JPH08183082A - Thermoplastic resin foam body - Google Patents

Thermoplastic resin foam body

Info

Publication number
JPH08183082A
JPH08183082A JP6328000A JP32800094A JPH08183082A JP H08183082 A JPH08183082 A JP H08183082A JP 6328000 A JP6328000 A JP 6328000A JP 32800094 A JP32800094 A JP 32800094A JP H08183082 A JPH08183082 A JP H08183082A
Authority
JP
Japan
Prior art keywords
foam
fused
plates
foam plates
thermoplastic resin
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.)
Pending
Application number
JP6328000A
Other languages
Japanese (ja)
Inventor
Naoyuki Futamura
直行 二村
Katsumi Yamaguchi
勝己 山口
Hideshi Asada
英志 浅田
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 Kasei Co Ltd
Original Assignee
Sekisui Plastics Co Ltd
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 Plastics Co Ltd filed Critical Sekisui Plastics Co Ltd
Priority to JP6328000A priority Critical patent/JPH08183082A/en
Publication of JPH08183082A publication Critical patent/JPH08183082A/en
Pending legal-status Critical Current

Links

Landscapes

  • Laminated Bodies (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Shaping Of Tube Ends By Bending Or Straightening (AREA)

Abstract

PURPOSE: To easily manufacture a thick-wall foam body by a method wherein a large number of band-form foam plates having a vertically long cross section are arranged in a lateral line adjacently to each other with the side faces facing each other, and the side faces of adjacent foam plates are integrally fused to each other. CONSTITUTION: A plurality of band-form foam plates 2 are obtained by extruding and foam molding a resin in a band plate form of a vertically long cross section from a die having a plurality of vertical slits. The foam plates 2 in a softened state are arranged in a lateral line adjacently to each other with the side faces facing each other, thereafter being molded into a planar or columnar thick-wall article having a predetermined thickness by roll molding vertically or crosswise. At this time, esp. fusion parts 3 between the foam plates 2, 2 are fused to each other so as to be approximately straight in a vertical direction (a thickness direction) in a cross section by being vertically compressed by roll molding. Alternatively, the respective foam plates 2 are bent in a zigzag or corrugated form to be integrally fused to each other by being vertically more compressed by roll molding.

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、熱可塑性樹脂発泡体に
関し、特に押出し発泡による厚物の発泡体を提供しよう
とするものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a thermoplastic resin foam, and more particularly to an extrusion foam for a thick foam.

【0002】[0002]

【従来の技術】ポリエチレン等を素材とする押出し発泡
成形による厚物発泡体は、Tダイの口金を通してサイジ
ングダイで形を成形する方法と、多数の小孔を有する口
金を通して押出し発泡したストランドを多数集束して互
いの隣接部で融着させる方法(例えば、実公昭61−2
6030号公報および特表平1−502252号公報)
がある。
2. Description of the Related Art Thick foams made of polyethylene or the like by extrusion foam molding have a method of molding a shape with a sizing die through a die of a T die, and a large number of strands extruded and foamed through a die having a large number of small holes. A method of converging and fusing at adjacent portions of each other (for example, Japanese Utility Model Publication No. 61-2).
No. 6030 gazette and special table 1-502252 gazette)
There is.

【0003】[0003]

【発明が解決しようとする課題】しかし、前者のTダイ
を使用する方法の場合、成形上の問題があって、一定以
上の厚みになると押出し成形が困難になり、例えば60
mm以上の厚物発泡体を成形する場合、かなりの発泡体
のフリー厚みが必要になるが、そのためにスリットの間
隙を大きくすると、発泡に要する樹脂圧力を維持するの
が困難になり、スリットから樹脂が押し出される以前に
金型内で発泡が始まり、良好な発泡状態とはならず、良
品質の成形品を得ることができない。
However, in the case of the former method using the T-die, there is a problem in molding, and if the thickness exceeds a certain value, extrusion molding becomes difficult.
When molding thick foams of mm or more, a considerable free thickness of the foam is required. However, if the slit gap is increased for this reason, it will be difficult to maintain the resin pressure required for foaming, and Foaming starts in the mold before the resin is extruded, a good foaming state does not occur, and a good quality molded product cannot be obtained.

