JP4113026B2 - Thermoplastic resin composition foamed molding method - Google Patents
Thermoplastic resin composition foamed molding method Download PDFInfo
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- JP4113026B2 JP4113026B2 JP2003099717A JP2003099717A JP4113026B2 JP 4113026 B2 JP4113026 B2 JP 4113026B2 JP 2003099717 A JP2003099717 A JP 2003099717A JP 2003099717 A JP2003099717 A JP 2003099717A JP 4113026 B2 JP4113026 B2 JP 4113026B2
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- gas
- pressure
- molding method
- injection molding
- thermoplastic resin
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- Injection Moulding Of Plastics Or The Like (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、発泡ガスを射出成形機に供給し、溶融した熱可塑性樹脂に混練・溶解させた後キャビティ内に射出することで、発泡した成形体を得る射出成形方法に関する。
【0002】
【従来の技術】
熱可塑性樹脂を用いた射出成形方法において、材料削減、軽量化等を目的として発泡を行うことが従来から検討されてきており、射出発泡成形を行う方法として、材料の熱可塑性樹脂に、熱分解型の化学発泡剤をマスターバッチとして使用する方法、また成形機のシリンダに物理発泡剤すなわち超臨界流体や発泡ガスを注入する方法が知られている。
発泡ガスを注入する方法として、低圧で射出成形機に発泡ガスを供給することで外観良好な、高発泡倍率の成形品を得る射出発泡方法が特開2002−79545公報に提案されている。
【0003】
しかしながら、従来の発泡ガスを注入する方法は、通常の射出成形機と同等長さのスクリュを用いると、発泡ガスを混練・溶解する二段目の計量・可塑化部の長さが短くなり、注入ガスと溶融樹脂の溶解・混練が十分行われないため、ガスと溶融樹脂が分離し、目的とする発泡成形品を得ることはできなかった。
従来の物理発泡射出成形装置のようにスクリュの先端にガスの含浸部分を付加しようとすると、付加の分だけスクリュの全長が長くなり、既存のシリンダを使用できないばかりでなく、成形機の全長も伸ばすための大幅な改造を行う必要が有った。また、このような物理発泡成形機においてはより多くのガスを溶解させるため、供給される発泡ガスの圧力に対し背圧は低く設定される。
しかし、既存シリンダを使用した一般的長さのスクリュを持つ物理発泡射出成形機において、背圧を供給ガス圧より低く設定すると混練・溶解が完全に行われない状態で計量が行われ、溶融樹脂と発泡ガスが分離したまま射出が行われ、成形品ができなくなるという現象が発生する。
【0004】
【本発明が解決しようとする課題】
本発明の目的は、物理発泡の従来技術の問題点であるスクリュ長さが既存長さのスクリュを持つ射出成形機において、外観の良い射出成形品を得るための射出発泡成形品を提供することにある。
【0005】
【課題を解決するための手段】
本発明の熱可塑性樹脂成形品の成形装置は、成形機のシリンダ内にて熱可塑性樹脂を溶融状態にする可塑化工程と、溶融状態になった熱可塑性樹脂に、ガス供給口から発泡ガスを供給してガスを混練・溶解させるガス供給溶解工程、得られたガス溶解溶融樹脂から発泡成形品を得る成形工程をもつ射出発泡成形機で、ガス供給・溶解の工程に用いられるスクリュが二段圧縮構造を成し、一段目で熱可塑性樹脂の可塑化を行いその下流で容積を拡大することにより溶融樹脂圧力をガス供給圧力より低下させるガス供給部と供給された発泡ガスと溶融樹脂を混練・溶解させる成形機を用いて、二段目圧縮部から計量部に掛けて、ガス供給圧力より高い圧力を持たせる事を特徴とする。
これにより、既存のシリンダと既存長さのスクリュを用いた場合でも、供給するガス圧より背圧を0.1〜5.0MPa高くすることにより既存のスクリュの全長を変更することなく可塑化時のガスの混練・溶解性を改善することが可能となり、発泡ガスと溶融樹脂の分離が防止され、良好な成形品を得ることができる。
【0006】
【実施例】
以下に、実施例、比較例を用いて本発明をより詳細に説明する。
なお、本発明実施例では、各測量は以下の方法によって行った。
(1)最大セル径:発泡体の発泡部断面を顕微鏡で観察し、セル50個のセル径を求め、その中で大きい順に選んだ10個の平均値を最大セル径とした。セルが楕円形の場合は(長径+短径)/2をセル径とした。
(2)平面性:成形品表面に光源を反射させ、成形品表面の凹凸の有無を確認した。
(3)シルバーストリーク:外観を目視により観察し、成形品表面に発生する白色のスジ状模様の有無を確認した。
【0007】
【実施例1】
