Screw extrusion press as well as conveying and mixing method for processing thermoplastic and not reticulating polymers

Information

  • Patent Application
  • 20070263479
  • Publication Number
    20070263479
  • Date Filed
    May 07, 2007
    17 years ago
  • Date Published
    November 15, 2007
    17 years ago
Abstract
A screw extrusion press for processing thermoplastic and not reticulating polymers comprises a conveying screw (1) in a cylinder (2). The screw comprises a conveying zone (7) and a mixing zone with 10 mixing rings (3). These mixing rings comprise a passage hole (5) that extends from the bottom (10) of the screw to the vicinity of the cylinder wall (20) where it opens out into a shear gap (9).
Description

The invention will be explained hereinafter with reference to a plurality of exemplary embodiments. In the drawing:



FIG. 1 shows a section through a cylinder arrangement of a screw extrusion press with a view of the screw; and



FIGS. 2-9 show different sectional views of embodiments of a mixing ring.





As shown in FIG. 1, a screw 1 is disposed in a cylinder 2 of a screw extrusion press, said screw comprising three mixing rings 3 and a conveying zone 7 with individual screw channels 8. The mixing rings 3 extend from the bottom of the screw, which is indicated at 10, to a shear gap 9 at the wall indicated at 20 of the cylinder 2. The width of the shear gap 9 may for example be about 1 mm in the radial dimension.


According to FIG. 2, a mixing ring 3 comprises a groove 4 that commences at the bottom 10 of the screw and extends as far as the shear gap 9. The groove on the inflow side 11 of the mixing ring 3 is thereby completely open, whilst the outflow side 12 is closed except for the shear gap 9. The flow direction of the molten mass is indicated at 13.


In the implementation shown in FIG. 3, the groove 4, which is milled in the radial direction, is completely open on the inflow side 11 and partly closed on the outflow side 12 so that here the molten mass comprises a larger outflow cross section than in the implementation according to FIG. 2, where only the shear gap 9 remains to form the outflow port.


Although the reference numeral 4 indicates a groove in the special case, it is understood to refer generally to a passage hole of any configuration.


In the embodiments shown in the FIGS. 4 through 8, one passage hole is configured to be a bore 5.



FIG. 4 shows an oblique arrangement of the bore 5 extending from the bottom 10 of the screw as far as the shear gap 9. Accordingly, this bore ends in the perimeter region of the mixing ring 3.


In the illustration shown in FIG. 5, the bore 5 ends on the outflow side 12. Here also, the bore commences at the bottom 10 of the screw on the inflow side 11. It is noted though, that the bore 5 shown in FIG. 5 constitutes an additional bore that is configured on the mixing ring 3. On same mixing ring there is also provided a passage hole (not shown), which opens out at least partially in the shear gap.


In FIG. 6, the bore ends partly on the outflow side 12 and partly in the shear gap 9, with the bore 5 again commencing at the bottom 10 of the screw on the inflow side 11.


Another variant may be achieved in that the sectioned portion shown on the top right side of FIG. 6 and which bounds the flow channel 5 toward the shear gap is advanced radially outward or is provided with a projection extending radially outward so that the shear gap 9 is configured to be very narrow toward the inflow side 11, more specifically even sealing it. This may for example be achieved in that the shear gap is so restricted there that it acts as a seal gap. In such a configuration, when viewed in the direction of the flowing molten mass, meaning from the inflow side 11 to the outflow side 12, there is first provided a seal gap (not shown) on the circumference of the mixing ring, and then, further downstream, a shear gap 9 into which the passage hole opens out.



FIG. 7 shows an inflow side comprising, in its upper part, a portion 14 extending at right angles to the screw axis and a portion 15 extending at an incline to the screw axis. The bottom of the screw is provided with a notch 16 from which the bore 5 extends at right angles to the screw axis and ends in the shear gap 9 which comprises a flaring portion 6 when viewed in the flow direction.


In the illustration shown in FIG. 8, the mixing ring 3 is inclined with respect to the screw axis, meaning that the inflow side 11 is inclined at an acute angle with respect to the axis of symmetry of the screw, whilst the outflow side 12 is inclined at an obtuse angle with respect to the axis of symmetry of the screw. In this exemplary embodiment, the bore 5 extends from the bottom 10 of the screw at an incline to the wall 20 of the cylinder, part of the bore ending in the shear gap 9 and another part of the bore ending on the outflow side 12.



