METHOD AND DEVICE FOR CONTINUOUSLY MODIFYING A POLYMER MELT MADE OF NON-EXTRACTED POLYAMIDE 6 WITH ONE OR MORE ADDITIVES

Abstract

A method and a device for admixing additives into a polymer melt made of non-extracted polyamide 6 are disclosed. The polymer melt is combined in a highly concentrated form with an additional melt flow without additives and mixed therewith. Additionally, a part of the melt is branched off from a main melt flow (3), wherein the sub-melt flow (4) is transported into a dispersing device (5) and is supplied and mixed with one or more additives (12). The side-melt flow (4) with additives is then returned into the main melt flow (3), mixed with the main melt flow, and subsequently supplied for further processing.

Claims

1. A process for the continuous modification of a polymer melt of non-extracted polyamide 6 (PA 6) with one or more additives, wherein a part of the melt is branched off from a main melt flow (3), this melt side-flow (4) is conveyed into a dispersing device (5), one or more additives are added and mixed, the additized melt side-flow (4) is then returned back to the main melt flow (3) where it is mixed and subsequently transported for further processing, characterized in that the melt supplied to the dispersing device (5) is conveyed into a first region and from there is conveyed by conveying elements into a second region; in the second region one or more additives are supplied via a side-feeder and wetted with the melt; the additives are dispersed and mixed in a third region, wherein for optimal dispersion kneading blocks and conveying elements are used alternately, followed by partially permeable conveying elements which are designed to rotate forwards and/or backwards; in a fourth region equipped with a closable degassing zone a degassing is performed or the melt is only conveyed; in a fifth region, which has backward-rotating and/or forward-rotating and/or neutral mixing elements, the additives are further mixed with the melt and then the additive-laden melt is discharged from the dispersing device (5) via conveying elements; and the melt which is discharged from the dispersing device (5) is conducted back into the main melt flow (3), where it is mixed statically and diluted to the final concentration.

2. The method according to claim 1, characterized in that the dispersing device (5) is a co-rotating twin-screw extruder.

3. The method according to claim 1, characterized in that the mixing elements in the fifth region are toothed discs and/or partially permeable conveying elements.

4. The method according to claim 1, characterized in that the additive is TiO.sub.2.

5. The method according to claim 1, characterized in that the rotational speed of the screws of the side feeder is adjustable independent of the rotational speed of the dispersing device (5).

6. The method according to claim 1, characterized in that the additive concentration in the melt side-flow (4) prior to the back-mixing with the main melt flow (3) is 10-30 wt. %.

7. The method according to claim 1, characterized in that the additive concentration in the main melt flow (3) after admixing the melt side-flow (4) is 0.03 to 3%.

8. The method according to claim 1, characterized in that a shear rate of 150 to 1800 sec.sup.1 is used in the dispersing device (5).

9. The method according to claim 1, characterized in that the maximum size of the additive particles in the back-mixed end product is 5 m.

10. The method according to claim 1, characterized in that the torque density of the dispersing device (5) does not exceed 10 Nm/cm.sup.3.

11. An apparatus for continuously modifying a polymer melt of non-extracted polyamide 6 (PA 6) with one or more additives, wherein a part of the melt is branched off from a main melt flow (3), this melt side-flow (4) is conveyed into a dispersing device (5) with at least five regions, one or more additives are added and mixed, thereafter the additized melt is conveyed again into the main metal flow (3), where it is mixed and subsequently conveyed to further processing, characterized in that i the melt is conveyed into a first region (13) of the dispersing device (5) equipped with conveying elements and from there is conveyed by conveying elements into a second region (14); on the second region (14) equipped with the conveying elements a side feeder is arranged, which feeds one or more additives into the dispersing device (5) and the introduced additives are wetted with the melt; in a third region (15) equipped alternately with kneading blocks and conveying elements followed by partially permeable conveying elements which are designed to rotate forwards and/or backwards, the additives are dispersed; in a fourth region (16) equipped with conveying elements or partially permeable a closable degassing device is arranged; in a fifth region (17), which has backward-rotating and/or forward-rotating and/or neutral mixing elements followed by conveying elements, the additives are further mixed with the melt and then the additive-laden melt is discharged from the dispersing device (5); and the melt which is discharged from the dispersing device (5) is conducted back into the main melt flow (3), where it is mixed statically and diluted to the final concentration, wherein the discharged melt is either directly conducted back into the main melt flow (3) for producing a single additive laden melt or is divided into multiple main melt flows which are respectively conducted into the main melt flows (7, 8) of the main melt flow (3) which is divided into multiple main melt flows for producing multiple melt flows having different additives.

12. Device according to claim 11, characterized in that the dispersing device (5) is a co-rotating twin-screw extruder.

13. Device according to claim 11, characterized in that the mixing elements in the fifth region are toothed discs and/or partially permeable conveying elements.

14. Device according to claim 11, characterized in that the rotational speed of the screws of the side feeder is adjustable independent of the rotational speed of the dispersing device (5).

15. Device according to claim 11, characterized in that the additive concentration in the melt partial flow (4) prior to the back-mixing with the main melt flow (3) is 10-30 wt. %.

16. Device according to claim 11, characterized in that the additive concentration in the main melt flow (3) after admixing of the melt partial flow (4) is 0.03 to 3%.

17. Device according to claim 11, characterized in that in the dispersing device (5) a shear rate of 150 to 1800 sec.sup.1 is used.

18. Device according to claim 11, characterized in that the torque density of the dispersing device (5) does not exceed 10 Nm/cm.sup.3.

Description

LIST OF REFERENCE NUMBERS

[0053] 1 first stage of the polymerization plant [0054] 2 second stage of the polymerization [0055] 3 main melt line [0056] 4 melt partial flow [0057] 5 disperser [0058] 6 main melt partial flow Bright [0059] 7 main melt partial flow Semi Dull [0060] 8 main melt partial flow Full Dull [0061] 9, 18 melt pump [0062] 10 extruder drive [0063] 11 twin screw [0064] 12 connection side feeder [0065] 13 first region (zone (a) and (b)) [0066] 14 second region (zone (c)) [0067] 15 third region (zone (d)) [0068] 16 fourth region (zone (s)) [0069] 17 fifth region (zone (f) and (g))