EP0859677B1 - Vorrichtung zum herstellen halbfester, thixotroper metallpasten - Google Patents

Vorrichtung zum herstellen halbfester, thixotroper metallpasten Download PDF

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Publication number
EP0859677B1
EP0859677B1 EP96943710A EP96943710A EP0859677B1 EP 0859677 B1 EP0859677 B1 EP 0859677B1 EP 96943710 A EP96943710 A EP 96943710A EP 96943710 A EP96943710 A EP 96943710A EP 0859677 B1 EP0859677 B1 EP 0859677B1
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EP
European Patent Office
Prior art keywords
set forth
shot sleeve
barrel
ram
temperature
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EP96943710A
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English (en)
French (fr)
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EP0859677A1 (de
EP0859677A4 (de
Inventor
Robert D. Carnahan
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Thixomat Inc
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Thixomat Inc
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    • 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
    • B22D17/30—Accessories for supplying molten metal, e.g. in rations
    • 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
    • B22D17/007—Semi-solid pressure die casting

Definitions

  • This invention relates to an apparatus for producing a thixotropic state in metallic materials in order to die cast, mold and forge these materials into articles of manufacture.
  • Metal compositions having dendritic structures at ambient temperatures conventionally have been melted and then subjected to high pressure die casting procedures. These conventional die casting procedures are limited in that they exhibit porosity, melt loss, contamination, excessive scrap, high energy consumption, lengthy duty cycles, limited die life, and restricted die configurations. Furthermore, conventional processing promotes formation of a variety of microstructural defects, such as porosity, that require subsequent, secondary processing of the articles and also result in use of conservative engineering designs with respect to mechanical properties.
  • Processes are known for forming these metal compositions such that their microstructures consist of rounded or spherical, degenerate dendritic particles surrounded by a continuous liquid phase as opposed to a classical equilibrium microstructure of dendrites surrounded by a continuous liquid phase.
  • These new structures exhibit non-Newtonian viscosity, an inverse relationship between viscosity and rate of shear, and are thus known as thixotropic materials.
  • One process requires heating of the metal composition or alloy to a temperature above its liquidus temperature and then subjecting the liquid metal alloy to a high shear rate as it is cooled into the region of two phase equilibria.
  • a result of the agitation during cooling causes the initially solidified phases of the alloy to form as rounded primary particles (as opposed to interconnected dendritic particles).
  • the primary solids are comprised of discrete, degenerate dendritic spherules surrounded by a matrix of an unsolidified portion of the liquid alloy.
  • Another method for forming thixotropic materials involves heating the metal alloy to a temperature at which most but not all of the metal is in a liquid state. The alloy is then fed into a temperature controlled zone where it is cooled to a constant temperature and agitated. The agitation of the material during cooling converts any remaining solid particles into degenerate dendritic spherules. In this method, it is preferred that when initiating agitation, the semisolid metal contain less solid than liquid.
  • US-A-5,040,589 on which pre-characterizing portion of claim 1 is based discloses an injection molding technique using metal alloys delivered in an "as cast" state.
  • the feed material is fed into a reciprocating screw injection unit where it is extemally heated and mechanically sheared by the action of a revolving screw. As the material is agitated by the screw, it is moved forward within the barrel.
  • the combination of partial melting and simultaneous shearing produces a slurry of a liquid containing discrete degenerate dendritic spherical particles, or in other words, a semisolid state exhibiting thixotropic properties.
  • the semisolid material thixotropic slurry is delivered by the screw to an accumulation zone in the barrel which is located between the extruder nozzle and the screw tip. As the slurry is delivered into this accumulation zone, the screw is simultaneously withdrawn in a direction away from the unit's nozzle. This limits the pressure build-up between the nozzle and the screw tip. Once an appropriate amount of slurry for the production of the article to be produced has accumulated in the accumulation zone, the screw is rapidly and automatically driven forward injecting the semisolid material thixotropic slurry into the die cavity and forming the desired solid article out of the semisolid thixotropic slurry.
  • An object of this invention is to allow for the use of semisolid material thixotropic slurry in an apparatus which is more recognizable to end users, such as metal part manufacturing companies.
  • Another object of this invention is to provide an apparatus which is of a conventional size as compared with previous die casting machines.
  • a further object of this invention is to provide an apparatus having an increased material capacity over prior thixotropic injection molding machines.
  • Still another object of this invention is to provide an apparatus which eliminates the need for maintaining an inventory of pre-sized billets for die casting purposes.
  • a related feature is that no longer will such pre-sized billets have to be rapidly and uniformly heated from a storage temperature to a nominal formation temperature and then physically transferred to a shot sleeve.
  • the present invention also eliminates the problems of typical die casting machines associated with shape retention of the preheated billets prior to loading of the billet into the shot sleeve.
