Process for producing polyester composition

• US 5,833,905 A
• Filed: 08/29/1997
• Issued: 11/10/1998
• Est. Priority Date: 08/30/1996
• Status: Expired due to Term

• Current Assignee: Diafoil Hoechst Company, Limited
• Original Assignee: Diafoil Hoechst Company, Limited
• Inventors: Miki, Takatoshi
• Primary Examiner(s): Acquah, Samuel A.
• Application Number:
  US08/920,007
• Time in Patent Office: 438 Days
• Field of Search: 525/437, 524/777, 524/401, 264/211.12, 264/211.21, 264/239, 264/299
• US Class Current: 264/211.21
• CPC Class Codes: B29C 2793/009 after shaping
• CPC Class Codes: B29C 48/08 flexible, e.g. films
• CPC Class Codes: B29C 48/288 in solid form, e.g. powder or granules
• CPC Class Codes: B29C 48/29 in liquid form
• CPC Class Codes: B29C 48/40 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
• CPC Class Codes: B29C 48/55 having reverse-feeding elements
• CPC Class Codes: B29C 48/76 Venting , drying means; Degassing means
• CPC Class Codes: B29C 48/767 through a degassing opening of a barrel
• CPC Class Codes: B29C 48/914 cooling drums
• CPC Class Codes: B29C 48/9165 Electrostatic pinning
• CPC Class Codes: B29K 2067/00 Use of polyesters or derivatives thereof, as moulding material
• CPC Class Codes: B29K 2105/0005 containing compounding ingredients releasing, lubricating or separating agents B29C33/56, fibers B29K2105/08, B29K2105/12; fillers B29K2105/16, recycled material B29K2105/26
• CPC Class Codes: B29K 2105/06 containing reinforcements, fillers or inserts
• CPC Class Codes: C08K 5/098 Metal salts of carboxylic acids
• CPC Class Codes: C08K 5/14 Peroxides
• CPC Class Codes: C08L 67/00 Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain of polyester-amides C08L77/12; of polyester-imides C08L79/08; Compositions of derivatives of such polymers

Abstract

The present invention relates to a process for producing a polyester sheet comprising melt-extruding a polyester resin by using a vent-type twin-screw extruder in sheet-wise onto the surface of a rotating chilling drum under the condition satisfying the following formula (1):

5.2×10.sup.-6 ×D.sup.2.8

≦Q/N≦15.8×10^-6 ×D².8 (1)

wherein D mm represents the inner diameter of the extruder cylinder, Q kg/hr represents the extrusion rate per unit time and N rpm represents the screw number of revolution.

Claims

1. A process for producing a polyester sheet comprising melt-extruding a polyester resin by using a vent-type twin-screw extruder in sheet-wise onto the surface of a rotating chilling drum under the condition satisfying the following formula (1):

space="preserve" listing-type="equation">5.2×

10.sup.-6 ×

D.sup.2.8 ≦

Q/N≦

15.8×

10.sup.-6 ×

D.sup.2.8 (

     1)

wherein D mm represents the inner diameter of the extruder cylinder, Q kg/hr represents the extrusion rate per unit time and N rpm represents the screw number of revolution.

2. The process according to claim 1, wherein the inner diameter of the extruder cylinder is not less than 150 mm.

3. The process according to claim 1 using a substantially undried polyester.

4. The process according to claim 1, wherein the drop of intrinsic viscosity of said polyester resin after melt extrusion is not more than 10% based on the intrinsic viscosity of the polyester before melt extrusion.

5. The process according to claim 1, which further comprises supplying said polyester resin and a slurry of inorganic and/or organic particles.

6. The process according to claim 5, wherein said polyester resin and said slurry are supplied to a same material feed opening of the extruder.

7. The process according to claim 5, wherein said slurry comprises the inorganic and/or organic particles and water used substantially as medium.

8. The process according to claim 1, wherein said polyester resin has not lower than 1×

10^-7 Ω

cm of a specific resistance when melted, a metal salt of an aliphatic monocarboxylic acid or dicarboxylic acid in amount of 0.5 to 1,000 ppm, calculated as metallic atom, based on the polyester resin, is simultaneously supplied with said polyester to the extruder, and the molten polyester sheet extruded onto a rotating chilling drum from the extruder is closely adhered to the surface of said chilling drum by use of an electrostatic pinning technique.

9. The process according to claim 8, wherein said metal salt is magnesium decanedicarboxylate.

10. The process according to claim 8, wherein said metal salt is magnesium monocarboxylate.

11. The process according to claim 8, wherein the surface speed of said rotating chilling drum is not lower than 40 m/min.

12. A process for producing a polyester sheet comprising

using a vent-type twin-screw extruder,

using a polyester resin having not lower than 1×

10^-7 Ω

cm of a specific resistance when melted as starting material,

supplying said polyester and a metal salt of an aliphatic monocarboxylic acid or dicarboxylic acid in amount of 0.5 to 1,000 ppm, calculated as metallic atom, based on the polyester resin, and

closely adhering the molten polyester sheet extruded onto a rotating chilling drum from the extruder to the surface of said chilling drum by use of an electrostatic pinning technique.

13. The process according to claim 12, which further comprises supplying said polyester resin, said metal salt and a slurry of inorganic and/or organic particles.

14. The process according to claim 13, wherein said polyester resin and said slurry are supplied to a same material feed opening of the extruder.

15. A process for producing a polyester sheet by using a vent-type twin-screw extruder, comprising conducting a melt-extrusion by supplying a polyester and a slurry of inorganic and/or organic particles to a same material feed opening of said extruder.