射出成形機としてスクリュ径D=φ112mm、スクリュのフライト部の長さLとした場合に、L/D=18の成形機を用いた。発泡ガスとしては市販のボンベにより供される二酸化炭素を用い、減圧弁とシリンダに取付けた逆止弁を通じシリンダ内に注入できる機構を設けている。二酸化炭素のボンベの圧力は7.2MPaであり、減圧弁により射出成形機への供給圧力を2MPaに保った。背圧は4MPaに保った。二酸化炭素の注入量は樹脂に対して0.7重量%であった。
【0008】
射出成形用金型として、製品寸法が900mm×440mmであって、キャビティの間隔(成形品厚み)を成形機のモータにより微調整でき、溶融樹脂を金型に配した5点のダイレクトゲートにより射出する構造の金型を成形機に取付け、金型温度50℃、冷却時間40秒、射出時の樹脂温度190℃になるように設定した。成形材料としてはブロックポリプロピレン[三井住友ポリオレフィン(株)製、MFR:45g/10分(230℃)]を用いた。
射出時に金型に溶融樹脂が未発泡でキャビティ間隙にフル充填になるように設定した。射出終了からコアバック開始までの間は0.5秒であり、コアバック速度は20mm/secとした。射出時、コアバック開始時およびコアバック終了時における金型のキャビティ内の間隙は1.2mmとした。
上記の条件で、射出発泡成形を行った成形品は、セル径が200〜300μmで、シルバーストリークの発生、製品形状に問題はなかった。発泡ガスの注入圧、発泡製品の製品厚み、最大セル径、平面性、シルバーストリーク発生状況を表1に示す。
【0009】
【実施例2】
背圧を3MPaとした他は、実施例1と同様に行なった。結果を表1に示す。
【0010】
【比較例1】
背圧を2MPaとした他は、実施例1と同様に行なった。結果を表1に示す。成形は出来たものの一部発泡不良が発生し、平面性が劣っていた。
【0011】
【比較例2】
背圧を1MPaとした他は、実施例1と同様に行なった。結果を表1に示す。樹脂と分離したガスがキャビティ内に射出され成形品は形状を成していなかった。
【0012】
【表1】
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an injection molding method for obtaining a foamed molded article by supplying foaming gas to an injection molding machine, kneading and dissolving in a molten thermoplastic resin, and then injecting it into a cavity.
[0002]
[Prior art]
In an injection molding method using a thermoplastic resin, foaming has been studied for the purpose of reducing material, reducing weight, etc., and as a method of performing injection foam molding, the material thermoplastic resin is thermally decomposed. A method of using a chemical foaming agent of a mold as a master batch and a method of injecting a physical foaming agent, that is, a supercritical fluid or a foaming gas, into a cylinder of a molding machine are known.
As a method for injecting foaming gas, Japanese Patent Application Laid-Open No. 2002-79545 proposes an injection foaming method in which a foamed gas is supplied to an injection molding machine at a low pressure to obtain a molded article having a good appearance and a high expansion ratio.
[0003]
However, the conventional method of injecting the foaming gas uses a screw of the same length as that of a normal injection molding machine, and the length of the second-stage metering / plasticizing part for kneading and dissolving the foaming gas is shortened. Since the injection gas and the molten resin were not sufficiently dissolved and kneaded, the gas and the molten resin were separated, and the intended foamed molded product could not be obtained.
