JPH10245446A - Production of foamed body - Google Patents

Production of foamed body

Info

Publication number
JPH10245446A
JPH10245446A JP4795197A JP4795197A JPH10245446A JP H10245446 A JPH10245446 A JP H10245446A JP 4795197 A JP4795197 A JP 4795197A JP 4795197 A JP4795197 A JP 4795197A JP H10245446 A JPH10245446 A JP H10245446A
Authority
JP
Japan
Prior art keywords
foam
shape
raw material
foamed body
compression
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
JP4795197A
Other languages
Japanese (ja)
Inventor
Hitoshi Shirato
斉 白土
Hideyuki Taguchi
秀之 田口
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 Chemical Co Ltd
Original Assignee
Sekisui Chemical 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 Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP4795197A priority Critical patent/JPH10245446A/en
Publication of JPH10245446A publication Critical patent/JPH10245446A/en
Pending legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a foamed body capable of forming a shape-recovering foamed body by compression in a short time by compressing a raw material foamed body in a state kept within a specific temperature range. SOLUTION: A raw material foamed body comprising an closed-cell resin foamed body is compressed in a state kept at a temp. 30 deg.C and the softening temperature of a resin forming the raw material foamed body, preferably, between 40 deg.C and (the softening temperature of the resin) -20 deg.C to provide a foamed body having delayed shape recovering properties. Thereby, the shape- recovering foamed body can be obtained in a shaft time while improving the productivity thereof. Furthermore, the foamed body having the thickness close to the objective one can be obtained.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、遅延した形状回復
性を有する発泡体(以下、「形状回復発泡体」と記す)
の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a foam having a delayed shape recovery property (hereinafter referred to as "shape recovery foam").
And a method for producing the same.

【0002】[0002]

【従来の技術】本発明の発明者らは、当初樹脂の弾性限
界内で気泡が収縮状態に保持されていて、樹脂の弾性回
復力により気泡の内外圧力と釣り合いながら徐々に元の
厚さに回復してゆく、独立気泡樹脂発泡体からなる原料
発泡体を収縮させて得た形状回復発泡体をすでに提案し
ている(特願平7−299654号等参照)。
2. Description of the Related Art The inventors of the present invention initially hold a bubble in a contracted state within the elastic limit of the resin, and gradually recover the original thickness while balancing the inner and outer pressures of the bubble by the elastic recovery force of the resin. A shape-recovery foam obtained by shrinking a raw material foam made of a closed-cell resin foam that recovers has already been proposed (see Japanese Patent Application No. 7-299654).

【0003】ところで、このような形状回復発泡体を得
る方法として、原料発泡体をプレス板間に挟み込む等し
て独立気泡(セル)内のガスを気泡壁を透過させて外部
に排気しながら圧縮する方法がある。しかしながら、気
泡内のガスが気泡壁を透過する速度が遅いので、この圧
縮を用いた方法では、原料発泡体を所定の厚みまで収縮
させるのにかなりの時間が必要で生産性が悪いと言う問
題がある。
As a method of obtaining such a shape-recovery foam, a gas in closed cells (cells) is compressed while exhausting the gas through closed cell walls by sandwiching the raw material foam between press plates or the like. There is a way to do that. However, since the speed at which the gas in the gas bubbles permeates the cell wall is slow, the method using this compression requires a considerable amount of time to shrink the raw material foam to a predetermined thickness, resulting in poor productivity. There is.

【0004】因みに、原料発泡体としての発泡倍率30
倍、厚み10mm、独立気泡率80%のポリエチレン発泡
体を圧縮(圧縮厚み0.5mm)して厚み2mmの形状回復
発泡体を得ようとすると、約40分の時間が必要であっ
た。
[0004] Incidentally, a foaming ratio of 30 as a raw material foam is obtained.
In order to obtain a shape-recovered foam having a thickness of 2 mm by compressing a polyethylene foam having a thickness of 10 mm and a closed cell ratio of 80% (compressed thickness of 0.5 mm), it took about 40 minutes.

【0005】[0005]

【発明が解決しようとする課題】本発明は、上記事情に
鑑みて、短時間で圧縮により形状回復発泡体を得ること
ができる発泡体の製造方法を提供することを目的として
いる。
SUMMARY OF THE INVENTION In view of the above circumstances, an object of the present invention is to provide a method for producing a foam capable of obtaining a shape-recovered foam by compression in a short time.

