JPH032894B2 - - Google Patents

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Publication number
JPH032894B2
JPH032894B2 JP8367882A JP8367882A JPH032894B2 JP H032894 B2 JPH032894 B2 JP H032894B2 JP 8367882 A JP8367882 A JP 8367882A JP 8367882 A JP8367882 A JP 8367882A JP H032894 B2 JPH032894 B2 JP H032894B2
Authority
JP
Japan
Prior art keywords
weight
blowing agent
zinc
foam
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
JP8367882A
Other languages
Japanese (ja)
Other versions
JPS58201825A (en
Inventor
Osamu Takagi
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 JP8367882A priority Critical patent/JPS58201825A/en
Publication of JPS58201825A publication Critical patent/JPS58201825A/en
Publication of JPH032894B2 publication Critical patent/JPH032894B2/ja
Granted legal-status Critical Current

Links

Description

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

本発明は発泡剤組成物に関する。 アゾジカルボンアミドは発泡剤として合成樹脂
発泡体を製造する際に広く使用されているが一般
に使用されているアゾジカルボンアミドの分解温
度は約200℃と高いから発泡させる際の雰囲気は
200〜220℃と高温になつており、分解温度を低下
させるために金属酸化物、脂肪酸の金属塩、アミ
ン類等を添加することが行なわれている。 しかしながら上記の方法ではアゾジカルボンア
ミドは低温において均一にかつ多量の気体を発生
しながら分解されることはできず、熱安定性の悪
い樹脂の発泡体を得ることはできなかつた。 又、軟質塩化ビニル樹脂発泡体は機械強度、外
観、感触等が良いので、ビニルレザー等各種用途
において使用されているが、柔軟性を付与するた
めに可塑剤が添加されており、可塑剤の表面への
移行によつて使用中に表面が粘着しやすくなつた
り、周囲の器物を汚染したり、発泡体自身から可
塑剤がなくなつて物性が低下する等の欠点を有し
ている。この欠点を改良するために、可塑剤を含
まない軟質塩化ビニル系樹脂として、エチレン−
酢酸ビニル共重合体に塩化ビニルをグラフト重合
したグラフト重合体を使用することが提案されて
いる。 しかしながら上記グラフト重合体は高温におけ
る耐熱性が悪く、アゾジカルボンアミド等の発泡
剤を使用して発泡体を製造する際には発泡剤の分
解温度以上である200〜220℃に加熱するため脱塩
素分解により発泡体が着色し、又グラフト重合体
の粘度が低下するため均一な気泡の発泡体が得ら
れないという欠点があつた。本発明の目的は上記
欠点に鑑み、アゾジカルボンアミドを主体とし、
低温で均一にかつ多量の気体を発生して分解する
発泡剤組成物を得ることにあり、本発明の要旨
は、アゾジカルボンアミド100重量部と脂肪酸亜
鉛1〜100重量部と水酸化亜鉛1〜100重量部から
なる発泡剤組成物に存する。 本発明における発泡剤組成物は、アゾジカルボ
ンアミド100重量部に対し脂肪酸亜鉛及び水酸化
亜鉛がそれぞれ1〜100重量部添加されて形成さ
れるが、脂肪酸亜鉛及び水酸化亜鉛の添加量が少
なくなるとアゾジカルボンアミドの分解温度を低
下せしめる効果が少なくなり、逆に多すぎると得
られた発泡体に悪影響を及ぼすので、それぞれ3
〜20重量部添加されるのが好ましい。 上記脂肪酸亜鉛としては任意の脂肪酸の亜鉛塩
が用いられ、たとえばラウリン酸亜鉛、パルミチ
ン酸亜鉛、ステアリン酸亜鉛、リシノール酸亜
鉛、オレイン酸亜鉛、ウンデシレン酸亜鉛等があ
げられる。 本発明において使用するグラフト重合体は、酢
酸ビニル含量が10〜55重量%のエチレン−酢酸ビ
ニル共重合体に、塩化ビニルが生成重合体中20〜
90重量%になるようにグラフト重合されたもので
あり、エチレン−酢酸ビニル共重合体中の酢酸ビ
ニルの含量は10重量%より少なくなるとグラフト
重合体の柔軟性が低下し軟質発泡体が得られず、
55重量%より多くなると発泡体の機械的物性が低
下するので10〜55重量%に限定されるのであり、
エチレン−酢酸ビニル共重合体のメルトインデツ
クスは小さくなるとグラフト重合体の溶融粘度が
大になり、発泡剤組成物との混練性、加工性等が
低下し、逆に大きくなると得られた発泡体の機械
的物性が低下するので、1〜30g/10分であるの
が好ましく、分塩化ビニルのグラフト量が20重量
%より少ないと塩化ビニルの特性が発現できず、
90重量%より多くなると架橋しにくくなるので塩
化ビニルはグラフト重合体中20〜90重量%になる
ようにグラフト重合されるのであり好ましくは40
〜89重量%である。本発明においては上記グラフ
ト重合体の発泡体を製造する際に前記発泡剤組成
物を使用するのであるが、発泡剤組成物の添加量
は製造する発泡体の密度により適宜決定されれば
よいが、一般にグラフト重合体100重量部に対し、
0.5〜30重量部添加されるのが好ましい。 本発明においては上記グラフト重合体と発泡剤
組成物を混合し得られた混合物から発泡体を製造
するのであるが、製造方法は任意の方法が採用さ
れてよく、たとえば上記混合物を発泡剤組成物の
分解温度以下の温度で溶融混練し、成形体を成形
し、成形体に電離性放射線を照射して架橋せし
め、しかる後発泡剤組成物の分解温度以上の温度
に加熱して発泡せしめる方法、上記混合物に有機
過酸化物を添加し、発泡剤組成物の分解温度以下
の温度で溶融混練して成形体を成形した後発泡剤
組成物の分解温度以上の温度に加熱して架橋及び
発泡せしめる方法等があげられる。 上記溶融混練して成形体を得るには任意の方法
が採用され、たとえば押出機、カレンダーロー
ル、射出成型機等が用いられ、溶融混練温度は発
泡剤組成物の分解温度は140〜160℃になつている
から、グラフト重合体の軟化温度以上であつて、
140℃以下の温度であるのが好ましい。又成形体
の形状は、たとえばシート状、ロツド状、ペレツ
ト状、チユーブ状等の形状があげられる。又発泡
せしめる温度は発泡剤組成物の分解温度以上であ
ればよいが、温度が高すぎるとグラフト重合体が
分解して得られた発泡体が着色するので160〜200
℃であるのが好ましい。 上記電離性放射線で架橋せしめる際には、架橋
密度が小さいと発泡せしめるときにガス抜けが生
じ高倍率の発泡体が得られず、逆に大きいと大き
な気泡が生じたり発泡中に成形体が裂けたりする
ので、ゲル分率が20〜70%になるように架橋せし
めるのが好ましい。 又、前記有機過酸化物は、発泡剤組成物の分解
温度が140〜160℃と低くなつているので、半減期
が1分のときの分解温度が150〜190℃のものが好
適に使用され、たとえばジクミルパーオキシド、
n−ブチル−4.4−ビス(t−ブチルパーオキシ)
吉草酸、ビス(t−ブチルパーオキシ)ジイソプ
ロピルベンゼン等があげられ、又その添加量はグ
ラフト重合体100重量部に対し0.1〜5.0重量部で
あるのが好ましい。 又上記混合物に、さらに一般に塩化ビニル樹脂
に使用されている安定剤、可塑剤、滑剤、充填
材、顔料等が添加されてもよい。 本発明の構成は上述の通りであり、発泡剤組成
物はアゾジカルボンアミド100重量部に脂肪酸亜
鉛及び水酸化亜鉛がそれぞれ1〜100重量部添加
されているので、分解温度は140〜160℃と低くな
り、分解は急激でありかつ多量の気体が発生する
ようになつており、塩化ビニル系樹脂の如き熱安
定性の悪い樹脂やエチレン−酢酸ビニル共重合
体、ゴム等から気泡が均一で低密度の発泡体を得
ることができる。又グラフト重合体は酢酸ビニル
含量が10〜55重量%のエチレン−酢酸ビニル共重
合体に塩化ビニルが生成重合体中20〜90重量%に
なるようにグラフト重合されたものであり、上記
発泡剤組成物を発泡剤として使用するのであるか
ら、グラフト重合体を熱分解することなく、160
〜200℃という比較的低温で発泡せしめることが
でき、着色がなく、均一な気泡を有する発泡体を
製造することができる。又得られた発泡体は軟質
であり、弾力性、柔軟性、感触、外観等がすぐれ
ており、自己消化性、耐薬品性等の塩化ビニル樹
脂の特性を有しているので、衣料用、家具用、内
装用、その他各種成形用のレザー、シート等広範
な用途に好適に利用することができる。 次に本発明を実施例を参照して説明する。 実施例1及び比較例1 アゾジカルボンアミド100重量部と第1表に示
した所定量のラウリン酸亜鉛、ステアリン酸亜
鉛、リシノール酸亜鉛、水酸化亜鉛、酸化亜鉛、
尿素又はクエン酸を乳鉢で混合して発泡剤組成物
を得た。得られた組成物を示差熱分析計に供給
し、5℃/分の速度で昇温して分解開始温度を測
定し結果を第1表に示した。 又得られた組成物1gを試験管に入れ、200℃
のシリコン浴槽につけて加熱し、加熱時間とガス
発生量との関係を測定し、第1図に示した。尚第
1図におけるガス発生量はアゾジカルボンアミド
1g当り換算されている。
The present invention relates to blowing agent compositions. Azodicarbonamide is widely used as a blowing agent in the production of synthetic resin foams, but the decomposition temperature of commonly used azodicarbonamide is as high as approximately 200°C, so the atmosphere during foaming must be
