JPS6365213B2 - - Google Patents

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Publication number
JPS6365213B2
JPS6365213B2 JP58056383A JP5638383A JPS6365213B2 JP S6365213 B2 JPS6365213 B2 JP S6365213B2 JP 58056383 A JP58056383 A JP 58056383A JP 5638383 A JP5638383 A JP 5638383A JP S6365213 B2 JPS6365213 B2 JP S6365213B2
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JP
Japan
Prior art keywords
polyolefin resin
surfactant
weight
inorganic
parts
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
Application number
JP58056383A
Other languages
Japanese (ja)
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JPS59179635A (en
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
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Priority to JP5638383A priority Critical patent/JPS59179635A/en
Publication of JPS59179635A publication Critical patent/JPS59179635A/en
Publication of JPS6365213B2 publication Critical patent/JPS6365213B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は高濃度に無機物を含有するポリオレフ
イン系樹脂発泡体の製造法に関する。 ポリオレフイン系樹脂に無機化合物を充填する
ことは無公害化、難燃化、省資源化を目的に行な
われている。例えばAl(OH)3、Mg(OH)2のよう
な水和物は特定の温度で結晶水を離脱させること
により難燃性を向上させることができ、いわゆる
ハロゲン系難燃剤に比して燃焼時に有毒ガスの発
生がなく安価であることから注目されている。 しかし、従来無機物充填ポリオレフイン系樹脂
成形物を常圧下で加熱発泡すると高発泡体が得に
くく、得られたとしても気泡が粗大で表面の肌荒
が著るしく、また高発泡体を得るには多量の発泡
剤を必要とした。 無機物充填ポリオレフイン系樹脂高発泡体を得
るために圧力下で架橋構造を導入し発泡剤を分解
させ、しかるのち常圧下で加熱膨脹する方法があ
るが連続生産が困難でバツチ工程で生産されるた
め生産効率が低下し、高価格になりがちであり、
また長尺発泡品製造が不可能なため用途が限定さ
れる傾向にあつた。 本発明はかゝる状況に鑑み鋭意検討の結果なさ
れたものであつて、その目的とするところは無機
物を高濃度に充填したポリオレフイン系樹脂の高
発泡倍率発泡体の製造法および気泡が細かく表面
が平滑美麗な発泡体を工業的に連続生産可能な方
法を提供することにある。 しかして本発明の要旨はポリオレフイン系樹脂
に無機化合物粉体、加熱分解型発泡剤および有機
過酸化物を混合、成形して無機物充填樹脂成形物
となし、しかるのち発泡剤の分解温度以上に加熱
して発泡体とする方法において、ポリオレフイン
系樹脂100重量部に対し界面活性剤0.05〜10重量
部を添加混合することを特徴とする無機物を充填
したポリオレフイン系樹脂発泡体の製造法にあ
る。 本発明はポリオレフイン系樹脂100重量部に対
して無機化合物粉体を50〜250重量部、界面活性
剤0.05〜10重量部、加熱分解型発泡剤および有機
過酸化物加橋剤を含む無機物充填ポリオレフイン
系樹脂成形物を発泡剤の分解温度以上に加熱して
常圧下で発泡することにより実施することができ
る。 本発明の実施にあつては界面活性剤の使用が必
須である。本発明で用いる界面活性剤の作用機構
については明確ではないが、界面活性剤の添加に
より樹脂組成物の表面張力を低下させるためと考
えられる。すなわち発泡時における気泡の大きさ
は均一ではなく異なつており、気泡の内部ガス圧
は気泡径が小さい程高くなるため、薄い膜を隔て
て隣接する気泡間でガスは径の小さい方から大き
い方へ透過していき最後に大きい方へ合一化され
ることにより気泡経がさらに大きくなる。従つて
気泡の大きい発泡体となる。このような気泡間の
差圧は表面張力に比例する性質があることから表
面張力を下げることにより気泡の合一化を防ぐこ
とができ気泡の細かい発泡体が得られる。また大
気泡になりにくいことから気泡膜の破壊が少なく
表面も平滑となり、ガス逃げも少ないことから発
泡剤の添加量も低減できると考えられる。 本発明に用いられる界面活性剤としてはアルキ
ルフエノール型やソルビタンエステル型のような
ノニオン系界面活性剤でも有効であるが特にシリ
コーン系界面活性剤およびフツ素系界面活性剤が
顕著に上記効果を奏する。かゝる界面活性剤とし
ては商品名NUCシリコーンL3550(日本ユニカー
(株)製)あるいはフロラードFC430(住友スリーエ
ム(株)製)等がある。界面活性剤の添加量はポリオ
レフイン系樹脂100重量部に対し0.05〜10重量部
の範囲である。0.05重量部未満では効果が発現で
きずまた10重量部を越えると樹脂本来の性質が著
しく損なわれ好ましくない。 本発明におけるポリオレフイン系樹脂とは高、
中、低圧法ポリエチレン、ポリプロピレン、ポリ
ブテン−1、エチレン−酢酸ビニル共重合体、エ
チレン−プロピレン共重合体、エチレン−α−オ
レフイン共重合体、エチレン−アクリル酸共重合
体、塩素化ポリエチレン、クロルスルホン化ポリ
エチレン、ポリブタジエン等からなる1種または
2種以上の混合物をいう。 本発明における無機化合物とは水酸化アルミニ
ウム、水酸化マグネシウム、塩基性炭酸マグネシ
ウム、水酸化カルシウム、酸化スズ水和物酸化ジ
ルコニウム、炭酸カルシウム、炭酸マグネシウ
ム、タルク、クレー、ベントナイト、アタパルジ
ヤイト、ホウ酸バリウム、ホウ酸亜鉛、石こう等
であり、これの1種または2種以上の混合物であ
る。 また上記無機化合物に周知の脂肪酸系、シラン
系またはチタン系カツプリング剤で表面処理して
もよい。これらの無機化合物は平均粒径0.01〜
50μの粉体である。その添加量はポリオレフイン
系樹脂100重量部に対し、30〜250重量部、好まし
くは50〜200重量部である。 本発明の有機過酸化物とは加熱により分解して
ラジカルを発生する化合物であり、たとえばジ−
t−ブチルパーオキサイド、ジクミルパーオキサ
イド、t−ブチルクミルパーオキサイド、α,α
−ビス(t−ブチルパーオキシ)P−ジイソプロ
ピルベンゼン、2.5−ジメチル−2.5−ジ(t−ブ
チルパーオキシ)ヘキサン、2.5−ジメチル−2.5
ジ(t−ブチルパーオキシ)ヘキシン−3、2.4
−ジクロロベンゾイルパーオキサイド、ベンゾイ
ルパーオキサイド、1.1−ジ−t−ブチルパーオ
キシ3.3.5−トリメチルシクロヘキサン、2.5−ジ
メチル−2.5−ジベンゾイルパーオキシヘキサン、
n−ブチル−4.4−ジ−t−ブチルパーオキシバ
レレート等である。尚必要に応じて架橋助剤を用
いてもよい。 本発明の加熱分解型発泡剤とは加熱により分解
して比較的急激にガスを発生する物質であり、例
えばアゾジカルボンアミド、ジニトロソペンタメ
チレンテトラミン、P.P′−オキシビスベンゼンス
ルホニルヒドラジド等の1種または2種以上の混
合物である。 発泡剤の混合量は目的とする発泡体の倍率によ
つて適宜選択されるが、本発明の発泡体において
は、ポリオレフイン系樹脂100重量部に対して5
〜50重量部添加されることが多い。これによつて
得られる発泡体の比重は0.2〜0.02である。 本発明においては上記ポリオレフイン系樹脂に
上記無機化合物、発泡剤、有機過酸化物および界
面活性剤を100℃前後でミキシングロールやバン
バリーミキサー等で混練したのち発泡剤の分解し
ない温度下でプレスあるいは押出機を用いて板状
成形品とする。必要に応じて着色剤、老化防止
剤、紫外線吸収剤、難燃剤、発泡助剤、架橋助
剤、滑剤などの添加剤を加えてもよい。この工程
において発泡剤、架橋剤が分解しない条件下で成
形しなければならない。このようにして得られた
無機物充填ポリオレフイン系樹脂成形物は赤外加
熱、熱風加熱、熱板加熱、液中あるいは液上加熱
等の単一あるいはこれらの複合手段により常圧下
で高発泡体とされる。 以下実施例に基き更に具体的に説明する。 実施例 1〜8 表−1に示す材料を100℃のミキシングロール
で混練し、100℃で1.5mm厚のシートにプレス成形
した。このシートを230℃のオーブンに投入し発
泡せしめた。その結果を表−2に示す。表−2よ
り界面活性剤を添加したものは発泡密度の低減が
図れ気泡も細かく表面平滑性にすぐれていた。そ
れに対し界面活性剤を添加してない比較例1〜3
においては気泡が荒く表面平滑性も劣つていた。
