• 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:
    Process for the production of plastic components, in particular of composite components, using at least two components to be mixed (A, B) in a mixing chamber and a cavity formed between a first and a second half (1, 2) of a mold, the cavity forming a molding portion (3) and a sprue area (4), wherein the sprue area (4) or the molding area (3) of the cavity is used as the mixing chamber.
    公开号:AT518860A4
    申请号:T50695/2016
    申请日:2016-07-29
    公开日:2018-02-15
    发明作者:Dipl Ing Dr Reith Lorenz；Weissinger Manuel；Ing Norbert Mueller Dr；Sperneder Gerhard；Schoefer Gerald
    申请人:Engel Austria Gmbh；
    IPC主号:
    专利说明:

    The invention relates to a method for the production of plastic components having the features of the preamble of claim 1, a forming tool for use in such a method and a forming machine with such a tool.
    The cavity formed in the molding tool has a sprue area and a molding area, wherein the molding area at least at the end of the manufacturing process substantially corresponds to the shape of the finished plastic component and is located in the runner at the end of the manufacturing process of the sprue.
    In the field of reactive processing, the trend is increasingly towards the processing or production of recyclable matrix systems. Particularly noteworthy in this context is the anionic polymerization of caprolactam as an efficient lightweight construction technology.
    For the production of polyamide 6 by anionic polymerization mostly two-component systems are used, which are mixed in a ratio of 1: 1 with each other. Component 1, hereinafter referred to as the activator component, consists of caprolactam and one or more substances from the group of polymerization activators, for example hexamethylene-dicarbamoyl-caprolactam. In addition, fillers or other additives, for example, for an improvement of the flame retardant, coloring, etc. may be attached. Component 2, hereinafter referred to as the catalyst component, consists of caprolactam and a polymerization catalyst or initiator. Usual here is the use of metal salts of caprolactam.
    The high-pressure resin injection process is increasingly used for the series production of fiber composite components and is characterized by the following process steps:
    A semi-finished fiber product (also called preform) is inserted into the cavity of the forming tool and the forming tool is closed. After removing the residual air from the cavity by applying a negative pressure, the injection process begins. Here, the reactive components (e.g., polyol and isocyanate in polyurethane production) are conveyed to the mixing head where they are mixed and expelled into the cavity. The submitted fiber composite semifinished product is impregnated, then the reactive system hardens completely and after the opening of the tool, the finished fiber composite component can be removed.
    In the processing of two-component or multi-component reactive systems in the high-pressure resin injection process, the use of high-pressure counterflow mixing heads has become established in series production. Exemplary embodiments are mentioned inter alia in DE102007023239A1.
    In principle, a differentiation is made in the mode of operation of such mixing heads between different operating modes: In the recirculation mode, the respective reactive components are circulated through the mixing head, but not mixed with each other, but each returned to the metering machine via a groove on the clearing slide of the mixing head. The clearing slide thus covers the mixing chamber.
    Backward movement of the scraper allows the injection mode to be started. Here, the reactive components are atomized under high pressure and mixed in countercurrent in the now exposed mixing chamber. In this way, even with components with different properties (viscosity, surface tension, any added fillers) ensure a homogeneous mixing. To complete the injection, the material still in the mixing chamber is forced towards the cavity by movement of the scraper (cleaning ram, ...) so that the mixing chamber is completely cleaned with each injection cycle. The reactive components are now recirculated.
    The dimensioning and embodiment of the Ausräumschiebers used is primarily related to the material to be processed and its amount, so this slide can be made metallic or ceramic, often this is also additionally cured. In particular, for the processing of ε-caprolactam, however, an adapted geometry is proposed in DE3238258C2.
    In high-pressure technology, in particular in the mixing of polyurethanes, it has become established to mix the components counter to the outlet direction of the mixing head in order to maximize the flow path of the components in the mixing chamber.
    Alternatively, already integrated mixing chambers have been proposed for the mixing of reactive components for the production of solid or foamed plastic parts:
    DE1 948 999 discloses such a tool integrated mixing chamber, which is arranged in the mold parting plane. After the hardening process of the reactive components, these can be removed from the mold together with the component. The supply of the two reactive components is therefore realized such that one is passed over the top into the mixing chamber and the second component over the bottom. On Werkzeugober- and bottom, so there is a feed each.
    A comparable arrangement disclosed in DE 2 422 976, the mixing chamber is in this case also in the parting plane and can be removed from the mold with the finished component, but this is only connected via a bore (pouring hole) with the cavity.
