JPS5962118A - Preparation of flexible foam material - Google Patents

Preparation of flexible foam material

Info

Publication number
JPS5962118A
JPS5962118A JP17375782A JP17375782A JPS5962118A JP S5962118 A JPS5962118 A JP S5962118A JP 17375782 A JP17375782 A JP 17375782A JP 17375782 A JP17375782 A JP 17375782A JP S5962118 A JPS5962118 A JP S5962118A
Authority
JP
Japan
Prior art keywords
foam
tensile strength
resin
elongation
olefine
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.)
Granted
Application number
JP17375782A
Other languages
Japanese (ja)
Other versions
JPH0218224B2 (en
Inventor
Toshimasa Osaki
大崎 利政
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 JP17375782A priority Critical patent/JPS5962118A/en
Publication of JPS5962118A publication Critical patent/JPS5962118A/en
Publication of JPH0218224B2 publication Critical patent/JPH0218224B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29DPRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D7/00Producing flat articles, e.g. films or sheets
    • B29D7/01Films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C67/00Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
    • B29C67/20Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 for porous or cellular articles, e.g. of foam plastics, coarse-pored
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To manufacture highly flexible foam material useful for clothings and sporting goods, etc. simply and economically at a high productivity by such an arrangement wherein more than 2 kinds of oelfine family resin of which elongation and tensile strength differ from each other are mixed and melted and caused to foam and after that said material is elongated. CONSTITUTION:More than 2 kinds of olefine family resin (polymer of olefine family monomer or copolymer primarily composed of monomers) of which elongation or/and tensile strength differ from other preferably by more than 20%, more preferably by more than 50% are mixed (preferably, 10-90wt% of one kind of olefine family resin are included) melted and caused to foam (preferably by a method whereby olefine family resin is bridged) and the material thus obtained is elongated preferably by more than 1.5 times by pinch rolls, etc.

Description

【発明の詳細な説明】 本発1y目゛↓オレフィン系ty+脂発泡体から柔軟な
発泡体を製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a flexible foam from an olefinic TY+fat foam.

独立気泡のオレフィン系樹脂発泡体は断熱性、遮音性、
クッション性等に優れているため種々の用途に使用され
ているが、一般にしなやか性、吸水性、通気性、衣料な
どに要求されるフィツト性等が欠けるため、上記性能を
必要とする用途G’lま使用できなかった。
Closed-cell olefin resin foam has thermal and sound insulation properties,
Although it is used for various purposes due to its excellent cushioning properties, it generally lacks flexibility, water absorption, breathability, and fit required for clothing, etc., so it is used for applications that require the above performance G' I couldn't use it at all.

従来、独立気泡の発泡体を連続気泡化する方法)j、 
、ニードルパンチで多数の孔を穿設する方法等の機械的
加工法、煮沸して気泡を大きくしてセル膜を伸dす方法
、樹脂のガラス転移温度以下の温度に冷却してのち圧縮
する方法等の物理的処理方法等、種々提案されているが
、打抜き設備、煮沸設備、冷却設備等、いずれも大型の
設備を必要とし、その分コストが上昇し、また生産性も
悪い等の欠点があり、満足できるもの1ユなかった。
Conventional method of converting closed cell foam into open cell)j,
, Mechanical processing methods such as punching a large number of holes with a needle punch, Boiling to enlarge the bubbles and stretching the cell membrane, Compressing after cooling to a temperature below the glass transition temperature of the resin. Various physical processing methods have been proposed, but they all require large equipment such as punching equipment, boiling equipment, cooling equipment, etc., which increases costs and has disadvantages such as poor productivity. There was nothing I was satisfied with.

零発りjの目的は上述の欠点を解消し、設備が簡単で、
連続気泡化の生産性が篩く、経済的な柔軟な発泡体のΦ
1.!遣方法を提供することにある。
The purpose of Zero Hatsuri J is to eliminate the above-mentioned drawbacks, have simple equipment,
Φ of economical flexible foam with high productivity of open cell formation
1. ! The goal is to provide a way to send money.

即ち、本発明の要旨は、伸び、抗張力の異なる少なくと
も2種類のオレフィン系樹脂を混合溶融し、発泡させた
のち、延伸することを特徴とする柔軟な発泡体の製造方
法に存する。
That is, the gist of the present invention resides in a method for producing a flexible foam, characterized by mixing and melting at least two types of olefin resins having different elongation and tensile strength, foaming, and then stretching.