The present invention relates to a method for producing a polyolefin resin foam containing a high concentration of inorganic substances. Filling polyolefin resins with inorganic compounds is carried out for the purpose of making them non-polluting, flame retardant, and conserving resources. For example, hydrates such as Al(OH) 3 and Mg(OH) 2 can improve flame retardancy by releasing water of crystallization at a specific temperature, and are more combustible than so-called halogen flame retardants. It is attracting attention because it does not emit toxic gas and is inexpensive. However, when a conventional inorganic-filled polyolefin resin molded product is heated and foamed under normal pressure, it is difficult to obtain a highly foamed product, and even if it is obtained, the bubbles are coarse and the surface is noticeably rough, and it is difficult to obtain a highly foamed product. A large amount of blowing agent was required. In order to obtain a highly foamed inorganic-filled polyolefin resin, there is a method of introducing a crosslinked structure under pressure to decompose the foaming agent, and then heating and expanding it under normal pressure, but continuous production is difficult and it is produced in a batch process. Production efficiency decreases and prices tend to increase,
Furthermore, since it is impossible to produce long foamed products, its applications tend to be limited. The present invention has been made as a result of intensive studies in view of the above situation, and its purpose is to provide a method for producing a high expansion ratio foam made of polyolefin resin filled with a high concentration of inorganic substances, and a method for producing a foam with fine air bubbles and a surface of the foam. The object of the present invention is to provide a method that allows continuous industrial production of smooth and beautiful foams. However, the gist of the present invention is to mix a polyolefin resin with an inorganic compound powder, a thermally decomposable blowing agent, and an organic peroxide, mold it to form an inorganic-filled resin molded product, and then heat it above the decomposition temperature of the blowing agent. A method for producing a polyolefin resin foam filled with an inorganic substance is characterized in that 0.05 to 10 parts by weight of a surfactant are added and mixed to 100 parts by weight of the polyolefin resin. The present invention is an inorganic-filled polyolefin containing 50 to 250 parts by weight of inorganic compound powder, 0.05 to 10 parts by weight of a surfactant, a thermally decomposable blowing agent, and an organic peroxide crosslinking agent per 100 parts by weight of a polyolefin resin. This can be carried out by heating the resin molded product to a temperature higher than the decomposition temperature of the foaming agent and foaming it under normal pressure. The use of surfactants is essential to the practice of this invention. Although the mechanism of action of the surfactant used in the present invention is not clear, it is thought that the addition of the surfactant lowers the surface tension of the resin composition. In other words, the size of the bubbles during foaming is not uniform but varies, and the internal gas pressure of the bubbles increases as the bubble diameter becomes smaller. Therefore, the gas flows between adjacent bubbles across a thin membrane from the smaller diameter to the larger diameter. The bubble diameter becomes larger as the bubbles permeate through the air and finally coalesce into a larger one. Therefore, it becomes a foam with large cells. Since the pressure difference between the cells has a property that it is proportional to the surface tension, by lowering the surface tension, coalescence of the cells can be prevented and a foam with fine cells can be obtained. In addition, since it is difficult to form large bubbles, the bubble film is less likely to be destroyed, and the surface is smooth, and there is less gas escape, so it is thought that the amount of blowing agent added can be reduced. As the surfactant used in the present invention, nonionic surfactants such as alkylphenol type and sorbitan ester type are also effective, but silicone type surfactants and fluorine type surfactants particularly exhibit the above-mentioned effects. . Such a surfactant is available under the trade name NUC Silicone L3550 (Nippon Unicar).