    EP1847367A1 further discloses a corresponding mixing chamber which is described as part of the tool or also the corresponding closing unit, but this can also be operated in recirculation, comparable to a high-pressure resin injection method already described above.
    Alternatively, at low pressure mixheads, the mixing chamber may be flushed with a cleaning substance (eg, solvents or one of the reactive components) after each shot, resulting in additional waste and loss of time, which is why these methods are not used in high cycle systems with short cycle times. For the processing of polyurethanes or epoxy resins, the use of high-pressure countercurrent mixing heads has proven to be largely successful, but there are still great challenges for the use and mixing of low-viscosity reactive media:
    The biggest weak point here is certainly the sealing of the clearing slide. Here you have to work with extremely accurate tolerances in the pm range. This increases enormously the corresponding manufacturing and maintenance costs, furthermore, these systems are very error-prone. In particular, the increased trend towards the production of fiber-reinforced components with up to 55% Faservolumsanteil further leads to considerable pressures for mold filling are required and thus the corresponding seal must be guaranteed even at up to 200 bar.
    Even slight leaks in the area of the evacuation slide lead to the residual material remaining in the mixing chamber where it hardens, thus it is no longer completely cleaned and malfunctions occur during the next injection cycle.
    The Austreibvorrichtung and their drive are arranged linearly behind one another in the high pressure countercurrent mixing heads according to the prior art, which is correspondingly reflected negatively in the overall height. The latter is disadvantageous in closing units with high pressing forces in general and especially in the closing units of injection molding machines, furthermore, correspondingly generous recesses must be taken into account in the respective forming tool.
    Furthermore, mixing of the components in conventional mixing heads designed for PUR results in the dispersion of gases, which in a subsequent consequence can lead to foaming and outgassing and thus impair the surface quality of the components obtained.
    The previously disclosed approaches for using tool-integrated mixing chambers do not solve the problem of mixing and processing of low-viscosity lactam melts in a satisfactory manner.
    First of all, the arrangement of the injection nozzles should be mentioned here. As is also known in the case of high-pressure countercurrent mixing heads, the directly opposite position of the component feed or injection nozzles favors a transverse foaming of the components. This entails a considerable process risk.
    The use of a tapered mixing chamber and a transfer of the reactive mixture into the shaping cavity via a pouring hole can also be considered to be particularly disadvantageous because the rejuvenation must be applied to the required mixing and injection pressure additional pressure from the injection unit.
    In addition, especially in the production of fiber-reinforced plastic components, the previously disclosed arrangements are not readily usable: Thus, a lateral flow of the inserted fiber feeder / preform causes it to be moved in the forming tool and form fiber clusters, which are no longer due to the reactive mixture be impregnated. Furthermore, resin accumulations in the gate area due to the usually highly exothermic crosslinking reactions lead to premature curing of the material. In particular, the pouring hole openings already described above can easily clog.
    Furthermore, those arrangements in which the component feed are arranged in different halves of the mold, additional structural disadvantages: So in both halves appropriate measures for temperature insulation must be made, the space required for the supply of components is considerably increased and also provisions for nozzle control, temperature control and media management must be realized for both halves.
    In the 2K processing of ε-caprolactam components for the anionic polymerization, it has been shown that the necessary pressures for homogeneous mixing of the components are rather low due to the low processing viscosity. Furthermore, unlike with polyurethane or epoxy resin systems, once the mixture has been made, the material no longer exhibits any tendency to separate.
    Nevertheless, it is often necessary for high-quality components to achieve the highest possible internal mold pressures of up to 200 bar. Even when a correspondingly high internal mold pressure is reached, the abovementioned mixing pressure in the sprue area must still be ensured.
    In summary, it can be said that there is still considerable room for improvement in the apparatus requirements for mixing and feeding liquid reactive systems.
    The object of the invention is to provide a generic method, a mold for use in such a method and a molding machine with such a mold, in which the problems discussed above are avoided.
    This object is achieved by a method having the features of claim 1, a molding tool for use in such a method, and a molding machine having such a molding tool. Advantageous embodiments of the invention are defined in the dependent claims.
    In a first variant of the invention, the gate region of the cavity serves as a mixing chamber; in a second variant of the invention, the molding region of the cavity serves as a mixing chamber.
    The invention is particularly suitable for the production of plastic components in the form of composite components, in particular lactambasierten two-component reactive systems.
    The process according to the invention is preferably provided for reactive materials with an activator component and a catalyst component and for the production of fiber-reinforced plastic components. The following disclosure refers to such a method by way of example.