末完1111 において用いられるオレフィン系手・1
脂とtま、エチレン、プロピレン、ブチレン等のオレフ
ィン系単f4体の重合体、共重合体、及びエチレン−酢
酸ビニル共重合体、エチレン−アクリル酸エチル共IR
合体、エチレン−塩化ビニル共重合体等のオレフィン系
lit量体を主体とする共重合体をいう。
Olefin system used in Suekan 1111 1
Polymers and copolymers of F4 olefins such as fat, ethylene, propylene, butylene, ethylene-vinyl acetate copolymers, ethylene-ethyl acrylate co-IR
It refers to a copolymer mainly composed of an olefin-based lit polymer such as a copolymer or an ethylene-vinyl chloride copolymer.

零発1!l]においては上記オレフィン系樹脂のうち、
伸び、抗張力(引張強度)の異なる少なくとも2種類が
用いられる。上記2種類とは、例えば低密度ポリエチレ
ンどうしでグレードの異なるものの組合せ等、伸び、抗
張力が異なれば同じ単量体からなる重合体の組合せであ
ってもよい。
Zero shot 1! l], among the above olefin resins,
At least two types with different elongation and tensile strength (tensile strength) are used. The above two types may be a combination of polymers made of the same monomers as long as they have different elongation and tensile strength, such as a combination of different grades of low density polyethylene.

要は伸び、抗張力の異なる少なくとも2つのオレフィン
系4↓l Ill″Vの組合せで、うって発泡体が形成
されるものであれば如何なる〃1合ぜてあってもよく、
例えば上記の他、低密度ポリエチレンと線状低密度ポリ
エチレン、低密度ポリエチレンと高密度ポリエチレン、
低密度ポリエチレンとエチレン−酢酸ビニル共重合体、
高密度ポリエチレンとポリプロピレン、ポリプロピレン
とプロピレン−エチレン共重合体笹掻々の組合せが可能
である。e更に上記オレフィン系樹脂を3種類以上混合
してもよいのをまもちろんである。伸び、抗張力の異な
りの程度としては、発泡体を延伸した場合に樹脂の間で
層のずれが生じる程度に異なっておればよく、伸び、抗
張力のうち少なくとも一方が20%以上異なっておれば
好ましく、両者が20%以上異なっておれば更にpfま
しく、特に好ましくは両者が50%以上異なっているこ
とである。少なくとも2種類のオレフィン系樹脂の混合
の割合上してtま、1りのオレフィン系樹脂が10〜9
0重M%の範囲で混合されているものが好ましい。2種
類目以降のAしフィン系樹脂の混合割合があまりに少な
すぎると、発泡体を延伸しても柔軟性が満足できるt’
zど発現されなりのである1゜末完+51においては上
記伸び、抗張力の異なる少なくとも2種類のオレフィン
系樹脂を混合溶融して発泡体上なすのであるが、発泡体
を製造する方法としては、従来のオレフィン系樹脂発f
1ル体の製造技術と同様の方法が使用できる。例に えば、」−記オレフイン系樹脂の混合杓ρjアゾジカル
ボンアミド等の熱分解型発泡剤を混合して押出機に投入
し、押出(浅内で上記発泡剤を分解して発泡性樹脂#1
成物とせしめ、Tグイ等の口金より吐出して発ffl1
する方法、低沸点の脂肪族炭化水索又tよハロゲン化炭
化水素等の物理型発泡剤を押出機の中途に圧入、又は上
記物理型発泡剤を押出+Qへ投入1jqの樹脂混合物に
あらかじめ含浸せしめることにより発泡性樹脂組成物を
つくり、口金より吐出発出せしめる方法、或tま+if
7記オレフィン系(61脂の混合物に熱分/j?型発泡
ハリを混合してこれを押出4後又tよりレンダ−ロール
等によって上記発泡剤が実質的に分解しない程度、圧力
で混線溶融してシート状に成1ヒし、該シート状成形体
に電離性放射線等を照射することによって架橋し、その
後上記発泡剤の分解温度場」−に加熱することにより架
橋発泡体を得る方法、R+1記すレフイン系樹脂混合物
に熱分解型発泡剤の他架橋剤を混合し、これを押出機又
tよりレンダ−ロール等によって発泡剤及び架橋剤が実
質的に分解しない程度、圧力で混線溶融してシート状に
成形し、これを架橋剤が分解する温度に加熱すること忙
よって架橋し、更に発泡剤の分解温度以上に加熱するこ
とKより架橋発泡体を得る方法等が挙けられる。上記製
造方法のうらオレフィン系樹脂を架橋する方法が、その
溶融t1it脂の粘度が調整され、均一微細な独立気泡
を有する発泡体が11すられ特に好ましい。
In short, it is a combination of at least two olefins 4↓lIll''V having different elongation and tensile strength, and any combination may be used as long as a foam is formed.
For example, in addition to the above, low density polyethylene and linear low density polyethylene, low density polyethylene and high density polyethylene,
low-density polyethylene and ethylene-vinyl acetate copolymer,
Combinations of high-density polyethylene and polypropylene, and polypropylene and propylene-ethylene copolymer Sasakaki are possible. Of course, three or more of the above olefin resins may be mixed. The degree of difference in elongation and tensile strength may be such that when the foam is stretched, the layers of the resin will shift, and it is preferable that at least one of elongation and tensile strength differs by 20% or more. It is more preferable that the two differ by 20% or more, and it is particularly preferable that the two differ by 50% or more. The mixing ratio of at least two types of olefin resins is 10 to 9.
Preferably, the content is 0% by weight. If the mixing ratio of the second and subsequent A fin resins is too small, the flexibility may not be satisfactory even when the foam is stretched.
At least two types of olefin resins having different elongation and tensile strength are mixed and melted to form a foam on a foam. olefin resin f
A method similar to the manufacturing technique for single-unit bodies can be used. For example, a pyrolytic foaming agent such as azodicarbonamide is mixed with a mixing ladle of olefin resin, and the mixture is fed into an extruder and extruded (the foaming agent is decomposed in a shallow chamber to form foamable resin #1).
Discharge the product from the nozzle of a T-guid, etc.ffl1
A physical blowing agent such as a low-boiling point aliphatic hydrocarbon or halogenated hydrocarbon is press-injected into the middle of the extruder, or the above-mentioned physical blowing agent is injected into the extrusion +Q and pre-impregnated with 1jq of resin mixture. A method of making a foamable resin composition by allowing the foam to flow and discharging it from a mouthpiece, or if
No. 7 Olefin type (61 fat mixture) is mixed with hot/j? type foaming tension, and after extrusion, cross-melting is carried out under pressure to the extent that the above foaming agent is not substantially decomposed using a render roll or the like from t. A method of obtaining a crosslinked foam by forming it into a sheet, crosslinking it by irradiating the sheet-like molded body with ionizing radiation, and then heating it to the decomposition temperature range of the blowing agent. A thermally decomposable blowing agent and a crosslinking agent are mixed into the reflex resin mixture marked R+1, and this is cross-melted using an extruder or a render roll etc. under pressure to the extent that the blowing agent and crosslinking agent are not substantially decomposed. Examples of the method include forming a sheet into a sheet, heating it to a temperature at which the crosslinking agent decomposes, crosslinking it, and then heating it to a temperature higher than the decomposition temperature of the blowing agent to obtain a crosslinked foam. Among the manufacturing methods, the method of crosslinking the olefin resin is particularly preferred because the viscosity of the molten resin can be adjusted and a foam having uniform, fine closed cells can be produced.

