초록 ▼

In the present invention, hollow thermoplastic foam tubes of any desired diameter are easily achieved as well as large sheets or planks of thermoplastic foam material in any width and thickness desired by spirally wrapping and fusing a thermoplastic foam profile having a desired size and shape. By e

In the present invention, hollow thermoplastic foam tubes of any desired diameter are easily achieved as well as large sheets or planks of thermoplastic foam material in any width and thickness desired by spirally wrapping and fusing a thermoplastic foam profile having a desired size and shape. By employing a thermoplastic foam extruder to produce a profile having a desired cross-sectional shape or configuration, and advancing the profile onto a rotating support member for being wrapped peripherally surrounding the rotating support and continuously bonding the abutting edges of the profile as the profile is spirally wound, a unique spiral forming and product manufacturing procedure and system is realized. By employing this unique spiral forming process, a hollow cylindrical thermoplastic foam tube is formed on a continuous basis, with the length thereof being controlled only by the needs of the customer. In addition, any desired diameter can be formed, by employing one or more cooperating rotating support members having a desired diameter, with the thickness of the tube being controlled by the thickness of the profile formed by the extrusion equipment.

대표청구항 ▼

In the present invention, hollow thermoplastic foam tubes of any desired diameter are easily achieved as well as large sheets or planks of thermoplastic foam material in any width and thickness desired by spirally wrapping and fusing a thermoplastic foam profile having a desired size and shape. By e