The temperature is as high as 200 to 220°C, and metal oxides, metal salts of fatty acids, amines, etc. are added to lower the decomposition temperature. However, in the above method, azodicarbonamide could not be decomposed uniformly at low temperature while generating a large amount of gas, and a resin foam with poor thermal stability could not be obtained. In addition, soft vinyl chloride resin foam has good mechanical strength, appearance, and feel, so it is used in various applications such as vinyl leather, but plasticizers are added to give it flexibility. This migration to the surface causes the surface to become sticky during use, contaminates surrounding utensils, and the foam itself loses its plasticizer, resulting in a decrease in physical properties. In order to improve this drawback, ethylene-
It has been proposed to use a graft polymer obtained by graft polymerizing vinyl chloride onto a vinyl acetate copolymer. However, the above-mentioned graft polymer has poor heat resistance at high temperatures, and when producing foam using a blowing agent such as azodicarbonamide, it is dechlorinated because it is heated to 200-220°C, which is above the decomposition temperature of the blowing agent. The disadvantage was that the foam was colored by decomposition and the viscosity of the graft polymer was reduced, making it impossible to obtain a foam with uniform cells. In view of the above-mentioned drawbacks, the object of the present invention is to mainly contain azodicarbonamide,
The purpose of the present invention is to obtain a blowing agent composition that uniformly generates and decomposes a large amount of gas at low temperatures. The blowing agent composition consists of 100 parts by weight. The blowing agent composition in the present invention is formed by adding 1 to 100 parts by weight of zinc fatty acid and zinc hydroxide to 100 parts by weight of azodicarbonamide, but when the amount of zinc fatty acid and zinc hydroxide added is small, The effect of lowering the decomposition temperature of azodicarbonamide will be reduced, and conversely, too much will have a negative effect on the foam obtained, so
It is preferable to add up to 20 parts by weight. As the fatty acid zinc, a zinc salt of any fatty acid can be used, and examples thereof include zinc laurate, zinc palmitate, zinc stearate, zinc ricinoleate, zinc oleate, zinc undecylenate, and the like. The graft polymer used in the present invention is an ethylene-vinyl acetate copolymer with a vinyl acetate content of 10 to 55% by weight, and 20 to 55% of vinyl chloride in the polymer.
It is graft polymerized to 90% by weight, and if the content of vinyl acetate in the ethylene-vinyl acetate copolymer is less than 10% by weight, the flexibility of the graft polymer will decrease and a soft foam will not be obtained. figure,
If it exceeds 55% by weight, the mechanical properties of the foam will deteriorate, so it is limited to 10 to 55% by weight.
As the melt index of the ethylene-vinyl acetate copolymer decreases, the melt viscosity of the graft polymer increases, resulting in poor kneading and processability with the blowing agent composition; It is preferable that the amount of grafted vinyl chloride is less than 20% by weight, since the mechanical properties of the vinyl chloride will deteriorate, so it is preferable that the amount is 1 to 30 g/10 minutes.
If the amount exceeds 90% by weight, it becomes difficult to crosslink, so vinyl chloride is graft-polymerized so that it accounts for 20 to 90% by weight in the graft polymer, and preferably 40% by weight.
~89% by weight. In the present invention, the blowing agent composition is used when producing the foam of the graft polymer, and the amount of the blowing agent composition to be added may be appropriately determined depending on the density of the foam to be produced. , generally for 100 parts by weight of the graft polymer,
