This invention relates to an extrusion screw having an mixing section.
The mixing of molten plastic with additives including colorants is an important step prior to extruding the molten plastic into an extruded shape by means of a die or prior to injecting molten plastic into a mold during an injection molding process. Typically, plastic pellets and various additives are fed into the feed of an extrusion machine which typically includes a barrel and an extrusion screw which rotates within the barrel. Typically, the barrel is a precise cylindrical bore having heated walls. The screw is typically an elongated auger like member having a generally cylindrical screw root and a continuous helical ridge or “flight” which projects from the body. The helical flight presents a narrow (typically about 1 cm in width), continuous flat surface which is preferably closely offset from the inside wall of the barrel. Preferably, the flight is configured so that the extrudate does not flow between the flight and the inside wall of the barrel but, rather, is “wiped” from the inside wall. The extrudate is typically a combination of plastic pellets, partially melted plastic pellets, molten plastic and possibly additives. The proportions of unmelted plastic and molten plastic vary depending on whether the extrudate is near the intake or near the outlet. A channel is defined between the turns of the flight. This channel conveys the extrudate down the length of the barrel as the extrusion screw turns within the barrel. In most cases, the extrusion screw includes a feed section in which the depth of the channel is generally constant and relatively deep (on the order of 15 mm for a 100 mm diameter screw), a transition section in which the depth of the channel decreases and a first metering section wherein the depth of the channel is reduced (on the order of 7 mm for a 100 mm diameter screw) and constant. The depth of such a channel is known in the art as the “root depth”. Typically, the inside wall of the barrel includes a heating band for melting the plastic pellets into a highly viscous molten plastic material. In order to accomplish thorough mixing, extrusion screws often include a mixing section. The purpose of a mixing section is to mix the molten plastic and additives as much as possible prior to a second metering section which forces the extrudate either into a die or an injection mold.
The present extrusion screw includes an mixing section. The mixing section has an inlet end for receiving extrudate and an outlet end for discharging extrudate. The mixing section includes a mixing section root, wiping lands and barrier lands. The mixing section root is generally cylindrical in shape. The wiping lands and the barrier lands are arranged on the mixing section root in an alternating fashion and are arranged to describe helixes as they extend from the inlet end to the outlet end. The wiping lands have outside surfaces which generally match the wall of the extrusion barrel. There is an offset between the outside surfaces of the barrier lands and the wall of the extrusion barrel. The wiping lands have a greater helix angle than the barrier lands. The wiping lands and the barrier lands define inlet channels which narrow toward the outlet end. The barrier lands and the wiping lands also define outlet channels which widen toward the outlet end.
Mixing channels are cut into the wiping lands and the barrier lands. The mixing channels are arranged to define helixes which are oriented generally at right angles to the wiping lands and the barrier lands. Accordingly, the mixing channels present channel wall surfaces that are oriented approximately at right angles to the wiping lands and the barrier lands. Because of this opposing orientation of the mixing channel wall surfaces in relation to the wiping lands and the barrier lands, a portion of the extrudate flowing from the inlet end to the outlet end changes direction when that portion of the extrudate encounters the inside wall surfaces of the mixing channels. This alteration of direction of a portion of the extrudate causes increased mixing of the extrudate.
Referring to the drawings,
Extrusion screw 2 as shown in
As can be seen in
As can be seen in
Because barrier lands 50 have a greater helix angle than wiping lands 30 when considered in the direction of rotation R, the alternating spaces between barrier lands 50 and wiping lands define inlet channels 34 which decrease in width from the inlet end to the outlet end. In this example embodiment, inlet channels 34 decrease in depth from the inlet end to the outlet end. Thus, since inlet channels 34 are wider and may also be deeper at the inlet end, inlet channels 34 are relatively open to the flow of extrudate at their inlet ends and relatively closed to the flow of extrudate at their outlet ends. Accordingly, each inlet channel 34 presents a first channel area at (when considered on a plane which is normal to axis A) at its inlet end which is greater than a second channel area at its outlet end.
Similarly, also because barrier lands 50 have a greater helix angle than wiping lands 30, the alternating spaces between barrier lands 50 and wiping lands 30 when considered in the direction opposite from the direction of rotation R define outlet channels 54 which increase in width from the inlet end to the outlet end. Further, outlet channels 54 may also increase in depth from their inlet ends to their outlet ends. Accordingly, because the cross section areas of outlet channels 54 (when projected on a plane normal to axis A) increase between their inlet ends and their outlet ends, outlet channels 54 are relatively closed to the flow of extrudate at their inlet ends and relatively open to the flow of extrudate at their outlet ends.
