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JPH0153295B2 - - Google Patents

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Publication number
JPH0153295B2
JPH0153295B2 JP8063181A JP8063181A JPH0153295B2 JP H0153295 B2 JPH0153295 B2 JP H0153295B2 JP 8063181 A JP8063181 A JP 8063181A JP 8063181 A JP8063181 A JP 8063181A JP H0153295 B2 JPH0153295 B2 JP H0153295B2
Authority
JP
Japan
Prior art keywords
weight
crosslinking
hydrogen peroxide
parts
blowing agent
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
JP8063181A
Other languages
Japanese (ja)
Other versions
JPS57195129A (en
Inventor
Eizo Mitsui
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.)
Eiwa Chemical Industries Co Ltd
Original Assignee
Eiwa Chemical Industries 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 Eiwa Chemical Industries Co Ltd filed Critical Eiwa Chemical Industries Co Ltd
Priority to JP8063181A priority Critical patent/JPS57195129A/en
Publication of JPS57195129A publication Critical patent/JPS57195129A/en
Publication of JPH0153295B2 publication Critical patent/JPH0153295B2/ja
Granted legal-status Critical Current

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

Description

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

本発明は水架橋性重合体用発泡剤組成物に関す
る。さらに詳しくは、架橋性基として加水分解可
能なシラン基を有するオレフイン系重合体の架橋
発泡体を得るに好適な発泡剤組成物に関する。 オレフイン系重合体の架橋発泡体を製造する方
法としては多くの公知技術がある。 オレフイン系重合体と発泡剤との混合物に、
放射線を照射することによつて架橋させたの
ち、加熱発泡する方法。 オレフイン系重合体に、過酸化物架橋剤と発
泡剤とを配合したのち、加熱することによつ
て、架橋および発泡を行なわせる方法。 しかし、これらの方法はいずれも技術として完
全なものでない。すなわち、の放射線架橋法で
は、特殊かつ高価な架橋装置が必要であり、しか
も工業的に使用し得る照射装置の機能上からして
肉厚の成形品については実質的には利用不可能で
ある。一方、の過酸化物による架橋法では、加
工温度および条件の注意深い制御が必要である。
この様な制御は、過酸化物架橋剤および発泡剤の
活性化温度とオレフイン系重合体の軟化温度との
間の精密な均衡を必要とする為、しばしば達成す
ることは困難である。 ところで、オレフイン系重合体の架橋発泡体の
製造方法として、上記した放射線架橋法や過酸化
物による架橋法以外に、水架橋性重合体を用いた
方法が知られている。すなわち、オレフイン系重
合体に、不飽和シラン化合物をグラフト共重合さ
せ、得られたシリコーングラフト化オレフイン系
重合体、あるいは、オレフイン炭化水素とオレフ
イン性不飽和シラン化合物から主としてなる共重
合体と、発泡剤およびシラノール縮合触媒とから
なる組成物の成形品を加熱することによつて発泡
させ、架橋は発泡操作の前または後あるいは発泡
操作と同時に、温水中に浸漬あるいは加熱水蒸気
雰囲気中に暴露することによつて行なわせる方法
である。しかしながら、本発明者の知る限りで
は、不均一な架橋度の成形体が得られたり、安定
した架橋度に達するのに時間がかかるといつた工
業的でない難点がある。特に肉厚成形品の場合に
は、製品の使用される環境や雰囲気によつて架橋
度の経時変化を伴い、安定した物性の維持が甚だ
困難である。 本発明者は上記諸欠点を解決することを目的と
し、鋭意研究の結果、水架橋性重合体をシラノー
ル縮合触媒の存在下、下記の発泡剤組成物を使用
し架橋発泡させることにより、肉厚で内部まで均
一に架橋された発泡体が得られることを見出し、
本発明を完成するに至つた。 本発明の発泡剤組成物は、アゾジカルボンアミ
ドに、炭酸塩過酸化水素化物、硼酸塩過酸化水素
化物およびリン酸塩過酸化水素化物よりなる群か
ら選ばれた少なくとも一種の過酸化水素付加無機
化合物を添加したものであり、過酸化水素付加無
機化合物の添加量は、アゾジカルボンアミド1重
量部に対して通常0.1重量部以上であれば良いが
好ましくは0.1〜2.0重量部、さらに好ましくは0.5
〜1.0重量部を用いるのが望ましい。アゾジカル
ボンアミドに添加して用いられる過酸化水素付加
無機化合物の具体例は、たとえば過炭酸ナトリウ
ム、過炭酸カリウム、過硼酸ナトリウム、過硼酸
カリウム、過リン酸ナトリウム、過リン酸カリウ
ム等を挙げることができ、これ等の化合物はそれ
ぞれ炭酸ナトリウム、炭酸カリウム、硼酸ナトリ
ウム、硼酸カリウム、リン酸ナトリウム、リン酸
カリウムに過酸化水素を作用させる方法等によつ
て得られる。 本発明でいう水架橋性重合体とは、主鎖または
側鎖に、加水分解可能な有機基を有するシランが
結合しているオレフイン系重合体をいい、オレフ
イン系重合体とオレフイン性不飽和シラン化合物
とのグラフト共重合体、オレフイン炭化水素とオ
レフイン性不飽和シラン化合物とのランダム共重
合体があり、具体的には下記のものがある。 1 オレフイン系重合体とオレフイン性不飽和シ
ラン化合物とのグラフト共重合体 (1) オレフイン性不飽和シラン化合物 一般式 RR′nSiY3-oで表わされるオレフイ
ン性不飽和シラン化合物(ここで、Rはオレフ
イン性ハイドロカーボンまたはハイドロカーボ
ンオキシ基、R′は脂肪族飽和ハイドロカーボ
ン基、Yは加水分解可能な有機基、nは0.1ま
たは2を表わす。Yが複数個であるときは、そ
れぞれ同一でなくても良い。)この不飽和シラ
ン化合物の具体例は、Rがたとえば、ビニル、
アリル、イソプロペニル、ブテニル、シクロヘ
キセニル、Yがメトキシ、エトキシ、ホルミル