  • Another object of this invention is to provide an apparatus which eliminates the need for physical handling or preheating of a solid charge before introduction to the shot sleeve of the die casting machine.
  • an apparatus for processing material into a thixotropic state comprising:
  • the apparatus has an extruder coupled to a shot sleeve and can be further coupled to a casting die.
  • the inlet can receive material into the barrel from a solid particulate or pelletized metal feeder, or liquid metal source, at the first temperature.
  • the outlet is adapted to transfer the material out of the barrel at the second temperature.
  • the temperature means e.g. heating elements about the barrel, serve to heat the material into the two phase region or alternatively to cool the material to the second temperature.
  • This second temperature is between the solidus and liquidus temperatures of the material wherein the material will be in a semisolid state, i.e., there is a thermodynamic equilibrium between the primary alpha solid phase and the liquid phase.
  • the shearing means can be a non-reciprocating extruder screw located within the barrel rotated to move the material through the barrel, from the inlet to the outlet, in manner which subjects the material to a mechanical shearing action as its temperature is being adjusted to the second temperature.
  • the combination of these actions produces the thixotropic structure consisting of rounded degenerate dendrites surrounded by a liquid phase within the material.
  • the shot sleeve can consist of a second heated barrel or sleeve and receives the material from the outlet of the extruder barrel.
  • the outlet nozzle of the shot sleeve may include a temperature control mechanism, although additional bands around the shot sleeve itself may prove beneficial for large capacity shot sleeves.
  • the ram may be a hydraulically actuated ram that can be preferably accelerated at velocities of up to 5 meters per second (200 inches per second)
  • the controller may be coupled to the feeder and the drive mechanism which rotates the extruder screw.
  • the controller also closes the valve means which seals the inlet into the shot sleeve during movement of the ram.
  • the valve prevents backflow of the material into the extruder during forward movement of the ram. Additionally, the valve prevents the inflow of material into the shot sleeve generally behind the ram when the ram is located between the inlet and the outlet nozzle of the shot sleeve.
  • the valve may be selected from a variety of slide gate valves or utilizing a trailing shroud or skirt on the ram, the form of which is known in the industry.
  • the invention also includes a gas and evacuation source as environment means which provides a protective atmosphere for the material while in the apparatus.
  • the protective atmosphere is non-reactive with the material and may be selected from a variety of non-reactive gases with Argon preferred for processing Mg alloys.
  • the material is forced in a die cavity defined by a two part mold including a stationary part and moveable part.
  • the shot sleeve is inclined relative to the casting die with the nozzle outlet below the inlet.
  • multiple extruders are used with a single shot sleeve to increase the charge capacity of the shot sleeve.
  • the present invention discloses an apparatus for processing materials into a thixotropic state and molding the material to form molded, die cast, or forged articles.
  • the present invention is adapted to use a room temperature feed stock of a metal or metal alloy. This eliminates the use of a melting furnaces in the die casting forging process along with the limitations associated therewith. It is also capable of accepting liquid feed stock and thus is immediately compatible with existing die cast foundry operations that might not be equipped to immediately adopt the use of solid feed stock in a chipped or pelletized form.
  • the apparatus of the present invention transforms the room temperature feed stock or liquid feed into a semisolid, thixotropic slurry which is fed as it is formed directly into the shot sleeve from which the metal is die cast molded, or forged.
  • the die casting apparatus 10 of the present invention will be seen as incorporating some features which have analogous features in conventional die casting equipment. This is actually beneficial since it allows individuals already familiar with die casting equipment to quickly become acclimated to the processing of thixotropic materials with the present invention. Furthermore, it provides the opportunity for die casting machines to be cost efficiently retro-fitted to enable the processing of materials into a thixotropic state. Principally, the apparatus 10 of the present invention includes a feeder 12, an extruder 14, a shot cylinder 16, a molding station 18 and a system controller 20 which coordinates the various operations of the other elements.
  • the feeder 12 is a gravity feeder and includes a feed hopper 22 in which the feed stock 24 is kept at room temperature.
  • the feed stock 24 is provided in either a pellet or chipped form, with the chip form being the most preferred, and is of a size within the range of 4-20 mesh.
  • One group of metal alloys which are suitable for use in the apparatus 10 of the present invention include the magnesium alloys. However, the present invention should not be interpreted as being so limited since it is believed that any metal or metal alloy which is capable of being die cast can be processed into a thixotropic state and will find utility with the present invention, in particular Al and Zinc based alloys.
  • the feed stock 24 is gravitationally discharged through an outlet orifice 26 into a volumetric feed cylinder 30.
  • a feed auger (not shown) is located within the cylinder 30 and is rotationally driven by a suitable drive mechanism 32, such as an electric motor. Rotation of the auger within the feed cylinder 30 advances the feed stock 24 at a predetermined rate for delivery to the extruder 14 through a connecting conduit 34.
  • a suitable drive mechanism 32 such as an electric motor.