尚、発泡体を製造するに当って、上記樹1指、発泡剤、
架橋剤の他、安定剤、紫外線l夙収剤、滑剤、顔料、帯
電防止剤、充填剤、補強剤等、通常用いられている添加
剤、助剤を混合することIjもちろん可能である。更に
ポリスチレン、アクリル樹脂、ABSIR脂、ポリゲタ
ジエン、ゴム等の樹脂を加えることも可能である。
In addition, in manufacturing the foam, the above-mentioned tree, a foaming agent,
In addition to the crosslinking agent, it is of course possible to mix commonly used additives and auxiliaries such as stabilizers, ultraviolet light absorbers, lubricants, pigments, antistatic agents, fillers, and reinforcing agents. Furthermore, it is also possible to add resins such as polystyrene, acrylic resin, ABSIR resin, polygetadiene, and rubber.

末完1jllにおいては前記のような方法で得られた発
泡体を61L仲すればよいのである。延伸する方法とし
てe」、ピンチ0−ル間で延伸する方法、テンタ一式延
伸機で延伸する方法等、従来公知の適宜の方法が使用で
き、また、−軸に延伸しても二611に延伸してもよい
。延伸の際の温度としては、発泡体の溶融温度場ドてあ
ればいかなる温度でもよいが、常温から発泡体を構成す
るオレフィン糸樹脂の軟化温度までの聞がμIましい。
In order to complete 1 liter of foam, 61 L of the foam obtained by the above method is sufficient. As a method of stretching, any conventionally known appropriate method can be used, such as stretching between 0 and 100 mm pinch, stretching with a tenter set stretching machine, etc. You may. The temperature during stretching may be any temperature as long as it is within the melting temperature of the foam, but it is preferably between room temperature and the softening temperature of the olefin thread resin constituting the foam.

