JP3186821B2 - Method for producing polyolefin resin foam and foam - Google Patents

Method for producing polyolefin resin foam and foam

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Publication number
JP3186821B2
JP3186821B2 JP06000192A JP6000192A JP3186821B2 JP 3186821 B2 JP3186821 B2 JP 3186821B2 JP 06000192 A JP06000192 A JP 06000192A JP 6000192 A JP6000192 A JP 6000192A JP 3186821 B2 JP3186821 B2 JP 3186821B2
Authority
JP
Japan
Prior art keywords
foam
polyolefin resin
appearance
extrusion
hydrogen
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 - Fee Related
Application number
JP06000192A
Other languages
Japanese (ja)
Other versions
JPH05262908A (en
Inventor
良郎 高羽
紳一郎 横井
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
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Filing date
Publication date
Application filed by Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP06000192A priority Critical patent/JP3186821B2/en
Publication of JPH05262908A publication Critical patent/JPH05262908A/en
Application granted granted Critical
Publication of JP3186821B2 publication Critical patent/JP3186821B2/en
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Description

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

【産業上の利用分野】本発明は、プロテクター等のスポ
ーツ用品、断熱材等の建材、或いは緩衝材、包装材、自
動車の内装材等の用途に適したポリオレフィン系樹脂発
泡体の製造方法及び発泡体に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a polyolefin resin foam suitable for use as a sporting goods such as a protector, a building material such as a heat insulating material, or a cushioning material, a packaging material, a car interior material and the like. About the body.

【0002】[0002]

【従来の技術】一般に、ポリオレフィン系樹脂を発泡さ
せる方法としては、加熱分解型の化学発泡剤を用いて発
泡させる発泡方法と、揮発性の有機発泡剤を用いて発泡
させる押出発泡方法とがある。そして押出発泡方法に用
いられる揮発性の有機発泡剤は、炭化水素類とハロゲン
化炭化水素類とに大別される。
2. Description of the Related Art In general, as a method of foaming a polyolefin resin, there are a foaming method of foaming using a thermal decomposition type chemical foaming agent and an extrusion foaming method of foaming using a volatile organic foaming agent. . The volatile organic blowing agents used in the extrusion foaming method are roughly classified into hydrocarbons and halogenated hydrocarbons.

【0003】この前者の炭化水素類は、発泡体の気泡膜
を通してのガスの逃散速度が大きいため、経時的な気泡
収縮が起こり易く、寸法安定性に欠け、長い熟成期間が
必要とされるという欠点がある。
[0003] The former hydrocarbons have a high gas escaping rate through a foamed cell membrane, and therefore are liable to shrink over time, lack dimensional stability, and require a long aging period. There are drawbacks.

【0004】後者のハロゲン化炭化水素類は、大部分は
前記炭化水素類と同様の欠点を有するが、ジクロロジフ
ルオロメタン(CFC12)とジクロロテトラフルオロ
エタン(CFC14)の二種類は、発泡体の経時的寸法
変化が少ないため、押出発泡用の発泡剤として、広く使
用されてきた。
Most of the latter halogenated hydrocarbons have the same disadvantages as the above-mentioned hydrocarbons, but the two types of dichlorodifluoromethane (CFC12) and dichlorotetrafluoroethane (CFC14) are not suitable for the aging of foams. Because of its small dimensional change, it has been widely used as a foaming agent for extrusion foaming.

【0005】[0005]

【発明が解決しようとする課題】しかし、近年、フロン
ガスによるオゾン層破壊とそれによって引き起こされる
生物的学的な悪影響が国際的な大問題となっており、前
記のジクロロジフルオロメタンとジクロロテトラフルオ
ロエタンのような水素を含まないクロロフルオロカーボ
ンは、使用削減或いは今世紀中の全廃の対象物質として
指定されるようになってきた。
However, in recent years, the destruction of the ozone layer by chlorofluorocarbon gas and the biological adverse effects caused thereby have become a major international problem, and the above-mentioned dichlorodifluoromethane and dichlorotetrafluoroethane have become major problems. Hydrogen-free chlorofluorocarbons such as have been designated as substances subject to reduced use or elimination throughout the century.

