• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A nozzle ring of an extruder for blowing tubular plastics film is divided into cooling sectors provided with adjusting elements. The thicknesses of the blown film are measured over the circumference thereof and a number of film sectors of equal circumferential length corresponding to the number of cooling sectors is established. Assuming that the film sector of maximum or minimum thickness has been extruded in the correct position for the purpose of determining the cooling sector associated with the film sector, the subsequent film sectors are in turn allocated to successive cooling sectors. The mean thickness distributions are determined from the measurements over the individual film sectors. Those cooling sectors to which film sectors were allocated having thin or thick portions exceeding a respective thin or thick portion threshold value which is a fraction of the value of the film sector with the absolute minimum or maximum thickness, respectively, are cooled or heated until the film thicknesses are within the permissible tolerance range.
    公开号:SU1187707A3
    申请号:SU802999195
    申请日:1980-10-29
    公开日:1985-10-23
    发明作者:Упмайер Хартмут；Клинге Герд；Винклер Герхард
    申请人:Виндмеллер Унд Хельшер (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to methods for adjusting the film thickness in an apparatus for producing a film by extrusion and can be used in chemical and petrochemical industries. The purpose of the invention is to increase the efficiency and accuracy of regulation. FIG. 1 shows an installation for producing a film by blow molding with a device for measuring thickness tolerances in a schematic side view; in fig. 2 is a communication diagram of a measuring device and actuators in the cooling sectors on the nozzle ring I in FIG. 3 is a quantitative picture of the comparison of individual film sectors to the cooling sectors, located on the nozzle ring. The method is carried out at the facility (Fig. 1 and 2). The thermoplastic melt is fed by an extruder 1 through a connecting element 2 to the blow head 3 of the installation, equipped with a cooling ring 4. In the blow head 3, it is converted into a film sleeve 5. At the level of the film hardening line 6, a film sizing device 7 is placed, which specifies the diameter of the film sleeve 5, as well as the width of the tape. Using flat-placed plates 8, the film sleeve 5 becomes flat, stretches through the exhaust device — exhaust rollers 9, as well as the reversing rollers following them, and then, in the form of a flat ribbon 10, is guided by guide rollers 11 to a stationary winding device - winding device 12. A measuring head 14 is located above the calibration device 7 on the annular yoke 13, and the arrow of the measuring head 14 moves in the direction of the sterling shown in FIG. 1, 2, at + 360 °. In order to avoid affecting the measurement result of the twisting of the film sleeve 5, which occurs due to the reverse movement of the film sleeve 5 before measurement and during the measurement, the reverse movement of the film sleeve 5 is stopped for a short time. This stop does not affect the measurement accuracy, since the speed of the annular yoke 13 and the measuring head 14. is much higher than the speed of the flat-facing plates 8 and the exhaust rollers 9. To measure the film thickness profile, the reverse movement is flat. The lying plates 8 and exhaust rollers 9 in order to remove the twist angle of the blown film sleeve 9 are briefly stopped and after a short stop, the duration of which depends on the speed of drawing of the film sleeve 5, the annular traverse 13 is actuated and the measuring head 14. Then the flat-bottom the plates 8 and draw rollers 9, and interrupting the reversible cement does not affect the quality of the roll. The measuring head 14 for measuring the elemental thickness of the film sleeve 5 can be located, for example, also at position 15, adjacent to the flat-lying plates 8,. or behind the pull rollers 9 on the edge of the flat tape 10 at position 16, in which case the double film thickness is measured, which can be used with sufficient accuracy to determine the thickness of the flat-lying film tape. The measuring signal is sent from the measuring head 14 via the measuring line 17 (the latter has a loop 17 that allows reversing movement) into the dashboard 18 dp of displaying the thickness profile readings and recording them on the diagram 19. The electrical measuring signal on line 20 can be entered to a microprocessor 21, which appropriately converts this signal along the connecting lines 22 22, ...,. sends a command to move executive bodies 23 in cooling sectors X, 4 After (fig. 3), as measuring head 14 makes one revolution, are formed in accordance with the number of cooling sectors X film, Xp sectors, and for each film sector the average thickness Sj is determined. These mean values, thicknesses § determine
    3
    parameters of the command signal to the cooling sectors X.
    In the exemplary embodiment (FIG. 3), the nozzle ring is divided into twelve cooling sectors. From the midpoints of the cooling sectors, designated I to XII, there are dashed lines that correspond to the progress lines of individual points of the extruded mass. Thick sections of the film correspond to the converging lines 24, and thin streaks correspond to the diverging lines 25. In the expansion area (Fig. 3) of the inflatable tubular film 5, the lines are reduced to a single diameter of the film, so that the mass points in the film area with zero tolerance The thickness passes along parallel lines 26, which, however, are inclined due to the presence of adjacent thick and thin sections.