  • Rotation of the auger within the feed cylinder 30 advances the feed stock 24 at a predetermined rate for delivery to the extruder 14 through a connecting conduit 34.
  • alternative delivery systems can be used where appropriate.
  • feeding can be by a robotic ladeling mechanism, by hand or by a pumping of the molten material, such as by electromagnetic or inductive pumping.
  • electromagnetic or inductive pumping can being employed, entirely obviating the need for an extruder.
  • an electromagnetic device or pump 39 of common design around a conveyance barrel 38 that connects to and delivers the slurry to the shot sleeve 16.
  • Devices of this kind are used by properly orienting and operating the electromagnetic field produced by the pump 39 to pump molten metals from one vessel to another e.g. from a feeder 30 of molten metal to the shot sleeve 16.
  • the electromagnetic field fulfills a further purpose by stirring and/or shearing the fluid which, if its temperature is allowed to drop into the two phase semisolid range, can be adjusted to alter the dendritic solid to nodular/rounded particles ratio imparting the thixotropic state to the slurry.
  • Mixing and stirring during this pumping/transfer process can be further augmented by incorporation of stationary turbulators or elements 41 on the inner diameter of the transfer barrel 38.
  • Such turbulators 41 enhance heat transfer from and to the material.
  • a preferred embodiment would come from a class of spiral vanes, alternately changing the rotation of the moving fluid from clockwise to counter-clockwise as it progresses toward the shot sleeve. This action will further benefit the establishment of the desired temperature in the semisolid material thixotropic slurry since the fluid will, in most instances, be introduced to the mechanism at or above it's melting point.
  • the conduit 34 is coupled to a feed throat 36 in a barrel 38 of the extruder 14.
  • the extruder barrel 38 defines a cylindrical passageway 40 which is lined with a sleeve 42 that increase the wear resistance of the barrel 38.
  • Suitable barrel 38 materials may include alloy 718, alloy 2888 and H21 tool steel.
  • Suitable sleeve 42 materials depend on the particular material being processed. For example, with magnesium these include cobalt-chromium alloys.
  • a rotatable extruder screw 44 Located with the passageway 40 of the barrel 38 is a rotatable extruder screw 44.
  • a helical vane 46 extends about the screw 44 and propels the feed stock 24 through the passageway 40 during rotation of the screw 44.
  • the extruder screw 44 is rotated by an appropriate drive mechanism 48, such as an electric motor.
  • the extruder screw 44 terminates in a tip 54 which is adjacent to the exit opening 56 of the passageway 40. This opening 56 in turn leads to the feed throat 58 of the shot cylinder 16 which is further described below.
  • the barrel 38 is encircled by a temperature control apparatus which causes the feed stock 24 to be heated or cooled, depending on the temperature and state at which the material 24 is introduced into the barrel 38, due to conduction through the barrel 38.
  • the temperature control apparatus can be provided with various types of heating or cooling elements in order to achieve this intended purpose.
  • heating/cooling 52 elements are representatively shown in FIG. 1 and consist of resistance band heaters or cooling coils.
  • An induction heating coil may be used in an alternate configuration to provide more rapid heat up of the barrel 38.
  • the band resistance heaters 52 are preferred in that they are more stable in operation, less expensive to obtain and operate and do not unduly limit heating rates or capacity, including cycle times.
  • the rear or aft end of the barrel 38 need not be provided with heaters. While heaters are seen in the figures, the actual number can be more or less depending on the specific application.
  • Tightly wrapped over the temperature control elements 52 is an insulative layer or blanket 50 which facilitates heat transfer through the barrel 38 to or from the melt.
  • a housing 86 can be disposed exteriorly about the length of the shot sleeve 16, but is generally not believed to be necessary.
  • the extruder 14 is rigidly mounted with respect to the shot cylinder 16.
  • the barrel 38 is provided with a radial flange 60 adjacent to the exit opening 56.
  • the flange 60 is secured by threaded fasteners 62 or other conventional fastening methods to a corresponding flange 64 adjacent the feed throat 58 of the shot sleeve 16.
  • the shot sleeve 16 includes cylindrical portion 66 which defines a passageway 70 therethrough. Suitable materials for the cylindrical portion 66 respectively include _typical shot sleeve materials of construction (tool steels).
  • the cylindrical portion 66 might also include a sleeve liner (not shown) constructed from cobalt-chromium alloys, silicon-nitride, and other materials found to give a longer useful life to the liner.
  • the feed throat 58 is generally located toward one end of the shot sleeve 16 and defines a passageway through both the barrel 66 and the liner 68. Generally located at the opposing end of the shot sleeve 16 is an outlet nozzle 72. The nozzle defines an outlet passageway 74 leading to the molding station 18.
  • an axially movable ram 76 which includes a head 78 to which is attached a rod 80.
  • Axial movement of the ram 76 is induced by an appropriate actuator 82, such as a hydraulic actuator, in which the rod 80 terminates.
  • the head 78 of the ram 76 can be advanced and retracted a distance within the passageway 70 such that, when in its retracted position, the feed throat 58 of the shot sleeve 16 is located between the head 78 and the outlet nozzle 72. In its extended or advance position, the head 78 of the ram 76 is located between the feed throat 58 and the outlet nozzle 72.
  • a blanket 85 of insulative material Positioned about the cylinder 66 and along substantially its entire length is a blanket 85 of insulative material.
  • the blanket 85 maintains the material accumulated within the passageway 70 at a temperature generally corresponding to the temperature at which the material is discharged from the extruder 14.