【0006】そのため、水素を含まないクロロフルオロ
カーボンの代替品の開発が積極的に進められ、水素含有
クロロフルオロカーボン及びノンクロロフルオロカーボ
ンが開発されてきた。
For this reason, the development of hydrogen-free chlorofluorocarbon substitutes has been actively promoted, and hydrogen-containing chlorofluorocarbons and non-chlorofluorocarbons have been developed.

【0007】しかし、そのいずれも発泡適性不足、ガス
逃散による気泡収縮等問題が多く、現在実用に供し得る
発泡剤はまだ開発されていない。
However, all of them have many problems such as insufficient foaming aptitude and bubble shrinkage due to gas escape, and a foaming agent which can be practically used at present has not yet been developed.

【0008】この気泡収縮を防止する方法としては、脂
肪族エステル化合物、例えばステアリン酸モノグリセリ
ド、或いは脂肪族アミド化合物、例えばステアリン酸ア
ミド等をそれぞれ収縮防止剤として配合する方法が知ら
れている。
As a method of preventing the shrinkage of air bubbles, a method is known in which an aliphatic ester compound such as stearic acid monoglyceride or an aliphatic amide compound such as stearic acid amide is blended as an anti-shrinkage agent.

【0009】しかしこれらはその配合量を比較的多くし
ないと(樹脂100重量部に対して1〜10重量部程
度)効果がでにくく、また配合量を多くすると、外滑性
が高くなりすぎて押出変動を引き起こし、外観が悪く、
押出安定性に欠け、吐出圧力も低下し、場合により押出
不能、或いは発泡不能となり、大口径の発泡成形が困難
になることがあった。また製造された発泡体の気泡表面
に界面活性剤が浮きでてくることもあり、このため同素
材及び他素材との接着性が低下したり、印刷性が低下し
たりするという問題があった。
However, these effects are difficult to obtain unless the blending amount is relatively large (about 1 to 10 parts by weight with respect to 100 parts by weight of the resin), and if the blending amount is large, the outer lubrication becomes too high. Causing extrusion fluctuations, poor appearance,
Lack of extrusion stability, lowering of discharge pressure, and in some cases, making extrusion impossible or foaming impossible, making it difficult to form large-diameter foam. In addition, the surfactant sometimes floats on the cell surface of the produced foam, and therefore, there has been a problem that the adhesiveness with the same material and other materials is reduced, and the printability is reduced. .

【0010】また、表皮収縮等により、前記用途に適し
た表面が平滑で、経時的寸法変化の少ない、外観良好な
ポリオレフィン系樹脂発泡体が容易に得られなかった。
Also, due to skin shrinkage and the like, a polyolefin-based resin foam having a smooth surface suitable for the above-mentioned applications, a small dimensional change with time, and a good appearance cannot be easily obtained.

【0011】本発明は、このような問題を解決するため
になされたもので、第1の発明は、オゾン層破壊の恐れ
の少ない、押出発泡性、接着性、印刷性の良い、経時的
寸法変化の少ない、外観良好な高倍率の押出発泡体が得
られる、ポリオレフィン系樹脂発泡体の製造方法を提供
することを目的とする。
The present invention has been made to solve such a problem.
According to the first invention, there is provided a high-magnification extruded foam having good appearance, good extruded foaming property, good adhesiveness, good printability, little dimensional change with time, and good appearance. It is an object of the present invention to provide a method for producing a polyolefin resin foam.

【0012】また第2の発明は、プロテクター等のスポ
ーツ用品、断熱材等の建材、或いは緩衝材、包装材、自
動車の内装材等の用途に適した表面平滑で経時的寸法変
化の少ない、外観良好な高倍率のポリオレフィン系樹脂
発泡体を得ることを目的とする。
A second aspect of the present invention is an external appearance that has a smooth surface and little dimensional change over time, which is suitable for applications such as sports equipment such as protectors, building materials such as heat insulating materials, cushioning materials, packaging materials, and interior materials for automobiles. It is an object of the present invention to obtain a good high magnification polyolefin resin foam.