【0004】後者の押出し発泡したストランドを集束す
る方法は従来から知られており、一般にストランド押出
し法と呼ばれている。この方法の問題点として、素材が
ポリエチレン系樹脂である場合、押出し発泡成形に適し
た粘度の温度依存性が著しく大きいために、押出し発泡
に適した粘度領域を示す適正温度が極めて狭く、樹脂温
度を適正温度より少しでも下げてしまうと、口金に有す
る多数の小孔の幾つかが詰ってしまい、良好な成形品を
得ることができない。
The latter method for focusing the extruded and foamed strands has been known in the past, and is generally called the strand extrusion method. The problem with this method is that when the material is a polyethylene resin, the temperature dependence of the viscosity suitable for extrusion foam molding is extremely large, so the appropriate temperature that shows the viscosity range suitable for extrusion foaming is extremely narrow, and the resin temperature If the temperature is lowered below the proper temperature, some of the numerous small holes in the die will be clogged, and a good molded product cannot be obtained.

【0005】また、このストランド押出しによる場合
は、ポリエチレン系樹脂単独でストランドの発泡体を作
るのが難しく、特に発泡倍率25倍以上の発泡体を作る
場合、各ストランドの接着不良が生じ易く、その成形が
ほとんど不可能である。そのため、この種の発泡体に使
われる樹脂自身の接着性を上げるために、一般にはアイ
オノマーやEVA等を混合することが行なわれている。
In addition, in the case of this strand extrusion, it is difficult to form a foam of a strand from polyethylene resin alone, and particularly when a foam having a foaming ratio of 25 times or more is produced, adhesion failure of each strand is likely to occur. Molding is almost impossible. Therefore, in order to improve the adhesiveness of the resin itself used in this type of foam, it is common practice to mix an ionomer, EVA or the like.

【0006】しかしこのような樹脂の混合による場合、
再利用が非常に難しくなり、リサイクル性の点で問題が
ある。
However, in the case of mixing such resins,
Reuse becomes very difficult, and there is a problem in terms of recyclability.

【0007】本発明は、上記に鑑みてなしたものであっ
て、特にリサイクル可能なポリエチレン樹脂等の比較的
接着性の低い樹脂素材単独のものであっても、また発泡
倍率が大きいものであっても、発泡体全体の発泡状態が
良好でかつ一体性に優れる良品質の厚物の熱可塑性樹脂
発泡体を得るを目的とするものである。
The present invention has been made in view of the above, and in particular, a resin material having a relatively low adhesiveness such as a recyclable polyethylene resin alone is used, and a foaming ratio is large. However, the object of the present invention is to obtain a good quality thick thermoplastic resin foam in which the foamed state of the entire foam is good and the integrity is excellent.

【0008】[0008]

【課題を解決するための手段】上記の課題を解決する本
発明の熱可塑性樹脂発泡体は、複数の縦型のスリットか
ら押出し発泡成形された断面縦長の熱可塑性樹脂の帯板
状発泡板を、軟化状態下で横列に並べて側面同士を合せ
て隣接させ、隣接部で互いに融着せしめて、比較的厚物
の発泡体に成形してなることを特徴とするものである。
A thermoplastic resin foam of the present invention for solving the above-mentioned problems is a strip-shaped foamed plate of thermoplastic resin having a vertically long cross section extruded and foamed from a plurality of vertical slits. In a softened state, the side surfaces are arranged side by side in a row so as to be adjacent to each other, and the adjacent portions are fused together to form a relatively thick foam.

【0009】また前記において、隣接する多数の帯板状
発泡板が、ジグザグ状や波状に屈曲して相互に融着一体
化せしめられてなるものが特に好適である。
Further, in the above, it is particularly preferable that a large number of adjacent strip-shaped foam plates are bent in a zigzag shape or a wavy shape and are fused and integrated with each other.