  • a series of heating elements similar to the band resistance heaters 52 discussed previously, can be positioned about the cylinder 66. Such heaters may prove useful with large capacity shot sleeves in the event the feed rate from the extruder 14 to the shot sleeve 16 is relatively long in comparison to conventional die casting techniques.
  • Temperature control bands 84 are also placed about the outlet nozzle to control its temperature and permit formation of a solid plug as discussed below.
  • the plug generally prevents drooling, oxygen entering into the shot sleeve 16, and also facilitates evacuation of the die of the molding station 18 when desired.
  • the barrel 66 is provided with a radial flange 88 adjacent to its nozzle end.
  • the flange 88 is secured to a stationary platen 90 of the molding station 18 by threaded fasteners 92 or another suitable fastening method. It may also have a flange and be held in position by a pair of hydraulic pulley cylinders that prevent unlatching during a shot cycle.
  • a casing 86 could be placed about the entire shot sleeve 16.
  • the stationary plate 90 cooperates with a movable platen 94 and each has respectively attached thereto a stationary mold half 96 and a moveable mold half 98.
  • Mold halves 96 and 98 include surfaces which combine to define a mold cavity 100 in the shape of the article being molded. Connecting the mold cavity 100 to the outlet passageway 74 of the nozzle are a runner 102, gate 104 and sprue 106.
  • the actuators 108 include movable rods 110, one end of which is fixedly secured to the movable platen 94 by a brace 112. Actuation of the actuators 108 causes the rods 110 to be advanced out of the actuators 108 and this in turn, through the brace 112, forces the movable platen 94 into surface-to-surface engagement with the stationary platen 90 as is generally indicated by the mold parting line 114.
  • evacuation occurs through a pair of lines 116 connected to evacuation source 118.
  • Line 116 and the evacuation source 118 can be provided with respect to either mold half 96. or 98 and one need not particularly be associated with either the stationary mold half 96 or the movable mold half 98.
  • the system controller 20 coordinates operation of the various elements of the apparatus 10 of the present invention.
  • the system controller 20 preferably includes a programmable microprocessing unit (MPU) 120 which is connected through line 122 to the drive mechanism 32 of the feeder 12, through line 124 to the drive mechanism 48 of the extruder 14, through line 126 to an actuator 140 of a slide gate 142, through line 128 to the actuator 82 of the shot sleeve 16 and through line 130 to the actuators 108 of the mold 18.
  • MPU programmable microprocessing unit
  • the system controller 20 is coupled to the gas and evacuation sources 118 and 118'and may be coupled to the induction coil heaters 50 and the band resistant heaters 52.
  • the heaters 50 and 52 are turned on to thoroughly heat the barrel 38 of the extruder 14 to the proper temperature or temperatures along its length.
  • the system controller 20 then actuates the drive mechanism 32 of the feeder 12 causing the auger within the feed cylinder 30 to rotate.
  • This auger propels the room temperature feed stock 24 into the transfer conduit 34 where a protective atmosphere is maintained by an inert gas atmosphere or evacuation source 132 connected to the transfer conduit 34 by supply line 134.
  • the source 132 and line 134 are used to introduce an inert gas, such as Argon, being provided into the environment within the extruder and shot sleeve as further described below.
  • the feed stock 24 passes through the feed throat 36 in the extruder barrel 38 where it comes into contact with the rotating extruder screw 44 which is being rotated by the drive mechanism 48 that was actuated through line 124 by the system controller 20.
  • the feed stock 24 is propelled therealong by the vane 46 of the screw 44.
  • the heat generated by the heaters 52 raises the temperature of the feed stock 24 to a temperature between its solidus temperature and its liquidus temperature.
  • the material of the feed stock 24 forms a semisolid state comprised of the liquid phase of some of its constituents in which is disposed a solid phase of other of its constituents.
  • the rotation of the screw 44 and vanes 46 induces shear into the semisolid material at a rate sufficient to prevent dendritic growth with respect to the solid particles in the semisolid material creating a thixotropic slurry.
  • the temperature induced in the slurry, as well as the shearing of the screw 44 will preferably provide for fraction solids (f S ) within the range of 0.05 f S to .66 f S in the semisolid material.
  • the feed stock 24 can be provided into the barrel 38 of the extruder 14 after having already been initially heated so that the material is in a semisolid state or in a fully molten (all liquid) superheated state.
  • the action of the screw 44 propels the material and the vane 46 induces shear to inhibit dendritic growth resulting in the thixotropic slurry.
  • the temperature control mechanism is adjusted so as to cool the material 24 from an all liquid state to a mixture of solid and liquid.
  • the thixotropic slurry is received into the shot sleeve 16 through the feed throat 58. While in the shot sleeve 16 the temperature of the slurry remains within ⁇ 5°C of the temperature of the slurry exiting the extruder 14.
  • the slurry is continuously fed into the passageway 70 by the screw 44 until an amount of slurry equivalent to that necessary for completely filling the die cavity 100 in a single shot is contained therein.
  • the system controller 20 by varying the drive inputs from the drive mechanisms 32 (in the feeder 12) and 48 (in the extruder 14) causes the proper amount of slurry to be metered into the shot sleeve 16.
  • an inert atmosphere is maintained within the passageways 70 and 40 of the shot sleeve 16 and extruder 14.
  • An inert gas, such as Argon is provided from a source 136 which communicate with the passageway 70 through lines 138.
