Apparatus and process for producing products from pigment-containing polymer mixtures

Patent metadata

Field	Value
Publication number	US-9561613-B2
Application number	US-201113809578-A
Country	US
Kind code	B2
Filing date	Jul 13, 2011
Priority date	Jul 14, 2010
Publication date	Feb 7, 2017
Grant date	Feb 7, 2017

Abstract

The invention relates to an apparatus and a process for producing pigment-containing, in particular carbon-black-containing, polymer mixtures comprising polycarbonates and optionally elastomers, and/or other components, where the mouldings produced therefrom have, after the shaping process via injection moulding or via extrusion, improved surface properties and improved mechanical properties.

First claim

The invention claimed is:

1. An apparatus for extruding a polymer mixture, comprising an extruder having a plasticizing zone,
a barrel,
a screw, and
a die plate having a polymer melt discharge,
wherein, at least starting from the plasticizing zone of said extruder and zones subsequent thereto in a direction of conveying, to a polymer-melt discharge at the die plate, a ratio between an external screw diameter and an internal barrel diameter over a longitudinal proportion of at least 50% of the screw in a region starting from the plasticizing zone of the extruder and the zones subsequent thereto in the direction of conveying, to the polymer-melt discharge at the die plate, is smaller than 98.4%, and the sum of the external screw diameter and a screw root diameter divided by twice an axial separation between two screws is smaller than 99.1%,
wherein the polymer mixture comprises at least one pigment, and wherein the extruder is a corotating twin- or multiscrew extruder.

2. The apparatus according to claim 1 , wherein the plasticizing zone of an extruder and the zones subsequent thereto in the direction of conveying, as far as the polymer-melt discharge at the die plate, at least one conveying element is present, where, for at least one conveying element, the ratio between external screw diameter and internal barrel diameter is smaller than 98.4% and the sum of external screw diameter and screw root diameter divided by twice the axial separation between two screws is smaller than 99.1%.

3. The apparatus according to claim 1 , wherein the apparatus has, at least starting from the plasticizing zone of an extruder and the zones subsequent thereto in the direction of conveying, as far as the polymer-melt discharge at the die plate, at least one kneading element, where, for at least one kneading element, the ratio between external screw diameter and internal barrel diameter is smaller than 98.4% and the sum of external screw diameter and screw root diameter divided by twice the axial separation between two screws is smaller than 99.1%.

4. The apparatus according to claim 1 , wherein the ratio between external screw diameter and internal barrel diameter over a longitudinal proportion of at least 50% of the screw in the region starting from the plasticizing zone of the extruder and the zones subsequent thereto in the direction of conveying, as far as the polymer-melt discharge at the die plate is in the range from greater than or equal to 92.6% to smaller than 98.2%, and the sum of external screw diameter and screw root diameter divided by twice the axial separation between two screws is from greater than or equal to 95.6% to smaller than 99.1%.

5. The apparatus according to claim 1 , wherein the ratio between external screw diameter and internal barrel diameter over a longitudinal proportion of at least 50% of the screw in the region starting from the plasticizing zone of the extruder and the zones subsequent thereto in the direction of conveying, as far as the polymer-melt discharge at the die plate is in the range from greater than or equal to 96.4% to smaller than 98.2%, and the sum of external screw diameter and screw root diameter divided by twice the axial separation between two screws is from greater than or equal to 97.9% to smaller than 99.1%.

6. The apparatus according to claim 1 , wherein the ratio between the length of the extruder screw and the external screw diameter is in the range from 20 to 50.

7. The apparatus according to claim 1 , wherein the diameter of the barrel bores is in the range from 18 mm to 180 mm.

8. A process for producing a polymer mixture comprising at least one polymer, at least one elastomer and at least one pigment, the process comprising providing the apparatus according to claim 1 , and processing components of the polymer mixture in the apparatus according to claim 1 .

9. The process according to claim 8 , wherein the polymer mixture comprises the following constituents:
A) from 10 to 99.899 parts by weight aromatic polycarbonate and/or aromatic polyester carbonate and/or other thermoplastics,
B) from 0.1 to 75 parts by weight [from 0.5 to 52 parts by weight,] of elastomer,
C) from 0.001 to 10 parts by weight of one or more organic or inorganic pigments,
D) from 0 to 5 parts by weight, of one or more additives, where all of the parts by weight data have been standardized in such a way that the sum of the parts by weight of all of components A+B+C+D in the composition is 100.

10. The process according to claim 9 , wherein the thermoplastics of component A is one selected from the group consisting of polycarbonate, polyamide, polyester, polylactide, polyether, thermoplastic polyurethane, polyacetal, fluoropolymer, polyether sulphones, polyolefin, polyimide, polyacrylate, polyphenylene oxide, polyphenylene sulphide, polyether ketone, polyaryl ether ketone, styrene polymers, polyvinyl chloride, and mixtures thereof.

11. The process according to claim 9 , wherein component B used comprises at least one of the following monomers and graft bases: B.1 from 5 to 95% by weight, of at least one vinyl monomer and B.2 from 95 to 5% by weight, of one or more graft bases with glass transition temperatures <10° C.

12. The process according to claim 9 , wherein at least one pigment of component C is selected from titanium dioxide, talc, calcium carbonate, barium sulphate, zinc sulphide, zinc oxide, iron oxide, chromium oxide, other organic and inorganic colour pigments, graphite, graphene, carbon nanotubes, phyllosilicates and carbon black.

13. The process according to claim 9 , wherein said one or more additives of component D added to the polymer mixture comprise flame retardants, heat stabilizers, antioxidants, UV stabilizers and/or mould-release agents.

14. The process according to claim 9 , wherein the polycarbonate was produced by interfacial process or melt-transesterification process.

15. The apparatus according to claim 1 , wherein the ratio between external screw diameter and internal barrel diameter over a longitudinal proportion of at least 50% of the screw in the region starting from the plasticizing zone of the extruder and the zones subsequent thereto in the direction of conveying, as far as the polymer-melt discharge at the die plate, and over at least one conveying element and/or at least one kneading element, is in the range from greater than or equal to 92.6% to smaller than 98.2%, and the sum of external screw diameter and screw root diameter divided by twice the axial separation between two screws is from greater than or equal to 95.6% to smaller than 99.1%.

16. The apparatus according to claim 1 , wherein the ratio between external screw diameter and internal barrel diameter over a longitudinal proportion of at least 50% of the screw in the region starting from the plasticizing zone of the extruder and the zones subsequent thereto in the direction of conveying, as far as the polymer-melt discharge at the die plate, and over at least one conveying element and/or at least one kneading element, is in the range from greater than or equal to 96.4% to smaller than 98.2%, and the sum of external screw diameter and screw root diameter divided by twice the axial separation between two screws is from greater than or equal to 97.9% to smaller than 99.1%.

Assignees

• Derfuss Birgit
• Bierdel Michael
• Conzen Carsten
• Covestro Deutschland Ag

Inventors

• Derfuss Birgit
• Bierdel Michael
• Conzen Carsten

Classifications

• B29C48/40

  using two or more parallel screws {or at least two parallel non-intermeshing screws}, e.g. twin screw extruders · CPC title

• B29C48/405

  Intermeshing co-rotating screws · CPC title

• B29C48/2517

  of intermeshing screws · CPC title

• C08L51/04

  grafted on to rubbers · CPC title

• B29K2105/0005

  containing compounding ingredients (releasing, lubricating or separating agents B29C33/56, fibers B29K2105/08, B29K2105/12; fillers B29K2105/16, recycled material B29K2105/26) · CPC title