【0013】[0013]

【課題を解決するための手段】本発明の第1の発明のポ
リオレフィン系樹脂発泡体の製造方法は、ポリオレフィ
ン系樹脂に、脂肪族エステル化合物または脂肪族アミド
化合物と、フッソ系界面活性剤とを配合し、これを押出
機中に投入し、炭素数2の水素含有クロロフルオロカー
ボンと炭素数1の水素含有クロロフルオロカーボンとか
らなる発泡剤を、押出機中に投入し、押出し発泡させる
ことを特徴とするものである。
According to a first aspect of the present invention, there is provided a method for producing a polyolefin resin foam, comprising the steps of: adding an aliphatic ester compound or an aliphatic amide compound to a polyolefin resin; Compounded and charged into an extruder, and a foaming agent comprising a hydrogen-containing chlorofluorocarbon having 2 carbon atoms and a hydrogen-containing chlorofluorocarbon having 1 carbon atom is charged into the extruder and extruded and foamed. Is what you do.

【0014】また第2の発明の発泡体は、請求項1記
のポリオレフィン系樹脂発泡体の製造方法によって、製
せられていることを特徴とするものである。
[0014] foam second invention, the process for producing a polyolefin resin foam of claim 1 Symbol placement, is characterized in that it is Seise.

【0015】本発明で使用されるポリオレフィン系樹脂
とは、オレフィン系炭化水素の重合体または共重合体で
あって、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−酢酸ビニル共重合体、エ
チレン−アクリル酸系共重合体、プロピレン−スチレン
共重合体、プロピレン−スチレン−エチレン−ブタジエ
ン共重合体、塩化ビニル−エチレン共重合体等を挙げる
ことができる。これらは、それぞれ単独または二種類以
上混合或いは架橋させて使用することができる。
The polyolefin resin used in the present invention is a polymer or copolymer of an olefinic hydrocarbon, such as polyethylene, polypropylene, ethylene-propylene copolymer, ethylene-vinyl acetate copolymer, ethylene -Acrylic acid copolymers, propylene-styrene copolymers, propylene-styrene-ethylene-butadiene copolymers, vinyl chloride-ethylene copolymers, and the like. Each of these can be used alone or in combination or cross-linked.

【0016】本発明で使用されるフッソ系界面活性剤と
しては、例えば、次式(1)または(2)で表されるパ
ーフルオロアルキルポリエーテルが挙げられる。
The fluorosurfactant used in the present invention includes, for example, perfluoroalkyl polyether represented by the following formula (1) or (2).

【化1】 (式中、mは1以上の整数、nは0以上の整数を示
す。)
Embedded image (In the formula, m represents an integer of 1 or more, and n represents an integer of 0 or more.)

【化2】 (式中、pは1以上の整数、qは0以上の整数を示
す。)
Embedded image (In the formula, p represents an integer of 1 or more, and q represents an integer of 0 or more.)

【0017】フッソ系界面活性剤は、樹脂100重量部
に対して、0.01〜5重量部の範囲で使用することが
できる。好ましくは0.1〜1重量部の範囲で使用する
のが望ましい。
The fluorosurfactant can be used in an amount of 0.01 to 5 parts by weight based on 100 parts by weight of the resin. Preferably, it is used in the range of 0.1 to 1 part by weight.

【0018】第1の発明で用いられる炭素数2の水素含
有クロロフルオロカーボンと炭素数1の水素含有クロロ
フルオロカーボンとからなる発泡剤は、前者を70〜3
0重量%、後者を30〜70重量%の比率で使用するの
が望ましい。
The blowing agent comprising a hydrogen-containing chlorofluorocarbon having 2 carbon atoms and a hydrogen-containing chlorofluorocarbon having 1 carbon atom, which is used in the first invention, has a former of 70 to 3
It is desirable to use 0% by weight and the latter in a proportion of 30 to 70% by weight.