If you try to add a gas-impregnated part to the tip of the screw as in the conventional physical foam injection molding device, the total length of the screw will be increased by the added amount, and not only can the existing cylinder be used, but the total length of the molding machine It was necessary to make a major remodeling to extend. Moreover, in such a physical foam molding machine, in order to dissolve more gas, the back pressure is set lower than the pressure of the supplied foam gas.
However, in a physical foam injection molding machine with a conventional length screw using an existing cylinder, if the back pressure is set lower than the supply gas pressure, the metering is performed in a state where the kneading and melting are not performed completely, and the molten resin Injecting is performed with the foaming gas separated from each other, resulting in a phenomenon that a molded product cannot be produced.
[0004]
[Problems to be solved by the present invention]
An object of the present invention is to provide an injection foam molded article for obtaining an injection molded article having a good appearance in an injection molding machine having a screw having an existing screw length, which is a problem of the prior art of physical foaming. It is in.
[0005]
[Means for Solving the Problems]
The apparatus for molding a thermoplastic resin molded article of the present invention includes a plasticizing step for bringing a thermoplastic resin into a molten state in a cylinder of a molding machine, and a foaming gas from a gas supply port into the molten thermoplastic resin. The injection foam molding machine has a gas supply and dissolution process for supplying and kneading and dissolving the gas, and a molding process for obtaining a foamed molded product from the obtained gas-dissolved molten resin. A compression structure is formed, the thermoplastic resin is plasticized in the first stage, and the volume is expanded downstream to reduce the molten resin pressure below the gas supply pressure, and the supplied foam gas and molten resin are kneaded. -Using a molding machine to be melted, the pressure is higher than the gas supply pressure from the second stage compression section to the measuring section.
As a result, even when an existing cylinder and an existing length screw are used, the back pressure is increased by 0.1 to 5.0 MPa higher than the gas pressure to be supplied without plasticizing the entire length of the existing screw. This makes it possible to improve the gas kneading / dissolving property, prevent separation of the foamed gas and the molten resin, and obtain a good molded product.
[0006]
【Example】
Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples.
In the embodiment of the present invention, each surveying was performed by the following method.
(1) Maximum cell diameter: The cross-section of the foamed part of the foam was observed with a microscope, the cell diameter of 50 cells was determined, and the average value of 10 cells selected in descending order was taken as the maximum cell diameter. When the cell is elliptical, (major axis + minor axis) / 2 was defined as the cell diameter.
(2) Flatness: The light source was reflected on the surface of the molded product, and the presence or absence of irregularities on the surface of the molded product was confirmed.
(3) Silver streak: The appearance was visually observed to confirm the presence or absence of a white streak pattern generated on the surface of the molded product.
[0007]
[Example 1]
When the screw diameter D = φ112 mm as the injection molding machine and the length of the flight part of the screw L, a molding machine with L / D = 18 was used. Carbon dioxide provided by a commercially available cylinder is used as the foaming gas, and a mechanism is provided that can be injected into the cylinder through a pressure reducing valve and a check valve attached to the cylinder. The pressure of the cylinder of carbon dioxide was 7.2 MPa, and the pressure supplied to the injection molding machine was kept at 2 MPa by a pressure reducing valve. The back pressure was kept at 4 MPa. The amount of carbon dioxide injected was 0.7% by weight based on the resin.
[0008]
As a mold for injection molding, the product dimensions are 900mm x 440mm, and the cavity interval (molded product thickness) can be finely adjusted by the motor of the molding machine, and injection is performed by a five-point direct gate with molten resin arranged in the mold. A mold having such a structure was attached to a molding machine, and the mold temperature was set to 50 ° C., the cooling time was 40 seconds, and the resin temperature at the time of injection was 190 ° C. As the molding material, block polypropylene [manufactured by Sumitomo Mitsui Polyolefin Co., Ltd., MFR: 45 g / 10 min (230 ° C.)] was used.
At the time of injection, the mold was set so that the molten resin was not foamed and the cavity gap was fully filled. The time from the end of injection to the start of the core back was 0.5 seconds, and the core back speed was 20 mm / sec. The gap in the mold cavity at the time of injection, at the start of the core back and at the end of the core back was 1.2 mm.