It is preferable to add 0.5 to 30 parts by weight. In the present invention, a foam is produced from the mixture obtained by mixing the above-mentioned graft polymer and a blowing agent composition, but any method may be adopted as the production method. A method of melt-kneading at a temperature below the decomposition temperature of the blowing agent composition, forming a molded body, irradiating the molded body with ionizing radiation to crosslink it, and then heating it to a temperature above the decomposition temperature of the blowing agent composition to foam it; An organic peroxide is added to the above mixture, melt-kneaded at a temperature below the decomposition temperature of the blowing agent composition to form a molded article, and then heated to a temperature above the decomposition temperature of the blowing agent composition to cause crosslinking and foaming. Examples include methods. Any method can be used to obtain the molded product by melt-kneading the above, such as an extruder, a calendar roll, an injection molding machine, etc., and the melt-kneading temperature is set to 140 to 160°C, which is the decomposition temperature of the blowing agent composition. Because the temperature is higher than the softening temperature of the graft polymer,
Preferably, the temperature is below 140°C. The shape of the molded product may be, for example, a sheet, rod, pellet, or tube shape. The foaming temperature may be higher than the decomposition temperature of the blowing agent composition; however, if the temperature is too high, the graft polymer will decompose and the resulting foam will be colored;
Preferably it is ℃. When cross-linking with the above-mentioned ionizing radiation, if the cross-linking density is low, gas will escape during foaming and a foam with a high magnification ratio will not be obtained. Therefore, it is preferable to carry out crosslinking so that the gel fraction is 20 to 70%. Furthermore, since the decomposition temperature of the blowing agent composition is as low as 140 to 160°C, the organic peroxide having a decomposition temperature of 150 to 190°C with a half-life of 1 minute is preferably used. , for example dicumyl peroxide,
n-butyl-4,4-bis(t-butylperoxy)
Examples include valeric acid, bis(t-butylperoxy)diisopropylbenzene, and the amount added is preferably 0.1 to 5.0 parts by weight per 100 parts by weight of the graft polymer. Further, stabilizers, plasticizers, lubricants, fillers, pigments, etc. which are generally used in vinyl chloride resins may be added to the above mixture. The structure of the present invention is as described above, and since the blowing agent composition contains 1 to 100 parts by weight of fatty acid zinc and zinc hydroxide each added to 100 parts by weight of azodicarbonamide, the decomposition temperature is 140 to 160°C. The decomposition is rapid and a large amount of gas is generated, and bubbles are uniform and low from resins with poor thermal stability such as vinyl chloride resins, ethylene-vinyl acetate copolymers, rubber, etc. Density foam can be obtained. The graft polymer is obtained by graft polymerizing an ethylene-vinyl acetate copolymer with a vinyl acetate content of 10 to 55% by weight so that vinyl chloride is 20 to 90% by weight in the resulting polymer, and the above-mentioned blowing agent is used. Since the composition is used as a blowing agent, the graft polymer can be heated to 160% without thermal decomposition.
It can be foamed at a relatively low temperature of ~200°C, and can produce a foam that is free from coloration and has uniform cells. In addition, the obtained foam is soft and has excellent elasticity, flexibility, feel, appearance, etc., and has the characteristics of vinyl chloride resin such as self-extinguishing property and chemical resistance, so it can be used for clothing, It can be suitably used for a wide range of applications such as leather for furniture, interior decoration, and various other molding applications, such as leather and seats. Next, the present invention will be explained with reference to examples. Example 1 and Comparative Example 1 100 parts by weight of azodicarbonamide and the specified amounts of zinc laurate, zinc stearate, zinc ricinoleate, zinc hydroxide, zinc oxide,
A blowing agent composition was obtained by mixing urea or citric acid in a mortar. The obtained composition was supplied to a differential thermal analyzer, and the temperature was increased at a rate of 5° C./min to measure the decomposition initiation temperature. The results are shown in Table 1. Also, put 1 g of the obtained composition into a test tube and heat it at 200°C.
The relationship between the heating time and the amount of gas generated was measured and is shown in Figure 1. The amount of gas generated in FIG. 1 is calculated per gram of azodicarbonamide.