【0010】前記の熱可塑性樹脂発泡体は、複数の縦型
のスリットを所定間隔に横列に並設してなる口金を備え
た押出機を用い、前記口金の各スリットから発泡剤を含
有した素材樹脂を断面縦長の帯板状に押出して発泡させ
るとともに、この押出し発泡された複数の帯板状発泡板
を、軟化状態にある間にサイジングダイを通して側面同
士を合せるように隣接させ、その隣接部において側面同
士を相互に融着一体化させ、さらに上下および左右から
のロール成形等の手段により押圧して、各発泡板同士の
間に隙間を生じさせないように、所定の厚みを有する形
状に成形することにより得ることができる。
For the thermoplastic resin foam, an extruder equipped with a die having a plurality of vertical slits arranged in a row at predetermined intervals in a row is used, and a material containing a foaming agent from each slit of the die is used. The resin is extruded in the form of a strip having a vertically long section to foam, and a plurality of the extruded foamed strip-shaped foam plates are adjoined so that their side faces are brought together through a sizing die while in a softened state, and the adjoining portion. In the above, the side surfaces are fused and integrated with each other, and further pressed by means such as roll molding from the upper and lower sides and the left and right sides to form a shape having a predetermined thickness so as not to create a gap between the foam plates. It can be obtained by

【0011】[0011]

【作用】上記の本発明の熱可塑性樹脂発泡体によれば、
多数の断面縦長の帯板状発泡板を横列に並べて側面同士
を合せるように隣接させ、隣接する発泡板の側面同士を
相互に融着一体化させているので、縦型のスリットより
押出し成形される帯板状発泡板の縦方向寸法を大きくと
ることにより、従来よりも厚物の発泡体を容易に得るこ
とができる。
According to the above thermoplastic resin foam of the present invention,
Since a large number of vertically elongated strip-shaped foam plates are arranged in rows and adjacent to each other so that their side faces are aligned, and the side faces of the adjacent foam plates are fused and integrated with each other, they are extruded from a vertical slit. By increasing the vertical dimension of the strip-shaped foam plate, a thick foam can be easily obtained as compared with the conventional one.

【0012】しかも複数の帯板状発泡板を横列に並べて
隣接させるので、これを押出し成形するスリットの間隙
をそれほど大きくする必要がなく、したがって発泡板そ
れぞれの発泡度合が均一化し、単一のスリットにより押
出し成形する場合に比して全体として均一な発泡状態の
発泡体を得ることができる。
Moreover, since a plurality of strip-shaped foam plates are arranged in a row and adjacent to each other, it is not necessary to increase the gap between the slits for extruding the foam plates. Therefore, the foaming degree of each foam plate is made uniform and a single slit is formed. As a result, it is possible to obtain a foamed body in a uniform foamed state as a whole as compared with the case of extrusion molding.

【0013】また隣接する断面縦長の帯板状発泡板が、
その側面全面にわたる広い面で融着するため、ストラン
ドタイプの集合体よりなるものに比し、融着面積が多く
なって発泡板相互間の接着強度が高くなる。
Further, adjacent strip-shaped foam plates having a vertically long cross section,
Since the fusion is performed over a wide surface over the entire side surface, the fusion area is increased and the adhesive strength between the foam plates is increased as compared with the case where the strand type aggregate is formed.

【0014】特に請求項2のように、各帯板状発泡板が
ジグザグ状や波状に屈折して融着一体化している場合、
隣接する発泡板同士の融着部が屈折状をなして融着面積
が増大するため、発泡板相互間の接着強度がさらに高く
なる。
In particular, when the strip-shaped foam plates are refracted into a zigzag shape or a wavy shape and are fused and integrated as described in claim 2,
Since the fused portion between the adjacent foam plates is bent to increase the fused area, the adhesive strength between the foam plates is further increased.