【0006】[0006]

【課題を解決するための手段】このような目的を達成す
るために、請求項1に記載の発明にかかる発泡体の製造
方法(以下、「請求項1の製造方法」と記す)は、独立
気泡樹脂発泡体からなる原料発泡体を圧縮させてなる遅
延した形状回復性を有する発泡体の製造方法において、
原料発泡体を30℃以上で原料発泡体を形成する樹脂の
軟化温度以下の温度に保持した状態で圧縮するようにし
た。
In order to achieve such an object, a method for producing a foam according to the first aspect of the present invention (hereinafter referred to as "a method for producing the first aspect") is independent. In a method for producing a foam having a delayed shape recovery property obtained by compressing a raw material foam made of a cellular resin foam,
The raw material foam was compressed while maintaining the temperature at 30 ° C. or higher and the softening temperature of the resin forming the raw material foam or lower.

【0007】請求項2に記載の発明にかかる発泡体の製
造方法(以下、「請求項2の製造方法」と記す)は、請
求項1の製造方法において、原料発泡体の圧縮によって
得られた収縮体を圧縮直後に20℃以下に冷却するよう
にした。
According to a second aspect of the present invention, there is provided a method of producing a foam (hereinafter referred to as a “method of producing a second aspect”) obtained by compressing a raw material foam in the production method of the first aspect. Immediately after compression, the contracted body was cooled to 20 ° C. or less.

【0008】請求項3に記載の発明にかかる発泡体の製
造方法(以下、「請求項2の製造方法」と記す)は、請
求項1または請求項2の製造方法において、表面から内
部の独立気泡内に連通する通気路を原料発泡体に予め所
定ピッチで穿設しておくようにした。
[0008] The method for producing a foam according to the invention according to claim 3 (hereinafter referred to as "the production method according to claim 2") is a method according to claim 1 or 2, wherein An air passage communicating with the inside of the cell was previously formed at a predetermined pitch in the raw material foam.

【0009】請求項1〜3の製造方法において、原料発
泡体を圧縮する方法としては、特に限定されないが、た
とえば、原料発泡体を所望の間隔で対面して配置された
2つの無端ベルトやローラ間に通して無端ベルトやロー
ラ間で所定時間圧縮する方法や、2枚のプレス板の間で
所定時間圧縮する方法等が挙げられる。
In the manufacturing method according to any one of claims 1 to 3, the method for compressing the raw material foam is not particularly limited. For example, two endless belts or rollers arranged with the raw material foam facing each other at a desired interval There is a method of compressing between endless belts and rollers for a predetermined period of time, or a method of compressing between two press plates for a predetermined period of time.

【0010】原料発泡体の加熱方法としては、特に限定
されないが、たとえば、プレス板を用いて圧縮する方法
では、プレス板内に棒状のヒータや加熱オイル等の熱媒
体の流路等を設け、プレス板自体をこのヒータや熱媒体
の熱によって加熱して圧縮と同時に原料発泡体をプレス
板を介して加熱する方法が挙げられ、無端ベルトやロー
ラを用いて圧縮する方法では、無端ベルトやローラをま
ず加熱しておき、無端ベルトやローラ間で圧縮すると同
時に無端ベルトやローラの熱で原料発泡体を加熱する方
法が挙げられる。また、無端ベルト、ローラあるいはプ
レス板を備えた圧縮装置自体を熱風加熱装置や赤外線加
熱装置内に設置し、圧縮装置で原料発泡体を圧縮すると
同時に熱風や赤外線によって原料発泡体を加熱する方法
でも構わない。
The method of heating the raw material foam is not particularly limited. For example, in the method of compressing using a press plate, a rod-shaped heater or a flow path of a heating medium such as heating oil is provided in the press plate. A method in which the press plate itself is heated by the heat of the heater or the heat medium to compress and simultaneously heat the raw material foam through the press plate, and in the method of compressing using the endless belt or roller, the endless belt or roller is used. Is heated first, and the raw material foam is heated by the heat of the endless belt or roller while being compressed between the endless belt or roller. Also, a method of installing a compression device itself having an endless belt, a roller or a press plate in a hot air heating device or an infrared heating device and compressing the raw material foam by the compression device and simultaneously heating the raw material foam by hot air or infrared light is also used. I do not care.