    From the Y and X cooling sectors, extruded films are thick or thin films, as indicated by parallel lines. The measuring profile is indicated by line 27.
    Plot with a minimum thickness of Xtnin It is placed in the middle of the film sector and belongs to sector X of cooling, on which it can be projected. Other film sectors of equal length relate to film sectors with thin sections 28.
    For individual film sectors, the average thicknesses are determined, which determine the magnitude of the command signal if the average film thickness exceeds the threshold value, which is the fractional part of the thickness extremum. The cooling sectors corresponding to the film sectors, which lie beyond the thresholds of values and thickenings or thinning, are cooled or heated simultaneously, as the film sectors are formed with the same length, and the average film thickness for individual sectors is determined by the measurement results, and the cooling sectors corresponding to film sectors with thin sections, the thickness of which exceeds the threshold value for the thickness of the thin section of the film, which is a fractional fraction of the absolute minimum value the thickness of the film sector is cooled
    877074
    until the film crowd reaches a value in the range of acceptable values.
    The invention is based on the fact that the sectors of the extruded film with thin sections have the greatest influence on the lateral movement of the adjacent film sectors. Especially fast adjustment at
    10, the deviation of the thickness of the film from the allowable thickness can be achieved as a result of the thin sections of the film being covered and eliminated. After the elimination of all thin
    15 places around the sleeve of the film inevitably establish an average thickness. In order to eliminate thin areas. According to the invention, sector-based cooling is used, since
    20, it contributes to a simple and rapid increase in the viscosity of the extruded mass, which leads to a thickening of the film and, consequently, to the elimination of thin spots.
    25 According to the proposed method, using actuators, the effect is only on the cooling sectors, which include film sectors with thin sections.
    3Q films whose thickness exceeds a certain threshold value.
    Thus, the cooling sectors, which correspond to film sectors with thin sections, the thickness of which is below the threshold value, do not receive a control pulse, so that the film sectors that are not yet oriented with respect to the cooling sectors, which are
    slightly deviates from the allowable values, there is no effect.
    With the progressive elimination of thin parts of the film, the film sectors are more accurately aligned with certain cooling sectors. Since the threshold value, depending on the circumstances, is only a certain percentage of the minimum thickness and decreases in proportion to this value to zero, the film sectors with increasingly thin sections are also covered by regulation, so that the cooling sectors related to them receive the appropriate command for thermal conditions.
    Since, as a result of an automatic increase or decrease in the winding speed of the film, the average value of the film thickness is kept constant, therefore, the number of sections with a thick film also gradually decreases to zero.
    Determining the threshold for thin spots is necessary because only one reduction in the corresponding minimum film thickness could not lead to any result.
    As soon as the minimum thickness decreases to the thickness value of the next thinner section, this means that there is no unambiguous minimum thickness, therefore, thin spots can be affected only when determining the threshold thickness value. Since this threshold value is variable, the adjustment becomes more accurate. In the same way, you can adjust the thickness of the thick sections of the film sleeve.
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    Fig.Z
    权利要求:
    Claims (2)
    [1]
    1. METHOD FOR REGULATING THE FILM THICKNESS IN THE INSTALLATION FOR PRODUCING FILM BY THE BLOWING METHOD WITH EXTRUDER equipped with a nozzle ring divided into cooling sectors connected with actuators, calibration, exhaust and winding devices for the film, which consists in measuring the film thickness of the extrudable film sleeve, corresponding to the number of cooling sectors, film sectors of equal length are formed around the sleeve perimeter and the average value of their thickness is determined by measuring individually film sectors, the film sector with the minimum or maximum thickness is taken to determine the related cooling sector on the nozzle ring as correctly extruded, and the next film sectors having the same length are brought into correspondence with the following cooling sectors, the temperature of which is changed until uniform distribution of thickness around the circumference of the film sleeve, characterized in that, in order to increase the efficiency and accuracy of regulation, as Cooling adjusted is selected sectors corresponding with the sectors film thinned or thickened portions whose values exceed a threshold value corresponding to the absolute extremum thickness portion, and is cooled or heated to provide the allowable value of the film thickness.
    [2]
    2. The method according to p. 1, characterized in that the cooling sectors corresponding to the film sectors, the thicknesses of which lie beyond the Threshold values of thickenings or "thinning", are cooled or heated simultaneously.