Under the above conditions, the molded product obtained by injection foaming had a cell diameter of 200 to 300 μm, and there was no problem in silver streak generation or product shape. Table 1 shows the injection pressure of the foaming gas, the product thickness of the foamed product, the maximum cell diameter, the flatness, and the occurrence of silver streak.
[0009]
[Example 2]
The same operation as in Example 1 was performed except that the back pressure was set to 3 MPa. The results are shown in Table 1.
[0010]
[Comparative Example 1]
The same procedure as in Example 1 was performed except that the back pressure was set to 2 MPa. The results are shown in Table 1. Although molding was possible, partial foaming failure occurred and the flatness was poor.
[0011]
[Comparative Example 2]
The same operation as in Example 1 was performed except that the back pressure was set to 1 MPa. The results are shown in Table 1. The gas separated from the resin was injected into the cavity, and the molded product was not shaped.
[0012]
[Table 1]
Claims (3)
前記発泡ガスとして二酸化炭素を用い、溶融樹脂計量時の発泡ガスの供給圧力を1 . 0
〜2MPa、背圧を供給される発泡ガス圧力に対し、0.1〜5.0MPa高い圧力として、可塑化・計量を行うことを特徴とする射出成形方法。This is an injection molding method for a thermoplastic resin molded article comprising a gas impregnating and dissolving step of supplying and impregnating and dissolving a foamed gas to a molten thermoplastic resin, and a molding step of obtaining a foamed molded product from the obtained gas-impregnated molten resin. And
The carbon dioxide used as a blowing gas, the supply pressure of the blowing gas during the molten resin metered 1.0
An injection molding method characterized by plasticizing and measuring at a pressure higher by 0.1 to 5.0 MPa than a foaming gas pressure to which a back pressure is supplied at ~ 2 MPa .
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JP2003099717A JP4113026B2 (en) | 2003-04-02 | 2003-04-02 | Thermoplastic resin composition foamed molding method |
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JP2003099717A JP4113026B2 (en) | 2003-04-02 | 2003-04-02 | Thermoplastic resin composition foamed molding method |
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JP5255852B2 (en) * | 2008-01-21 | 2013-08-07 | 東洋機械金属株式会社 | Gas foam injection molding machine |
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JP4119044B2 (en) * | 1999-06-30 | 2008-07-16 | 株式会社日本製鋼所 | Method for molding thermoplastic resin foam |
JP4355409B2 (en) * | 1999-10-22 | 2009-11-04 | 株式会社日本製鋼所 | Plasticizer for molding thermoplastic resin foam |
JP4104034B2 (en) * | 1999-06-18 | 2008-06-18 | 株式会社日本製鋼所 | Plasticizing equipment for molding thermoplastic resin foam |
JP3851748B2 (en) * | 1999-11-29 | 2006-11-29 | 学校法人金沢工業大学 | Injection molding method for fine foamable material and injection molding machine for producing fine foamable material |
JP3521306B2 (en) * | 1999-12-08 | 2004-04-19 | 株式会社日本製鋼所 | Method and apparatus for producing sandwich foam |
JP2001179779A (en) * | 1999-12-24 | 2001-07-03 | Meiki Co Ltd | Apparatus for injecting gas-dissolved resin and injection molding method |
JP4233240B2 (en) * | 2000-06-22 | 2009-03-04 | 三井化学株式会社 | Injection foam molding method, and injection molding machine and resin composition suitable therefor |
JP4551003B2 (en) * | 2001-01-05 | 2010-09-22 | 積水化学工業株式会社 | Method for producing thermoplastic elastomer foam and thermoplastic elastomer foam |
JP2002337186A (en) * | 2001-05-21 | 2002-11-27 | Mitsui Chemicals Inc | Method for supplying material to injection molding machine or extrusion machine |
JP2003191272A (en) * | 2001-12-25 | 2003-07-08 | Sekisui Chem Co Ltd | Method for manufacturing thermoplastic resin foam |
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