JP2896832B2 - Mold for extruded thermoplastic resin foam - Google Patents

Mold for extruded thermoplastic resin foam

Info

Publication number
JP2896832B2
JP2896832B2 JP5185045A JP18504593A JP2896832B2 JP 2896832 B2 JP2896832 B2 JP 2896832B2 JP 5185045 A JP5185045 A JP 5185045A JP 18504593 A JP18504593 A JP 18504593A JP 2896832 B2 JP2896832 B2 JP 2896832B2
Authority
JP
Japan
Prior art keywords
mold
resin
thermoplastic resin
present
contact angle
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP5185045A
Other languages
Japanese (ja)
Other versions
JPH0740418A (en
Inventor
静 堀野
匡泰 坪根
吉則 梶本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sekisui Kaseihin Kogyo KK
Original Assignee
Sekisui Kaseihin Kogyo KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sekisui Kaseihin Kogyo KK filed Critical Sekisui Kaseihin Kogyo KK
Priority to JP5185045A priority Critical patent/JP2896832B2/en
Publication of JPH0740418A publication Critical patent/JPH0740418A/en
Application granted granted Critical
Publication of JP2896832B2 publication Critical patent/JP2896832B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、熱可塑性樹脂押出発泡
体用金型に関し、特に押出発泡体用金型内の流路におけ
る溶融樹脂とこれに接する金型表面の材質に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a mold for extruded thermoplastic resin foam, and more particularly to a molten resin in a flow path in the mold for extruded foam and a material of a surface of the mold in contact with the molten resin.

【0002】[0002]

【従来の技術】熱可塑性樹脂押出発泡体用金型の材質と
しては、鉄を主成分としたS45CやS55Cさらにク
ロムを少量合金にしたSCM−4やSCM−3等が使わ
れている。そして、金型内の溶融樹脂と接する金型表面
の表面処理材質としてはクロムメッキ、テフロンコ−テ
ィング、無電解ニッケルメッキ等がある。しかし、これ
らの表面処理材質では下記のような問題点がある。 (1)クロムメッキ、無電解ニッケルメッキの場合には
溶融樹脂とのスベリ性が良くないため金型出口先端部で
発熱を起こし、品質低下の原因となる。また、金型出口
先端部で添加剤がビルドアップして先端部に付着し、製
品表面にラインが発生する。 (2)テフロンコ−ティングの場合には溶融樹脂とのス
ベリ性は良くても、耐摩耗性が良くないため、長期間使
用すると表面処理剤が剥がれ、製品表面にラインが発生
する。
2. Description of the Related Art As a material for a mold for extruded thermoplastic resin foam, S45C or S55C containing iron as a main component and SCM-4 or SCM-3 containing a small amount of chromium as an alloy are used. Examples of surface treatment materials for the surface of the mold in contact with the molten resin in the mold include chrome plating, Teflon coating, electroless nickel plating, and the like. However, these surface treatment materials have the following problems. (1) In the case of chromium plating or electroless nickel plating, since the sliding property with the molten resin is not good, heat is generated at the tip end of the mold outlet, which causes quality deterioration. Further, the additive builds up at the tip end of the mold outlet and adheres to the tip portion, and a line is generated on the product surface. (2) In the case of Teflon coating, although the sliding property with the molten resin is good, the abrasion resistance is not good. Therefore, when used for a long period of time, the surface treating agent peels off and lines are formed on the product surface.

【0003】[0003]

【発明が解決しようとする課題】本発明者は、かかる問
題点を改善するため種々検討した結果、熱可塑性樹脂押
出発泡体用金型の表面材質と溶融樹脂との接触角、及
び、樹脂流路の表面粗さ及び金型内流路の絞り込み比を
特定の範囲に選択することによって上記の問題点を解決
し、品質の向上した発泡体を得ることを見出し本発明を
完成したもので、本発明の目的は、適正なスベリ性を維
持することができる熱可塑性樹脂押出発泡体用金型を提
供することにある。
The present inventor has conducted various studies to improve the above problems, and as a result, has found that the contact angle between the surface material of the mold for the thermoplastic resin extruded foam and the molten resin, and the resin flow. By solving the above problems by selecting the surface roughness of the road and the narrowing ratio of the flow path in the mold within a specific range, it was found that a foam having improved quality was obtained, and the present invention was completed. An object of the present invention is to provide a mold for a thermoplastic resin extruded foam that can maintain appropriate sliding properties.