  • the molten material entering the shot sleeve 16 will have a relatively high viscosity as the shear stress is reduced.
  • the charge will accumulate in a manner that disposes most of its mass on the bottom surface of the shot sleeve 16.
  • the system controller 20 causes the actuator 82 to advance the ram 76. Generally simultaneously with the advancement of the ram 76 and preferably slightly therebefore. the system controller 20 also slows or stops rotation of the screw 44 and causes the actuator 140 to advance the slide gate 142 so as to obstruct the exit opening 56 of the extruder 14.
  • Closing of the slide gate 142 serves two purposes including preventing the backflow of the slurry into the extruder 14 during advancement of the ram 76 and preventing the slurry from being dispensed into the shot sleeve 16 behind the advancing ram 76.
  • the ram 76 can be provided with a ram skirt or shroud 143 that will occlude the inlet throat 58.
  • the shroud 143 extends rearward from the head 78 of the ram 76 a distance which is greater than the stroke of the ram 76.
  • the shroud 143 occludes the inlet throat 58 and continues to do so until the ram 76 is again fully retracted. In this way, material is not inadvertently deposited rearward of the head of the ram 76.
  • the ram 76 is activated utilising the controller 20 to initially accelerate to a velocity of approximately 2.5 to 12.5 cm/sec (1 to 5 in/sec). This compacts the shot charge in the forward end of the sleeve 16 adjacent to the nozzle 72. The relatively slow speed permits compaction and squeezes or forces excess argon or another protective gas out of the charge space by leakage through the annular space between the ram 76 and shot sleeve 16. Immediately upon compacting the charge to a predetermined ram 76 position, the velocity of the ram 76 is rapidly increased raising the pressure to a level sufficient to blow a plug 146 from the nozzle passageway 74 into a sprue cavity 148 designed to catch it.
  • the velocity increases to a programmed level, typically in the range of 1 to 3 meters/ seconds (40 to 120 inches/second) in the case of magnesium alloys.
  • the controller 20 drops the pressure to a level as low as 10% of the steady state value achieved, and motion of the ram 76 is then arrested to reduce the pressure to zero or a negative value.
  • the controller 20 permits a wide choice of velocity profiles in which the pressure/velocity relationship can be varied by position during the shot cycle, which may typically be as short as 40 milliseconds or up to 200 milliseconds, of the ram 76, depending on the shot size.
  • the material located within the outlet passageway 74 solidifies within the passageway forming a solid plug which seals off the passageway 74. This prevents the drooling of material from the passageway 74 during opening of the mold halves 96 and 98 and removal of the molded article.
  • This opening of the mold is also synchronized by the system controller 20 which causes the actuators 108 to retract the movable platen 94 and mold 98 away from the stationary platen 90 and mold 96. This action also serves to break the sprue from the residual plug.
  • a transfer mechanism removes the molded article from the movable mold 98 and the system controller 20 then causes the actuators 108 to re-close the mold for the next operating cycle.
  • a seal is formed by an appropriate sealing mechanism 144 which is retained with one of the mold halves 96 or 98.
  • an appropriate sealing mechanism would be an O-ring variety.
  • the mold cavity is evacuated by one or both evacuation sources 118 generally creating a vacuum within the mold cavity 100.
  • the plug 146 During subsequent molding of the next article, advancement of the ram 76 will cause the plug 146 to be forced out of the outlet passageway 74 and into the sprue 106.
  • the sprue 106 extends beyond the gate 104 and is provided with a recess 148 which is intended to receive the solidified plug 146 without interfering with the flowing of the slurry through the gate 104 and runner 102 into the mold cavity 100.
  • the plug 146 After molding, the plug 146 is retained with the solidified material of the gate 104 and runner 102 and will be trimmed from the article during the subsequent trimming step.
  • the shot sleeve 16 is inclined with respect to the mold 18 as seen in FIG. 2.
  • the shot sleeve 16 is inclined at an angle A such that the nozzle 72 is positioned downward from the inlet throat 58.
  • the downward inclination of the shot sleeve 16 is from 5° to 45° out of horizontal and more preferable from 15° to 30°. This promotes movement of the slurry away from the inlet throat 58 from the extruder 14 and into the shot sleeve 16.
  • the inclination of the shot sleeve 16 causes the full charge of slurry volume to be located at the nozzle 72 end of the shot sleeve 16 before actuation of the ram 76. This further prevents the slurry charge from being forced out of the feed throat 58 and into the extruder 14.
  • the barrel 38 of the extruder 14 can be inclined relative to the shot sleeve 16 so that the barrel 38 feed throat 36 is elevated relative to its outlet opening 56.
  • the shot sleeve 16 is configured to directly deposit the thixotropic slurry into one die 96' of a forging press 18'.
  • the system controller 20 actuates an actuator, generally designated at 108', moves a movable platen 98'causing the desired article to be forged from the semisolid material thixotropic slurry.
  • FIG. 4 Another embodiment of the present invention is seen in FIG. 4.
  • two or more extruders 14 are connected to a common large capacity shot sleeve 16. Accordingly, larger artides can thus be molded without being limited by the capacity of a single extruder 14. In substantially all other respects, this embodiment operates the same as the first described embodiment.
  • the extruder can be canted at an angle B, less than 90°, relative to the axis of the shot sleeve 16 so that material 24 is directed into the shot sleeve 16 generally in the direction of the nozzle 72. This can be done with or without inclining the barrel 38 relative to the shot sleeve 16.