オキシ、アセトキシ、プロピオノキシないし、
アルキル、R′がメチル、エチル、プロピル、
デシル、フエニルであるものである。これらの
中で最も好ましいものは、ビニルトリメトキシ
シラン、ビニルトリエトキシシラン、ビニルト
リアセトキシシランである。 (2) オレフイン系重合体 上記不飽和シランがグラフト共重合する幹と
なるべきオレフイン系重合体は、ポリエチレ
ン、エチレン―酢酸ビニル共重合体、エチレン
―アクリル酸共重合体、ポリプロピレン、塩素
化ポリエチレン等広範囲のものである。 ラジカル発生剤の存在下、オレフイン系重合体
にオレフイン性不飽和シラン化合物をグラフト共
重合させて、不飽和シラン化合物グラフト化オレ
フイン系重合体が得られる。 2 オレフイン炭化水素とオレフイン性不飽和シ
ラン化合物とのランダム共重合体 オレフイン炭化水素と上記したオレフイン性不
飽和シラン化合物との共重合は、重合開始剤を使
用し、両者の重合が生じる任意の条件で行えば良
い。 本発明は架橋方法として、公知技術である水雰
囲気に暴露するという方法とは異なり、発泡剤組
成物中に、分解することにより水を生成する物質
を予め配合しておくことによつて、アゾジカルボ
ンアミドの分解と同時にシラン架橋に必要な水の
発生があり、発泡と架橋を同時に行なうことを特
徴とするものである。すなわち発泡剤組成物から
発生する水により架橋せしめ、短時間に架橋が終
了するので、発泡操作の前後、あるいは同時にか
かわりなく水雰囲気に暴露する必要はなく製造の
時間短縮を図ることができる。アゾジカルボンア
ミドの熱分解によるガス発生と、水の発生が同時
に起こる為、発泡と架橋の時間的、粘弾性的な均
衡は大変良く、従つて、成形体の気泡は均一微細
で非常に弾力性のあるスポンジとなる。 本発明の発泡剤組成物は、水架橋性重合体用発
泡剤組成物として上記の点で優れているばかりで
なく、膨張に有効なガス発生量が非常に多く、又
アゾジカルボンアミドの分解残渣が少ないという
長所もある。 アゾジカルボンアミドに過炭酸ナトリウムを配
合して得た発泡剤の200℃、20分後のガス発生量
を第1表に示す。ガス発生量は、ガスビユーレツ
トに接続された試験管に発泡剤を流動パラフイン
10ml中に分散させ測定した。尚比較の為にアゾジ
カルボンアミド単独、過炭酸ナトリウム単独の場
合についても同様に測定した。 他の過酸化水素付加無機化合物についても同様
に測定したところ、ほぼ同等のガス量増大効果が
認められた。 分解機構の解明は甚だ困難であるが、本発明の
発泡剤組成物の第1成分であるアゾジカルボンア
ミドの分解機構が添加した過炭酸ナトリウム等の
過酸化水素付加無機化合物により何らかの変化を
したものと考えられる。
The present invention relates to a blowing agent composition for water-crosslinkable polymers. More specifically, the present invention relates to a blowing agent composition suitable for obtaining a crosslinked foam of an olefinic polymer having a hydrolyzable silane group as a crosslinkable group. There are many known techniques for producing crosslinked foams of olefin polymers. A mixture of an olefin polymer and a blowing agent,
A method of crosslinking by irradiating with radiation and then heating and foaming. A method in which a peroxide crosslinking agent and a foaming agent are blended into an olefin polymer and then heated to effect crosslinking and foaming. However, none of these methods is perfect as a technique. That is, the radiation crosslinking method requires special and expensive crosslinking equipment, and furthermore, due to the functionality of industrially usable irradiation equipment, it is practically impossible to use it for thick molded products. . On the other hand, the peroxide crosslinking method requires careful control of processing temperature and conditions.
Such control is often difficult to achieve because it requires a precise balance between the activation temperature of the peroxide crosslinker and blowing agent and the softening temperature of the olefinic polymer. By the way, in addition to the above-mentioned radiation crosslinking method and peroxide crosslinking method, methods using water crosslinkable polymers are known as methods for producing crosslinked foams of olefinic polymers. That is, a silicone-grafted olefin polymer obtained by graft copolymerizing an unsaturated silane compound to an olefin polymer, or a copolymer mainly composed of an olefin hydrocarbon and an olefinic unsaturated silane compound, and a foamed A molded article of a composition consisting of an agent and a silanol condensation catalyst is foamed by heating, and crosslinking is achieved by immersing