    SU ... 1187707
    1187707.
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    同族专利:
    公开号 | 公开日
    FI803702L|1981-06-13|
    FI74235C|1988-01-11|
    FI74235B|1987-09-30|
    IT1134105B|1986-07-24|
    JPS5693519A|1981-07-29|
    FR2471269A2|1981-06-19|
    US4351785A|1982-09-28|
    DE2950003A1|1981-06-19|
    FR2471269B2|1984-09-07|
    GB2067312A|1981-07-22|
    CH650973A5|1985-08-30|
    BR8007933A|1981-06-16|
    IT8025663D0|1980-10-30|
    GB2067312B|1984-08-30|
    CA1153173A|1983-09-06|
    JPH0551451B2|1993-08-02|
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    引用文献:
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    US3474160A|1965-04-27|1969-10-21|Industrial Nucleonics Corp|Method and apparatus for controlling blown film extruder|
    US3438088A|1967-01-19|1969-04-15|Beloit Corp|Control for maintaining uniform gauge on blown film|
    US3557351A|1967-04-12|1971-01-19|Industrial Nucleonics Corp|Property measurement signal filtering method and apparatus for eliminating predetermined components|
    CA988265A|1970-07-17|1976-05-04|Hartmut Upmeier|Flattening and take-off apparatus for blown tubular plastics film|
    US3751537A|1970-01-12|1973-08-07|Owens Illinois Inc|Process for controlling dimensions of the product in foamed plastic extrusion|
    DE2232930A1|1971-07-06|1973-02-01|Hepworth Plastics Ltd|METHOD AND DEVICE FOR THE PRODUCTION OF PIPES OF EQUAL WALL THICKNESS IN THE EXTRUSION PROCESS|
    DE2553069C3|1974-11-27|1981-05-27|Teijin Ltd., Osaka|Slot nozzle for producing a polymer film of uniform thickness|
    FR2321229B1|1975-08-13|1980-02-08|Cit Alcatel|
    DE2721609C2|1977-05-13|1986-07-10|Reifenhäuser KG, 5210 Troisdorf|Control device for a plant for the production of blown plastic films|
    DE2816583A1|1978-04-17|1979-10-18|Windmoeller & Hoelscher|METHOD AND DEVICE FOR OPTIMIZING THE OUTPUT PERFORMANCE OF A BLOWED FILM EXTRUDER SYSTEM USING A PROCESS COMPUTER|
    US4209475A|1978-10-20|1980-06-24|Mobil Oil Corporation|Method and apparatus for effecting uniform film thickness|DE3002903C2|1980-01-28|1986-12-04|Windmöller & Hölscher, 4540 Lengerich|Method for controlling the film thickness on a blown film extruder|
    DE3014989C2|1980-04-18|1991-01-24|Windmöller & Hölscher, 4540 Lengerich|Method for controlling the film thickness on a blown film extruder|
    DE3311345C2|1983-03-21|1986-02-20|RSM Regel-, Steuer- und Messtechnik GmbH, 4000 Düsseldorf|Process for keeping the wall thickness constant when extrudingelongated objects from thermoplastics, such as foils, pipes, hoses, cable sheathing, plates and profiles and measuring and regulating devices for extruders, extrusion presses or the like for elongated objects|
    US4517145A|1983-11-07|1985-05-14|American Hoechst Corporation|Extrusion die and process for thickness control|
    DE8501177U1|1985-01-18|1986-05-22|Alpine Ag, 8900 Augsburg|Pull-off device for plastic tubular films|
    DE3518155C2|1985-05-21|1987-11-12|Reifenhaeuser Gmbh & Co Maschinenfabrik, 5210 Troisdorf, De|
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    US4760627A|1987-03-23|1988-08-02|Enrique Schele|Apparatus for an oscillating pinch roll assembly utilized in the extrusion of blown films|
    DE8707626U1|1987-05-27|1987-08-13|Alpine Ag, 8900 Augsburg, De|
    DE4013610C2|1989-10-26|1992-05-21|Reifenhaeuser Gmbh & Co Maschinenfabrik, 5210 Troisdorf, De|
    DE4036868A1|1990-11-19|1992-05-21|Windmoeller & Hoelscher|Thickness meter for blown film tubing - is mounted on ring round tubing and above extruder nozzle, and is rotated independently of speed of rotating or reversing extruder head|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE2950003A|DE2950003C2|1979-12-12|1979-12-12|Process for regulating the film thickness on a blown film extruder|
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