【0015】[0015]

【実施例】次に本発明の実施例を図面に基いて説明す
る。
Embodiments of the present invention will now be described with reference to the drawings.

【0016】図1および図2は、本発明に係る厚物の熱
可塑性樹脂発泡体の1実施例を示しており、図3は同上
の押出し発泡成形に使用する口金の正面図を示してい
る。
1 and 2 show one embodiment of a thick thermoplastic resin foam according to the present invention, and FIG. 3 shows a front view of a die used for extrusion foam molding of the same. .

【0017】図1の示す厚物の熱可塑性樹脂発泡体
(1)は、図3に示す複数の縦型のスリット(12)を
有する口金(11)から断面縦長の帯板状に押出し発泡
成形した複数の帯板状発泡板(2)を、軟化状態下にお
いて横列に並べて側面同士を合せるように隣接させ、例
えば上下および左右からのロール成形により、所要の厚
みを有する厚物の板状や柱状に成形したもので、特に発
泡板(2)(2)同士の融着部(3)を、ロール成形に
よる上下からの圧縮の程度によって、断面において上下
方向(厚み方向)に略真直ぐになるように融着させるよ
うに成形した場合を示している。
The thick thermoplastic resin foam (1) shown in FIG. 1 is extruded and foamed from a die (11) having a plurality of vertical slits (12) shown in FIG. The plurality of strip-shaped foamed plates (2) are arranged in a row in a softened state and are adjacent to each other so that their side surfaces are aligned with each other. It is formed in a columnar shape, and in particular, the fused portion (3) between the foam plates (2) and (2) becomes substantially straight in the vertical direction (thickness direction) in the cross section depending on the degree of compression from the upper and lower sides by roll forming. It shows the case of molding so as to be fused.

【0018】この場合、隣接する帯板状発泡板(2)
(2)は、側面の広い面で融着してるために、従来のス
トランド融着による場合よりも融着面積が多くて、発泡
板(2)相互間の接着強度が高くなる。
In this case, the adjacent strip-shaped foam plates (2)
Since (2) is fused on the wide side surface, the fusion area is larger than in the case of the conventional strand fusion, and the adhesive strength between the foam plates (2) is increased.

【0019】このほか、上下からのロール成形による圧
縮を大きくする等の手段により、例えば図2のように各
帯板状発泡板(2)をジグザグ状や波状に屈曲させて、
屈曲した発泡板(2)の側面同士を相互に融着一体化さ
せるようにしてもよい。
In addition, each strip-shaped foam plate (2) is bent into a zigzag shape or a wavy shape as shown in FIG. 2 by means such as increasing the compression by roll forming from above and below.
The side surfaces of the bent foam plate (2) may be fused and integrated with each other.

【0020】この場合、融着部(3)が屈曲状をなすた
めに、融着面積が多くなって発泡板(2)相互の接着強
度が増し、発泡板(2)の融着部(3)の剥れが生じ難
くなり、一体性にさらに優れることになる。
In this case, since the fused portion (3) has a bent shape, the fused area is increased and the adhesive strength between the foam plates (2) is increased, and the fused portion (3) of the foam plate (2) is increased. ) Is less likely to occur, and the unity is further improved.

【0021】この熱可塑性樹脂発泡体(1)の素材樹脂
としては、ポリエチレンやポリプロピレンおよびオレフ
ィンを主体とする共重合体等のポリオレフィン系樹脂の
ほか、スチレンやメチルスチレン等のポリスチレン系樹
脂その他の一般に押出し発泡成形可能な各種の熱可塑性
樹脂を使用できる。
As the material resin of the thermoplastic resin foam (1), in addition to polyolefin resins such as polyethylene, polypropylene and copolymers mainly composed of olefins, polystyrene resins such as styrene and methylstyrene are generally used. Various thermoplastic resins capable of extrusion foam molding can be used.