    It is therefore proposed to mix the activator and the catalyst component directly in the sprue area or in the molding area of a cavity of a forming tool.
    In the first variant of the invention, the at least two components are preferably conducted into the sprue area or the molded part area by actively actuable injection nozzles or comparable closure elements. In particular, for highly reactive systems with short curing times thus also the flow paths are considerably shortened after mixing.
    In both variants of the invention, needle valve nozzles are preferably used, the nozzle needles in the closed position sealing the component feed directly on the sprue area and in the open position an outlet opening of between 0.2 and 2 mm for the material flow into the sprue area. A particularly effective mixing of the components can be achieved if the exit of the components from the respective outlet opening is realized not as a jet but as a spray cone.
    With the use of needle valve nozzles, measures should preferably be taken to achieve a sufficiently precise adjustment of the stroke of the valve needle, in particular since the mixing pressure can also be set very precisely by the length of the stroke for a given flow velocity.
    In addition to the size of the material-supplying holes in the runner and their distance is for flow optimization of the entire runner, the angle at which meet the components in the injection, as parameters to be optimized available. This angle largely corresponds to the angle of the nozzles to each other.
    An embodiment of the sprue area is normal to the parting plane. In particular, in the production of fiber composite components, this arrangement has the considerable advantage that there is no displacement of fibers or rovings when impregnating the fabric.
    The entire sprue area is realized in one half of the forming tool and is completely filled with the reactive mixture during the process and hardens with the component. In this way, the runner hardening sprue can be removed from the mold during the process.
    Preferably, the gate area may also be implemented as an insert to provide a, e.g. on the fiber insert tuned to achieve variation of the flow velocity or the mixing pressure.
    In particular, it can be helpful for demolding to arrange an ejector directly in the sprue area.
    Preferably, a vacuum module can be arranged directly in the sprue area.
    Alternatively, it can be advantageous for the control of the process to use a pressure sensor arranged directly in the sprue area.
    The polymerization formulations used in the production of fiber-reinforced plastic components are adjusted in terms of their additives so that depending on the temperature curing times between 60 and 300s can be achieved. The heat capacity of the textile inserts used (glass or carbon fiber) has a considerable influence on the reaction profile so that the optimum curing temperature for pure resin or fiber-reinforced areas differ. Due to the resin accumulation in the sprue area, therefore, a separate temperature control of the same can be provided.
    Likewise, the media supply can be tempered separately in or on the tool to keep the thermal load of the material low, in particular, a temperature range between 90 and 140 ° C has proven itself.
    Since, depending on the arrangement in the tool, the accessibility of the sprue area can be rather difficult, it is also proposed as an option to provide a closable cleaning or rinsing line or a switchable drain hole in the sprue area.
    A method according to the invention for the production of fiber-reinforced polyamide components can be carried out in a first variant (mixing in the sprue area) as follows:
    First, a fiber insert is placed in a molding portion of a cavity of a forming tool and this closed and optionally evacuated. Then activator and catalyst component, which are provided by a metering unit with the desired pressure and flow in a molten form, fed via tempered lines the injection nozzles. With the beginning of the supply of the components, the closing nozzles are opened (this can happen shortly before, during or even shortly after the beginning of the feeding of the melt components). With the exit into the gate area, the mixing of the reactive components takes place and the mixture is expelled into the molding area of the forming tool. Here, the fiber insert is impregnated. With increasing filling level and pressure build-up in the forming tool and the sprue area is filled with reactive mixture. Upon completion of the injection, the shut-off nozzles are closed. The reactive mixture hardens under temperature. After curing, the forming tool is opened and the component with sprue can be removed. Optionally, the sprue can already be removed in the tool and the component can only be removed afterwards.
    In a second variant of the invention, the injection and mixing of the components takes place directly in the molding section.
    To mix the components, the nozzles of the mixing system are preferably introduced separately into the two halves of the mold, a nozzle is introduced in the first half and a nozzle is introduced into the second half.
    The nozzles can be directed directly towards each other or arranged at an oblique angle to each other. Likewise, the nozzles can be arranged with a defined axial offset from each other. The arrangement of the nozzles can significantly influence the mixing behavior in the mixing area.