【0019】脂肪族エステル化合物としては、ステリア
ン酸モノグリセリド、ステリアン酸ジグリセリド、ラウ
リン酸ジグリセリド、ラウリン酸モノグリセリド、パル
ミチン酸モノグリセリド、パルミチン酸ジグリセリド等
を用いることができる。脂肪族アミド化合物としては、
ラウリン酸アミド、ミリスチン酸アミド、パルミチン酸
アミド、ステリアン酸アミド、アラキシン酸アミド、ベ
ヘニン酸アミド、ステリアン酸ステアリルアミド、N−
メチルステリアン酸アミド、N−N’−ジメチルステリ
アン酸アミド、ジラウリン酸アミド等を用いることがで
きる。
As the aliphatic ester compound, steric acid monoglyceride, steric acid diglyceride, lauric acid diglyceride, lauric acid monoglyceride, palmitic acid monoglyceride, palmitic acid diglyceride and the like can be used. As the aliphatic amide compound,
Lauric acid amide, myristic acid amide, palmitic acid amide, stearic acid amide, alaxic acid amide, behenic acid amide, stearyl acid stearylamide, N-
Methylsterian acid amide, N-N'-dimethylstearic acid amide, dilauric acid amide, and the like can be used.

【0020】水架橋性ポリオレフィン樹脂に多価アルコ
ールを入れた場合、押出機中で架橋が急速に進行し、表
面が平滑で安定した発泡体が得られないため、架橋性ポ
リオレフィン樹脂の場合には脂肪族アミド化合物を用い
るのが望ましい。
When a polyhydric alcohol is added to the water-crosslinkable polyolefin resin, crosslinking proceeds rapidly in the extruder, and a stable foam having a smooth surface cannot be obtained. It is desirable to use an aliphatic amide compound.

【0021】気泡核剤、架橋触媒、酸化防止剤、滑剤、
静電防止剤、難燃剤、顔料等は適宜必要に応じて添加す
ることができる。例えばタルク、シリカ、炭酸カルシウ
ム、ステアリン酸カルシウム、珪酸カルシウム、重曹等
の気泡核剤、或いはジブチル錫ジアセテート、ジブチル
錫ジラウレート、酢酸第1錫、カブリル酸第1錫、ナフ
テン酸錫、カブリル酸亜鉛、ステアリン酸亜鉛等のシラ
ノール縮合触媒、フェノール系、有機チオ酸系、有機リ
ン酸系、有機アミン系、有機スズ系等の酸化防止剤等を
添加することができる。
A bubble nucleating agent, a crosslinking catalyst, an antioxidant, a lubricant,
Antistatic agents, flame retardants, pigments, and the like can be appropriately added as needed. For example, bubble nucleating agents such as talc, silica, calcium carbonate, calcium stearate, calcium silicate, sodium bicarbonate, or dibutyltin diacetate, dibutyltin dilaurate, stannous acetate, stannous cabrate, tin naphthenate, zinc cabrate, A silanol condensation catalyst such as zinc stearate, or an antioxidant such as a phenol-based, organic thioacid-based, organic phosphoric acid-based, organic amine-based, or organic tin-based can be added.

【0022】[0022]

【作用】第1の発明では、オゾン層破壊特定物質の発泡
剤(水素を含有しないクロロフルオロカーボン)を使用
せずに、非特定物質の分解し易い水素含有クロロフルオ
ロカーボンを発泡剤として用いることにより、オゾン層
を破壊する恐れが少なくなる。
According to the first aspect of the present invention, a hydrogen-containing chlorofluorocarbon, which is easily decomposed by a non-specific substance, is used as a foaming agent without using a foaming agent (chlorofluorocarbon containing no hydrogen) of the ozone depleting specific substance. The risk of destruction of the ozone layer is reduced.

【0023】またフッソ系界面活性剤を、従来使用して
いる収縮防止剤の脂肪族エステル化合物或いは脂肪族ア
ミド化合物と併用して使用することにより、脂肪族エス
テル化合物或いは脂肪族アミド化合物の従来使用してい
る量を減らすことができる。これにより押出発泡性、接
着性、印刷性が改善される。
By using a fluorosurfactant in combination with a conventionally used aliphatic ester compound or aliphatic amide compound as a shrinkage preventive, the conventional use of an aliphatic ester compound or aliphatic amide compound is possible. You can reduce the amount you are doing. Thereby, extrusion foaming property, adhesiveness, and printability are improved.