【0022】特に接着性の低いポリオレフィン系樹脂、
中でも密度が0.91〜0.93g/cm2 の低密度ポ
リエチレン単独の樹脂を素材とすることもでき、この場
合にも発泡板相互間に接着強度を充分に確保できる。
A polyolefin resin having particularly low adhesiveness,
Above all, a resin of low density polyethylene alone having a density of 0.91 to 0.93 g / cm @ 2 can be used as a raw material, and in this case, sufficient adhesive strength can be secured between the foam plates.

【0023】本発明の熱可塑性樹脂発泡体の厚みや幅、
密度や発泡倍率は、融着される帯板状発泡板の縦横の寸
法や融着枚数、発泡度等によって適宜設定でき、中でも
密度が0.18〜0.018g/cm2 、発泡倍率50
倍以下のもので、厚みが50〜200mmの比較的厚物
の発泡体に好適に適用でき、また連続気泡率が50%以
下の発泡構造を有するものにも適用できる。
The thickness and width of the thermoplastic resin foam of the present invention,
The density and the expansion ratio can be appropriately set depending on the vertical and horizontal dimensions of the band-plate-shaped foam plate to be fused, the number of sheets to be fused, the degree of foaming, among others, the density is 0.18 to 0.018 g / cm 2, and the expansion ratio is 50.
It can be suitably applied to a relatively thick foam having a thickness of 50 to 200 mm and a foam structure having an open cell ratio of 50% or less.

【0024】帯板状発泡板を縦型で押出す押出機におけ
る口金(11)のスリット(12)の数、間隙(w)、
縦方向寸法(h)およびスリット間隔(s)は、得よう
とする熱可塑性樹脂発泡体の厚みや幅、密度(発泡倍
率)等に応じて適宜設定できるが、スリットの間隙
(w)は3mm以下、好ましくは0.5〜2mmであ
る。すなわち、スリット間隙(w)が前記より大きくな
ると、押出し発泡成形された発泡密度が不均一になり易
く好ましくない。また前記間隙(w)が0.5mm以下
になると、発泡体を軟化状態下で縦型に保持するのが困
難になり好ましいものではない。縦型のスリットをジグ
ザグ状あるいは波状に形成しておくことも可能である。
The number of slits (12) of the die (11) in the extruder for vertically extruding the strip-shaped foam plate, the gap (w),
The lengthwise dimension (h) and the slit spacing (s) can be appropriately set according to the thickness and width of the thermoplastic resin foam to be obtained, the density (foaming ratio), etc., but the slit gap (w) is 3 mm. Below, it is preferably 0.5 to 2 mm. That is, if the slit gap (w) is larger than the above, the foam density obtained by extrusion foam molding tends to be non-uniform, which is not preferable. Further, if the gap (w) is 0.5 mm or less, it becomes difficult to hold the foam in a vertical shape in a softened state, which is not preferable. It is also possible to form the vertical slit in a zigzag shape or a wavy shape.

【0025】得ようとする熱可塑性樹脂発泡体の幅が大
きい場合、複数の押出機を並設してそれぞれの口金のス
リットから押出される帯板状発泡板を融着一体化させる
ようにしてもよい。
When the width of the thermoplastic resin foam to be obtained is large, a plurality of extruders are installed side by side so that the strip-shaped foam plates extruded from the slits of the respective caps are fused and integrated. Good.

【0026】上記のように押出し発泡成形された多数の
帯板状発泡板(2)を横列に並べて相互に融着するの
で、前記帯板状発泡板(2)の縦方向寸法を大きくとる
ことにより、全体として厚みの大きな厚物発泡体を得る
ことができる。
Since a large number of strip-plate foam plates (2) extruded and foam-molded as described above are arranged in rows and fused to each other, the longitudinal dimension of the strip-plate foam plates (2) should be large. Thereby, a thick foamed product having a large thickness as a whole can be obtained.