    The mixing of the components takes place directly in the component surface. In this case, a one- or two-sided mixing dome can be formed in the mixing area. The mixing region can also be formed as a pairing of a concave and a convex mold wall. Finally, the mixing area may be smooth on both the outside and inside of the component, i. no additional geometric adjustments are made in the mixing area. The geometric behavior of the tool wall in the mixing area can also influence the mixing behavior. Thus, the resulting mixing behavior is determined by the nozzle geometry, the nozzle control, the arrangement of the nozzles to each other and the design of the tool wall in the region of the nozzle. For this purpose, interchangeable inserts can be provided in the mold.
    The mixing area can be covered with an unchanged continuous preform, i. H. It is provided in a preferred embodiment of the preform no special training in the mixing area. Alternatively, the preform can be wholly or partially thinned or recessed in the mixing area. This local adaptation of the preform can influence the mixing behavior in the mixing area.
    The advantage of the second variant of the invention is that on the one hand no clearing slide or cleaning ram is necessary, which is the end of the
    Injection displaces the remaining material in the mixing chamber. If no scraper or cleaning ram is provided in a conventional mold assembly in a mold half, then a sprue or a sprue rib o. Ä. Remain. With the solution described here, in which the injection and the mixing takes place directly in the molding area, no gate geometry remains, which would have to be separated if necessary and causes waste quantities.
    Embodiments of the invention will be discussed with reference to the figures. Show it:
    Fig. 1 is a schematic representation of an inventive
    forming machine
    Fig. 2 shows a detail of the molding tool of the molding machine of Fig. 1 in a first variant of the invention
    Fig. 3a, b shows a detail of the molding tool of the molding machine of Fig. 1 in a first variant of the invention for two different times in the manufacturing process
    4a-4e show a detail of the forming tool of the forming machine according to FIG. 1 in a second variant of the invention for different different times in the production method; FIGS. 5-8 show different embodiments of the forming tool according to the second variant of the invention
    In Fig. 1, an exemplary forming machine for producing fiber reinforced plastic components with a mold having a first and a second half 1, 2 is shown. The mold is clamped on two relatively movable mold clamping plates 6, 7. In the open mold already an insert is inserted in the form of a preform. For controlling or regulating the shaping machine, a controller 8 is provided, by way of example only two control lines are shown. Lines that carry information to the controller 8 are not shown.
    The activator component A and the catalyst component B are provided by a metering unit by means of two piston injection units 9, 10.
    Alternatively (not shown), this can also be done by a high or low pressure dosing. Via feed lines 11, 12 (for example, they are designed as material-carrying hoses outside the mold and as channels in the mold), the components A, B are directed to the injection nozzles (not shown) and further into the mixing chamber for mixing.
    FIG. 2 shows that part of the cavity (sprue area 4) which, in the first variant of the invention, functions as a mixing chamber and in which the components A, B are brought together.
    Fig. 3a, 3b shows the use of switchable by the controller 8 nozzles with closure needles 13. The direction of movement of the closure needles 13 is illustrated by arrows. 3a shows the position of the closure needles 13 in the closed state, in which case the closure needles 13 seal directly on the sprue area 4, so that there is no fluid-conducting connection between the nozzle side and the sprue area 4. 3b shows the position of the closure needles 13 during the injection, in this case the closure needles 13 are at least as far moved backwards, so that an outlet opening is exposed, through which the respective component A, B can flow into the sprue 4.
    Figs. 4 to 8 relate to the second variant of the invention, in which the molding portion 3 acts as a mixing chamber. In this case, a semifinished fiber product 5 provided in the mixing area with a passage opening 14 can be used (alternatively, the semifinished fiber product 5 could be thinned out in the mixing area). It can be formed in the mixing region, a one- or two-sided Mischkalotte 15 (see Fig .. 6 - 7). Alternatively or additionally, a convex wall region 16 may be provided (compare FIG. 8). Finally, the mixing area may be smooth on both the outside and inside, i. no additional geometric adjustments are made in the mixing area.
    Fig. 4a shows the mold in the open state. The closure needles 13 close the supply lines 11, 12.
    Fig. 4b shows the mold in the state of Fig. 4a, wherein in the mold a semi-finished fiber 5 was inserted for the production of a fiber-reinforced plastic component.
    Fig. 4c shows the mold in the closed state. The closure needles 13 close the supply lines 11, 12.
    Fig. 4d shows the mold in the closed state. The closure needles 13 have been moved away from the cavity-facing openings of the supply lines 11, 12 so far that the components A, B can be injected (FIG. 4e).