【0011】圧縮時の原料発泡体の温度は、30℃以上
で原料発泡体を形成する樹脂の軟化温度以下に限定され
るが、好ましくは、40℃以上で樹脂の軟化温度−20
℃以下である。なお、30℃を下回ると、圧縮に要する
時間が従来と大差なくなり、軟化温度を越えると、圧縮
中に樹脂が応力緩和し、得られた形状回復発泡体の形状
回復性が悪くなる。
The temperature of the raw material foam at the time of compression is limited to 30 ° C. or higher but not higher than the softening temperature of the resin forming the raw material foam.
It is below ° C. If the temperature is lower than 30 ° C., the time required for compression is not much different from the conventional one. If the softening temperature is exceeded, the resin relaxes the stress during compression, and the shape recovery property of the obtained shape recovery foam deteriorates.

【0012】原料発泡体、すなわち形状回復発泡体を形
成する樹脂としては、特に限定されないが、圧縮永久歪
み(JIS K 6767に準拠)が20%以下のも
の、特に10%以下のものが形状回復性に優れ好まし
く、たとえば、ポリエチレン,ポリプロピレン,エチレ
ン−プロピレン共重合体,エチレン−プロピレン−ジエ
ン共重合体,エチレン−酢酸ビニル共重合体等のオレフ
ィン系樹脂、ポリメチルアクリレート,ポリメチルメタ
クリレート,エチレン−エチルアクリレート共重合体等
のアクリル系樹脂、ブタジエン−スチレン,アクリロニ
トリル−スチレン,スチレン,スチレン−ブタジエン−
スチレン,スチレン−イソプレン−スチレン,スチレン
−アクリル酸等のスチレン系樹脂、アクリロニトリル−
ポリ塩化ビニル,ポリ塩化ビニル−エチレン等の塩化ビ
ニル系樹脂、ポリフッ化ビニル,ポリフッ化ビニリデン
等のフッ化ビニル系樹脂、6−ナイロン,6・6−ナイ
ロン,12−ナイロン等のアミド樹脂、ポリエチレンテ
レフタレート,ポリブチレンテレフタレート等の飽和エ
ステル系樹脂、ポリカーボネート、ポリフェニレンオキ
サイド、ポリアセタール、ポリフェニレンスルフィド、
シリコーン樹脂、熱可塑性ウレタン樹脂、ポリエーテル
エーテルケトン、ポリエーテルイミド、各種エラストマ
ーやこれらの架橋体等の熱可塑性樹脂が挙げられる。
The raw material foam, that is, the resin forming the shape-recovery foam is not particularly limited, but the one having a compression set (according to JIS K 6767) of 20% or less, particularly 10% or less, is used for the shape recovery. For example, olefin resins such as polyethylene, polypropylene, ethylene-propylene copolymer, ethylene-propylene-diene copolymer, ethylene-vinyl acetate copolymer, polymethyl acrylate, polymethyl methacrylate, ethylene- Acrylic resins such as ethyl acrylate copolymer, butadiene-styrene, acrylonitrile-styrene, styrene, styrene-butadiene-
Styrene resins such as styrene, styrene-isoprene-styrene, styrene-acrylic acid, acrylonitrile-
Polyvinyl chloride resins such as polyvinyl chloride and polyvinyl chloride-ethylene; vinyl fluoride resins such as polyvinyl fluoride and polyvinylidene fluoride; amide resins such as 6-nylon, 6.6-nylon and 12-nylon; polyethylene Saturated ester resins such as terephthalate and polybutylene terephthalate, polycarbonate, polyphenylene oxide, polyacetal, polyphenylene sulfide,
Examples include thermoplastic resins such as silicone resins, thermoplastic urethane resins, polyetheretherketone, polyetherimide, various elastomers, and crosslinked products thereof.

【0013】原料発泡体の独立気泡率は、得ようとする
形状回復発泡体が必要とする回復量により決まり、5%
以上であれば使用することが可能であるが、特に好まし
い範囲は30%〜100%である。原料発泡体の製造方
法は、プラスチックフォームハンドブックに記載されて
いる方法を含め公知の方法が挙げられ、熱分解型発泡剤
および物理型発泡剤を用いたいずれの発泡方法を用いて
も構わない。
The closed cell ratio of the raw material foam is determined by the amount of recovery required by the shape recovery foam to be obtained, and is 5%.
If it is above, it can be used, but a particularly preferred range is 30% to 100%. The method for producing the raw material foam includes known methods including the method described in the Plastic Foam Handbook, and any foaming method using a pyrolytic foaming agent and a physical foaming agent may be used.