FIG. 9 shows a configuration of the mixing ring according to FIG. 2 in which, on the inflow side, the shear gap, which is slightly larger than the shear gap 9 in FIG. 2, is closed with a sealing ring 21 so that the shear gap 9 remaining for the molten mass is shorter.

Claims
  • 1. A screw extrusion press for processing thermoplastic and not reticulating polymers, with a conveying screw (1) having a conveying zone (7) and a mixing zone with a mixing ring (3) that extends from a bottom (10) of the screw to a wall (20) of the cylinder, said mixing ring (3) comprising passage holes (4, 5), wherein a shear gap (9) is formed between an outer perimeter wall of the mixing ring (3) and the cylinder wall (20) and that at least one passage hole (4, 5) extends from the bottom (10) of the screw or from the vicinity thereof and opens out, at least in part, in said shear gap (9).
  • 2. The screw extrusion press as set forth in claim 1, wherein the shear gap (9) varies in height (6) in the flow direction.
  • 3. The screw extrusion press as set forth in claim 1, wherein the shear gap is sealed (21) on an inflow side (11) of the mixing ring (3).
  • 4. The screw extrusion press as set forth in claim 1, wherein the passage hole (4) comprises a groove (5) that is open on an inflow side (11) of the mixing ring (3) and that opens out into the shear gap on an outflow side (12).
  • 5. The screw extrusion press as set forth in claim 1, wherein the passage hole (4) comprises a groove (5) that is open on an inflow side (11) of the mixing ring (3) and that is partially closed on an outflow side (12).
  • 6. The screw extrusion press as set forth in claim 1, wherein a cross section of the passage hole (4) varies with regard to both its size and its shape in the flow direction.
  • 7. The screw extrusion press as set forth in claim 1, wherein a cross section of the passage hole (4) decreases in the flow direction.
  • 8. The screw extrusion press as set forth in claim 1, wherein when a plurality of passage holes (4) are spaced on a circumference of a mixing ring (3), these passage holes vary in cross section and shape about the circumference.
  • 9. The screw extrusion press as set forth in claim 1, wherein the passage hole (4, 5) extends at an acute angle with respect to an axis of the screw when viewed in the flow direction.
  • 10. The screw extrusion press as set forth in claim 1, wherein the passage hole (4, 5) extends at right angles with respect to an axis of the screw when viewed in the direction of the flow.
  • 11. The screw extrusion press as set forth in claim 1, wherein a passage hole is configured to be a bore (5).
  • 12. The screw extrusion press as set forth in claim 11, wherein the bore (5) opens out into the shear gap (9).
  • 13. The screw extrusion press as set forth in claim 12, wherein the bore (5) ends in parts in the shear gap (9) and in parts on the outflow side (12) of the mixing ring (3).
  • 14. The screw extrusion press as set forth in claim 1, wherein wall margins on the inflow side (11) and on the outflow side (12) of a mixing ring (3) are inclined at an angle different from the right angle with respect to an axis of symmetry of the screw extrusion press (1).
  • 15. The screw extrusion press as set forth in claim 1, wherein, if a plurality of mixing rings (3) are arranged on a screw extrusion press (1), these mixing rings (3) have different configurations as set forth in any one of the aforementioned claims.
  • 16. A method of conveying and mixing a thermoplastic and not reticulating polymer, a conveying screw (1) with a conveying zone and with a mixing zone with a mixing ring (3) being utilized for conveying and mixing, said mixing ring (3) extending from a bottom (10) of the screw to a cylinder wall (20) of the screw extrusion press and the polymers being mixed by conveying them through passage holes (4, 5) on the mixing ring (3), wherein the polymers are conveyed through at least one passage hole toward a shear gap and flow axially past at least part of the mixing ring (3) along the shear gap (9), said shear gap being formed between an outer perimeter wall of the mixing ring (3) and the cylinder wall (20).
Priority Claims (1)
Number Date Country Kind
10 2006 022 123.0 May 2006 DE national