【0027】実施例1 低密度ポリエチレン樹脂(日本ユニカー社製、商品名:
DFDJ−6776、メルトインデックス:0.3g/
10min、115℃においてヒートシール強度0.9
5N)100部に対して、気泡調整剤(ベーリンガー・
インゲルハイム社製、商標名ハイドロセロール)0.2
0部を添加した混合物を、1時間当たり110kgの量
となるように第1の押出機のホッパーから供給し、発泡
剤としてブタンを3.6kg/hrで先端部で供給し、
図3に示すような縦40mm、横1mmのスリットが8
mm間隔で配列形成された口金(11)から押出し発泡
成形し、その直後にロール成形すると、厚み60mm、
幅160mm、発泡体密度0.18g/cm3 (発泡倍
率5〜6倍)、連続気泡率18%の発泡体を得ることが
できた。この発泡体は発泡状態が全体に均一化して断面
が一様であり、一体性良好な発泡体であった。
Example 1 Low-density polyethylene resin (manufactured by Nippon Unicar Co., Ltd., trade name:
DFDJ-6776, melt index: 0.3 g /
Heat seal strength 0.9 at 10 min at 115 ° C
5N) to 100 parts, a bubble regulator (Boehringer
Ingelheim, trade name Hydrocelol) 0.2
The mixture to which 0 part was added was supplied from the hopper of the first extruder so that the amount thereof was 110 kg per hour, and butane as a foaming agent was supplied at the tip part at 3.6 kg / hr.
There are 8 slits 40mm long and 1mm wide as shown in Fig. 3.
When extrusion molding is performed from a die (11) arrayed at mm intervals, and immediately after that, roll molding is performed, a thickness of 60 mm,
A foam having a width of 160 mm, a foam density of 0.18 g / cm 3 (foaming ratio of 5 to 6), and an open cell ratio of 18% could be obtained. This foam had a uniform foaming state and a uniform cross section, and was a foam with good integrity.

【0028】実施例2 実施例1とは、ブタンの注入量を10.8g/hr、ハ
イドロセロール0.16部に変更した以外は、実施例1
と同じ条件(実施例1と同様の構造で縦40mm、横m
m0.6mmのスリットが5mm間隔に配列形成された
口金を使用)で押出すと、厚み60mm、幅200m
m、発泡体密度0.023g/cm3 (発泡倍率約30
倍)、連続気泡率38%の発泡体を得ることができた。
この発泡体も、発泡状態および一体性ともに良好であっ
た。
Example 2 Example 1 is the same as Example 1 except that the injection amount of butane was changed to 10.8 g / hr and hydrocerol was changed to 0.16 parts.
Under the same conditions as above (40 mm in length and m in width with the same structure as in Example 1)
When using a die with slits of 0.6 mm arranged at 5 mm intervals, the thickness is 60 mm and the width is 200 m.
m, foam density 0.023 g / cm3 (foaming ratio about 30
It was possible to obtain a foam having an open cell ratio of 38%.
This foam was also good in foaming state and integrity.

【0029】実施例3 実施例1と同じ配合で、1時間当たり130kgの量と
なるように第1の押出機のホッパーから供給し、発泡剤
としてブタンを4.3kg/hrで先端部で供給し、縦
10mm、横1mmのスリットを8mm間隔に配列した
口金から押出したところ、厚み150mm、幅150m
m、発泡密度0.18g/cm3 、連続気泡率28%の
発泡体を得ることができた。この発泡体も、発泡状態お
よび一体性ともに良好であった。
Example 3 The same composition as in Example 1 was supplied from the hopper of the first extruder so that the amount was 130 kg per hour, and butane as a foaming agent was supplied at the tip portion at 4.3 kg / hr. Then, when a slit having a length of 10 mm and a width of 1 mm is extruded from a die having 8 mm intervals, a thickness of 150 mm and a width of 150 m.
m, foam density of 0.18 g / cm 3, and open cell rate of 28% could be obtained. This foam was also good in foaming state and integrity.