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  • Mechanical Engineering (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Forging (AREA)

Claims (30)

  1. Vorrichtung (10) zum Verarbeiten eines Materials zu einem thixotropen Zustand, welche Vorrichtung (10) enthält:
    ein Extruderrohr (38) mit einem Einlass (36) und einem Auslass (56), wobei der Einlass (36) an einem Ende des Rohrs angeordnet ist und geeignet ist, Material in das Rohr hinein bei einer ersten Temperatur aufzunehmen, und der Auslass (56) geeignet ist, das Material aus dem Rohr (38) herauszutransportieren;
    eine Zufuhreinrichtung (12) zum Zuführen von Material in das Rohr (38) durch den Einlass hindurch;
    eine Temperiereinrichtung (52) zum Steuern der Temperatur des Materials auf eine zweite Temperatur, bei der das Material in einem halbfesten Zustand ist, welche zweite Temperatur zwischen einer Temperatur liegt, bei der das Material fest ist und bei der das Material flüssig ist;
    eine Schereinrichtung (14) zum Einleiten einer Scherwirkung in das Material derart, dass dendritisches Wachsen gehindert wird und die Bildung sphärischer, degenerierter Dendrite innerhalb des Materials induziert wird und das Material in einem halbfesten, thixotropen Zustand gehalten wird, welche Schereinrichtung (14) das Material auch durch das Rohr (38) von dem Einlass (36) zu dem Auslass (56) bewegt;
    eine Umgebungseinrichtung (136) zum Schaffen einer Schutzatmosphäre für das in der Vorrichtung (10) befindliche Material, welche Schutzatmosphäre mit dem Material nicht reagiert;
    welche Vorrichtung gekennzeichnet ist durch:
    eine von dem Rohr (38) getrennte und verschiedene Schusshülse (16), die einen Einlass (58) und eine Auslassdüse (72) aufweist, welcher Einlass (58) insgesamt an einem Ende der Schusshülse (16) angeordnet ist und welche Auslassöffnung (72) im wesentlichen an einem entgegengesetzten Ende der Schusshülse (16) angeordnet ist, wobei der Einlass (58) der Schusshülse (16) derart angeordnet ist, dass er das Material aus dem Auslass (36) des Rohrs (38) aufnimmt;
    einen Kolben (76), der innerhalb der Schusshülse (16) für eine axiale Bewegung zwischen vorderen und hinteren Positionen angebracht ist und einen Kopf enthält und derart angebracht ist, dass, wenn der Kolben (76) in der hinteren Position ist, der Einlass (58) der Schusshülse (16) zwischen dem Kopf und der Auslassdüse (72) angeordnet ist;
    eine Betätigungseinrichtung (82) zum Hervorrufen einer axialen Bewegung des Kolbens (76) in der Schusshülse (16) zwischen den vorderen und hinteren Positionen, wodurch das Material aus der Schusshülse durch die Auslassdüse (72) ausgestoßen wird;
    eine Ventileinrichtung (142, 143) zum Schließen und Dichten des Einlasses (58) der Schusshülse (16) während der Bewegung des Kolbens (76), wodurch ein Rückfluss des Materials durch den Einlass (58) während der Vorwärtsbewegung des Kolbens (76) verhindert wird;
    eine Steuereinrichtung (20), die angeschlossen ist an die und koordiniert die Zufuhreinrichtung (12), die Schereinrichtung (44, 46), die Temperiereinrichtung (52), die Betätigungseinrichtung (82), die Ventileinrichtung (142, 143) und die Umgebungseinrichtung (136) zum Betreiben der Vorrichtung einschließlich der Zumessung einer vorbestimmten Menge des Materials in die Schusshülse (16);
    welche vorbestimmte Menge einer Menge entspricht, die von der Auslassdüse (72) während eines Zyklus des Kolbens (76) abgegeben werden kann.
  2. Vorrichtung nach Anspruch 1, wobei das Rohr (38) geeignet ist, die Materialien in einem festen Zustand aufzunehmen.
  3. Vorrichtung nach Anspruch 1, wobei das Rohr (38) geeignet ist, die Materialien in einem flüssigen Zustand aufzunehmen.
  4. Vorrichtung nach Anspruch 1, wobei das Rohr (38) geeignet ist, die Materialien in einem halbfesten Zustand aufzunehmen.
  5. Vorrichtung nach Anspruch 1, wobei die zweite Temperatur höher ist als die erste Temperatur.
  6. Vorrichtung nach Anspruch 1, wobei die Schereinrichtung (14) eine drehbare Schraube und einen Antriebsmechanismus (44, 45) zum Drehen der Schraube derart enthält, dass das Material aus dem Auslass des Rohrs (38) herausbewegt wird.
  7. Vorrichtung nach Anspruch 1, wobei die Schereinrichtung (14) eine elektromagnetische Pumpe (39) derart enthält, dass das Material aus dem Rohr (38) herausbewegt wird.