【0024】[0024]

【実施例】以下本発明の実施例、比較例について説明す
EXAMPLES Examples of the present invention and comparative examples will be described below .

【0025】実施例1〜6 メルトインデックス(MI:190℃)2.0、密度
0.92の低密度ポリエチレンに表1に示す割合で、フ
ッソ系界面活性剤、ステアリン酸モノグリセリド、タル
クを混合した後、直径40mmm、L/D=28の単軸
押出機に供給し、溶融混練した後、押出機中央に設けら
れた発泡剤注入口から、炭素数2の水素含有クロロフル
オロカーボン(モノクロロジフルオロエタン、HCFC
−142b)と、炭素数1の水素含有クロロフルオロカ
ーボン(モノクロロジフルオロメタン、HCFC−2
2)とを、それぞれ表1に示す割合で混合した発泡剤
を、発泡倍率が35倍になるように、表1に示す割合で
圧入した。バレル内で更に充分混練したのち、バレル先
端部及び金型で発泡最適温度まで冷却して、金型先端か
ら所定形状に押出した。混練された樹脂は金型先端から
吐出されると同時に発泡して、ポリエチレン発泡体が得
られた。
Examples 1 to 6 A low-density polyethylene having a melt index (MI: 190 ° C.) of 2.0 and a density of 0.92 was mixed with a fluorosurfactant, stearic acid monoglyceride and talc in the proportions shown in Table 1 . Thereafter, the mixture was supplied to a single-screw extruder having a diameter of 40 mmm and L / D = 28, melt-kneaded, and then fed through a foaming agent inlet provided in the center of the extruder through a hydrogen-containing chlorofluorocarbon having 2 carbon atoms (monochlorodifluoroethane, HCFC).
-142b) and a hydrogen-containing chlorofluorocarbon having 1 carbon atom (monochlorodifluoromethane, HCFC-2
2) and a blowing agent mixed in respective proportions shown in Table 1, so that the expansion ratio becomes 35 times, was injected at a ratio shown in Table 1. After further kneading in the barrel, the mixture was cooled to the optimum foaming temperature at the barrel tip and the mold, and extruded into a predetermined shape from the mold tip. The kneaded resin was discharged from the die tip and foamed at the same time as the polyethylene foam was obtained.

【0026】得られた発泡体について、押出安定性、外
観、経時寸法安定性、熟成期間を調べた。結果を表1に
示す。押出安定性は押出発泡成形の安定性を、外観は目
視観察で、また熟成期間は、23℃、相対湿度65%
(RH)の恒温恒湿槽による発泡体に必要な熟成期間を
示したものである。また、経時寸法安定性は目視観察
で、接着性は所定の接着剤を用いて鋼材に接着させたと
きの接着力を比較した。判定基準は次による。
The obtained foam was examined for extrusion stability, appearance, dimensional stability over time, and aging period. The results are shown in Table 1 . Extrusion stability refers to the stability of extrusion foam molding;
Visual observation and aging period: 23 ° C, relative humidity 65%
(RH) The aging period required for foams in a thermo-hygrostat
It is shown. Also, over time dimensional stability by visual observation, the adhesive was compared with the adhesive strength when adhered to the steel by using a predetermined adhesive. The criteria are as follows.

【0027】 押出安定性:○良い △若干変動あり ×変動大 外観 :◎収縮なし○表皮収縮少しあり△収縮あり×収縮大 経時寸法安定性:◎収縮なし○表皮収縮少しあり△収縮あり×収縮大 熟成期間 :◎なし ○1日以内 △3日以内 ×3日以上 接着性 :◎問題なし ○良好 △接着性不足気味 ×接着性悪い (接着力) >1600 1500〜1600 1400〜1500 <1400 (gf/25mm)Extrusion stability: good ○ slightly fluctuated × large fluctuation Appearance: ◎ no shrinkage ○ slight skin shrinkage △ shrinkage × large shrinkage dimensional stability over time: ◎ no shrinkage ○ slight skin shrinkage △ shrinkage × shrinkage Large aging period: ◎ None ○ Within 1 day △ Within 3 days × 3 days or more Adhesiveness: ◎ No problem ○ Good △ Poor adhesiveness × Poor adhesiveness (Adhesive strength)> 1600 1500-1600 1400-1500 <1400 ( (gf / 25mm)