As can be seen in
In this example, as can be best seen in
The skilled reader may be able to imagine how the various surfaces of the wiping lands, barrier lands and mixing channels might interact with the extrudate as extrudate progresses through mixing section 10. As mixing section 10 rotates in direction R, extrudate will be pushed down inlet channels 34 and over barrier lands 50 and into outlet channels 54. As this flow from inlet channels 34 into outlet channels 54 occurs, the positive large helix angles of wiping lands 30 and barrier lands 50 and the direction of rotation R causes wiping lands 30 and barrier lands 50 to spiral from the inlet end toward the outlet end consistent with the general direction of the flow of the extrudate thereby forcing the extrudate to generally flow from the inlet end toward the outlet end and also from the inlet channels into the outlet channels in an Archimedian fashion. However, the negative helix angle of mixing channels 60, causes the mixing channels to progress in a direction that is at least partially opposite from the flow direction of the extrudate when mixing section 10 is turned in direction of rotation R. Consequently, as extrudate flowing from inlet channels 30 to outlet channels 50 encounters mixing channel surfaces 68, a portion of the extrudate is redirected in a direction that is different from the remainder of the extrudate and this different direction may be understood, at least in relative terms, as if that portion of extrudate is counter-flowing in relation to the remainder of the extrudate. This redirection of a portion of the extrudate significantly enhances the mixing of the extrudate as it passes through mixing section 10.
The skilled reader will readily appreciate that the above described mixing section 10 provides an extrusion screw with significant advantages. The mixing of extrudate is significantly enhanced by presenting flights of mixing channels arranged at a helix angle which is roughly at right angles to the wiping lands of the mixing section in order to present mixing channel surfaces which progress in a counter-flow fashion as the mixing section rotates. Extrudate which encounters the mixing channel surfaces moving in a counter-flow direction, changes direction thereby enhancing the mixing of the extrudate.
It is to be understood that while certain forms of this invention have been illustrated and described, it is not limited thereto, except in so far as such limitations are included in the following claims and allowable equivalents thereof.
This application is a continuation of U.S. Non-provisional patent application Ser. No. 14/600,852 filed on Jan. 20, 2015, which is incorporated herein by reference. U.S. Non-provisional patent application Ser. No. 14/600,852 claimed the benefit of U.S. Provisional Patent Application No. 61/928,855 filed on Jan. 17, 2014, which is incorporated herein by reference.
Number | Name | Date | Kind |
---|---|---|---|
3486192 | Le Roy | Dec 1969 | A |
3587450 | Smith et al. | Jun 1971 | A |
3652064 | Lehnen | Mar 1972 | A |
3788614 | Gregory | Jan 1974 | A |
3941535 | Street | Mar 1976 | A |
4085461 | Maillefer | Apr 1978 | A |
4227870 | Kim | Oct 1980 | A |
4330214 | Willert | May 1982 | A |
4405239 | Chung | Sep 1983 | A |
4639143 | Frankland, Jr. | Jan 1987 | A |
4752136 | Colby | Jun 1988 | A |
4944906 | Colby | Jul 1990 | A |
4964730 | Alzner | Oct 1990 | A |
5215764 | Davis | Jun 1993 | A |
5318357 | Colby | Jun 1994 | A |
5816698 | Durina | Oct 1998 | A |
6497508 | Womer | Dec 2002 | B1 |
6547431 | Womer | Apr 2003 | B1 |
7014353 | Womer | Mar 2006 | B2 |
7032843 | Johnson et al. | Apr 2006 | B1 |
20040141406 | Womer et al. | Jul 2004 | A1 |
20110222363 | Mazzocca | Sep 2011 | A1 |
20150298356 | Williams | Oct 2015 | A1 |
Entry |
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Indian Office Action for Application No. 3765/KOLNP/2015 dated Apr. 24, 2019. |
Number | Date | Country | |
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20180126596 A1 | May 2018 | US |
Number | Date | Country | |
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61928855 | Jan 2014 | US |
Number | Date | Country | |
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Parent | 14600852 | Jan 2015 | US |
Child | 15704763 | US |