it in hot water or exposing it to a heated steam atmosphere before, after, or simultaneously with the foaming operation. This method is performed by However, as far as the present inventors know, there are disadvantages that are not suitable for industrial use, such as molded bodies having a non-uniform degree of crosslinking and the fact that it takes time to reach a stable degree of crosslinking. Particularly in the case of thick molded products, the degree of crosslinking changes over time depending on the environment and atmosphere in which the product is used, making it extremely difficult to maintain stable physical properties. With the aim of solving the above-mentioned drawbacks, the inventors of the present invention have conducted extensive research and found that by crosslinking and foaming a water-crosslinkable polymer using the following blowing agent composition in the presence of a silanol condensation catalyst, We discovered that it is possible to obtain a foam that is uniformly crosslinked to the inside.
The present invention has now been completed. The blowing agent composition of the present invention comprises azodicarbonamide and at least one hydrogen peroxide-added inorganic compound selected from the group consisting of carbonate hydrogen peroxide, borate hydrogen peroxide, and phosphate hydrogen peroxide. The amount of hydrogen peroxide-added inorganic compound added is usually 0.1 parts by weight or more per 1 part by weight of azodicarbonamide, preferably 0.1 to 2.0 parts by weight, and more preferably 0.5 parts by weight.
It is desirable to use ~1.0 part by weight. Specific examples of hydrogen peroxide-added inorganic compounds used by adding to azodicarbonamide include sodium percarbonate, potassium percarbonate, sodium perborate, potassium perborate, sodium perphosphate, potassium perphosphate, etc. These compounds can be obtained by a method of reacting hydrogen peroxide with sodium carbonate, potassium carbonate, sodium borate, potassium borate, sodium phosphate, or potassium phosphate, respectively. The water-crosslinkable polymer as used in the present invention refers to an olefin polymer in which a silane having a hydrolyzable organic group is bonded to the main chain or side chain, and includes an olefin polymer and an olefinic unsaturated silane. There are graft copolymers with compounds and random copolymers of olefinic hydrocarbons and olefinically unsaturated silane compounds, and specific examples include the following. 1 Graft copolymer of olefinic polymer and olefinic unsaturated silane compound (1) Olefinic unsaturated silane compound Olefinic unsaturated silane compound represented by the general formula RR′nSiY 3-o (where R is Olefinic hydrocarbon or hydrocarbonoxy group, R' is an aliphatic saturated hydrocarbon group, Y is a hydrolyzable organic group, n is 0.1 or 2. When there is more than one Y, they are not the same. ) Specific examples of this unsaturated silane compound include R such as vinyl,
Allyl, isopropenyl, butenyl, cyclohexenyl, Y is methoxy, ethoxy, formyloxy, acetoxy, propionoxy,
Alkyl, R′ is methyl, ethyl, propyl,