(manufactured by Sumitomo 3M Ltd.) or Florado FC430 (manufactured by Sumitomo 3M Ltd.). The amount of surfactant added is in the range of 0.05 to 10 parts by weight per 100 parts by weight of the polyolefin resin. If it is less than 0.05 parts by weight, no effect can be achieved, and if it exceeds 10 parts by weight, the original properties of the resin will be significantly impaired, which is not preferable. The polyolefin resin in the present invention has a high
Medium and low pressure polyethylene, polypropylene, polybutene-1, ethylene-vinyl acetate copolymer, ethylene-propylene copolymer, ethylene-α-olefin copolymer, ethylene-acrylic acid copolymer, chlorinated polyethylene, chlorsulfone Refers to one type or a mixture of two or more types of polyethylene, polybutadiene, etc. Inorganic compounds in the present invention include aluminum hydroxide, magnesium hydroxide, basic magnesium carbonate, calcium hydroxide, tin oxide hydrate, zirconium oxide, calcium carbonate, magnesium carbonate, talc, clay, bentonite, attapulgite, barium borate, Zinc borate, gypsum, etc., and one or a mixture of two or more thereof. Moreover, the surface of the above-mentioned inorganic compound may be treated with a well-known fatty acid-based, silane-based, or titanium-based coupling agent. These inorganic compounds have an average particle size of 0.01~
It is a 50μ powder. The amount added is 30 to 250 parts by weight, preferably 50 to 200 parts by weight, per 100 parts by weight of the polyolefin resin. The organic peroxide of the present invention is a compound that decomposes when heated to generate radicals, such as di-
t-butyl peroxide, dicumyl peroxide, t-butyl cumyl peroxide, α, α
-bis(t-butylperoxy)P-diisopropylbenzene, 2.5-dimethyl-2.5-di(t-butylperoxy)hexane, 2.5-dimethyl-2.5
Di(t-butylperoxy)hexyne-3, 2.4
-dichlorobenzoyl peroxide, benzoyl peroxide, 1.1-di-t-butylperoxy3.3.5-trimethylcyclohexane, 2.5-dimethyl-2.5-dibenzoylperoxyhexane,
n-butyl-4.4-di-t-butyl peroxyvalerate and the like. Additionally, a crosslinking aid may be used if necessary. The thermally decomposable blowing agent of the present invention is a substance that decomposes upon heating and relatively rapidly generates gas, such as one type of azodicarbonamide, dinitrosopentamethylenetetramine, PP'-oxybisbenzenesulfonyl hydrazide, etc. Or a mixture of two or more. The mixing amount of the blowing agent is appropriately selected depending on the desired expansion ratio of the foam, but in the foam of the present invention, 5 parts by weight per 100 parts by weight of the polyolefin resin.
~50 parts by weight is often added. The foam thus obtained has a specific gravity of 0.2 to 0.02. In the present invention, the above-mentioned inorganic compound, blowing agent, organic peroxide, and surfactant are kneaded with the above-mentioned polyolefin resin using a mixing roll or Banbury mixer at around 100°C, and then pressed or extruded at a temperature that does not decompose the blowing agent. It is made into a plate-shaped product using a machine. Additives such as colorants, anti-aging agents, ultraviolet absorbers, flame retardants, foaming aids, crosslinking aids, and lubricants may be added as necessary. In this step, the molding must be carried out under conditions in which the blowing agent and crosslinking agent do not decompose. The inorganic-filled polyolefin resin molded product obtained in this way is made into a highly foamed body under normal pressure by infrared heating, hot air heating, hot plate heating, submerged or above liquid heating, or a combination of these methods. Ru. A more specific explanation will be given below based on Examples. Examples 1 to 8 The materials shown in Table 1 were kneaded using a mixing roll at 100°C, and press-molded at 100°C into a 1.5 mm thick sheet. This sheet was placed in an oven at 230°C and foamed. The results are shown in Table-2. As shown in Table 2, the foaming density was reduced with the addition of a surfactant, and the bubbles were fine and the surface smoothness was excellent. Comparative Examples 1 to 3 in which no surfactant was added
The bubbles were rough and the surface smoothness was poor.