【0030】実施例4 実施例2と同じ配合で、1時間当り130kgの量とな
るように第1の押出機のホッパーから供給し、発泡剤と
してブタンを12.8kg/hrで先端部で供給し、縦
10mm、横0.6mmのスリットを5mm間隔に配列
した口金から、該口金を厚物用にして押出し成形する
と、厚み150mm、幅180mm、発泡体密度0.0
23g/cm3 、連続気泡率38gの発泡体を得ること
ができた。この発泡体の発泡状態および一体性はともに
良好であった。
Example 4 The same composition as in Example 2 was supplied from the hopper of the first extruder so that the amount was 130 kg per hour, and butane as a foaming agent was supplied at the tip portion at 12.8 kg / hr. Then, from a die in which slits having a length of 10 mm and a width of 0.6 mm are arranged at intervals of 5 mm, the die is extruded and molded for a thick material, and a thickness of 150 mm, a width of 180 mm, and a foam density of 0.0
A foam having a rate of 23 g / cm @ 3 and an open cell rate of 38 g could be obtained. The foamed state and the integrity of this foam were both good.

【0031】比較例1 実施例4の厚み、発泡体密度の製品をTダイを使って押
出し発泡成形を行なったが、良好な厚物の発泡体を得る
ことができなかった。
Comparative Example 1 A product having the same thickness and foam density as in Example 4 was extruded and foamed using a T-die, but a good thick foam could not be obtained.

【0032】比較例2 比較例1と同様の製品のストランドによる押出し成形を
実施したが、発泡適性温度にするために押出機先端の温
度を下げると、口金のストランド押出し用の孔が何本か
詰ってしまったことと、ストランド1本1本の接着性が
悪くなり、良好な発泡体を得ることができなかった。
COMPARATIVE EXAMPLE 2 The same product as in Comparative Example 1 was extruded by using a strand. However, when the temperature at the tip of the extruder was lowered in order to attain a foaming-appropriate temperature, several holes for strand extrusion of the die were found. Since it was clogged and the adhesiveness of each strand was deteriorated, a good foam could not be obtained.

【0033】[0033]

【発明の効果】上記したように本発明の熱可塑性樹脂発
泡体によれば、縦型で押出し発泡された帯板状発泡板の
複数を横列に並べて相互に融着一体化させているので、
従来よりも厚物の発泡体を得ることができる。しかも各
帯板状発泡板として押出し発泡成形するので、全体とし
て均一な発泡状態を得ることができ、またストランドタ
イプの集合体よりなるものに比して隣接する帯板状発泡
板同士の接着強度が高く、ポリエチレン樹脂等の接着性
の低い樹脂を素材とするものを融着形成したものであっ
ても、一体性良好なものとなる。
As described above, according to the thermoplastic resin foam of the present invention, since a plurality of strip-shaped foam plates extruded in a vertical form are arranged in a row and are fused and integrated with each other,
It is possible to obtain a foam that is thicker than before. Moreover, since each strip-shaped foam plate is extruded and foam-molded, a uniform foaming state can be obtained as a whole, and the adhesive strength between adjacent strip-plate foam plates is higher than that of a strand type aggregate. Even if a resin made of a resin having high adhesiveness and low adhesiveness such as polyethylene resin is formed by fusion bonding, good integration can be obtained.

【0034】特に、請求項2のように、隣接する帯板状
発泡板がジグザグ状や波状に屈曲して融着一体化してい
る場合、その融着部が屈折状をなして融着面積が増大す
るために、発泡板相互間の接着強度がさらに高くなり、
素材がポリエチレン等の接着性の低いものであっても、
充分に高い接着強度を保有する。
Particularly, when the adjacent strip-shaped foamed plates are bent in a zigzag shape or a wavy shape to be fused and integrated as described in claim 2, the fused portion has a refraction shape and the fused area is Due to the increase, the adhesive strength between the foam plates is further increased,
Even if the material is one with low adhesion such as polyethylene,
Has sufficiently high adhesive strength.

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

【図1】本発明の熱可塑性樹脂発泡体の1実施例を示す
斜視図である。
FIG. 1 is a perspective view showing one embodiment of a thermoplastic resin foam of the present invention.