【0014】また、原料発泡体には、充填剤、補強繊
維、着色剤、紫外線吸収剤、酸化防止剤、難燃剤等を必
要に応じて混合されていても構わない。充填剤として
は、たとえば、炭酸カルシウム、タルク、クレー、酸化
マグネシウム、酸化亜鉛、カーボンブラック、二酸化ケ
イ素、酸化チタン、ガラス粉、ガラスビーズ等が挙げら
れる。
The raw material foam may contain a filler, a reinforcing fiber, a coloring agent, an ultraviolet absorber, an antioxidant, a flame retardant, and the like, if necessary. Examples of the filler include calcium carbonate, talc, clay, magnesium oxide, zinc oxide, carbon black, silicon dioxide, titanium oxide, glass powder, glass beads and the like.

【0015】補強繊維としては、たとえば、ガラス繊
維、炭素繊維等が挙げられる。着色剤としては、たとえ
ば、酸化チタン等の顔料が挙げられる。酸化防止剤とし
ては、一般に用いれるものであれば、特に限定されず、
たとえば、テトラキス〔メチレン(3,5−ジ−t−ブ
チル−4−ヒドロキシハイドロシンナメート)〕メタ
ン、チオジプロピオン酸ジラウリル、1,1,3−トリ
ス(2−メチル−4−ヒドロキシ−5−t−ブチルフェ
ニル)ブタン等が挙げられる。
Examples of the reinforcing fibers include glass fibers and carbon fibers. Examples of the coloring agent include pigments such as titanium oxide. The antioxidant is not particularly limited as long as it is generally used,
For example, tetrakis [methylene (3,5-di-t-butyl-4-hydroxyhydrocinnamate)] methane, dilauryl thiodipropionate, 1,1,3-tris (2-methyl-4-hydroxy-5- t-butylphenyl) butane and the like.

【0016】難燃剤としては、ヘキサブロモフェニルエ
ーテル,デカブロモジフェニルエーテル等の臭素系難燃
剤、ポリリン酸アンモニウム,トリメチルホスフェー
ト,トリエチルホスフェート等の含リン酸系難燃剤、メ
ラミン誘導体、無機系難燃剤等の1種又は2種以上の混
合物が挙げられる。形状回復発泡体の形状は、特に限定
されないが、シート状、ロッド状、チューブ状をしたも
のなどが挙げられ、形状回復前の形状と形状回復後の形
状とが非相似形となるものでも構わない。
Examples of the flame retardant include brominated flame retardants such as hexabromophenyl ether and decabromodiphenyl ether, phosphoric acid-containing flame retardants such as ammonium polyphosphate, trimethyl phosphate and triethyl phosphate, melamine derivatives, inorganic flame retardants and the like. One type or a mixture of two or more types may be mentioned. The shape of the shape-recovery foam is not particularly limited, and examples thereof include a sheet-like shape, a rod-like shape, and a tube-like shape, and the shape before shape recovery and the shape after shape recovery may be non-similar. Absent.

【0017】請求項2の製造方法において、冷却温度
は、20℃以下に限定されるが、好ましくは10℃以下
である。なお、冷却温度が20℃を上回ると、圧縮によ
って収縮した収縮体が巻取り機等によって巻き取る途中
で形状回復してしまう恐れがある。また、圧縮部と冷却
部との間には、断熱層を設けることが好ましい。
In the manufacturing method according to the second aspect, the cooling temperature is limited to 20 ° C. or lower, but is preferably 10 ° C. or lower. If the cooling temperature is higher than 20 ° C., the shrinkable body shrunk by compression may recover its shape during winding by a winder or the like. Further, it is preferable to provide a heat insulating layer between the compression section and the cooling section.

【0018】請求項3の製造方法において、通気路とし
ては、直線状だけでなく、螺旋状、円弧状など特にその
形状が限定されない。通気路の断面形状は、特に限定さ
れず、たとえば、円形、三角形、四角形、星形、線状、
波線状等が挙げられる。
In the manufacturing method according to the third aspect, the shape of the ventilation path is not limited to a straight line, but is not particularly limited to a spiral shape or an arc shape. The cross-sectional shape of the air passage is not particularly limited, for example, a circle, a triangle, a square, a star, a line,
Wavy lines and the like can be mentioned.