【0004】[0004]

【問題点を解決するための手段】本発明の要旨は溶融樹
脂と接触する金型流路面で少なくとも金型出口から手前
5mmまでの間は溶融樹脂との接触角が45〜65°で
ある表面材質の金型で、樹脂流路の表面粗さが6.3S
以下でありかつ、金型内流路の絞り込み比が3〜40で
ある熱可塑性樹脂押出発泡体用金型、及び、熱可塑性樹
脂がポリスチレン系樹脂、ポリエチレン系樹脂、ポリプ
ロピレン系樹脂、ポリフェニレンオキシド系樹脂、及び
ポリエステル系樹脂或いはこれらの樹脂の共重合体また
は混合樹脂であることを特徴とする前記の熱可塑性樹脂
押出発泡体用金型である。
SUMMARY OF THE INVENTION The gist of the present invention is to provide a mold having a surface having a contact angle with the molten resin of at least 45 mm from the exit of the mold at least 5 mm from the exit of the mold. Mold of material, surface roughness of resin channel is 6.3S
The following is a mold for a thermoplastic resin extruded foam having a narrowing ratio of a channel in the mold of 3 to 40, and the thermoplastic resin is a polystyrene resin, a polyethylene resin, a polypropylene resin, a polyphenylene oxide resin. The mold for a thermoplastic resin extruded foam described above, which is a resin, a polyester-based resin, a copolymer of these resins, or a mixed resin.

【0005】本発明において、溶融樹脂との接触角測定
法は次の方法によって行う。 使用測定器:エルマ社製 接触角測定器(ゴニオメ−タ
−式) 金属片3mm×20mm×50mmにポリスチレン1粒
子(約0.014g)を載せ、160℃ 15HR(ポ
リスチレンの場合)加熱ギヤオ−ブンにて加熱後、接触
角測定器にて金属と溶融樹脂の接触角を測定する。ま
た、本発明における金型流路の絞り込み比とは次に式に
よって表される値である。
In the present invention, a method for measuring a contact angle with a molten resin is performed by the following method. Measuring instrument used: Contact angle measuring instrument (goniometer type) manufactured by Elma Inc. One polystyrene particle (about 0.014 g) is placed on a metal piece 3 mm × 20 mm × 50 mm, and heated at 160 ° C. and 15 HR (for polystyrene) After heating, the contact angle between the metal and the molten resin is measured by a contact angle measuring device. The narrowing ratio of the mold flow channel in the present invention is a value represented by the following equation.

【0006】[0006]

【数1】 (Equation 1)

【0007】次に本発明について詳細に述べる。本発明
における熱可塑性樹脂押出発泡体とは、熱可塑性樹脂と
発泡剤とを押出機内で溶融混練した後、大気中に押し出
して得られたもので、熱可塑性樹脂としては、ポリスチ
レン系樹脂、ポリエチレン系樹脂、ポリプロピレン系樹
脂、ポリフェニレンオキシド系樹脂及びポリエステル系
樹脂或いはこれらの樹脂の共重合体または混合樹脂等で
ある。発泡剤としては従来よりこの種の押出発泡体の発
泡剤として使用されているものであれば何れでも良く、
例えばノルマルブタン、イソブタン或いは両者の混合
物、プロパン等、或いは炭化水素のフルオロクロル置換
体、若しくはハロゲン化炭化水素等である。更に発泡を
コントロ−ルするためタルク等の核剤、その他必要に応
じて適宜の配合剤を添加しても良い。
Next, the present invention will be described in detail. The thermoplastic resin extruded foam in the present invention is obtained by melting and kneading a thermoplastic resin and a foaming agent in an extruder, and extruding the mixture into the atmosphere.As the thermoplastic resin, polystyrene resin, polyethylene Resins, polypropylene resins, polyphenylene oxide resins and polyester resins, and copolymers or mixed resins of these resins. Any foaming agent may be used as long as it is conventionally used as a foaming agent for this type of extruded foam.
For example, normal butane, isobutane or a mixture thereof, propane or the like, or a fluorochloro-substituted hydrocarbon or a halogenated hydrocarbon is used. Further, a nucleating agent such as talc or the like, if necessary, may be added to control foaming.