    LIST OF REFERENCES: 1 first half of the molding tool 2 second half of the molding tool 3 molding area of the cavity 4 sprue area of the cavity 5 semi-finished fiber product 6 first mold clamping plate 7 second mold mounting plate 8 control
    9 piston injection unit for component A
    10 piston injection unit for component B
    11 Feed line for component A
    12 supply line for component B 13 valve needle 14 passage opening in the semifinished fiber 15 15 formed in the mold mixing dome 16 formed in the mold convex wall area
    Innsbruck, July 29, 2016
    权利要求:
    Claims (15)
    [1]
    claims:
    A process for producing plastic components, in particular composite components, using at least two components to be mixed (A, B) in a mixing chamber and a cavity formed between a first and a second half (1, 2) of a mold, the cavity a molding portion (3) and a sprue area (4), characterized in that as the mixing chamber, the sprue area (4) or the molding portion (3) of the cavity is used.
    [2]
    2. Method according to the preceding claim, wherein in the molding portion (3) of the empty cavity a - possibly with a through hole (5) or locally thinned - semi-finished fiber (5) is inserted.
    [3]
    3. The method according to at least one of the preceding claims, wherein the sprue area (4) is filled and the filling polymerized into a gate and the sprue is demolded with the plastic component.
    [4]
    4. The method according to at least one of the preceding claims, wherein ε-caprolactam components are used.
    [5]
    5. A mold for use in a method according to at least one of the preceding claims, wherein the mold has a cavity with a mold part area (3) and a gate area (4) and a mixing chamber for mixing at least two components to be mixed (A, B), characterized in that the mixing chamber is formed by the sprue area (4) or by the molding portion (3) of the cavity.
    [6]
    6. Forming tool according to the preceding claim, wherein the molding tool feed lines (11,12) for the at least two components (A, B), which are each closed by a closure needle (13).
    [7]
    7. A mold according to the preceding claim, wherein the closure needles (13) seal directly on the sprue area (4).
    [8]
    8. A mold according to at least one of the preceding claims, wherein the molding tool has feed lines (11, 12) for the at least two components (A, B) which together with the sprue area (4) in only one of the first and second halves (1, 2) of the mold are arranged.
    [9]
    9. A mold according to at least one of the preceding claims, wherein the mold has feed lines (11,12) for the at least two components (A, B), which are thermally decoupled from the forming tool, preferably by insulation or sheaths, which are particularly preferably made of plastic or ceramic.
    [10]
    10. Forming tool according to the preceding claim, wherein for the supply lines (11,12) on the one hand and the mixing chamber on the other hand separate temperature control are provided.
    [11]
    11. A mold according to at least one of the preceding claims, wherein the gate region (4) is arranged normal to a parting plane of the first and second halves (1,2) of the mold.
    [12]
    12. Forming tool according to at least one of the preceding claims, wherein with the sprue area (4) a closable cleaning or flushing line or a switchable drain hole is connected.
    [13]
    13. Forming tool according to at least one of the preceding claims, wherein an ejector and / or a vacuum module is or are provided for the sprue area (4).
    [14]
    14. Forming tool according to at least one of the preceding claims, wherein the molding tool adjacent to the mixing chamber forming part of the molding portion (3) in one half (1,2) or two halves (1, 2) formed Mischkalotte (15) and / / or a convex wall portion (16) projecting into the molding portion (3).