【0019】通気路の大きさは、特に限定されないが、
断面積を7mm2 (断面が円形の場合、直径3mm程
度)以下とすることが好ましく、その最大(幅)を独立
気泡の平均気泡径以下とすることがより好ましい。すな
わち、大き過ぎると気泡構造が破壊され、元の形状に回
復しなくなる恐れがある。通気路の中心の間隔は、特に
限定されないが、通気路の断面が気泡径より小さい場
合、気泡径の2倍以上とし、通気路の断面が気泡径より
大きい場合、隣接する通気路の外縁間の距離が気泡径以
上とすることが好ましい。
Although the size of the ventilation path is not particularly limited,
The cross-sectional area is preferably 7 mm 2 (when the cross section is circular, about 3 mm in diameter) or less, and more preferably the maximum (width) thereof is equal to or less than the average cell diameter of the closed cells. That is, if it is too large, the bubble structure may be broken, and the original shape may not be recovered. The interval between the centers of the air passages is not particularly limited. When the cross section of the air passage is smaller than the bubble diameter, it is set to twice or more the bubble diameter. Is preferably not less than the bubble diameter.

【0020】通気路の深さは、必要とする回復時間によ
り決定され、特に限定されないが、表面から3つ以上内
部の独立気泡まで達していることが好ましい。さらに、
通気路は、原料発泡体の表面に対して垂直に設けても構
わないし、表面に対して所定の角度を付けて設けるよう
にしても構わない。また、形状回復発泡体の内部に向か
って螺旋状に設けるようにしても構わない。
The depth of the ventilation path is determined by the required recovery time, and is not particularly limited. It is preferable that the ventilation path reaches at least three or more internal closed cells from the surface. further,
The ventilation path may be provided perpendicular to the surface of the raw material foam, or may be provided at a predetermined angle to the surface. Moreover, you may make it provide spirally toward the inside of a shape recovery foam.

【0021】通気路を穿設する方法としては、特に限定
されないが、孔状の通気路を設ける場合、針(剣山)、
ドリル、電子ビーム、レーザー光線等を用いる方法が挙
げられ、溝状の通気路を設ける場合、カッター(刃物)
等を用いる方法が挙げられる。
The method of forming the ventilation path is not particularly limited, but when a hole-shaped ventilation path is provided, a needle (Kenyama),
A method using a drill, an electron beam, a laser beam, or the like can be used. When a groove-shaped ventilation path is provided, a cutter (knife) is used.
And the like.

【0022】[0022]

【発明の実施の形態】以下に、本発明の実施の形態を、
図面を参照しつつ詳しく説明する。図1は本発明にかか
る発泡体の製造方法の第1の実施の形態をあらわしてい
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below.
This will be described in detail with reference to the drawings. FIG. 1 shows a first embodiment of a method for producing a foam according to the present invention.

【0023】この製造方法は、図1に示すように、ロー
ル状に巻回された帯状の原料発泡体1を、圧縮装置2a
の2枚のプレス板21,21の間に連続的に送り込み、
プレス板21,21をプレス板21,21の内部に設け
られた棒状のヒータ(図示せず)によって加熱して原料
発泡体1をプレス板21,21の間で30℃以上で原料
発泡体1を形成する樹脂の軟化温度以下の温度に加熱し
ながら圧縮し、原料発泡体1を所定の厚みまで収縮した
収縮体3とする。
In this manufacturing method, as shown in FIG. 1, a strip-shaped raw material foam 1 wound in a roll shape is compressed by a compression device 2a.
Continuously between the two press plates 21, 21 of
The press plates 21 and 21 are heated by a rod-shaped heater (not shown) provided inside the press plates 21 and 21, and the raw material foam 1 is heated between the press plates 21 and 21 at 30 ° C. or more. The raw material foam 1 is compressed while being heated to a temperature equal to or lower than the softening temperature of the resin forming the resin foam, thereby forming a contracted body 3 which is contracted to a predetermined thickness.

【0024】つぎに、この収縮体3を、連続的に冷却室
4内に導入し、冷却室4内で、冷却機5から送り込まれ
た冷風によって20℃以下に冷却して形状回復発泡体6
としたのち、巻取り装置7で連続的に巻取るようになっ
ている。なお、図1中、8は、プレス板21,21の熱
が冷却室4内に伝わらないようにする断熱材である。
Next, the contracted body 3 is continuously introduced into the cooling chamber 4, and is cooled to 20 ° C. or less in the cooling chamber 4 by cold air sent from the cooler 5, and the shape-recovered foam 6 is cooled.
After that, the winding device 7 continuously winds. In FIG. 1, reference numeral 8 denotes a heat insulating material that prevents heat of the press plates 21 and 21 from being transmitted into the cooling chamber 4.