延伸倍率としては、目的とする発泡体の柔軟性によって
異なるが、>i!! ?it 1−5倍以上延伸するの
がOfよ[、い。延伸すると、発泡体を構成するLころ
の、伸び、抗張力の異なるAレフイン系樹脂の間で層の
J゛れが生じ、発泡体がある程度連続気11ル化され、
発1(J体に柔軟性が発現されるのである。
The stretching ratio varies depending on the desired flexibility of the foam, but >i! ! ? It is best to stretch it 1-5 times or more. When stretched, the layers of the A-refined resins with different elongation and tensile strength of the L rollers that make up the foam are distorted, and the foam becomes open to some extent.
Development 1 (flexibility is expressed in the J body.

零発り1の柔軟なう゛^泡休体製jf’i方決tま、上
述の如く構成されているから、廷仲する没前を設けるだ
けで筒中に製i:lfでき、生pc性も^く、経済的に
11−’)優れIC柔軟性をず〕するイ^泡体が得られ
るのである。したがって得られた発泡体は、衣ri用、
スポーツ用等しなやか性、吸水性、フィツト性等の性能
が要求される用途に好適に使用される。
Since the flexible material made from zero foam is constructed as described above, it can be made in the cylinder by simply providing a holder for intermediation, and it has raw PC properties. Moreover, it is possible to obtain a foam that is economically 11-') excellent in IC flexibility. Therefore, the obtained foam can be used for clothing,
Suitable for use in sports and other applications that require performance such as flexibility, water absorption, and fit.

以F木発明製造方法を実施例により説明する。Hereinafter, the invention and manufacturing method for F wood will be explained with reference to examples.

実施例 伸び200%、抗張力(引張強度)250Kg/cd(
JIS K 1702)、密度0.923、メルトイン
デックス4.0y/10分の低密度ポリエチレン704
704部と、伸び500 % 、抗張力450Kf/a
d。
Example elongation 200%, tensile strength (tensile strength) 250Kg/cd (
JIS K 1702), low density polyethylene 704 with density 0.923, melt index 4.0y/10min
704 parts, elongation 500%, tensile strength 450Kf/a
d.

密度0.918、メ71/ )インデックス1(1/1
0分の線状低密度ポリエチレン3(lfflhL部と、
アゾジカルボンアミド15重量部と、助剤3.5重F1
部と1C混合し、押出機で溶融して厚み13mmのシー
ト状に押出し、その後、電子線照射機にて3.5Mra
d の電子線を照射して架441 L 、次いで300
℃のA−シン内を通して加熱し約3゜倍に発/fitさ
せて、均一微細な独立気泡を有する厚み約4mmの発泡
シートをf!J ft oこの発泡シートを、速度比の
異なる2対のピンチロール間にて、常温で、2倍に一1
+l+延伸して、連続/2.泡率が高く柔軟性を有する
1vみ約λ8門の発泡シートを11+た。
Density 0.918, Me71/) Index 1 (1/1
0 minute linear low density polyethylene 3 (lfflhL part,
15 parts by weight of azodicarbonamide and 3.5 parts by weight of auxiliary agent F1
and 1C, melted with an extruder and extruded into a sheet with a thickness of 13 mm, and then 3.5 Mra with an electron beam irradiation machine.
441L, then 300
A foam sheet with a thickness of about 4 mm having uniform fine closed cells is heated by passing it through an A-thin at ℃ and expanding/fitting it by about 3 degrees. J ft o This foam sheet was rolled at room temperature between two pairs of pinch rolls with different speed ratios.
+l+stretched and continuous/2. A foam sheet with a high foam rate and flexibility and a diameter of approximately λ8 was prepared.

得られた発泡シートの物性値、及び延伸n11の発泡シ
ートの物性値を測定した結果を第1表に示す。
Table 1 shows the results of measuring the physical property values of the obtained foamed sheet and the physical property values of the stretched foamed sheet at n11.

第1表 尚、測定番こおいて目、圧縮強jwcまJIS K−6
767により、腰強atまスティフネス8]を用い、連
続気泡;p< ij空気比較式比重d1により測定した
Table 1: Measurement number: square, compressive strength: JIS K-6
767, using an open cell; p < ij air comparison formula specific gravity d1.

第1表から、本発明により得られた発泡シートは連続気
泡率か+:’:+ < 、柔軟性を口することがわかる
From Table 1, it can be seen that the foamed sheet obtained according to the present invention has an open cell ratio of +:':+< and flexibility.

