Plastic and nonmetallic article shaping or treating: processes – Direct application of fluid pressure differential to... – Including hydrostatic or liquid pressure
Reexamination Certificate
2002-03-22
2004-03-23
McDowell, Suzanne E. (Department: 1732)
Plastic and nonmetallic article shaping or treating: processes
Direct application of fluid pressure differential to...
Including hydrostatic or liquid pressure
Reexamination Certificate
active
06709625
ABSTRACT:
RELATED APPLICATION
This application claims priority to German Application 101 14 419.9, filed on Mar. 23, 2001, the entire teaching of which are incorporated herein by reference.
BACKGROUND OF THE INVENTION
An injection molding process used in the manufacture of molded parts from thermoplastic plastic is known, for example from U.S. Pat. No. 4,101,617. A fluid under pressure is introduced into the still molten plastic melt. The melt is pressed against the cavity wall of the injection-molding die by the pressure thus produced in the interior of the melt; collapsed points due to contraction of volume during cooling are thus avoided.
Nitrogen gas is conventionally used as the fluid, which is injected into the melt under pressure. It has the advantage that as an inert gas, it is not subjected to a chemical reaction in the hot melt. The disadvantage is thus taken into account that the nitrogen is in most cases very expensive to produce. Either the injection-molding device has to be supplied with nitrogen from cylinders or the gas is recovered on site—for greater gas requirement—for example, by means of molecular filters.
The requirements increasing ever further on the economic viability of the process necessitate ever shorter injection-molding cycles with as high as possible quality of the molded parts to be manufactured. In order to achieve the shorter cycles, various attachments have been made:
European granted patent 0 400 308 proposes, after gas injection into the melt, to allow the gas to emerge again at a point remote from the point of injection; circulation of the gas through the cavity provided is then effected. A cooler is integrated into the gas circuit. A more rapid cooling process for the melt should thus be effected, since cooled gas is supplied in the closed circuit.
German Offenlegungsschrift 4 219 915, however, is geared to using cooled gas, which is injected into the melt. Provision is thus made, namely, in that the gas is cooled to temperatures as far as −160° C. The plastic material should cool as rapidly as possible in this manner; the time span from injection of the melt into the injection-molding die to releasing is thus reduced.
SUMMARY OF THE INVENTION
In the previously known processes, it is disadvantageous that, firstly now as before, expensive nitrogen is necessary, and secondly in spite of all measures, the cooling effect remains limited due to the restricted thermal capacity of the gas. Regardless of that, due to the considerable difference in viscosity between melt and gas, there is the problem that flow markings appear now and then on the surface of the molded part, which negatively influence the quality of the molded part to be manufactured.
One aspect of the invention is therefore to further develop the injection-molding process of the generic type, so that the disadvantages are avoided at least in part. The process should thus make it possible to manage without the use of expensive nitrogen. Furthermore, as short as possible a cooling time should be realizable, which noticeably shortens the injection-molding process. Finally, the process should also ensure that as homogeneous as possible a flow path of the melt into the injection-molding die takes place, so that transfer markings can be avoided as far as possible.
In one embodiment, a process is provided for injection molding of molded parts made from thermoplastic plastic material having at least one cavity. This process includes the injection of plastic melt from an injection unit along a melt flow path into a cavity of an injection-molding die in step a). Liquid is injected in step b) into the still molten plastic material so that the latter is pressed against the walls of a cavity, and the plastic material is then allowed to solidify in step c) until the latter forms the molded parts in a self-supporting manner. The molded part is then released in step d) from a cavity of the injection molding die. After injecting the plastic melt in step a) and after injecting the liquid in step b), both the melt flow path and a flow path via which the liquid is injected are closed. The releasing step in this embodiment only takes place when the injected liquid has transferred at least partly to a gaseous state of aggregation. Before releasing the molded part from the cavity, pressure in the interior of the molded part is relieved.
A core concept of the invention is thus geared to using a liquid having high thermal capacity as fluid to be injected into the melt, wherein this ensures that a rapid cooling process takes place, so that the cycle time of the injection-molding cycle can be noticeably reduced. Use is made here of the high thermal absorption during the change in the state of aggregation, by means of which the internal pressure is additionally increased.
Any group of thermoplastics, regardless of whether they are provided with additives, such as glass fibers, chemical or physical propellants or similar, is provided here as plastic material.
During this procedure, it has been shown, surprisingly, that due to the said features, flow markings hardly appear, which are otherwise to be feared and to be observed during the gas-internal pressure process. This is attributed to the comparable viscosity of the liquid melt with the injected liquid of high thermal capacity.
According to a first further development, provision is made in that during the above process step b), some of the still molten plastic material is displaced from the cavity into a spillover cavity. The flow of plastic material from the cavity into the side cavity is thus, in one embodiment, controlled by valve means, which are opened or closed according to a temporal model. Specific influencing of the overflow of melt from the main to the side cavity is thus possible. Furthermore, it is conceivable to use several side cavities, which are controlled independently of one another.
The liquid can be injected into the cavity along the melt flow path through the sprue region directly or via the machine nozzle, through which the plastic melt is supplied, or alternatively to that into the cavity directly by means of an injection nozzle, wherein when the requirement is to form several cavities, a separate injection nozzle is provided for each cavity.
In the second case, it can be advantageous if some of the plastic material situated in the cavity is driven back out again from the cavity during the above step b) by the injected liquid in the direction of the injection unit.
A further improvement in the flow behavior of the melt or the control of this behavior can be seen when, before injection of the thermoplastic plastic melt, a pressure which is increased with respect to the ambient pressure is built up in the cavity by introducing a gas. This gas pressure can be controlled and/or regulated during the above step a) as a function of how the injection pressure of the melt increases during its injection. In one embodiment, the gas pressure is operated according to a predetermined pressure or time profile. It can thus be let down gradually, but also suddenly.
It has proved to be a particularly advantageous embodiment that the liquid is tempered before injection into the still molten plastic material. The thought here is namely that the liquid is cooled to a preset temperature range. A temperature range between about −20° C. and +20° C., in a particular embodiment between about 4° C. and 15° C., is thus provided particularly advantageously. However, it can also be necessary, for example, for materials which are damaged by sudden cooling, to heat the liquid to a preset temperature range. A temperature range between about 20° C. and 150° C., in a particular embodiment between about 40° C. and 100° C., is thus provided particularly advantageously.
At the temperature ranges indicated above, the use of water was thought of first and foremost. However, it is also conceivable to use, for example, liquefied gases, such as carbon dioxide or nitrogen, in order to particularly strengthen the cooling effect. When using such liquids, a temperature rang
Battenfeld GmbH
Hamilton Brook Smith & Reynolds P.C.
McDowell Suzanne E.
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