They are decyl and phenyl. The most preferred among these are vinyltrimethoxysilane, vinyltriethoxysilane, and vinyltriacetoxysilane. (2) Olefin-based polymers The olefin-based polymers that should become the backbone for graft copolymerization with the above unsaturated silane include polyethylene, ethylene-vinyl acetate copolymer, ethylene-acrylic acid copolymer, polypropylene, chlorinated polyethylene, etc. It is wide-ranging. An olefinic unsaturated silane compound is graft copolymerized onto an olefinic polymer in the presence of a radical generator to obtain an olefinic polymer grafted with an unsaturated silane compound. 2 Random copolymer of olefin hydrocarbon and olefinic unsaturated silane compound The copolymerization of olefin hydrocarbon and the above-mentioned olefinic unsaturated silane compound is carried out using a polymerization initiator, and under any conditions under which polymerization of both occurs. You can do it with As a crosslinking method, unlike the known method of exposing to a water atmosphere, the present invention uses an azozoan as This method is characterized by the generation of water necessary for silane crosslinking at the same time as the decomposition of the dicarbonamide, and foaming and crosslinking are performed simultaneously. That is, since crosslinking is carried out by water generated from the blowing agent composition and the crosslinking is completed in a short time, there is no need to expose it to a water atmosphere before, during or after the foaming operation, and the production time can be shortened. Gas generation due to thermal decomposition of azodicarbonamide and water generation occur simultaneously, so the temporal and viscoelastic balance between foaming and crosslinking is very good. Therefore, the cells in the molded product are uniform, fine, and extremely elastic. It becomes a sponge. The blowing agent composition of the present invention is not only excellent in the above points as a blowing agent composition for water-crosslinkable polymers, but also generates a very large amount of gas effective for expansion, and is free from decomposition residues of azodicarbonamide. It also has the advantage of having less Table 1 shows the amount of gas generated after 20 minutes at 200°C from a blowing agent obtained by blending azodicarbonamide with sodium percarbonate. The amount of gas generated is determined by adding a blowing agent to a test tube connected to a gas burette and placing it in liquid paraffin.
It was dispersed in 10 ml and measured. For comparison, the same measurements were conducted for azodicarbonamide alone and sodium percarbonate alone. When other hydrogen peroxide-added inorganic compounds were similarly measured, almost the same gas amount increasing effect was observed. Although it is extremely difficult to elucidate the decomposition mechanism, the decomposition mechanism of azodicarbonamide, which is the first component of the blowing agent composition of the present invention, is somehow changed by the added hydrogen peroxide-added inorganic compound such as sodium percarbonate. it is conceivable that.