比較例 実施例における樹脂の部分を、実施例と同じ低密度ポリ
エチレン100重鷲部にした他な:を実施例1と同様に
して厚み約4龍の発泡シートを製造した。このイ^泡シ
ートを同様に常温で2倍に一軸延伸しようとしたが、延
伸が内錐で途中で発泡シートが切断してしまった。
Comparative Example A foamed sheet with a thickness of approximately 4 mm was produced in the same manner as in Example 1, except that the resin part in Example was replaced with the same 100% low density polyethylene as in Example. I tried to uniaxially stretch this foam sheet to double the original length at room temperature in the same way, but the foam sheet was cut midway through the inner conical stretch.

特許出願人 積水化学工業株式会社 代表者藤沼基利patent applicant Sekisui Chemical Co., Ltd. Representative Mototoshi Fujinuma

Claims (1)

【特許請求の範囲】 し 伸び、抗張力の異なる少なくとも2種類のオレフィ
ン系(3脂を混合溶融し、発泡させたのち、延伸するこ
とを特徴とする柔軟な発泡体の製造方法。 2 伸び、抗張力のうち少なくとも一方が20%以上異
なったものである特許請求の範囲第1項記載の製造方法
。 3、 延伸がL5倍以上されるものである特許ハ11求
の範[」第1頃又ti第2項記載の製造方法。 4、副レフイン系(3−]脂のうちの1種類が10〜9
0重1廿%の範囲で混合されている特K「請求のIIn
囲第1項、第2頃又ti第3項記戦の製造方法。
[Claims] A method for producing a flexible foam, characterized by mixing and melting at least two types of olefins (three resins) having different elongation and tensile strength, foaming, and then stretching. 2. Elongation and tensile strength 3. The manufacturing method according to claim 1, wherein at least one of them differs by 20% or more. 3. The method of claim 1, in which the stretching is performed by L5 times or more. The manufacturing method according to item 2. 4. One type of secondary reflex (3-) fat is 10 to 9
Special K "Claim IIn" mixed in the range of 0 weight 1 廿%
1. Method of manufacturing the products described in Section 1 and Section 2 of Section 3.
JP17375782A 1982-10-01 1982-10-01 Preparation of flexible foam material Granted JPS5962118A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17375782A JPS5962118A (en) 1982-10-01 1982-10-01 Preparation of flexible foam material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17375782A JPS5962118A (en) 1982-10-01 1982-10-01 Preparation of flexible foam material

Publications (2)

Publication Number Publication Date
JPS5962118A true JPS5962118A (en) 1984-04-09
JPH0218224B2 JPH0218224B2 (en) 1990-04-24

Family

ID=15966569

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17375782A Granted JPS5962118A (en) 1982-10-01 1982-10-01 Preparation of flexible foam material

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61248726A (en) * 1985-04-26 1986-11-06 Kazuhiko Nanbu Method and device for manufacturing soft resin foam sheet
WO2006043570A1 (en) * 2004-10-18 2006-04-27 Sekisui Chemical Co., Ltd. Method for producing polyolefin based resin crosslinked foamed sheet and polyolefin based resin crosslinked foamed sheet
WO2009044690A1 (en) * 2007-10-02 2009-04-09 Sekisui Chemical Co., Ltd. Stretched thermoplastic resin foam sheet and process for production of the same

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61248726A (en) * 1985-04-26 1986-11-06 Kazuhiko Nanbu Method and device for manufacturing soft resin foam sheet
WO2006043570A1 (en) * 2004-10-18 2006-04-27 Sekisui Chemical Co., Ltd. Method for producing polyolefin based resin crosslinked foamed sheet and polyolefin based resin crosslinked foamed sheet
JPWO2006043570A1 (en) * 2004-10-18 2008-05-22 積水化学工業株式会社 Method for producing polyolefin resin cross-linked foam sheet and polyolefin resin cross-linked foam sheet
US7854871B2 (en) 2004-10-18 2010-12-21 Sekisui Chemical Co., Ltd. Method for producing polyolefin-based resin crosslinked foamed sheet and polyolefin-based resin crosslinked foamed sheet
JP4696074B2 (en) * 2004-10-18 2011-06-08 積水化学工業株式会社 Method for producing polyolefin resin cross-linked foam sheet and polyolefin resin cross-linked foam sheet
WO2009044690A1 (en) * 2007-10-02 2009-04-09 Sekisui Chemical Co., Ltd. Stretched thermoplastic resin foam sheet and process for production of the same
JPWO2009044690A1 (en) * 2007-10-02 2011-02-10 積水化学工業株式会社 Thermoplastic resin stretched foam sheet and method for producing the same
US8529817B2 (en) 2007-10-02 2013-09-10 Sekisui Chemical Co., Ltd. Stretched thermoplastic resin foam sheet and process for production of the same

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JPH0218224B2 (en) 1990-04-24

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