In the conventional plastic moulding process, plastic pellets are put into the hopper of a screw extruder that grinds and melts the plastic. Once the plastic material is up to the injection temperature it is injected by screw rotation and translation of the screw thereby injecting the molten plastic into a mould. Typically, the mould is quite hot. Once filled and cooled, the mould is opened and the now injection moulded part removed. In this prior art process the sprue, gates, flashing and defective parts are recycled by regrinding and returning them to the hopper to be re-moulded to reduce waste and therefor lower the cost of the part.
Medical plastics are very expensive per pound and may not be reground or reused beyond one heat signature. Overheated and reheated medical plastic can breakdown chemically and become toxic in medical applications. Although conventional moulding technology is capable of making medical device parts, it is not able to meet the need to form inexpensive and non-toxic parts from medical plastic. Therefore, there is a need to improve upon the prior art moulding techniques.
In contrast to the prior art, the system of the present invention begins with a precision preformed plastic pellet that is essentially equal in volume to the volume of the completed part. That is, the amount of plastic in the pellet that is to be injected, is equal to the capacity of the mould cavity. Essentially, all the plastic is displaced into the final moulded part.
Heating the single pellet is done in two stages. The preformed pellet is inserted into a nozzle and undergoes a first conductive heating process for a period of time “T” while stationary. The pellet is in intimate contact with the injector pin cavity within the nozzle. Temperature controlled electric heaters supply heat by conduction into the pellet that softens it. Next the softened pellet is quickly rammed through a small orifice where the power required to push the pellet through the hole is converted into heat in the pellet. This is the second heating step and it occurs over a time “t” shorter than the initial heating time T. The orifice is very near the mould gate and the second stage heating process both heats the plastic and fills the mould to capacity by displacing all the plastic from the injection nozzle cavity into the mould cavity.
The Process of the Invention
Overall the process is sequential and repeats as a cycle.
The process may be considered to begin with the step 1 creation of a precise sized pellet 30 from a preform 20, which is shown in detail in
In some embodiments, the pellet 30 may be pre-moulded into the required cylindrical shape, length and volume.
Next in step 2, as represented in
Next in step 3, as represented in
In the next, step 4, as represented in
In the next step 5, as represented in the flow chart of
Steps 4 and 5 occur essentially simultaneously. They are partitioned and illustrated in sequence as
Once the plastic 31 is sufficiently cool, the resultant part is removed from the mould 16, as represented in step 6 of the flow-chart of
The electrical nozzle heating system establishes a repeatable and stable temperature gradient along the nozzle, backer plate, and mould path. Typically the nozzle is the hottest element at temperature T with the backer plate a few degrees less based mostly on the amount of power exerted on the pellet to force it through the orifice. The mould is usually the coldest element in the path by intention. This process when repeated produces another part of essentially identical heat inputs. The plastic degradation is both slight and repeatable, a characteristic that is desirable for medical parts. The temperature differentials between the elements along the injection path are very well controlled and parts are made with great uniformity and reproducibility.
The Apparatus of the Invention
In furtherance of the description provided above the components of the embodiment shown in
Turning first to
In both embodiments, a pellet 30 has been loaded into the injector pin cavity that is an elongate cylindrical cavity 33 formed in the nozzle 12. The nozzle 12 carries an injection pin 42 that has a small diameter pintle nose 43 seen most clearly in
After the pellet 30 is loaded into the elongate cylindrical cavity as seen in
Next, as shown in
Alternatively, as shown in the embodiment of
The last moments of the high speed injection are shown in
In at least one instance the machine as shown in
An example of such a component is shown in
The process of forming a moulded component such as is shown in
In summary, in the various embodiments shown and described, after a relatively long thermal heating interval T an injection pin enters the nozzle and pushes the softened plastic through a small aperture along the injection path into the mould, this injection phase has a very short duration t. The amount of work done and therefore the amount additional or secondary heat supplied to the pellet is directly proportional to this time interval t. The time interval may be controlled by the air pressure supplied to the air cylinder as well as the valve duration of the controller.
The mould 16 is down stream from the heater 36 and is relatively cool therefore when the hot plastic 31 is displaced into the cold mould it very quickly cools and solidifies. By displacing essentially 100% of the plastic into a mould cavity there is no waste. Adding heat quickly along the path by forcing the plastic through the orifice into the cold mould very little time is spent at high temperature reducing chemical degradation of the plastic.
Typically, there will be a two-piece mould 16 with a parting line 40 of conventional design and contrition. However, the coldness of the mould allows the mould to be made with clearances that allow quick expulsion of air 17 from the mould by the plastic 31 without the creation of flash along the parting lines of the mould as seen at reference numeral 17 and described above.
The mould 16 itself butts up against a backer plate 14, which is in turn in contact with the nozzle 12. Placing the backer plate and nozzle in contact with each other causes the mould to warm above ambient temperature. However the tight control of nozzle temperature means that there is a tightly controlled temperature profile between these components and the mould is relatively “cold” and the temperature difference between the nozzle and the mould proper is very stable. In essence, the controlled heating within the nozzle establishes a very reproducible temperature gradient between the nozzle, pintle plate and mould structures. Although well above ambient temperature the mould is downstream thermally and is therefore “cold” by comparison.
The “cold” mould eliminates flash on the part even though the mould parting line is quite leaky to air. The plastic when it reaches the parting line of the mould “freezes” sealing the mould cavity. As described above the and during injection the injection pin pintle enters the backer plate displacing essentially 100% of the heated plastic into the mould. After a short cooling time the mould is opened and the injection moulded part is ejected. The process then repeats to create the next part.
A representative graph of the relative temperatures of the relevant components as well as the changes which occur to the pellet/material as the moulding process occurs is illustrated in
This application is a divisional application of U.S. application Ser. No. 16/100,265; filed on Aug. 10, 2018 and issued as U.S. Pat. No. 10,836,085 on Nov. 17, 2020. This application claims the benefit of U.S. Provisional Application 62/545,567 filed Aug. 15, 2017 entitled Micro Moulding Machine and Process.
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Entry |
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Mar. 26, 2020 USPTO Office Action (U.S. Appl. No. 16/100,265). |
Number | Date | Country | |
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20210053260 A1 | Feb 2021 | US |
Number | Date | Country | |
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62545567 | Aug 2017 | US |
Number | Date | Country | |
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Parent | 16100265 | Aug 2018 | US |
Child | 17089992 | US |