【表】 実施例2,3及び比較例2,3 第2表に示した組成の配合物を、混練ロールに
より90℃で混練し、次にプレスにより100℃で加
熱加圧して厚さ2mmの発泡性シートを得た、得ら
れた発泡性シートに電離性放射線を第2表に示し
た所定量照射して架橋シートを得た。架橋シート
のゲル分率を第2表に示した。次に架橋シートを
熱風乾燥機に供給し、第2表に示した条件で加熱
して発泡体を得た。発泡体の密度及び状態を第2
表に示した。 尚ゲル分率は架橋シートを60℃のテトラヒドロ
フランで48時間抽出し、不溶分を重量%で示し
た。
[Table] Examples 2 and 3 and Comparative Examples 2 and 3 The compositions shown in Table 2 were kneaded at 90°C using a kneading roll, and then heated and pressed at 100°C using a press to form a 2 mm thick sheet. A foamable sheet was obtained.The foamable sheet obtained was irradiated with ionizing radiation in a predetermined amount shown in Table 2 to obtain a crosslinked sheet. The gel fraction of the crosslinked sheet is shown in Table 2. Next, the crosslinked sheet was supplied to a hot air dryer and heated under the conditions shown in Table 2 to obtain a foam. The density and condition of the foam are
Shown in the table. The gel fraction was determined by extracting the crosslinked sheet with tetrahydrofuran at 60°C for 48 hours, and the insoluble content was expressed as weight %.