【表】 本発明の発泡剤組成物は、配合されたアゾジカ
ルボンアミドの単位当たりのガス発生量が増大す
る為、アゾジカルボンアミドを非常に有効に利用
することができ使用量を減少することができる。
すなわち、アゾジカルボンアミドが分解する際、
ガス化する部分が多いので分解残渣は少なくな
り、発泡体の製造工程においては分解残渣による
成形品及び成形機器への障害もほとんどなくな
る。 本発明において、対象樹脂は水架橋性重合体で
あるが、他のゴム、樹脂を混合し使用しても良
い。たとえば、ポリエチレン、ポリプロピレン、
ポリブテン等のオレフイン系樹脂、エチレン―酢
酸ビニル、エチレン―ビニルアルコール、エチレ
ン―プロピレン、プロピレン―ブタジエン等のビ
ニル共重合体、ポリブタジエンやABS,SBR等
のブタジエンの単独または共重合体、塩素化ポリ
エチレン等がある。又、場合によつては、過酸化
物架橋剤を添加し、水架橋と過酸化物架橋との併
用をすることもできる。混合する樹脂の種類、
量、水架橋と過酸化物架橋の比、程度により、
種々の物性の発泡体を得ることができる。 又、本発明の発泡剤組成物は、さらに他の発泡
剤を混合して混合型発泡剤として用いても良い。
たとえば、ジニトロペンタメチレンテトラミン、
アゾジカルボンアミドの重金属塩、4,4′―オキ
シビス(ベンゼンスルホニルヒドラジド)、p―
トルエンスルホニルヒドラジド等の有機発泡剤、
重炭酸ナトリウム、炭酸アンモニウム等の無機発
泡剤、揮発性発泡剤等がある。又、尿素、尿素化
合物、亜鉛華、ステアリン酸亜鉛等の公知の発泡
助剤を併用しても良い。 本発明の発泡剤組成物は、水架橋性重合体100
重量部に対して通常0.3〜80重量部用いるが、目
的とする発泡倍率、成形方法、併用する過酸化水
素付加無機化合物の種類、量、混合型発泡剤の場
合には混合する発泡剤とそのガス発生量等種々の
要素を勘案して適宜変化させれば良い。 本発明においては、炭酸カルシウム、炭酸マグ
ネシウム、硫酸カルシウム、硫酸アルミニウム、
シリカ、タルク、クレー、ガラス繊維等の無機充
てん剤や木粉、粉末繊維素、木材パルプ等の有機
充てん剤、架橋促進剤、酸化防止剤、紫外線吸収
剤、可塑剤、滑剤、難燃剤、顔料、カツプリング
剤、核剤等の添加を妨げるものではなく必要に応
じて使用して良い。 発泡成形体の架橋の有無あるいは架橋の程度は
ゲル分率を測定することにより求めた。 (ゲル分率の測定方法) 重量Wgの成形体をキシレン還流下で10時間加
熱した後、100℃の熱風循環式オーブンにて乾燥
しW′gの不溶成分を得た。 ゲル分率(%)=W′/W×100 以下に本発明の実施例を挙げて詳しく説明す
る。 実施例 1 水架橋性重合体(三菱油化社製:リンクロン
LF―710A)100重量部に、ジブチル錫ジラウレ
ート1重量%を含有する低密度ポリエチレンマス
ターバツチ1重量部およびアゾジカルボンアミド
3.5重量部、過炭酸ナトリウム2.0重量部、亜鉛華
1.5重量部を加え、ロールミル上で温度120〜125
℃で5分間混合した。混合物のゲル分率は0重量
%であつた。 次に、混合物を深さ10mm、120mm平方の金型に
入れ、120Kg/cm2の圧力下、160℃で10分間加熱し
たのち、除圧し発泡させた。発泡成形体は比重
0.065g/cm3で気泡は均一微細で弾力性に富んだ
白色の美麗なものであつた。ゲル分率は75重量%
であつた。 比較例 実施例1において、過炭酸ナトリウムを除いた
以外は実施例1と同様にして加熱発泡させたが、
発泡体の表面からガス抜けが起こり収縮した。成
形体の比重は0.28g/cm2、ゲル分率は8重量%で
あつた。 実施例 2 実施例1において、過炭酸ナトリウムを過硼酸
ナトリウムに変えた以外は実施例1と同様にして
発泡成形体を得た。発泡成形体は比重0.068g/
cm3で気泡は均一微細で弾力性に富んだ白色の美麗
なものであつた。ゲル分率は75重量%であつた。 実施例 3 実施例1において、過炭酸ナトリウムを過リン
酸カリウムに変えた以外は実施例1と同様にして
発泡成形体を得た。発泡成形体は比重0.068g/
cm3で気泡は均一微細で弾力性に富んだ白色の美麗
なものであつた。ゲル分率は75重量%であつた。 実施例 4 水架橋性重合体(三菱油化社製:リンクロン
LF―710A)100重量部に、ジブチル錫ジラウレ
ート1重量%を含有する低密度ポリエチレンマス
ターバツチ1重量部およびアゾジカルボンアミド
3.5重量部、過炭酸ナトリウム3.5重量部、亜鉛華
2.0重量部、軽質炭酸カルシウム30重量部を加え、
ロールミル上で温度120〜125℃で10分間混合し
た。混合物のゲル分率な0重量%であつた。 次に、混合物を深さ10mm、120mm平方の金型に
入れ、120Kg/cm2の圧力下、160℃で10分間加熱し
たのち、除圧し発泡させた。発泡成形体は比重
0.071g/cm3で気泡は均一微細で弾力性に富んだ
白色の美麗なものであつた。ゲル分率は58重量%
であつた。 実施例 5 水架橋性重合体(三菱油化社製:リンクロン
LF―710A)80重量部に、低密密度ポリエチレン
20重量部、ジブチル錫ジラウレート1重量%を含
有する低密度ポリエチレンマスターバツチ0.8重
量部およびジクミルパーオキサイド0.2重量部、
アゾジカルボンアミド3.5重量部、過炭酸ナトリ
ウム2.0重量部、尿素系助剤1.5重量部を加え、ロ
ールミル上で温度120〜125℃で5分間混合した。
混合物のゲル分率は0重量%であつた。 次に、混合物をミルからシートとして取り出
し、180℃のソルトバスにて8分間加熱発泡させ
た。発泡成形体は比重0.068g/cm3で気泡は均一
微細で弾力性に富んだ白色の美麗なものであつ
た。ゲル分率は80重量%であつた。 実施例 6 水架橋性重合体(三菱油化社製:リンクロン
LF―710A)100重量部に、ジブチル錫ジラウレ
ートを含有する低密度ポリエチレンマスターバツ
チ1.2重量部およびアゾジカルボンアミド3.5重量
部、過炭酸ナトリウム1.0重量部、過硼酸ナトリ
ウム1.0重量部を加え、ロールミル上で5分間混
合した。混合物のゲル分率は0重量%であつた。 次に、混合物をミルからシートとして取り出
し、ギヤオーブン中で温度220℃で5分間加熱す
ることにより、発泡させた。得られた発泡成形体
は比重0.065g/cm3で気泡は均一微細で弾力性に
富んだ白色の美麗なものであつた。ゲル分率は65
重量%であつた。
[Table] The blowing agent composition of the present invention increases the amount of gas generated per unit of azodicarbonamide blended, so azodicarbonamide can be used very effectively and the amount used can be reduced. can.
That is, when azodicarbonamide decomposes,
Since there are many parts to be gasified, there will be less decomposition residue, and in the foam manufacturing process, there will be almost no damage to molded products and molding equipment due to decomposition residue. In the present invention, the target resin is a water-crosslinkable polymer, but other rubbers and resins may be mixed and used. For example, polyethylene, polypropylene,