【0028】比較例1〜6 フッソ系界面活性剤を使用しない以外は、実施例1〜6
同じ低密度ポリエチレン樹脂、ステアリン酸モノグリ
セリド、タルク、HCFC−142b、HCFC−22
を用い、表1に示す割合に配合し、実施例1〜6と同じ
方法でポリエチレン発泡体を製造した。結果を表1に
す。評価項目、評価方法は実施例1〜6の場合と同じで
ある。
[0028] except not using the Comparative Examples 1 to 6 fluorine based surfactant, Examples 1-6
The same low-density polyethylene resin, stearic acid monoglyceride, talc, HCFC-142b and, HCFC-22
, And blended in the proportions shown in Table 1 to produce polyethylene foams in the same manner as in Examples 1 to 6 . The results are shown in Table 1 . Evaluation items and evaluation methods are the same as those in Examples 1 to 6 .

【0029】[0029]

【表1】 [Table 1]

【0030】表1から分かるように、フッソ系界面活性
剤を、脂肪族エステル化合物と併用した場合には、フッ
ソ系界面活性剤自体の量が0.1重量%と少量添加で
も、押出安定性、外観、経時寸法安定性、熟成期間が良
くなった。
[0030] As can be seen 1 or al table, a fluorine-based surfactant, when used in combination with aliphatic ester compound, in amounts and of small additions of 0.1 wt% of fluorine-based surface active agent itself, extrusion stability The properties, appearance, dimensional stability over time, and aging period were improved.

【0031】また通常配合量を比較的多くしないと(樹
脂100重量部に対して1〜10重量部程度)効果がで
ない脂肪族エステル化合物の量を0.5〜0.9%と1
%以下に減少させても、フッソ系界面活性剤との併用に
より押出安定性、外観、経時寸法安定性、熟成期間が良
くなった。
Usually, the amount of the aliphatic ester compound which is not effective unless the blending amount is relatively large (about 1 to 10 parts by weight with respect to 100 parts by weight of the resin) is 0.5 to 0.9% and 1%.
%, The extrusion stability, appearance, dimensional stability over time, and aging period were improved by the combined use with a fluorosurfactant.

【0032】これに対しフッソ系界面活性剤を、脂肪族
エステル化合物と併用して使用しない場合は、脂肪族エ
ステル化合物の量を少なくした場合は、押出安定性、接
着性は良いが、外観、経時寸法安定性、熟成期間は悪化
した。逆に、脂肪族エステル化合物の量を多くした場合
には、外観、経時寸法安定性、熟成期間は良いが、押出
安定性、接着性が悪化した。従って、押出安定性、接着
性、外観、経時寸法安定性、熟成期間の全てを満足させ
るものは得られなかった。
On the other hand, when the fluorosurfactant is not used in combination with the aliphatic ester compound, when the amount of the aliphatic ester compound is reduced, the extrusion stability and adhesiveness are good, but the appearance, The dimensional stability over time and the aging period deteriorated. Conversely, when the amount of the aliphatic ester compound was increased, the appearance, the dimensional stability over time, and the aging period were good, but the extrusion stability and the adhesiveness were deteriorated. Therefore, none satisfying all of extrusion stability, adhesiveness, appearance, dimensional stability with time, and aging period could be obtained.

【0033】実施例7〜9は第1の発明において、水架
橋性ポリエチレンの例を示したものである。架橋性ポリ
エチレンの場合は、前記したように、架橋性ポリエチレ
ンに多価アルコールを入れた場合、押出機中で架橋が急
速に進行し、表面が平滑で安定した発泡体が得られない
ため、脂肪族アミド化合物を用いた。
Examples 7 to 9 show examples of the water-crosslinkable polyethylene in the first invention. In the case of the crosslinkable polyethylene, as described above, when a polyhydric alcohol is added to the crosslinkable polyethylene, the crosslinking proceeds rapidly in the extruder, and a smooth foam having a smooth surface cannot be obtained. A group amide compound was used.