【0025】すなわち、この製造方法によれば、原料発
泡体1を30℃以上で原料発泡体1を形成する樹脂の軟
化温度以下の温度に加熱した状態で圧縮するので、樹脂
が応力緩和しない程度に柔らかくなり、気泡壁を透過し
て独立気泡内のガスが抜けやすくなる。したがって、圧
縮に要する時間が短縮できる。また、このように圧縮に
より収縮した収縮体を圧縮直後に20℃以下に冷却する
ようにしたので、巻取り装置7で巻取られるまで形状回
復発泡体6が形状回復を起こすことがない。 すなわ
ち、所定の厚みの形状回復発泡体6を確実に得ることが
できるようになる。
That is, according to this production method, the raw material foam 1 is compressed while being heated to a temperature not lower than the softening temperature of the resin forming the raw material foam 1 at 30 ° C. or more, so that the resin does not relax the stress. And the gas in the closed cells easily escapes through the cell wall. Therefore, the time required for compression can be reduced. In addition, since the contracted body contracted by the compression is cooled to 20 ° C. or less immediately after the compression, the shape recovery foam 6 does not recover its shape until it is wound by the winding device 7. That is, it is possible to reliably obtain the shape-recovery foam 6 having a predetermined thickness.

【0026】図2は、本発明にかかる発泡体の製造方法
の第2の実施の形態をあらわしている。
FIG. 2 shows a second embodiment of the method for producing a foam according to the present invention.

【0027】この製造方法は、圧縮装置2bとして、圧
縮装置2aと同様に内部に棒状のヒータを備えたプレス
板21とプレス板21との間に無端ベルト22,22を
2段に設けたものを用い、原料発泡体1を上側のプレス
板21と上側の無端ベルト22との間、無端ベルト22
と無端ベルト22との間、下側の無端ベルト22と下側
のプレス板21との間の順で通して圧縮し、収縮体3を
得るようにした以外は、第1の実施の形態と同様になっ
ている。
In this manufacturing method, two endless belts 22, 22 are provided between a press plate 21 provided with a rod-shaped heater inside and a press plate 21 as the compression device 2b as in the compression device 2a. The raw material foam 1 is placed between the upper press plate 21 and the upper endless belt 22 by the endless belt 22.
And the endless belt 22, and between the lower endless belt 22 and the lower press plate 21, in order, to compress and obtain the contracted body 3. It is similar.

【0028】すなわち、この製造方法によれば、圧縮装
置2bの幅を小さくしても、圧縮部の長さを長くするこ
とができる。すなわち、装置の設置スペースが少なくて
済むようになる。
That is, according to this manufacturing method, even if the width of the compression device 2b is reduced, the length of the compression section can be increased. That is, the installation space for the device is reduced.

【0029】図3は、本発明にかかる発泡体の製造方法
の第3の実施の形態をあらわしている。
FIG. 3 shows a third embodiment of the method for producing a foam according to the present invention.

【0030】この製造方法は、圧縮装置2aに代えて、
対面する2つの無端ベルト23,23を有し、この無端
ベルト23,23の駆動ロール24,24内および加圧
ロール5,・・・,25内に熱媒体を通す流路(図示せ
ず)がそれぞれ設けられた圧縮層2cを用い、原料発泡
体1を流路に通された熱媒体によって加熱された駆動ロ
ール24,24および加圧ロール25,・・・,25の
熱により加熱された無端ベルト23,23との間に通
し、原料発泡体1を加熱しつつ圧縮するようにした以外
は、第1の実施の形態と同様になっている。
In this manufacturing method, instead of the compression device 2a,
It has two endless belts 23 facing each other, and a flow path (not shown) for passing the heat medium through the drive rolls 24, 24 and the pressure rolls 5, ..., 25 of the endless belts 23, 23. Are heated by the heat of the drive rolls 24, 24 and the pressurizing rolls 25,..., 25, which are heated by the heat medium passed through the raw material foam 1 through the flow path, using the compression layer 2c provided with each. The configuration is the same as that of the first embodiment except that the raw material foam 1 is compressed while being heated by being passed between the endless belts 23, 23.

【0031】図4は、本発明にかかる発泡体の製造方法
の第4の実施の形態をあらわしている。この製造方法
は、冷却室4に代えて、複数の冷却ロール41,41,
42,・・・,42で収縮体3を直ちに20℃以下に冷
却するようにした以外は、第1の実施の形態と同様にな
っている。
FIG. 4 shows a fourth embodiment of the method for producing a foam according to the present invention. In this manufacturing method, a plurality of cooling rolls 41, 41,
The structure is the same as that of the first embodiment except that the contracted body 3 is immediately cooled to 20 ° C. or lower at 42,.