Olefin resins such as polybutene, vinyl copolymers such as ethylene-vinyl acetate, ethylene-vinyl alcohol, ethylene-propylene, propylene-butadiene, polybutadiene and butadiene mono or copolymers such as ABS, SBR, chlorinated polyethylene, etc. There is. In some cases, a peroxide crosslinking agent may be added to allow water crosslinking and peroxide crosslinking to be used together. Type of resin to be mixed,
Depending on the amount, ratio and degree of water crosslinking and peroxide crosslinking,
Foams with various physical properties can be obtained. Further, the blowing agent composition of the present invention may be further mixed with other blowing agents and used as a mixed blowing agent.
For example, dinitropentamethylenetetramine,
Heavy metal salt of azodicarbonamide, 4,4'-oxybis(benzenesulfonylhydrazide), p-
Organic blowing agents such as toluenesulfonyl hydrazide,
Examples include inorganic blowing agents such as sodium bicarbonate and ammonium carbonate, and volatile blowing agents. Further, known foaming aids such as urea, urea compounds, zinc white, and zinc stearate may be used in combination. The blowing agent composition of the present invention contains 100% water-crosslinkable polymer.
Usually 0.3 to 80 parts by weight is used, but the desired expansion ratio, molding method, type and amount of hydrogen peroxide-added inorganic compound to be used together, and in the case of a mixed blowing agent, the blowing agent to be mixed and its It may be changed as appropriate in consideration of various factors such as the amount of gas generated. In the present invention, calcium carbonate, magnesium carbonate, calcium sulfate, aluminum sulfate,
Inorganic fillers such as silica, talc, clay, and glass fiber, organic fillers such as wood flour, powdered cellulose, and wood pulp, crosslinking accelerators, antioxidants, ultraviolet absorbers, plasticizers, lubricants, flame retardants, and pigments. , coupling agents, nucleating agents, etc., may be used as necessary. The presence or absence of crosslinking or the degree of crosslinking in the foamed molded article was determined by measuring the gel fraction. (Method for Measuring Gel Fraction) A molded article weighing Wg was heated under xylene reflux for 10 hours and then dried in a hot air circulation oven at 100°C to obtain an insoluble component of W'g. Gel fraction (%)=W'/W×100 The present invention will be described in detail below with reference to Examples. Example 1 Water-crosslinkable polymer (manufactured by Mitsubishi Yuka Co., Ltd.: Linklon
LF-710A) 100 parts by weight, 1 part by weight of low-density polyethylene masterbatch containing 1% by weight of dibutyltin dilaurate, and azodicarbonamide
3.5 parts by weight, 2.0 parts by weight of sodium percarbonate, zinc white
Add 1.5 parts by weight and heat on roll mill to temperature 120-125
Mixed for 5 minutes at °C. The gel fraction of the mixture was 0% by weight. Next, the mixture was placed in a 10 mm deep and 120 mm square mold, heated at 160° C. for 10 minutes under a pressure of 120 Kg/cm 2 , and then the pressure was removed to cause foaming. Specific gravity of foam molded products
At 0.065 g/cm 3 , the bubbles were uniform, fine, highly elastic, and beautiful white. Gel fraction is 75% by weight
It was hot. Comparative Example In Example 1, heating and foaming was carried out in the same manner as in Example 1 except that sodium percarbonate was omitted.