    [15]
    15. Forming machine with a molding tool according to at least one of the preceding claims. Innsbruck, July 29, 2016
    类似技术:
    公开号 | 公开日 | 专利标题
    EP0137250B1|1989-05-17|Multiple nozzle for bringing together at least two free-flowing reactants forming plastic, in particular foamed plastic, in order to start the reaction by mixing, and method of operating said multiple nozzle
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    EP1144174B1|2002-08-14|Apparatus for producing injection molded parts reinforced with long fibers
    EP1771290B1|2011-01-19|Injection molding machine and injection molding method
    DE2934350A1|1981-03-12|METHOD AND DEVICE FOR GENERATING A FLOWABLE REACTION MIXTURE THAT MAKES A SOLID OR FOAM
    EP0424624A2|1991-05-02|Injection mould for pieces injected from plastifiable material, in particular from plastifiable liquid crystal polymers
    DE19632315C1|1998-05-14|Method and device for the simultaneous production of small injection molded parts from thermoplastic or crosslinking polymers
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    EP0818295A1|1998-01-14|Needle valve nozzle system for a plastic injection moulding apparatus, in particular for working silicone rubbers
    EP1855858A1|2007-11-21|Mixing head for highly viscous starting material
    EP0846050A1|1998-06-10|Injection moulding machine with integrated hot channel system
    DE102006018812A1|2007-10-25|Blending device for reactive plastic components and method for operating such a mixing device
    DE10356931A1|2005-06-30|Injection molding tool, e.g. for producing small parts with good surface finish, involves inlet valve moving into tool to also act as ejector pin
    EP0894603A1|1999-02-03|Method for injection moulding of articles
    EP3362267B1|2020-06-17|Injection moulding machine with a coating unit
    DE1124234B|1962-02-22|Injection molding machine for processing thermoplastics
    DE102011105765B4|2014-11-20|Method for injection molding of plastic molded parts made of thermoplastic material
    DE4221423A1|1994-01-05|Injection moulding of thermoplastic components - has 1 and 2 polymer storage chambers, with vol. of the 2nd chamber being variable to control flow out of 1st chamber to cavity
    DE2543877B1|1977-04-14|Device for producing molded parts from homogeneous or foam materials
    DE102021115687A1|2021-12-30|Injection unit for a molding machine and method for injection
    DE102010050231A1|2012-05-03|Injection molding apparatus used in manufacture of plastic product, has cleaning agent and plastic material supply lines which are lockably connected by purge valve which is immediately arranged after plastic material supply line
    DE10239339A1|2004-03-11|Intermediate melt storage accumulator between a plasticizing unit and a molding tool has valves to control inlet and outlet flow from the storage chamber
    同族专利:
    公开号 | 公开日
    AT518860B1|2018-02-15|
    DE102017117083A1|2018-02-01|
    US20180029312A1|2018-02-01|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3605183A|1966-12-08|1971-09-20|Du Pont|Mixing and casting lactam compositions|
    GB1165251A|1967-01-05|1969-09-24|Ankerwerk Gebr Goller|Process for Producing Dimensionally Correct Molded Parts from Caprolactam and Apparatus for Carrying Out Same|
    DE2031737A1|1970-06-26|1971-12-30|Bayer|Device for filling cavities in workpieces with foams|
    DE2252201A1|1972-10-25|1974-05-22|5090 Leverkusen|DEVICE FOR MANUFACTURING MOLDED PARTS FROM FAST-REACTING CHEMICAL COMPONENTS|
    EP0206100A2|1985-06-22|1986-12-30|Bayer Ag|Method and apparatus for making moulded articles of solid or microcellular plastic material, in particular a free-flowing reactive mixture forming polyurethane of at least two free-flowing reaction components|
    US5514322A|1992-11-20|1996-05-07|Toyota Jidosha Kabushiki Kaisha|Rim method of molding thermoplastic resin|
    AT511514A2|2011-06-09|2012-12-15|Engel Austria Gmbh|METHOD FOR PRODUCING, PARTICULARLY FIBER-REINFORCED, THERMOPLASTIC PLASTIC PARTS|
    EP2743061A1|2012-12-13|2014-06-18|Fundacion Tecnalia Research & Innovation|Device for polymerizing lactams in molds|
    DE102013203618A1|2013-03-04|2014-09-04|Bayerische Motoren Werke Aktiengesellschaft|Method for manufacturing plastic component for vehicle, involves supplying substrates with different amounts of additive or additive with varying proportions of matrix material, in form of separate dots for forming mold of component|
    BE756664A|1969-09-27|1971-03-01|Bayer Ag|DEVICE FOR THE PRODUCTION OF MOLDED PARTS FROM CHEMICAL COMPONENTS THAT REACT RAPIDLY WITH ONE ANOTHER|
    NL7405818A|1973-05-11|1974-11-13|
    DE3238258C2|1982-02-26|1984-05-17|Krauss-Maffei AG, 8000 München|Mixing head|
    DE102006018812A1|2006-04-22|2007-10-25|Krauss Maffei Gmbh|Blending device for reactive plastic components and method for operating such a mixing device|
    DE102007023239B4|2007-05-18|2010-03-11|Frimo Group Gmbh|Method and device for producing a polyurethane from at least two liquid starting components|DE102018115291A1|2018-06-26|2020-01-02|Kraussmaffei Technologies Gmbh|Method of manufacturing a composite part|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA50695/2016A|AT518860B1|2016-07-29|2016-07-29|Process for the production of plastic components|ATA50695/2016A| AT518860B1|2016-07-29|2016-07-29|Process for the production of plastic components|
    DE102017117083.9A| DE102017117083A1|2016-07-29|2017-07-28|Process for the production of plastic components|
    US15/663,143| US20180029312A1|2016-07-29|2017-07-28|Method for the production of plastic parts|
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