【0008】押出機については特に制限されるものでは
なく、発泡剤を含有する溶融熱可塑性樹脂組成物は押出
機の先端にある金型より大気中に押し出されると同時に
発泡する。本願発明においては、溶融樹脂と接触する押
出機の金型表面材質の接触角が45〜65°にあること
が必要で、この条件を満足することによって熱可塑性樹
脂押出発泡体の適正なスベリ性を維持できることが確認
出来た。この範囲を外れた時、接触角が45°未満の場
合スベリ性が良くないため、ヘッド圧力が上がる傾向と
なり、金型出口近くで発熱が起こり、外観が粗くなっ
た。また、接触角が65°を越える時は、スベリ性が良
過ぎて金型先端部での圧力保持が出来ず、偏肉が発生し
やすくなる傾向となった。又、この材質のものは耐久性
が無いため、長期連続運転ができなかった。なお、ここ
で接触角について、本願発明では金型出口から手前5m
mまでの間と規定するが、この金型出口から手前5mm
までとは金型出口先端部から溶融樹脂の流路面に沿って
5mmの位置までの間をいい、本願発明で接触角を金型
出口から手前5mmと規定した理由は、これ以下の長さ
の金型出口のものは製作上困難であり、また、加工精度
をあげることが出来ないからである。適性発泡領域を得
るための絞り込み比の範囲についてであるが、3未満の
場合は金型出口先端部で内部発泡を起こし品質が低下す
る。また、40を越えると吐出量が高い場合に表面ムラ
が発生する。
The extruder is not particularly limited, and the molten thermoplastic resin composition containing a foaming agent is extruded into the atmosphere from a mold at the tip of the extruder and foams at the same time. In the present invention, it is necessary that the contact angle of the mold surface material of the extruder in contact with the molten resin is 45 to 65 °, and by satisfying this condition, the appropriate slip property of the extruded thermoplastic resin foam is obtained. Can be maintained. When the contact angle is out of this range, if the contact angle is less than 45 °, the sliding property is not good, so that the head pressure tends to increase, and heat is generated near the exit of the mold, resulting in a rough appearance. On the other hand, when the contact angle exceeds 65 °, the slipperiness is too good to maintain the pressure at the tip of the mold, which tends to cause uneven thickness. In addition, since this material was not durable, long-term continuous operation could not be performed. The contact angle here is 5 m before the die exit in the present invention.
m, but 5 mm before this mold exit
Means up to a position of 5 mm along the flow path surface of the molten resin from the tip end of the mold outlet. The reason for defining the contact angle as 5 mm before the mold exit in the present invention is that the length is less than this. The reason for this is that the mold outlet is difficult to manufacture, and the processing accuracy cannot be improved. Regarding the range of the narrowing-down ratio for obtaining an appropriate foaming area, if it is less than 3, internal foaming occurs at the tip end of the mold outlet, and the quality deteriorates. On the other hand, if it exceeds 40, surface unevenness occurs when the ejection amount is high.

【0009】ところで、従来使用されている金型の表面
材質の接触角について測定した結果を示すと次の通りで
ある。 接触角測定方法:エルマ社製の接触角測定器(ゴニオメ
−タ−式)を使用し、表面処理を施した3mm×20m
m×50mmの金属片上に熱可塑性樹脂1粒子を載せ、
加熱ギヤオ−ブンにて加熱後、接触角測定器にて金属と
溶融樹脂の接触角を測定する。加熱条件としては、ポリ
スチレンの場合は160℃で15HR、LDPEの場合
は120℃で15HRであった。接触角測定結果の結果
は表1の通りである。
By the way, the result of measuring the contact angle of the surface material of a conventionally used mold is as follows. Contact angle measuring method: 3 mm x 20 m with surface treatment using a contact angle measuring device (goniometer type) manufactured by Elma Corporation
One particle of thermoplastic resin is placed on a metal piece of mx 50 mm,
After heating with a heating gear oven, the contact angle between the metal and the molten resin is measured with a contact angle measuring device. The heating conditions were 15 HR at 160 ° C. for polystyrene and 15 HR at 120 ° C. for LDPE. Table 1 shows the results of the contact angle measurement results.