【表】【table】

【表】【table】

【表】 ○:良好
×:表面肌アレ、凹凸
実施例 9 実施例3に示す配合処方を90〜100℃のバンバ
リミキサーで混練したのちペレツト化し、40mm押
出機で80〜100℃の温度で厚み3mm、巾200mmのシ
ートに成形した。このシートを加熱発泡炉に投入
し、長尺の発泡体を得た。この発泡体は密度
0.050g/cm3、気泡数18ケ/cmで表面が平滑な良
好な発泡体であつた。 実施例 10〜11 表−3に示す材料を115℃のミキシングロール
で混練し120℃で3mm厚みのシートにプレス成形
した。このシートを230℃のオーブンに投入し発
泡せしめた。その結果を表−4に示す。表−4よ
り界面活性剤を添加したものは発泡密度が小で気
泡が細かく、表面平滑性にすぐれたものが得られ
た。これに対し界面活性剤を添加していない比較
例4においては発泡体が不完全で表面平滑性も劣
つていた。
[Table] ○: Good
×: Surface roughness, unevenness Example 9 The formulation shown in Example 3 was kneaded in a Banbury mixer at 90 to 100°C, then pelletized, and a sheet with a thickness of 3 mm and a width of 200 mm was made using a 40 mm extruder at a temperature of 80 to 100°C. It was molded into. This sheet was placed in a heating foaming furnace to obtain a long foam. This foam has a density
It was a good foam with a smooth surface and a weight of 0.050 g/cm 3 and a number of cells of 18 cells/cm. Examples 10 to 11 The materials shown in Table 3 were kneaded using a mixing roll at 115°C and press-molded at 120°C into a 3 mm thick sheet. This sheet was placed in an oven at 230°C and foamed. The results are shown in Table-4. From Table 4, it was found that the foams to which a surfactant was added had a low foaming density, fine bubbles, and excellent surface smoothness. On the other hand, in Comparative Example 4 in which no surfactant was added, the foam was incomplete and the surface smoothness was poor.