【図2】本発明の熱可塑性樹脂発泡体の他の実施例を示
す断面図である。
FIG. 2 is a sectional view showing another embodiment of the thermoplastic resin foam of the present invention.

【図3】本発明の熱可塑性樹脂発泡体を製造するのに使
用する押出機の口金を示す正面図である。
FIG. 3 is a front view showing a die of an extruder used for producing the thermoplastic resin foam of the present invention.

【符号の説明】[Explanation of symbols]

(1) 熱可塑性樹脂発泡体 (2) 押出し発泡板 (3) 融着部 (1) Thermoplastic resin foam (2) Extruded foam plate (3) Fusion part

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B29L 7:00 9:00 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display area B29L 7:00 9:00

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】複数の縦型のスリットから押出し発泡成形
された断面縦長の熱可塑性樹脂の帯板状発泡板を、軟化
状態下で横列に並べて側面同士を合せて隣接させ、隣接
部で互いに融着せしめて、比較的厚物の発泡体に成形し
てなることを特徴とする熱可塑性樹脂発泡体。
1. A strip-plate foam plate made of a thermoplastic resin having a vertically long section extruded and foamed from a plurality of vertical slits is arranged in a row in a softened state so that the side faces thereof are adjacent to each other and adjacent to each other. A thermoplastic resin foam, which is formed by being fused and formed into a relatively thick foam.
【請求項2】隣接する複数の帯板状発泡板が、ジグザグ
状や波状に屈曲して相互に融着一体化せしめられてなる
請求項1に記載の熱可塑性樹脂発泡体。
2. The thermoplastic resin foam according to claim 1, wherein a plurality of adjoining strip-shaped foam plates are bent in a zigzag shape or a wavy shape so as to be fused and integrated with each other.
JP6328000A 1994-12-28 1994-12-28 Thermoplastic resin foam body Pending JPH08183082A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6328000A JPH08183082A (en) 1994-12-28 1994-12-28 Thermoplastic resin foam body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6328000A JPH08183082A (en) 1994-12-28 1994-12-28 Thermoplastic resin foam body

Publications (1)

Publication Number Publication Date
JPH08183082A true JPH08183082A (en) 1996-07-16

Family

ID=18205392

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6328000A Pending JPH08183082A (en) 1994-12-28 1994-12-28 Thermoplastic resin foam body

Country Status (1)

Country Link
JP (1) JPH08183082A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0922554A1 (en) * 1997-12-08 1999-06-16 Dow Deutschland Inc. Multilayer foams
GB2489212A (en) * 2011-03-15 2012-09-26 Gurit Uk Ltd Structural foam manufacture
EP2669446B1 (en) * 2008-04-10 2015-07-29 Velcro Industries B.V. Securing exterior construction material
US10934716B2 (en) 2018-09-17 2021-03-02 Velcro Ip Holdings Llc Construction underpayment

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0922554A1 (en) * 1997-12-08 1999-06-16 Dow Deutschland Inc. Multilayer foams
WO1999029483A1 (en) * 1997-12-08 1999-06-17 The Dow Chemical Company Multilayer foams
EP2669446B1 (en) * 2008-04-10 2015-07-29 Velcro Industries B.V. Securing exterior construction material
US9637926B2 (en) 2008-04-10 2017-05-02 Velcro BVBA Membrane roofing
US9752326B2 (en) 2008-04-10 2017-09-05 Velcro BVBA Membrane roofing
US9963880B2 (en) 2008-04-10 2018-05-08 Velcro BVBA Membrane roofing
GB2489212A (en) * 2011-03-15 2012-09-26 Gurit Uk Ltd Structural foam manufacture
GB2489212B (en) * 2011-03-15 2013-11-20 Gurit Uk Ltd Sandwich panel and manufacture thereof
US10934716B2 (en) 2018-09-17 2021-03-02 Velcro Ip Holdings Llc Construction underpayment
US11332938B2 (en) 2018-09-17 2022-05-17 Velcro Ip Holdings Llc Construction underlayment

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