【0010】[0010]

【表1】 [Table 1]

【0011】本発明においては、樹脂流路の表面粗さが
6.3S以下であり、かつ、金型内流路の絞り込み比が
3〜40を必須要件とする。流路表面粗さを6.3S以
下としたのは6.3Sを超えると材質のスベリ性が良く
ても表面が粗すぎて抵抗が大きくなり、外観を悪くする
結果となった。また、金型流路の絞り込み比は、先に示
した式(1)で規定されるもので、絞り込み比が40を
越えると、吐出量が高い場合に表面ムラが発生し、3未
満では金型出口先端部で内部発泡を起こし製品の品質が
低下する。本発明における金型のスリットの形状は、特
に制限されるものではなく、環状や板状等何れでも良
い。
In the present invention, it is essential that the surface roughness of the resin flow path is 6.3 S or less and the narrowing ratio of the flow path in the mold is 3 to 40. The reason why the surface roughness of the flow channel is set to 6.3S or less is that if the surface roughness exceeds 6.3S, the resistance is increased due to the surface being too rough even if the sliding property of the material is good, resulting in poor appearance. The narrowing ratio of the mold flow path is defined by the above-described equation (1). If the narrowing ratio exceeds 40, surface unevenness occurs when the discharge amount is high. Internal foaming occurs at the tip of the mold outlet, and the quality of the product deteriorates. The shape of the slit of the mold in the present invention is not particularly limited, and may be any of an annular shape and a plate shape.

【0012】本発明を図をもって説明すると、図1は本
願発明にかかる金型の説明図であり、図2は本願発明に
かかる他の金型の説明図である。図1において、金型1
は溶融樹脂の流路2を有し、溶融樹脂は流路2を通過し
て金型出口3より環状に発泡押し出される。本願発明に
おいて規定した特性を有する部分は斜線を施した部分で
ある。図2は板状に押出し発泡に使用する金型の説明図
であり、本願発明において規定した特性を有する部分は
斜線を施した部分である。
FIG. 1 is an explanatory view of a mold according to the present invention, and FIG. 2 is an explanatory view of another mold according to the present invention. In FIG. 1, a mold 1
Has a flow path 2 of a molten resin, and the molten resin passes through the flow path 2 and is foamed and extruded in an annular shape from a mold outlet 3. Portions having the characteristics defined in the present invention are hatched portions. FIG. 2 is an explanatory view of a mold used for extruding and foaming into a plate shape. Portions having characteristics specified in the present invention are hatched portions.

【0013】[0013]

【実施例】次に実施例をもって本発明を説明する。 実施例1〜3、比較例1〜5 本発明の条件を具備した押出金型を使用して得られた発
泡体と本発明の条件を欠いた押出金型を使用して得られ
た発泡体を対比すると、表2及び表3の通りである。
Next, the present invention will be described by way of examples. Examples 1 to 3 and Comparative Examples 1 to 5 Foams obtained using an extrusion die having the conditions of the present invention and foams obtained using an extrusion die lacking the conditions of the present invention Are as shown in Tables 2 and 3.

【0014】[0014]

【表2】 [Table 2]

【0015】[0015]

【表3】 [Table 3]

【0016】[0016]

【発明の効果】以上述べたように、本発明は、熱可塑性
樹脂押出発泡体用金型の金型流路内における溶融樹脂と
接触する金型流路面で少なくとも金型出口から手前5m
mまでの間は溶融樹脂との接触角が45〜65°で、樹
脂流路の表面粗さが6.3S以下であり、かつ、金型内
流路の絞り込み比が3〜40と規定したことによって、 1)金型先端部の発熱が少ない。 2)ダイスエルが小さい。 3)製品表面にラインの発生が少ない。 等の効果が得られるのである。
As described above, the present invention relates to a mold for a thermoplastic resin extruded foam, which is at least 5 m in front of the mold outlet on the mold flow path surface in contact with the molten resin in the mold flow path.
Until m, the contact angle with the molten resin was 45 to 65 °, the surface roughness of the resin flow path was 6.3S or less, and the narrowing ratio of the flow path in the mold was 3 to 40. Thus, 1) heat generation at the tip of the mold is small. 2) The die swell is small. 3) There are few lines on the product surface. And the like.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明にかかる金型形状の断面図FIG. 1 is a sectional view of a mold according to the present invention.