Gas leakage occurred from the surface of the foam, causing it to shrink. The molded article had a specific gravity of 0.28 g/cm 2 and a gel fraction of 8% by weight. Example 2 A foamed molded article was obtained in the same manner as in Example 1 except that sodium percarbonate was replaced with sodium perborate. The specific gravity of the foam molded product is 0.068g/
The bubbles were uniform , fine, elastic, and beautiful white in size. The gel fraction was 75% by weight. Example 3 A foamed molded article was obtained in the same manner as in Example 1 except that sodium percarbonate was replaced with potassium perphosphate. The specific gravity of the foam molded product is 0.068g/
The bubbles were uniform , fine, elastic, and beautiful white in size. The gel fraction was 75% by weight. Example 4 Water-crosslinkable polymer (manufactured by Mitsubishi Yuka Co., Ltd.: Linklon
LF-710A) 100 parts by weight, 1 part by weight of low-density polyethylene masterbatch containing 1% by weight of dibutyltin dilaurate, and azodicarbonamide
3.5 parts by weight, 3.5 parts by weight of sodium percarbonate, zinc white
Add 2.0 parts by weight and 30 parts by weight of light calcium carbonate,
Mixed for 10 minutes on a roll mill at a temperature of 120-125°C. The gel fraction of the mixture was 0% by weight. Next, the mixture was placed in a 10 mm deep and 120 mm square mold, heated at 160° C. for 10 minutes under a pressure of 120 Kg/cm 2 , and then the pressure was removed to cause foaming. Specific gravity of foam molded products
The bubbles were 0.071 g/cm 3 and were uniform, fine, highly elastic, and beautiful white. Gel fraction is 58% by weight
It was hot. Example 5 Water-crosslinkable polymer (manufactured by Mitsubishi Yuka Co., Ltd.: Linklon
LF-710A) 80 parts by weight, low density polyethylene
20 parts by weight, 0.8 parts by weight of a low-density polyethylene masterbatch containing 1% by weight of dibutyltin dilaurate and 0.2 parts by weight of dicumyl peroxide,
3.5 parts by weight of azodicarbonamide, 2.0 parts by weight of sodium percarbonate, and 1.5 parts by weight of a urea-based auxiliary agent were added and mixed on a roll mill at a temperature of 120 to 125°C for 5 minutes.
The gel fraction of the mixture was 0% by weight. Next, the mixture was taken out as a sheet from the mill and heated and foamed in a 180°C salt bath for 8 minutes. The foamed molded product had a specific gravity of 0.068 g/cm 3 , the bubbles were uniform, fine, and had a beautiful white color with high elasticity. The gel fraction was 80% by weight. Example 6 Water-crosslinkable polymer (manufactured by Mitsubishi Yuka Co., Ltd.: Linklon
To 100 parts by weight of LF-710A), 1.2 parts by weight of a low-density polyethylene masterbatch containing dibutyltin dilaurate, 3.5 parts by weight of azodicarbonamide, 1.0 parts by weight of sodium percarbonate, and 1.0 parts by weight of sodium perborate were added, and the mixture was heated on a roll mill. and mixed for 5 minutes. The gel fraction of the mixture was 0% by weight. The mixture was then removed from the mill as a sheet and foamed by heating in a gear oven at a temperature of 220° C. for 5 minutes. The resulting foamed molded product had a specific gravity of 0.065 g/cm 3 , the cells were uniform and fine, and the foam was a beautiful white product with high elasticity. Gel fraction is 65
It was in weight%.

