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Method for producing extruded resin sheet

A technology of resin boards and resins, applied in applications, household appliances, and other household appliances, etc., can solve the problems that the extruded resin board is difficult to peel off from the roller, the resin board needs time to cool down, and the production efficiency is reduced.

Active Publication Date: 2009-06-10
SUMITOMO CHEM CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Simply increasing the temperature of the second or third roll to prevent the extruded resin sheet from cooling rapidly will cause problems such as the resin sheet taking time to cool and the extruded resin sheet being difficult to peel off the roll
As a result, productivity may decrease

Method used

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  • Method for producing extruded resin sheet
  • Method for producing extruded resin sheet
  • Method for producing extruded resin sheet

Examples

Experimental program
Comparison scheme
Effect test

Embodiment

[0081] Hereinafter, the present invention will be described in more detail with reference to Examples, but the present invention is not limited to the Examples. The composition of the extrusion equipment used in the following examples and comparative examples is as follows:

[0082]Extruder 1: screw diameter 100 mm, single screw, with vent (manufactured by Hitachi Zosen Corp);

[0083] Extruder 2: screw diameter 35 mm, single screw, with vent (manufactured by Hitachi Zosen Corp);

[0084] Feed manifold: Class 2 2-layer distribution (manufactured by Hitachi Zosen Corp);

[0085] Die 3: T-shaped die, lip width 1500 mm, lip gap 1 mm (manufactured by Hitachi Zosen Corp);

[0086] Rolls: Horizontal, three cooling rolls with a length of 1600 mm and a diameter of 300 mm.

[0087] Extruder 1, 2 and die 3 press figure 1 As shown in the arrangement, the feed diverter block is arranged at the specified position. Three cooling rolls, ie, first, second and third rolls named sequential...

Embodiment 1、2、4~11 and comparative example 1、2、5~12

[0118]

[0119] Resins of the kinds shown in Tables 1 and 2 were melt-kneaded in an extruder 1, and then sent to a feed manifold and a die 3 in sequence. Then, the molten thermoplastic resin 4 extruded through the die 3 is passed between first to third rolls to be molded and cooled. Extruded resin sheets having thicknesses shown in Tables 1 and 2 were thus obtained.

[0120] In the subcolumn of "Between the second and the third roller" in the "Roll configuration" column in Tables 1 and 2, the term "adhesion under pressure" refers to the The thermoplastic resin is further sandwiched between the second and third rolls to be shaped and cooled while being wound on the second roll. The term "releasing" means that the thermoplastic resin after being sandwiched between the first and second rolls is wound on the third roll to be molded and cooled without being sandwiched between the second and third rolls. The "surface temperature of the first roll", "the surface temperature of th...

Embodiment 3、12、13 and comparative example 3、4、13、14

[0122] Resins of the kinds shown in Tables 1 and 2 were melt-kneaded in an extruder 1 as a resin layer A, and then sent to a feed manifold. On the other hand, resins of the kinds shown in Tables 1 and 2 were melt-kneaded in the extruder 2 as the resin layer B, and then sent to the feed manifold. Co-extrusion molding was carried out so that the resin layer A sent from the extruder 1 to the feed manifold formed the main body layer, and the resin layer B sent from the extruder 2 to the feed manifold formed the surface layer (one side / upper side).

[0123] Then, the molten thermoplastic resin extruded through the die 3 is passed between the first to third rolls to be shaped and cooled. Extruded resin sheets of a double-layer structure having thicknesses shown in Tables 1 and 2 were thus obtained. "Thickness" in the column of extruder 1 and "thickness" in the column of extruder 2 in Tables 1 and 2 represent the thickness of the resin layer A and the thickness of the resin layer ...

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Abstract

Disclosed is a method for producing an extruded resin sheet comprising: heat-melting a thermoplastic resin and then extruding it into a sheet-form through a die; pressure-forming the extruded molten thermoplastic resin with a first roll and a second roll; and further pressure-forming the formed resin with the second roll and a third roll while wrapping the formed resin around the second roll, wherein the first roll is a roll having an outer circumferential surface of metal, the second roll is a highly rigid metal roll, and the third roll is an elastic roll having a metal thin film at its outer circumferential surface. The present invention provides a method for producing an extruded resin sheet with excellent appearance.

Description

technical field [0001] The present invention relates to a method for producing an extruded resin sheet, in particular to a method for producing an extruded resin sheet having an excellent appearance. Background technique [0002] Extruded resin sheets made of thermoplastic resins have been used in an extremely wide variety of applications such as lighting equipment, signboards, building materials, home appliances, and optical applications including portable phones, liquid crystal televisions, and monitors. Generally, in the production process of an extruded resin sheet made of thermoplastic resin, molten thermoplastic resin is shaped into a sheet-like form while pressurizing and cooling it by squeezing it between two rolls. During this process, if the cooling rate is too high, strain may remain in the produced resin sheet. Therefore, devices that provide one or more rolls after the second roll and perform stepwise pressurization and cooling operations have been manufactured...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B29C47/90B29C47/92B29L7/00B29C48/40B29C48/90B29C48/92
CPCB29K2105/0008B29K2105/005B29C2043/467B29K2105/0026B29C47/0004B29C43/24B29C47/0021B29K2105/0032B29C43/52B29K2105/256B29C47/40B29C47/043B29K2995/0022B29L2009/00B29C47/8845B29C2043/468B29C47/065B29K2105/0044B29C43/46B29C43/222B29K2101/12B29C48/92B29C2948/92704B29C48/022B29C48/08B29C48/17B29C48/21B29C48/40B29C48/914B29C48/9155B29C48/9185B29C2948/92923B29C48/00
Inventor 前川智博畠山和彦
Owner SUMITOMO CHEM CO LTD