  8. Vorrichtung nach Anspruch 7, wobei das Rohr (38) in sich Elemente (41) enthält, die einen kurvigen Kanal schaffen, der die Scherung unterstützt.
  9. Vorrichtung nach Anspruch 1, wobei, wenn der Kolben (76) in einer vorderen Position ist, der Kopf (78) zwischen dem Einlass (58) der Schusshülse (16) und der Auslassdüse (72) ist.
  10. Vorrichtung nach Anspruch 1, wobei die Steuereinrichtung (20) eine Mikroprozessoreinheit (MPU) enthält, welche Mikroprozessoreinheit die Geschwindigkeit koordiniert, mit der die Schereinrichtung (14) das Material durch den Auslass (56) hindurchbewegt.
  11. Vorrichtung nach Anspruch 1, wobei die Ventileinrichtung (142, 143) einen Absperrschieber (142) enthält, der den Einlass (58) der Schusshülse (16) abdeckt, wenn sich der Kolben (76) in der vorderen Position befindet.
  12. Vorrichtung nach Anspruch 1, wobei die Ventileinrichtung (142, 143) eine an dem Kolben (76) ausgebildete Abdeckung (143) aufweist, die sich relativ zu dem Kolben (76) nach hinten erstreckt und den Einlass (58) der Schusshülse (16) abdeckt, wenn der Kolben (76) in seiner vorderen Position ist.
  13. Vorrichtung nach Anspruch 1, wobei die Schutzatmosphäre ein Edelgas enthält, wodurch eine Oxidation des Materials innerhalb der Vorrichtung verhindert wird.
  14. Vorrichtung nach Anspruch 1, wobei die Schutzatmosphäre die Bildung wenigstens eines teilweisen Vakuums enthält.
  15. Vorrichtung nach Anspruch 1, wobei die Temperiereinrichtung (52) das Material im wesentlichen auf die zweite Temperatur aufheizt, bevor das Material aus dem Rohr (38) heraustransportiert wird.
  16. Vorrichtung nach Anspruch 1, wobei die Temperiereinrichtung (52) das Material im wesentlichen auf der zweiten Temperatur hält, während das Material sich in der Schusshülse (16) befindet.
  17. Vorrichtung nach Anspruch 1, wobei die Temperiereinrichtung (52) eine Mehrzahl von Heizelementen enthält, die das Rohr (38) aufheizen können.
  18. Vorrichtung nach Anspruch 1, wobei die Umgebungseinrichtung (136) eine Stopfenformeinrichtung zum Ausbilden eines verfestigten Stopfens des Materials in der Düse (72) enthält.
  19. Vorrichtung nach Anspruch 18, wobei die Stopfenformeinrichtung einen Temperatursteuermechanismus an der Düse (72) enthält, um das darin befindliche Material nach dem Ausbilden des Gegenstandes zu kühlen und zu verfestigen.
  20. Vorrichtung nach Anspruch 1, wobei die Auslassdüse (72) mit einer Gießform gekoppelt ist.
  21. Vorrichtung nach Anspruch 20, wobei die Gießform eine Vakuumeinrichtung (118, 116) zum Evakuieren des Formhohlraums enthält.
  22. Vorrichtung nach Anspruch 21, wobei die Vakuumeinrichtung (118, 116) die Bildung eines verfestigten Stopfens des Materials in der Auslassdüse (72) enthält.
  23. Vorrichtung nach Anspruch 1, wobei die Schusshülse (16) nicht horizontal orientiert ist.
  24. Vorrichtung nach Anspruch 23, wobei die Schusshülse (16) derart orientiert ist, dass ihr Einlass (58) relativ zu dem Düsenauslass (72) angehoben ist.
  25. Vorrichtung nach Anspruch 24, wobei die Schusshülse (16) innerhalb eines Bereiches von 5° bis 45° relativ zur Horizontalen geneigt ist.
  26. Vorrichtung nach Anspruch 24, wobei die Schusshülse (16) innerhalb eines Bereiches von 15° bis 30° relativ zu der Horizontalen geneigt ist.
  27. Vorrichtung nach Anspruch 1, wobei die Auslassdüse (72) mit einem Gesenk (18') verbunden ist, welches Gesenk (18') geeignet ist, das Material aus der Schusshülse (16) in einen darin ausgebildeten Formhohlraum hinein aufzunehmen.
  28. Vorrichtung nach Anspruch 27, wobei das Gesenk (18') eine Vakuumeinrichtung zum Herstellen zumindest eines teilweisen Vakuums in dem Formhohlraum enthält.
  29. Vorrichtung nach Anspruch 27, wobei die Vakuumeinrichtung die Bildung eines verfestigten Stopfens in dem Material enthält, das innerhalb der Auslassdüse (72) angeordnet ist.
  30. Vorrichtung nach Anspruch 1, wobei die Ventileinrichtung (142, 143) einen an dem Kolben (76) ausgebildeten Rand aufweist, der den Einlass (58) zu dem Kolben (76) in der vorderen Position verdeckt.
EP96943710A 1995-12-12 1996-12-12 Vorrichtung zum herstellen halbfester, thixotroper metallpasten Expired - Lifetime EP0859677B1 (de)

