-06 | 2003-11-18 | Frederick J. Buja | Method and apparatus for controlling a mold melt-flow process using temperature sensors |
DE102004051109B4 (de) * | 2004-10-19 | 2007-01-18 | Siemens Ag | Verfahren zum Betrieb einer Spritzgießmaschine |
DE102005015491B4 (de) * | 2005-04-05 | 2006-12-07 | Battenfeld Gmbh | Spritzgiessverfahren |
DE102005016617B3 (de) * | 2005-04-12 | 2006-12-14 | Battenfeld Gmbh | Spritzgießverfahren |
US7585166B2 (en) * | 2005-05-02 | 2009-09-08 | Buja Frederick J | System for monitoring temperature and pressure during a molding process |
DE102006014554A1 (de) * | 2006-03-20 | 2007-10-04 | Electronics Gmbh Vertrieb Elektronischer Geräte | Verfahren zum Befüllen des Formhohlraums einer Druckgießvorrichtung mit Gießmaterial und Druckgießvorrichtung zur Durchführung des Verfahrens |
WO2008022122A2 (en) * | 2006-08-14 | 2008-02-21 | Buja Frederick J | System and method employing a thermocouple junction for monitoring of physiological parameters |
DE102007061775A1 (de) * | 2007-12-20 | 2009-07-02 | Geiger Technik Gmbh | Spritzgussverfahren und zugehörige Anlage |
CA2724641C (en) | 2008-05-20 | 2020-03-24 | Avant Medical Corp. | Autoinjector system |
US8177749B2 (en) | 2008-05-20 | 2012-05-15 | Avant Medical Corp. | Cassette for a hidden injection needle |
US8052645B2 (en) | 2008-07-23 | 2011-11-08 | Avant Medical Corp. | System and method for an injection using a syringe needle |
EP2174769A1 (de) * | 2008-10-07 | 2010-04-14 | Neo-plastic Dr. Doetsch Diespeck GmbH | Spritzgussverfahren und zugehörige Anlage |
DE102010002174A1 (de) * | 2010-02-22 | 2011-08-25 | Robert Bosch GmbH, 70469 | Verfahren zur Regelung eines Spritzgießprozesses |
US8986205B2 (en) | 2010-05-14 | 2015-03-24 | Frederick J. Buja | Sensor for measurement of temperature and pressure for a cyclic process |
EP2699293B8 (de) | 2011-04-20 | 2022-07-20 | Amgen Inc. | Autoinjektorvorrichtung |
USD898908S1 (en) | 2012-04-20 | 2020-10-13 | Amgen Inc. | Pharmaceutical product cassette for an injection device |
EP2968760B1 (de) | 2013-03-15 | 2024-01-03 | Amgen Inc. | Medikamentenkassette, autoinjektor und autoinjektorsystem |
US10492990B2 (en) | 2013-03-15 | 2019-12-03 | Amgen Inc. | Drug cassette, autoinjector, and autoinjector system |
EP3027380B1 (de) * | 2013-08-01 | 2019-06-19 | Imflux Inc. | Spritzgiessmaschinen und verfahren zur berücksichtigung von veränderungen bei den materialeigenschaften während des spritzgiessens |
CN105473304B (zh) * | 2013-08-01 | 2018-07-10 | 艾姆弗勒克斯有限公司 | 考虑注塑运行期间材料特性的变化的注塑机和方法 |
AT514836B1 (de) * | 2013-09-30 | 2015-06-15 | Engel Austria Gmbh | Verfahren zur Bestimmung eines Siegelpunktes |
DE102013111328A1 (de) * | 2013-10-14 | 2015-04-16 | Kraussmaffei Technologies Gmbh | Verfahren zur Beurteilung verfahrenstechnischer Eigenschaften von Spritzgießwerkzeugen |
JP6619837B2 (ja) | 2017-04-25 | 2019-12-11 | キストラー ホールディング アクチエンゲゼルシャフト | 射出成形における射出成形部品質の再現方法及びその方法を行う射出成形ユニット |
DE102017207586A1 (de) * | 2017-05-05 | 2018-11-08 | Arburg Gmbh + Co Kg | STEUERN UND REGELN DES DRUCKS EINER ZYKLISCH ARBEITENDEN SPRITZGIEßMASCHINE |
EP3546179B1 (de) * | 2018-03-28 | 2021-01-13 | Kistler Holding AG | Verfahren zum reproduzieren einer spritzgiessteilequalität beim spritzgiessen und spritzgiessanlage zum durchführen des verfahrens |
CN112955297A (zh) * | 2018-09-13 | 2021-06-11 | 艾姆弗勒克斯有限公司 | 用于基于实际塑料熔化压力或腔体压力来控制注射成型过程的方法 |
DE102022206727A1 (de) * | 2022-06-30 | 2024-01-04 | Baden-Württemberg Stiftung Ggmbh | Verfahren und Vorrichtung zur Prozessüberwachung während einer Herstellung eines Fertigteils aus einem heißvernetzenden Werkstoff in einem Urformverfahren |
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1995
- 1995-10-02 DE DE19536566A patent/DE19536566C1/de not_active Expired - Fee Related
-
1996
- 1996-10-02 US US09/051,069 patent/US5945046A/en not_active Expired - Fee Related
- 1996-10-02 WO PCT/DE1996/001895 patent/WO1997012740A2/de active IP Right Grant
- 1996-10-02 DE DE59602740T patent/DE59602740D1/de not_active Expired - Lifetime
- 1996-10-02 JP JP9513891A patent/JPH11512665A/ja active Pending
- 1996-10-02 AT AT96945150T patent/ATE183132T1/de active
- 1996-10-02 CA CA002233650A patent/CA2233650A1/en not_active Abandoned
- 1996-10-02 EP EP96945150A patent/EP0854778B1/de not_active Expired - Lifetime
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KUNSTSTOFFE, Bd. 77, Dezember 1987, CARL HANSER VERLAG, M]NCHEN, Seiten 1232-1236, XP002029029 RIES AACHEN STILLHARD: "Druck}bertragung beim Spritzgiessen durch verbessertes Umschalten auf Nachdruck" * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102022127260A1 (de) | 2022-10-18 | 2024-04-18 | Arburg Gmbh + Co Kg | Prozesskennzahlermittlung |
WO2024083904A1 (de) | 2022-10-18 | 2024-04-25 | Arburg Gmbh + Co Kg | Prozesskennzahlermittlung |
Also Published As
Publication number | Publication date |
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EP0854778B1 (de) | 1999-08-11 |
DE59602740D1 (de) | 1999-09-16 |
US5945046A (en) | 1999-08-31 |
JPH11512665A (ja) | 1999-11-02 |
CA2233650A1 (en) | 1997-04-10 |
WO1997012740A3 (de) | 1997-07-03 |
ATE183132T1 (de) | 1999-08-15 |
EP0854778A2 (de) | 1998-07-29 |
DE19536566C1 (de) | 1997-02-06 |
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