In the present invention, hollow thermoplastic foam tubes of any desired diameter are easily achieved as well as large sheets or planks of thermoplastic foam material in any width and thickness desired by spirally wrapping and fusing a thermoplastic foam profile having a desired size and shape. By employing a thermoplastic foam extruder to produce a profile having a desired cross-sectional shape or configuration, and advancing the profile onto a rotating support member for being wrapped peripherally surrounding the rotating support and continuously bonding the abutting edges of the profile as the profile is spirally wound, a unique spiral forming and product manufacturing procedure and system is realized. By employing this unique spiral forming process, a hollow cylindrical thermoplastic foam tube is formed on a continuous basis, with the length thereof being controlled only by the needs of the customer. In addition, any desired diameter can be formed, by employing one or more cooperating rotating support members having a desired diameter, with the thickness of the tube being controlled by the thickness of the profile formed by the extrusion equipment. ange of 80,000 to 250,000. 4. A method for manufacturing thermoplastic polyester resin foam as recited in claim 1, wherein the extruded foaming resin obtained in the extrusion foaming step is in the shape of a sheet, plate or board. 5. A method for manufacturing thermoplastic polyester resin foam as recited in claim 1, wherein the melting and kneading step and moisture removing step are carried out in a twin screw extruder, and the foaming agent injecting step and extrusion foaming step are carried out in a single screw extruder. 6. A method for manufacturing thermoplastic polyester resin foam as recited in claim 1, wherein said composition further comprises fresh thermoplastic polyester resin. 7. A method for manufacturing thermoplastic polyester resin foam as recited in claim 1, wherein said recyclable thermoplastic polyester resin is a ground material. 8. A method for manufacturing thermoplastic polyester resin foam as recited in claim 5, wherein said recyclable thermoplastic polyester resin is a ground material. 9. A method for manufacturing thermoplastic polyester resin foam as recited in claim 1, further comprising modifying said recyclable thermoplastic polyester resin by a crosslinking agent before the melting and kneading step. 10. A method for manufacturing thermoplastic polyester resin foam as recited in claim 1, further comprising: a forming step for forming the thermoplastic polyester resin foam extruded and foamed in the extrusion foaming step into a formed piece of a specific shape, a cutting step for cutting off a trimming loss portion of said formed piece, a grinding and recovering step for grinding and trimming loss portion and collecting as recovered material, and a recovered material feedback step for feeding the recovered material into the melting and kneading step. 11. A method for manufacturing thermoplastic polyester resin foam as recited in claim 10, wherein the thermoplastic polyester resin is crosslinked to increase the weight-average molecular weight of the thermoplastic polyester resin. 12. A method for manufacturing thermoplastic polyester resin foam comprising: a melting and kneading step for melting and kneading a composition comprising at least one moisture-containing recycled thermoplastic polyester resin, and a crosslinking agent selected from the group consisting of an acid dianhydride, a ring-opened compound thereof, and a compound having at least three carboxyl groups, in a first stage comprising an extruder comprising at least one twin screw to obtain a molten resin, a moisture removing step for removing moisture in the molten resin by venting said molten resin under vacuum from said first stage to obtain a dehumidified molten resin, a foaming agent injecting step, for injecting a physical foaming agent into the dehumidified molten resin to modify the dehumidified molten resin into a foaming molten resin, and an extrusion foaming step for extruding and foaming the foaming molten resin into a low pressure region to obtain thermoplastic polyester resin foam, wherein said recycled thermoplastic polyester resin is PET, having a foaming index of at least 0.4, or adjusted to have a foaming index of at least 0.4, and the amount of the recycled thermoplastic polyester resin is not less than 26.8%, and up to 90.9% relative to the total amount of supplied materials except the foaming agent. 13. A method for manufacturing thermoplastic polyester resin foam comprising: a melting and kneading step for melting and kneading a composition comprising at least one moisture-containing recycled thermoplastic polyester resin, and a crosslinking agent selected from the group consisting of an acid dianhydride, a ring-opened compound thereof, and a compound having at least three carboxyl groups, in an extruder comprising at least one twin screw to obtain a molten resin, a moisture removing step for removing moisture in the molten resin by venting said molten resin under vacuum at a pressure of 20 Torr or less from said extruder to obtain a dehumidified molten resin, a foaming agent injecting step for injecting a physical foaming agent into the dehumidified molten resin to modify the dehumidified molten resin into a foaming molten resin, and an extrusion foaming step for extruding and foaming the foaming molten resin into a low pressure region to obtain thermoplastic polyester resin foam, wherein said recycled thermoplastic polyester resin is PET, having a foaming index of at least 0.4, or adjusted to have a foaming index of at least 0.4, and the amount of the recycled thermoplastic polyester resin is not less than 26.8%, and up to 90.9% relative to the total amount of supplied materials except the foaming agent. 14. A method for manufacturing thermoplastic polyester resin foam as recited in claim 13, wherein the thermoplastic polyester resin is crosslinked to increase the weight-average molecular weight of the thermoplastic polyester resin. 15. A method for manufacturing thermoplastic polyester resin foam as recited in claim 13, wherein the foaming molten resin is foamed more than three times, and the weight-average molecular weight of the thermoplastic polyester resin is increased to 80,000-250,000. 