Claims (1)

【特許請求の範囲】 1 アゾジカルボンアミドに、炭酸塩過酸化水素
化物、硼酸塩過酸化水素化物およびリン酸塩過酸
化水素化物よりなる群から選ばれた少なくとも一
種の過酸化水素付加無機化合物を添加してなる水
架橋性重合体用発泡剤組成物。 2 過酸化水素付加無機化合物が、過炭酸ナトリ
ウムである特許請求の範囲第1項記載の発泡剤組
成物。 3 過酸化水素付加無機化合物が、過硼酸ナトリ
ウムである特許請求の範囲第1項記載の発泡剤組
成物。
[Scope of Claims] 1. At least one hydrogen peroxide-added inorganic compound selected from the group consisting of carbonate hydrogen peroxide, borate hydrogen peroxide, and phosphate hydrogen peroxide is added to azodicarbonamide. A foaming agent composition for a water-crosslinkable polymer. 2. The blowing agent composition according to claim 1, wherein the hydrogen peroxide-added inorganic compound is sodium percarbonate. 3. The blowing agent composition according to claim 1, wherein the hydrogen peroxide-added inorganic compound is sodium perborate.
JP8063181A 1981-05-26 1981-05-26 Foaming agent composition for water-crosslinkable polymer Granted JPS57195129A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8063181A JPS57195129A (en) 1981-05-26 1981-05-26 Foaming agent composition for water-crosslinkable polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8063181A JPS57195129A (en) 1981-05-26 1981-05-26 Foaming agent composition for water-crosslinkable polymer

Publications (2)

Publication Number Publication Date
JPS57195129A JPS57195129A (en) 1982-11-30
JPH0153295B2 true JPH0153295B2 (en) 1989-11-13

Family

ID=13723701

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Country Status (1)

Country Link
JP (1) JPS57195129A (en)

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Also Published As

Publication number Publication date
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