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US57123095A 1995-12-12 1995-12-12
PCT/US1996/019763 WO1997021509A1 (en) 1995-12-12 1996-12-12 Apparatus for processing semisolid thixotropic metallic slurries
US571230 2000-05-16

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102218511A (zh) * 2011-04-29 2011-10-19 太原科技大学 一种制备半固态合金浆料的装置及方法
WO2013067567A1 (de) * 2011-11-10 2013-05-16 Mold-Thix-Consulting Bueltermann Gmbh Vorrichtung, anlage und verfahren zum druckgiessen von metallischem material im thixotropen zustand

Families Citing this family (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3817786B2 (ja) 1995-09-01 2006-09-06 Ｔｋｊ株式会社 合金製品の製造方法及び装置
US5983978A (en) * 1997-09-30 1999-11-16 Thixomat, Inc. Thermal shock resistant apparatus for molding thixotropic materials
US5983976A (en) 1998-03-31 1999-11-16 Takata Corporation Method and apparatus for manufacturing metallic parts by fine die casting
US6135196A (en) * 1998-03-31 2000-10-24 Takata Corporation Method and apparatus for manufacturing metallic parts by injection molding from the semi-solid state
US6250363B1 (en) 1998-08-07 2001-06-26 Alcan International Ltd. Rapid induction melting of metal-matrix composite materials
ATE213187T1 (de) * 1998-11-25 2002-02-15 Ritter Aluminium Giesserei Gmb Druckgiessverfahren zur herstellung von gussstücken aus legierungen mit thixotropen eigenschaften sowie vorrichtung zur duchführung des verfahrens
GB2354471A (en) * 1999-09-24 2001-03-28 Univ Brunel Producung semisolid metal slurries and shaped components therefrom
GB2354472A (en) * 1999-09-24 2001-03-28 Univ Brunel Manufacturing castings from immiscible metallic liquids
JP3337136B2 (ja) * 1999-09-30 2002-10-21 日精樹脂工業株式会社 金属材料の射出成形における計量方法
JP3377185B2 (ja) * 1999-09-30 2003-02-17 日精樹脂工業株式会社 金属材料の射出成形機及び射出成形方法
JP3449544B2 (ja) * 1999-12-28 2003-09-22 日精樹脂工業株式会社 金属材料の射出成形用スクリュ
DE10002670C2 (de) * 2000-01-24 2003-03-20 Ritter Aluminium Giesserei Gmb Druckgießverfahren und Vorrichtung zu seiner Durchführung
US6432160B1 (en) * 2000-06-01 2002-08-13 Aemp Corporation Method and apparatus for making a thixotropic metal slurry
CA2417822C (en) * 2000-08-11 2009-09-15 Brunel University Method and apparatus for making metal alloy castings
DE10044630A1 (de) * 2000-09-09 2002-03-21 Alu Menziken Ind Ag Menziken Verfahren zum Herstellen von Metall mit thixotropem Verhalten und Vorrichtung zur Durchführung des Verfahrens
DE10052638B4 (de) * 2000-10-24 2011-05-05 Kahn, Friedhelm, Dr.-Ing. Schmelz-und Gießverfahren zur Erzeugung hochwertiger Bauteile mit freizügiger Formgebung
DE10100632A1 (de) * 2001-01-09 2002-07-11 Rauch Fertigungstech Gmbh Verfahren zum Bereitstellen einer teilerstarrten Legierungssuspension und Verrichtungen
US20020170696A1 (en) * 2001-05-18 2002-11-21 Ron Akers Apparatus for molding metals
DE10312772A1 (de) * 2003-03-23 2004-11-11 Menges, Georg, Prof. Dr.-Ing. Verarbeitung metallischer Legierungen in einem Druckgieß- oder Spritzgießverfahren
US7509993B1 (en) 2005-08-13 2009-03-31 Wisconsin Alumni Research Foundation Semi-solid forming of metal-matrix nanocomposites
JP2009512558A (ja) * 2005-10-24 2009-03-26 ビューラー・ドルックグス・アクチエンゲゼルシャフト ダイカスト方法及びダイカスト装置
DE102006002341A1 (de) * 2006-01-18 2007-07-26 Kompetenzzentrum Neue Materialien Nordbayern Gmbh Spritzgießwerkzeug
US20080079202A1 (en) * 2006-10-03 2008-04-03 Husky Injection Molding Systems Ltd. Dryer Of Metal Molding System, Amongst Other Things
TW201729922A (zh) 2015-10-22 2017-09-01 艾克科技公司 用於壓鑄設備的壓鑄儲筒及其製造方法
CN111390139B (zh) * 2019-11-28 2021-10-29 刘兴军 一种有色金属颗粒半固态成型设备与工艺
DE102020113633B3 (de) * 2020-05-20 2021-05-20 Universität Kassel Druckgießzelle und Druckgussverfahren

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8305066D0 (en) * 1983-02-23 1983-03-30 Secretary Industry Brit Casting of material
US5040589A (en) * 1989-02-10 1991-08-20 The Dow Chemical Company Method and apparatus for the injection molding of metal alloys
JP2955863B2 (ja) * 1989-04-14 1999-10-04 新日本製鐵株式会社 金属の鋳造方法
JP3176121B2 (ja) * 1992-04-13 2001-06-11 本田技研工業株式会社 金属射出成形装置

Cited By (4)

* Cited by examiner, † Cited by third party
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WO2013067567A1 (de) * 2011-11-10 2013-05-16 Mold-Thix-Consulting Bueltermann Gmbh Vorrichtung, anlage und verfahren zum druckgiessen von metallischem material im thixotropen zustand
US9339867B2 (en) 2011-11-10 2016-05-17 Mold-Thix-Consulting Bueltermann Gmbh Device, system and method for die-casting metallic material in the thixotropic state
US9802246B2 (en) 2011-11-10 2017-10-31 Mold-Thix-Consulting Bueltermann Gmbh Device, system and method for die-casting metallic material in the thixotropic state

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EP0859677A4 (de) 1998-08-26
DE69619847D1 (de) 2002-04-18
AU1287597A (en) 1997-07-03
WO1997021509A1 (en) 1997-06-19
DE69619847T2 (de) 2002-11-07

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