16. A method for manufacturing thermoplastic polyester resin foam as recited in claim 13, wherein the thermoplastic polyester resin foam obtained in the extrusion foaming step is in the shape of a sheet, plate or board. 17. A method for manufacturing thermoplastic polyester resin foam as recited in claim 13, wherein the melting and kneading step and moisture removing step are carried out in a twin screw extruder, and the foaming agent injecting step and extrusion foaming step are carried out in a single screw extruder. 18. A method for manufacturing thermoplastic polyester resin foam as recited in claim 13, wherein said composition further comprises fresh thermoplastic polyester resin. 19. A method for manufacturing thermoplastic polyester resin foam as recited in claim 13, wherein said recyclable thermoplastic polyester resin is a ground material. 20. A method for manufacturing thermoplastic polyester resin foam as recited in claim 17, wherein said recyclable thermoplastic polyester resin is a ground material. 21. A method for manufacturing thermoplastic polyester resin foam as recited in claim 13, further comprising modifying said recyclable thermoplastic polyester resin by a crosslinking agent before the melting and kneading step. 22. A method for manufacturing thermoplastic polyester resin foam as recited in claim 13, wherein said venting in the moisture removing step is performed by applying a pressure of 10 Torr or less. 23. A method for manufacturing thermoplastic polyester resin foam as recited in claim 22, wherein said venting in the moisture removing step is performed by applying a pressure of 4.5 or less. 24. A method for manufacturing thermoplastic polyester resin foam as recited in claim 23, wherein said venting in the moisture removing step is performed by applying a pressure of 4.5 Torr. 25. A method for manufacturing thermoplastic polyester resin foam comprising: providing at least one moisture-containing recycled thermoplastic polyester resin; grinding said recyclable thermoplastic polyester resin to obtain a ground thermoplastic polyester resin; passing said ground thermoplastic polyester resin through punch holes of a diameter to obtain sized ground thermoplastic polyester resin, wherein the diameter is 10 mm to 15 mm, a melting and kneading step for melting and kneading a composition comprising at least one moisture-containing recycled thermoplastic polyester resin, and a crosslinking agent selected from the group consisting of an acid dianhydride, a ring-opened compound thereof, and a compound having at least three carboxyl groups, in an extruder comprising at least one twin screw to obtain a molten resin, a moisture removing step for removing moisture in the molten resin by venting s aid molten resin under vacuum from said extruder to obtain a dehumidified molten resin, a foaming agent injecting step for injecting a physical foaming agent into the dehumidified molten resin, and an extrusion foaming step for extruding and foaming the foaming molten resin into a low pressure region to obtain thermoplastic polyester resin foam, wherein said recycled thermoplastic polyester resin is PET, having a foaming index of at least 0.4, or adjusted to have a foaming index of at least 0.4, and the amount of the recycled thermoplastic polyester resin is not less than 26.8%, and up to 90.0% relative to the total amount of supplied materials except the foaming agent. 26. A method for manufacturing thermoplastic polyester resin foam as recited in claim 25, wherein the thermoplastic polyester resin is crosslinked to increase the weight-average molecular weight of the thermoplastic polyester resin. 27. A method for manufacturing thermoplastic polyester resin foam as recited in claim 26, wherein the foaming molten resin is foamed more than three times, and the weight-average molecular weight of the thermoplastic polyester resin is increased to 80,000-250,000. 28. A method for manufacturing thermoplastic polyester resin foam as recited in claim 25, wherein the thermoplastic polyester resin foam obtained in the extrusion foaming step is in the shape of a sheet, plate or board. 29. A method for manufacturing thermoplastic polyester resin foam as recited in claim 25, wherein the melting and kneading step and moisture removing step are carried out in a twin screw extruder, and the foaming agent injecting step and extrusion foaming step are carried out in a single screw extruder. 30. A method for manufacturing thermoplastic polyester resin foam as recited in claim 25, wherein said composition further comprises fresh thermoplastic polyester resin. 31. A method for manufacturing thermoplastic polyester resin foam as recited in claim 25, further comprising modifying said recyclable thermoplastic polyester resin by a crosslinking agent before the melting and kneading step. 32. A method for manufacturing thermoplastic polyester resin foam as recited in claim 25, further comprising: a forming step for forming the thermoplastic polyester resin foam extruded and foamed in the extrusion foaming step into a formed piece of a specific shape, a cutting step for cutting off a trimming loss portion of said formed piece, a grinding and recovering step for grinding the trimming loss portion and collecting as recovered material, and a recovered material feedback step for feeding the recovered material into the melting and kneading step. 33. A method for manufacturing thermoplastic polyester resin foam as recited in claim 32, wherein the thermoplastic polyester resin is crosslinked to increase the weight-average molecular weight of the thermoplastic polyester resin. luorocarbon is a perfluoroketone. 17. The method of claim 16 wherein said perfluoroketone is selected from the group consisting of CF3CF2C(O)CF(CF3)2,(CF3)2CFC(O)CF(CF3)2,CF3(CF2)2C(O)CF(CF3)2,CF3(CF2)3C(O)CF(CF3)2,CF3(CF2)5C(O)CF3,CF3CF2C(O)CF2CF2CF3,CF3C(O)CF(CF3)2,perfluorocyclohexanone, and mixtures thereof. 18. The method of claim 16 wherein said perfluoroketone is CF3CF2C(O)CF(CF3)2. 19. The method of claim 15 wherein said fluorocarbon is a hydrofluoroketone that is selected from the group consisting of HCF2CF2C(O)CF(CF3)2,CF3C(O)CH2C(O)CF3,C2H5C(O)CF(CF3)2,CF2CF2C(O)CH3,(CF3)2CFC(O)CH3,CF3CF2C(O)CHF2,CF3CF2C(O)CH2F, CF3CF2C(O)CH2CF3,CF3CF2C(O)CH2CH3,CF3CF2C(O)CH2CHF2,CF3CF2C(O)CH2CHF2,CF3CF2C(O)CH2CH2F, CF3CF2C(O)CHFCH3,CF3CF2C(O)CHFCHF2,CF3CF2C(O)CHFCH2F, CF3CF2C(O)CF2CH3,CF3CF2C(O)CF2CHF2,CF3CF2C(O)CF2CH2F, (CF3)2CFC(O)CHF2,(CF3)2CFC(O)CH2F, CF3CF(CH2F)C(O)CHF2,CF3CF(CH2F)C(O)CH2F,