【表】【table】

【表】 以上のように本発明によれば無機物を多量に添
加しても気泡が細かく表面平滑性にすぐれた無機
物充填発泡体の製造が可能となつた。
[Table] As described above, according to the present invention, it has become possible to produce an inorganic-filled foam with fine cells and excellent surface smoothness even when a large amount of inorganic material is added.

Claims (1)

【特許請求の範囲】 1 ポリオレフイン系樹脂に無機化合物粉体、加
熱分解型発泡剤および有機過酸化物を混合、成形
して無機物充填樹脂成形物となし、しかるのち発
泡剤の分解温度以上に加熱して発泡体とする方法
において、ポリオレフイン系樹脂100重量部に対
し界面活性剤0.05〜10重量部を添加混合すること
を特徴とする無機物を充填したポリオレフイン系
樹脂発泡体の製造法。 2 界面活性剤がフツ素系またはシリコーン系界
面活性剤である特許請求の範囲第1項記載の製造
法。
[Scope of Claims] 1 A polyolefin resin is mixed with an inorganic compound powder, a thermally decomposable blowing agent, and an organic peroxide, and molded to form an inorganic-filled resin molded product, which is then heated to a temperature higher than the decomposition temperature of the blowing agent. 1. A method for producing a polyolefin resin foam filled with an inorganic substance, which comprises adding and mixing 0.05 to 10 parts by weight of a surfactant to 100 parts by weight of the polyolefin resin. 2. The manufacturing method according to claim 1, wherein the surfactant is a fluorine-based or silicone-based surfactant.
JP5638383A 1983-03-31 1983-03-31 Production of inorganic substance-filled polyolefin resin foam Granted JPS59179635A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5638383A JPS59179635A (en) 1983-03-31 1983-03-31 Production of inorganic substance-filled polyolefin resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5638383A JPS59179635A (en) 1983-03-31 1983-03-31 Production of inorganic substance-filled polyolefin resin foam

Publications (2)

Publication Number Publication Date
JPS59179635A JPS59179635A (en) 1984-10-12
JPS6365213B2 true JPS6365213B2 (en) 1988-12-15

Family

ID=13025727

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5638383A Granted JPS59179635A (en) 1983-03-31 1983-03-31 Production of inorganic substance-filled polyolefin resin foam

Country Status (1)

Country Link
JP (1) JPS59179635A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0678449B2 (en) * 1989-07-27 1994-10-05 東レ株式会社 Pad materials and interior materials for vehicles
ATE366299T1 (en) * 2000-05-17 2007-07-15 Henkel Kgaa DETERGENT OR CLEANING PRODUCT MOLDS

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5240577A (en) * 1975-09-29 1977-03-29 Dainichiseika Color Chem Thermoplastic resin for expansion molding
JPS5679131A (en) * 1979-11-30 1981-06-29 Furukawa Electric Co Ltd:The Preparation of resin foam highly loaded with inorganic material
JPS56133140A (en) * 1980-03-24 1981-10-19 Nippon Ekika Seikei Kk Manufacture of foamed sheet filled and having surface skin
JPS5787433A (en) * 1980-11-20 1982-05-31 Tokyo Ink Kk Polyolefin resin composition for extrusion foaming
JPS57115432A (en) * 1981-01-08 1982-07-17 Furukawa Electric Co Ltd:The Highly-inorganic-filled foam of high expansion ratio and its manufacutre

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5240577A (en) * 1975-09-29 1977-03-29 Dainichiseika Color Chem Thermoplastic resin for expansion molding
JPS5679131A (en) * 1979-11-30 1981-06-29 Furukawa Electric Co Ltd:The Preparation of resin foam highly loaded with inorganic material
JPS56133140A (en) * 1980-03-24 1981-10-19 Nippon Ekika Seikei Kk Manufacture of foamed sheet filled and having surface skin
JPS5787433A (en) * 1980-11-20 1982-05-31 Tokyo Ink Kk Polyolefin resin composition for extrusion foaming
JPS57115432A (en) * 1981-01-08 1982-07-17 Furukawa Electric Co Ltd:The Highly-inorganic-filled foam of high expansion ratio and its manufacutre

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Publication number Publication date
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