Method and device for the reprocessing of a thermoplastic polycondensate

• US 7,380,973 B2
• Filed: 10/30/2003
• Issued: 06/03/2008
• Est. Priority Date: 11/26/1998
• Status: Expired due to Fees

• Current Assignee: Buehler AG
• Original Assignee: Buehler AG
• Inventors: Goedicke, Frank, Innerebner, Federico
• Primary Examiner(s): SOOHOO, TONY GLEN
• Application Number:
  US10/697,661
• Publication Number:
  US 20040072920A1
• Time in Patent Office: 1,678 Days
• Field of Search: 366/83, 366/84, 366/85, 366/75, 366/76.3
• US Class Current: 366/75
• CPC Class Codes: B29B 7/485 with three or more shafts provided with screws
• CPC Class Codes: B29B 7/66 Recycling the material B29B7/566 takes precedence
• CPC Class Codes: B29B 7/826 Apparatus therefor
• CPC Class Codes: B29B 7/845 Venting, degassing or removing evaporated components in devices with rotary stirrers
• CPC Class Codes: B29B 7/86 for working at sub- or superatmospheric pressure B01F33/70 takes precedence
• CPC Class Codes: B29C 48/03 characterised by the shape of the extruded material at extrusion
• CPC Class Codes: B29C 48/29 in liquid form
• CPC Class Codes: B29C 48/43 Ring extruders
• CPC Class Codes: B29C 48/435 Sub-screws
• CPC Class Codes: B29C 48/763 Vent constructions, e.g. venting means avoiding melt escape
• CPC Class Codes: B29C 48/767 through a degassing opening of a barrel
• CPC Class Codes: B29K 2067/00 Use of polyesters or derivatives thereof, as moulding material
• CPC Class Codes: B29K 2105/26 Scrap or recycled material

Abstract

Method and device for reprocessing a thermoplastic polycondensate, in particular for the recycling of thermoplastic polycondensates, such as polyethylene terephthalate, polyester or polyamide is provided. The polycondensate is introduced into an extruder in a solid state. The polycondensate is then heated to a temperature below melting temperature and degassed or dried at below atmospheric pressure or with an inert gas added. Preferably, to prevent the polycondensate flakes from escaping through a degassing opening, a conveying device is used to convey the escaping flakes back into the extruder. The dried flakes are then melted.

Claims

1. An Extruder for the reprocessing of a thermoplastic polycondensate, comprising:

an inlet opening for introducing the polycondensate to be reprocessed in the solid state,

an outlet opening for discharging the reprocessed polycondensate in the melted state,

a plurality of closely intermeshing screw shanks, which are arranged in a barrel, extending from the inlet opening in the direction of an outlet opening and having at least a first conveying zone, for conveying the polycondensate in the solid state, a second conveying zone, for conveying the polycondensate in the melted state, and also kneading elements, arranged between the first conveying zone and the second conveying zone, for melting the polycondensate,

at least one degassing opening, provided in the barrel in the region of the first conveying zone, and

heating means for heating the barrel in the region of the first conveying zone,

wherein the barrel is divided into an inner barrel and an outer barrel and the screw shanks are arranged in an annular form between the inner barrel and the outer barrel, the screw shanks separating an outer space, formed between the outer barrel and the screw shanks, from an inner space, formed between the inner barrel and the screw shanks, and wherein, in the region of the first conveying zone, the polycondensate is located either in the inner space and the degassing opening is connected to the outer space, or the polycondensate is located in the outer space and the degassing opening is connected to the inner space, and

wherein, in the first conveying zone and in the region of the inlet opening therein, the pitch of each screw shank is reduced in the direction of the outlet opening.

2. The extruder according to claim 1, further comprising:

pressure reducing means, connected to wherein the degassing opening is subjected to a negative pressure and/or an inert gas serving for flushing purposes is carried away via the degassing opening, for (1) subjecting the degassing opening to a negative pressure and/or (2) carrying away an inert gas.

3. The extruder according to claim 2,

wherein the barrel has in the region of the first conveying zone at least one opening for the feeding in of the inert gas.

4. The extruder according to claim 1,

wherein a conveying device is provided at the degassing opening.

5. The extruder according to claim 1,

wherein the kneading elements have a total length L, the ratio L/D of the total length L of the kneading elements to the diameter D of the screw shanks lying between 1 and 2.

6. An extruder for the reprocessing of a thermoplastic polycondensate, comprising:

an inlet opening for introducing the polycondensate to be reprocessed in the solid state,

an outlet opening for discharging the reprocessed polycondensate in the melted state,

a plurality of closely intermeshing screw shanks, which are arranged in a barrel, extending from the inlet opening in the direction of an outlet opening and having at least a first conveying zone, for conveying the polycondensate in the solid state, a second conveying zone, for conveying the polycondensate in the melted state, and also kneading elements, arranged between the first conveying zone and the second conveying zone, for melting the polycondensate, and

at least one degassing opening, provided in the barrel in the region of the first conveying zone,

wherein the barrel is divided into an inner barrel and an outer barrel and the screw shanks are arranged in an annular form between the inner barrel and the outer barrel, the screw shanks separating an outer space, formed between the outer barrel and the screw shanks, from an inner space, formed between the inner barrel and the screw shanks, and wherein, in the region of the first conveying zone, the polycondensate is substantially located either in the inner space and the degassing opening is connected to the outer space, or the polycondensate is substantially located in the outer space and the degassing opening is connected to the inner space, and

wherein, in the first conveying zone and in the region of the inlet opening therein, the pitch of each screw shank is reduced in the direction of the outlet opening.

7. The extruder according to claim 6,

wherein the barrel has in the region of the first conveying zone at least one opening for the feeding in of the inert gas, and

wherein the at least one opening for the feeding in of the inert gas is separate from and in addition to both the inlet opening and the at least one degassing opening.