【0034】実施例7〜9 メルトインデックス(MI;190℃)2.0、密度
0.92の架橋性低密度ポリエチレン、フッソ化合物、
ステアリン酸アミド、タルク、ジブチル錫ジラウレー
ト、HCFC−142b、HCFC−22を用い、表2
示す割合に配合し、実施例1〜6と同じ方法で架橋性
ポリエチレン発泡体を製造した。
Examples 7 to 9 Crosslinkable low-density polyethylene having a melt index (MI; 190 ° C.) of 2.0 and a density of 0.92, a fluorine compound,
Using stearic acid amide, talc, dibutyltin dilaurate, HCFC-142b and HCFC-22, Table 2
And a crosslinkable polyethylene foam was produced in the same manner as in Examples 1 to 6 .

【0035】得られた発泡体の押出発泡性、外観、経時
寸法安定性、熟成期間、接着性を調べた結果を表2に
す。評価項目、評価方法は実施例1〜6の場合と同じで
ある。
Table 2 shows the results of examining the extruded foamability, appearance, dimensional stability over time, aging period, and adhesiveness of the obtained foam. Evaluation items and evaluation methods are the same as those in Examples 1 to 6 .

【0036】比較例7〜9 フッソ系界面活性剤を使用しない以外は、実施例7〜9
同じ架橋性低密度ポリエチレン、ステアリン酸アミ
ド、タルク、ジブチル錫ジラウレート、HCFC−14
2b、HCFC−22を用い、表2に示す割合に配合
し、実施例7〜9と同じ方法で架橋性ポリエチレン発泡
体を製造した。
[0036] except not using the Comparative Examples 7-9 fluorine-based surfactant, Examples 7-9
The same crosslinkable low density polyethylene, stearic amide, talc, dibutyltin dilaurate and, HCFC-14
2b and HCFC-22 were blended in the proportions shown in Table 2 to produce a crosslinkable polyethylene foam in the same manner as in Examples 7 to 9 .

【0037】得られた発泡体の押出発泡性、外観、経時
寸法安定性、熟成期間、接着性を調べた結果を表2に
す。評価項目、評価方法は実施例7〜9の場合と同じで
ある。
Table 2 shows the results of examining the extruded foamability, appearance, dimensional stability over time, aging period, and adhesiveness of the obtained foam. Evaluation items and evaluation methods are the same as those in Examples 7 to 9 .

【0038】[0038]

【表2】 [Table 2]

【0039】表2から分かるように、架橋性ポリエチレ
ンの場合も前記した非架橋性ポリエチレンと同様の結果
になり、フッソ系界面活性剤と脂肪族アミド化合物とを
併用した場合には、押出安定性、外観、経時寸法安定
性、熟成期間が良くなった。
[0039] As can be seen 2 or al table, when the crosslinkable polyethylene also become same results as non-crosslinked polyethylene described above, when used in combination with the fluorine-based surfactant and an aliphatic amide compound, extrusion stability The properties, appearance, dimensional stability over time, and aging period were improved.

【0040】これに対しフッソ系界面活性剤と脂肪族ア
ミド化合物とを併用して使用しない場合は、脂肪族アミ
ド化合物の量を少なくした場合は、押出安定性、接着性
は良いが、外観、経時寸法安定性、熟成期間が悪化し
た。
On the other hand, when the fluorosurfactant and the aliphatic amide compound are not used in combination, when the amount of the aliphatic amide compound is reduced, the extrusion stability and adhesiveness are good, but the appearance, The dimensional stability over time and the aging period deteriorated.

【0041】逆に、脂肪族アミド化合物の量を多くした
場合は、外観及び経時寸法安定性、熟成期間は良いが、
押出安定性、接着性が悪化した。従って、押出安定性、
接着性、外観、経時寸法安定性、熟成期間の全てを満足
させるものは得られなかった。
Conversely, when the amount of the aliphatic amide compound is increased, the appearance, the dimensional stability with time and the aging period are good, but
Extrusion stability and adhesion deteriorated. Therefore, extrusion stability,
A product satisfying all of the adhesiveness, appearance, dimensional stability over time, and aging period could not be obtained.