【0032】[0032]

【実施例】以下に、本発明の実施例をより詳しく説明す
る。 (実施例1)低密度ポリエチレン(三菱化学社製、LF
440HB、Tm(融点)=112.5℃)100重量
部、発泡剤としてのアゾジカルボンアミド(大塚化学社
製、AZ−HM)15重量部、発泡助剤としての酸化亜
鉛1重量部、過酸化物としてのジクミルパーオキサイド
0.5重量部を押出機(φ=50mm、L/D=22)に
投入し、混練したのち厚み3mmの原料シートとして押し
出し、原料シートを押し出し直後に175℃のベルト上
で5分間加熱して架橋させ、架橋シートを得た。
Embodiments of the present invention will be described below in more detail. (Example 1) Low density polyethylene (manufactured by Mitsubishi Chemical Corporation, LF
440HB, 100 parts by weight of Tm (melting point = 112.5 ° C.), 15 parts by weight of azodicarbonamide (AZ-HM, manufactured by Otsuka Chemical Co., Ltd.) as a foaming agent, 1 part by weight of zinc oxide as a foaming aid, peroxide 0.5 part by weight of dicumyl peroxide as a product is put into an extruder (φ = 50 mm, L / D = 22), kneaded, extruded as a raw material sheet having a thickness of 3 mm, and immediately after extruding the raw material sheet at 175 ° C. Crosslinking was performed by heating on a belt for 5 minutes to obtain a crosslinked sheet.

【0033】この架橋シートを250℃の熱風炉へ入れ
発泡させて発泡倍率33倍(33cc/g、独立気泡率
88%、厚み10mmの原料発泡体を得た。この原料発泡
体に、φ500μmの針で厚み方向に8孔/cm2 の密度
で孔を開けたのち、この原料発泡体を図1と同様に棒状
のヒータを内部に備えたプレス板で40℃まで加熱しつ
つ上下から0.5mmまで圧縮して10分間圧縮状態を保
ち収縮体を得たのち、この収縮体を常温雰囲気で放置し
て形状回復発泡体を得た。
The crosslinked sheet was placed in a hot air oven at 250 ° C. and foamed to obtain a raw foam having a foaming ratio of 33 times (33 cc / g, a closed cell ratio of 88%, and a thickness of 10 mm. The raw foam had a diameter of 500 μm. After forming holes at a density of 8 holes / cm 2 in the thickness direction with a needle, this raw material foam was heated to 40 ° C. from above and below from above and below while being heated to 40 ° C. by a press plate having a rod-shaped heater inside as in FIG. After being compressed to 5 mm and kept in a compressed state for 10 minutes to obtain a contracted body, the contracted body was left in a normal temperature atmosphere to obtain a shape-recovered foam.

【0034】(実施例2)実施例1と同様にして得た収
縮体を図4に示すように冷却ロールで直ちに3℃に冷却
して形状回復発泡体を得た。
Example 2 A shrinkable body obtained in the same manner as in Example 1 was immediately cooled to 3 ° C. with a cooling roll as shown in FIG. 4 to obtain a shape-recovered foam.

【0035】(比較例1)圧縮時に加熱しなかった以外
は、実施例1と同様にして形状回復発泡体を得た。 (比較例2)圧縮時に120℃まで加熱するとともに、
圧縮時間を2分間とした以外は、実施例1と同様にして
形状回復発泡体を得た。
(Comparative Example 1) A shape-recovered foam was obtained in the same manner as in Example 1 except that heating was not performed during compression. (Comparative Example 2) While being heated to 120 ° C during compression,
A shape recovery foam was obtained in the same manner as in Example 1 except that the compression time was changed to 2 minutes.

【0036】上記実施例1,2および比較例1,2で得
られた形状回復発泡体の厚みおよびこの形状回復発泡体
を常温常圧下で1ヶ月放置したのちの厚みを計測し、そ
の結果を表1に示した。
The thickness of the shape-recovered foams obtained in Examples 1 and 2 and Comparative Examples 1 and 2, and the thickness after leaving the shape-recovered foams at room temperature and normal pressure for one month were measured. The results are shown in Table 1.

【0037】[0037]

【表1】 [Table 1]

【0038】上記表1から本発明の請求項1の製造方法
によれば、短時間で原料発泡体を収縮させて形状回復発
泡体を得られることがわかる。また、請求項2の製造方
法のようにすれば、より目的の厚みに近い形状回復発泡
体を得られることがよくわかる。
From the above Table 1, it can be seen that according to the production method of the first aspect of the present invention, the shape-recovered foam can be obtained by shrinking the raw foam in a short time. Further, it can be clearly understood that the shape-recovery foam having a thickness closer to the intended thickness can be obtained by using the manufacturing method of the second aspect.