【図2】本発明にかかる他の金型形状の断面斜視図FIG. 2 is a sectional perspective view of another mold shape according to the present invention.

【符号の説明】[Explanation of symbols]

1 押出機 2 流路 3 金型出口 Reference Signs List 1 extruder 2 flow path 3 mold outlet

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平6−287338(JP,A) 特開 昭57−105324(JP,A) 特開 昭63−95929(JP,A) 特開 平1−281916(JP,A) 特開 平4−131219(JP,A) 特公 昭46−10675(JP,B1) (58)調査した分野(Int.Cl.6,DB名) B29C 47/00 - 47/96 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-6-287338 (JP, A) JP-A-57-105324 (JP, A) JP-A-63-95929 (JP, A) JP-A-1- 281916 (JP, A) JP-A-4-131219 (JP, A) JP-B-46-10675 (JP, B1) (58) Fields investigated (Int. Cl. 6 , DB name) B29C 47/00-47 / 96

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 溶融樹脂と接触する金型流路面で少なく
とも金型出口から手前5mmまでの間は溶融樹脂との接
触角が45〜65°である表面材質の金型で、樹脂流路
の表面粗さが6.3S以下であり、かつ、金型内流路の
絞り込み比が3〜40である熱可塑性樹脂押出発泡体用
金型。
1. A mold having a surface material having a contact angle with the molten resin of 45 to 65 ° at least from the mold outlet to 5 mm in front of the mold flow path surface in contact with the molten resin. A mold for extruded thermoplastic resin having a surface roughness of 6.3S or less and a narrowing ratio of a channel in the mold of 3 to 40.
【請求項2】 熱可塑性樹脂がポリスチレン系樹脂、ポ
リエチレン系樹脂、ポリプロピレン系樹脂、ポリフェニ
レンオキシド系樹脂及びポリエステル系樹脂或いはこれ
らの樹脂の共重合体または混合樹脂であることを特徴と
する請求項1記載の熱可塑性樹脂押出発泡体用金型。
2. The method according to claim 1, wherein the thermoplastic resin is a polystyrene resin, a polyethylene resin, a polypropylene resin, a polyphenylene oxide resin, a polyester resin, a copolymer of these resins, or a mixed resin. The mold for extruded thermoplastic resin foam according to the above.
JP5185045A 1993-07-27 1993-07-27 Mold for extruded thermoplastic resin foam Expired - Lifetime JP2896832B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5185045A JP2896832B2 (en) 1993-07-27 1993-07-27 Mold for extruded thermoplastic resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5185045A JP2896832B2 (en) 1993-07-27 1993-07-27 Mold for extruded thermoplastic resin foam

Publications (2)

Publication Number Publication Date
JPH0740418A JPH0740418A (en) 1995-02-10
JP2896832B2 true JP2896832B2 (en) 1999-05-31

Family

ID=16163833

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5185045A Expired - Lifetime JP2896832B2 (en) 1993-07-27 1993-07-27 Mold for extruded thermoplastic resin foam

Country Status (1)

Country Link
JP (1) JP2896832B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2385553B (en) * 1998-10-28 2003-10-15 Dart Container Method for making a corrugation-free foam and foams made by the method
US6428297B1 (en) 1998-10-28 2002-08-06 Dart Container Corporation Apparatus for making a corrugation-free foam
JP6511674B2 (en) * 2016-02-01 2019-05-15 株式会社日本製鋼所 Prepreg manufacturing method
JP6691988B2 (en) * 2019-03-18 2020-05-13 株式会社日本製鋼所 Prepreg manufacturing method

Also Published As

Publication number Publication date
JPH0740418A (en) 1995-02-10

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