【表】【table】

【表】 実施例4〜7及び比較例4,5 第3表に示したグラフト共重合体100重量部、
アゾジカルボンアミド18重量部、ステアリン酸亜
鉛2重量部及び水酸化亜鉛1重量部よりなる配合
物を、長さ100mm、幅1.5mmのスリツトを有する金
型が設置された、口径50mmの二軸押出機に供給
し、100℃で10Kg/hrの速度で押出して、厚さ1.3
mmの発泡性シートを得た。得られた発泡性シート
に第3表に示した所定量の電離性放射線を照射し
て架橋シートを得、180℃の熱風乾燥機に供給し、
4分間加熱して発泡シートを得た。 架橋シートのゲル分率、発泡シートの密度及び
状態を第3表に示した。
[Table] Examples 4 to 7 and Comparative Examples 4 and 5 100 parts by weight of the graft copolymer shown in Table 3,
A formulation consisting of 18 parts by weight of azodicarbonamide, 2 parts by weight of zinc stearate and 1 part by weight of zinc hydroxide was extruded using a twin-screw extrusion having a diameter of 50 mm and equipped with a mold having a slit of 100 mm in length and 1.5 mm in width. It was fed to a machine and extruded at 100℃ at a rate of 10Kg/hr to a thickness of 1.3
A foamable sheet of mm was obtained. The obtained foamable sheet was irradiated with a predetermined amount of ionizing radiation shown in Table 3 to obtain a crosslinked sheet, which was then fed to a hot air dryer at 180°C.
A foamed sheet was obtained by heating for 4 minutes. Table 3 shows the gel fraction of the crosslinked sheet and the density and condition of the foamed sheet.