【0042】[0042]

【発明の効果】第1の発明では、オゾン層破壊特定物質
の発泡剤(水素を含有しないクロロフルオロカーボン)
を使用せずに、非特定物質の分解し易い水素含有クロロ
フルオロカーボンを発泡剤として用いるので、オゾン層
を破壊する恐れを少なくすることができ、公害防止に寄
与することができる。
According to the first aspect of the present invention, a foaming agent of a specific substance that depletes ozone (chlorofluorocarbon containing no hydrogen) is used.
Since the hydrogen-containing chlorofluorocarbon, which easily decomposes a non-specific substance, is used as a foaming agent without using, it is possible to reduce the risk of destruction of the ozone layer and to contribute to pollution prevention.

【0043】また第1の発明のフッソ系界面活性剤を併
用することにより、従来用いられている収縮防止剤の脂
肪族エステル化合物或いは脂肪族アミド化合物の配合量
を押出発泡性に影響のない、また接着性、印刷性の影響
の少ない所まで減小させることができるので、押出発泡
性、接着性、印刷性の良い、経時的寸法変化の少ない、
外観良好な高倍率のポリオレフィン系樹脂発泡体を製造
することができる。
By using the fluorosurfactant of the first invention together, the compounding amount of the conventionally used aliphatic ester compound or aliphatic amide compound of the anti-shrinkage agent does not affect the extrusion foaming property. In addition, since it can be reduced to a place where the influence of adhesiveness and printability is small, extrusion foaming property, adhesiveness, good printability, little dimensional change with time,
A polyolefin resin foam having a good appearance and a high magnification can be produced.

【0044】また第2の発明により、プロテクター等の
スポーツ用品、断熱材等の建材、或いは緩衝材、包装
材、自動車の内装材等の用途に適した表面平滑で経時的
寸法変化の少ない、外観良好な高倍率のポリオレフィン
系樹脂発泡体を得ることができる。
According to the second aspect of the present invention, the outer appearance is suitable for applications such as sports equipment such as protectors, building materials such as heat insulating materials, cushioning materials, packaging materials, and interior materials for automobiles, and has a small dimensional change with time. A good high magnification polyolefin-based resin foam can be obtained.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ポリオレフィン系樹脂に、脂肪族エステ
ル化合物または脂肪族アミド化合物と、フッソ系界面活
性剤とを配合し、これを押出機中に投入し、炭素数2の
水素含有クロロフルオロカーボンと炭素数1の水素含有
クロロフルオロカーボンとからなる発泡剤を、押出機中
に投入し、押出し発泡させることを特徴とするポリオレ
フィン系樹脂発泡体の製造方法。
(1) An aliphatic esthetic resin is added to a polyolefin resin.
Compound or aliphatic amide compound and a fluorine-based surfactant
And an extruder, and this is put into an extruder, which has 2 carbon atoms.
Hydrogen-containing chlorofluorocarbon and C1 hydrogen
A blowing agent consisting of chlorofluorocarbon and
Characterized by being extruded and foamed
A method for producing a fin-based resin foam.
【請求項2】 請求項1記載のポリオレフィン系樹脂発
泡体の製造方法によって、製せられていることを特徴と
する発泡体。 【0001】
2. The polyolefin resin according to claim 1,
It is manufactured by the method of manufacturing foam
Foam. [0001]
JP06000192A 1992-03-17 1992-03-17 Method for producing polyolefin resin foam and foam Expired - Fee Related JP3186821B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06000192A JP3186821B2 (en) 1992-03-17 1992-03-17 Method for producing polyolefin resin foam and foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06000192A JP3186821B2 (en) 1992-03-17 1992-03-17 Method for producing polyolefin resin foam and foam

Publications (2)

Publication Number Publication Date
JPH05262908A JPH05262908A (en) 1993-10-12
JP3186821B2 true JP3186821B2 (en) 2001-07-11

Family

ID=13129437

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06000192A Expired - Fee Related JP3186821B2 (en) 1992-03-17 1992-03-17 Method for producing polyolefin resin foam and foam

Country Status (1)

Country Link
JP (1) JP3186821B2 (en)

Also Published As

Publication number Publication date
JPH05262908A (en) 1993-10-12

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