【0039】[0039]

【発明の効果】本発明にかかる発泡体の製造方法は、以
上のように構成されているので、短時間で形状回復発泡
体を得ることかできる。したがって、形状回復発泡体の
生産性が向上する。
The method for producing a foam according to the present invention is configured as described above, so that a shape-recovery foam can be obtained in a short time. Therefore, the productivity of the shape recovery foam is improved.

【0040】しかも、請求項2の製造方法のようにすれ
ば、より目的の厚みに近い形状回復発泡体を得ることが
できる。また、請求項3の製造方法のようにすれば、原
料発泡体をより短時間で収縮状態にすることができる。
Further, according to the manufacturing method of the second aspect, it is possible to obtain a shape-recovery foam having a thickness closer to a desired thickness. Further, according to the manufacturing method of the third aspect, the raw material foam can be brought into a contracted state in a shorter time.

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

【図1】本発明にかかる発泡体の製造方法の第1の実施
の形態をあらわす製造装置の概略説明図である。
FIG. 1 is a schematic explanatory view of a manufacturing apparatus showing a first embodiment of a method for manufacturing a foam according to the present invention.

【図2】本発明にかかる発泡体の製造方法の第2の実施
の形態をあらわす製造装置の概略説明図である。
FIG. 2 is a schematic explanatory view of a manufacturing apparatus showing a second embodiment of the method for manufacturing a foam according to the present invention.

【図3】本発明にかかる発泡体の製造方法の第3の実施
の形態をあらわす製造装置の概略説明図である。
FIG. 3 is a schematic explanatory view of a manufacturing apparatus showing a third embodiment of the method for manufacturing a foam according to the present invention.

【図4】本発明にかかる発泡体の製造方法の第4の実施
の形態をあらわす製造装置の概略説明図である。
FIG. 4 is a schematic explanatory view of a manufacturing apparatus showing a fourth embodiment of the method for manufacturing a foam according to the present invention.

【符号の説明】[Explanation of symbols]

1 原料発泡体 2a、2b、2c 圧縮装置 3 収縮体 4 冷却室 41,42 冷却ロール 6 形状回復発泡体 DESCRIPTION OF SYMBOLS 1 Raw material foam 2a, 2b, 2c Compressor 3 Shrink body 4 Cooling chamber 41, 42 Cooling roll 6 Shape recovery foam

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】独立気泡樹脂発泡体からなる原料発泡体を
圧縮させてなる遅延した形状回復性を有する発泡体の製
造方法において、原料発泡体を、30℃以上で原料発泡
体を形成する樹脂の軟化温度以下の温度に保持した状態
で圧縮することを特徴とする発泡体の製造方法。
1. A method for producing a foam having delayed shape recovery by compressing a raw foam made of a closed-cell resin foam, wherein the raw foam is formed at a temperature of 30 ° C. or higher. A method for producing a foam, comprising compressing the foam while maintaining the temperature at or below the softening temperature of the foam.
【請求項2】原料発泡体の圧縮によって得られた収縮体
を圧縮直後に20℃以下に冷却する工程を備えている請
求項1に記載の発泡体の製造方法。
2. The method for producing a foam according to claim 1, further comprising a step of cooling the contracted body obtained by compressing the raw material foam to 20 ° C. or lower immediately after the compression.
【請求項3】表面から内部の独立気泡内に連通する通気
路が原料発泡体に予め所定ピッチで穿設されている請求
項1または請求項2に記載の発泡体の製造方法。
3. The method for producing a foam according to claim 1, wherein an air passage communicating from the surface to the inside of the closed cells is formed in the raw foam at a predetermined pitch in advance.
JP4795197A 1997-03-03 1997-03-03 Production of foamed body Pending JPH10245446A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4795197A JPH10245446A (en) 1997-03-03 1997-03-03 Production of foamed body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4795197A JPH10245446A (en) 1997-03-03 1997-03-03 Production of foamed body

Publications (1)

Publication Number Publication Date
JPH10245446A true JPH10245446A (en) 1998-09-14

Family

ID=12789675

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4795197A Pending JPH10245446A (en) 1997-03-03 1997-03-03 Production of foamed body

Country Status (1)

Country Link
JP (1) JPH10245446A (en)

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