【表】【table】

【表】 実施例8〜10及び比較例6〜9 酢酸ビニル含量35重量%、メルトインデツクス
4のエチレン−酢酸ビニル共重合体に、塩化ビニ
ルが生成重合体中55重量%になるようにグラフト
重合されたグラフト重合体と第4表に示した所定
量のジアゾカルボンアミド、ジクミルパーオキサ
イド、ラウリン酸亜鉛、ステアリン酸亜鉛、オレ
イン酸亜鉛、及び水酸化亜鉛よりなる組成の配合
物を90℃の混練ロールにより混練し、次にプレス
により100℃で加熱加圧して厚さ2mmの発泡性シ
ートを得た。得られた発泡性シートを180℃の熱
風乾燥機に供給し、4分間加熱して発泡シートを
得た。発泡シートの密度、気泡状態及び着色状態
を第4表に示した。
[Table] Examples 8 to 10 and Comparative Examples 6 to 9 An ethylene-vinyl acetate copolymer with a vinyl acetate content of 35% by weight and a melt index of 4 was grafted so that vinyl chloride was 55% by weight in the resulting polymer. A composition consisting of the polymerized graft polymer and predetermined amounts of diazocarbonamide, dicumyl peroxide, zinc laurate, zinc stearate, zinc oleate, and zinc hydroxide shown in Table 4 was heated at 90°C. The mixture was kneaded using a kneading roll, and then heated and pressed using a press at 100°C to obtain a foamable sheet with a thickness of 2 mm. The obtained foamable sheet was supplied to a hot air dryer at 180°C and heated for 4 minutes to obtain a foamed sheet. Table 4 shows the density, cell state and coloring state of the foam sheet.

【表】 実施例11〜14及び比較例10〜12 第5表に示したグラフト重合体100重量部、ア
ゾジカルボンアミド18重量部、ステアリン酸亜鉛
2重量部、水酸化亜鉛1重量部及びジクミルパー
オキサイド0.8重量部よりなる配合物を、長さ100
mm、幅1.5mmのスリツトを有する金型が設置され
た口径50mmの二軸押出機に供給し、100℃で10
Kg/hrの速度で押出して、厚さ1.3mmの発泡性シ
ートを得た。得られた発泡性シートを、180℃の
熱風乾燥機に供給し、4分間加熱して発泡シート
を得た。発泡シートの密度及び状態を第5表に示
した。
[Table] Examples 11 to 14 and Comparative Examples 10 to 12 100 parts by weight of the graft polymer shown in Table 5, 18 parts by weight of azodicarbonamide, 2 parts by weight of zinc stearate, 1 part by weight of zinc hydroxide, and dicumyl A formulation consisting of 0.8 parts by weight of peroxide was applied to a length of 100 mm.
It was fed to a twin screw extruder with a diameter of 50 mm equipped with a mold with a slit of 1.5 mm in width and 10 mm in width at 100°C.
A foamed sheet with a thickness of 1.3 mm was obtained by extrusion at a rate of Kg/hr. The obtained foamable sheet was supplied to a hot air dryer at 180°C and heated for 4 minutes to obtain a foamed sheet. Table 5 shows the density and condition of the foam sheet.

【表】【table】 【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明及び比較の発泡剤組成物の加熱
時間とガス発生量の関係を示すグラフである。 図中1〜11は発泡剤組成物の配合番号〜
のガス発生量曲線を示す。
FIG. 1 is a graph showing the relationship between heating time and gas generation amount for blowing agent compositions of the present invention and comparison. In the figure, 1 to 11 are the formulation numbers of the blowing agent composition.
shows the gas generation amount curve.

Claims (1)

【特許請求の範囲】[Claims] 1 アゾジカルボンアミド100重量部と脂肪酸亜
鉛1〜100重量部と水酸化亜鉛1〜100重量部から
なる発泡剤組成物。
1. A blowing agent composition comprising 100 parts by weight of azodicarbonamide, 1 to 100 parts by weight of fatty acid zinc, and 1 to 100 parts by weight of zinc hydroxide.
JP8367882A 1982-05-17 1982-05-17 Foaming agent composition and preparation of foamed article using said foaming agent composition Granted JPS58201825A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8367882A JPS58201825A (en) 1982-05-17 1982-05-17 Foaming agent composition and preparation of foamed article using said foaming agent composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8367882A JPS58201825A (en) 1982-05-17 1982-05-17 Foaming agent composition and preparation of foamed article using said foaming agent composition

Publications (2)

Publication Number Publication Date
JPS58201825A JPS58201825A (en) 1983-11-24
JPH032894B2 true JPH032894B2 (en) 1991-01-17

Family

ID=13809134

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8367882A Granted JPS58201825A (en) 1982-05-17 1982-05-17 Foaming agent composition and preparation of foamed article using said foaming agent composition

Country Status (1)

Country Link
JP (1) JPS58201825A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60197744A (en) * 1984-03-21 1985-10-07 Adeka Argus Chem Co Ltd Preparation of halogen-containing foamed resin material

Also Published As

Publication number Publication date
JPS58201825A (en) 1983-11-24

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