JPH0363987B2 - - Google Patents

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Publication number
JPH0363987B2
JPH0363987B2 JP59094208A JP9420884A JPH0363987B2 JP H0363987 B2 JPH0363987 B2 JP H0363987B2 JP 59094208 A JP59094208 A JP 59094208A JP 9420884 A JP9420884 A JP 9420884A JP H0363987 B2 JPH0363987 B2 JP H0363987B2
Authority
JP
Japan
Prior art keywords
mold
foaming
raw material
rubber
foam
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 - Lifetime
Application number
JP59094208A
Other languages
Japanese (ja)
Other versions
JPS60238333A (en
Inventor
Sadao Kumasaka
Shigeo Horikoshi
Tamaki Kamanaka
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.)
Toyo Quality One Corp
Original Assignee
Toyo Rubber Chemical Industrial 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 Toyo Rubber Chemical Industrial Co Ltd filed Critical Toyo Rubber Chemical Industrial Co Ltd
Priority to JP59094208A priority Critical patent/JPS60238333A/en
Publication of JPS60238333A publication Critical patent/JPS60238333A/en
Publication of JPH0363987B2 publication Critical patent/JPH0363987B2/ja
Granted legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Moulding By Coating Moulds (AREA)

Description

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

本発明はゴム状弾性をもつたエラストマーから
なる発泡体の製造方法に関し、特に、独立気泡構
造であるにもかかわらず連続気泡体並の柔軟性を
具備したゴム発泡体を得るための製造方法に係
る。 天然ゴム或いは種々の合成ゴムを用いたゴム発
泡体が従来から広範な用途に用いられている。こ
れらゴム発泡体の製造方法としては、ゴムラテツ
クスの機械的な撹拌によつて起泡された泡の隔膜
を硬化剤で固定する方法の他、所謂型外発泡が広
く行なわれている。この方法では、ゴム原料中に
アゾジカーボンアミド等の分解性発泡剤および架
橋剤その他の配合剤を練り込んで原料コンパウン
ドとし、これを充填率100%で型内に充填し、プ
レスで強固に閉型して加熱することにより原料コ
ンパウンド中の発泡剤を分解させる。こうして内
圧が高まつた状態で型を開放すると、発泡剤から
生成した分解ガスの発泡作用により原料コンパウ
ンドが急激に膨張してゴム発泡体が得られる。 上記の型外発泡で製造されたゴム発泡体は、機
械的発泡によつて得らたものに比較してセルが微
細で、緻密な組織を有している。また通常の場
合、その気泡構造は殆ど100%が独立気泡となる。
この独立気泡構造に起因して、型外発泡で製造さ
れたゴム発泡体は柔軟性に欠け、パツキン、シー
ル材、印刷用ロール或いは化粧用パフ等の用途に
対する適応性に劣るという問題がある。 そこで、型外発泡を行なうに際し、原料コンパ
ウンド中にオイルを一緒に練り込むことによつ
て、得られる独立気泡構造のゴム発泡体に柔軟性
を付与することが従来から行なわれている。しか
し、従来行なわれているオイル添加法ではゴム原
料100重量部に対し、せいぜい100重量部程度まで
のオイルしか練り込むことができず、連続気泡あ
るいは連続気泡率の高い樹脂発泡体に略等しい柔
軟性を得ることは困難であつた。 発明者等は上記事情に鑑み、柔軟性に優れたゴ
ム発泡体を型外発泡によつて製造するべく鋭意研
究を行なつた結果、ゴムエラストマーとしてポリ
ノルボルネン樹脂を用い、また原料コンパウンド
中に練り込むオイルとしてナフテンオイルを用い
ると、ゴムエラストマー原料100重量部に対して
200〜500重量部という多量のオイル添加が可能と
なり、製品に連続気泡体並の優れた柔軟性を付与
できることを見出し、本願発明に到達したもので
ある。 即ち、本発明は、ポリノルボルネン樹脂100重
量部に対してナフテンオイル200〜500重量部、適
量の発泡剤および架橋剤その他の配合剤を添加し
て混練することにより原料コンパウンドを調整
し、該原料コンパウンドを充填率100%で型内に
充填した後、プレスで強固に閉型して加熱するこ
とにより発泡剤を分解させ、続いて型を開放する
ことにより前記原料コンパウンドを発泡膨張させ
て発泡体とすることを特徴とするゴム発泡体の製
造方法である。 本発明においてゴム原料に用いるポリノルボル
ネン樹脂は、シクロペンタジエンから得られるビ
スジエンオリゴマーをデイールス・アルダー反応
で重合させて得られるポリマーである。該ポリノ
ルボルネン樹脂はフランス国のC.D.F.CHIMIE社
で開発されたもので、我国では「ノーソレツク
ス」の商品名で日本ゼオン株式会社が輸入販売を
行なつている。 本発明に用いるナフテンオイルは環式飽和炭化
水素からなり、炭素数3〜8までのものが知られ
ているが、炭素数5のシクロペンタン及び炭素数
6のシクロヘキサンが最も一般的である。 本発明における発泡剤、架橋剤、その他の配合
剤としては、従来の型外発泡で用いているものと
同じものを使用することができる。即ち、発泡剤
としては、例えばアゾジカーボンアミド、ジニト
ロソペンタメチレンテトラミン、p−トルエンス
ルホニルヒドラジン、アゾビスイソブチロニトリ
ル、ジアゾアミノアゾベンゼン、トルエンスルホ
ニルセミカルバジド等を用いればよい。また架橋
剤としては、例えばジクミルパーオキサイド、
2,5−ジメチル−2,5−(ターシヤリーブチ
ル)パーオキサイド、1,3ビス(ターシヤリー
ブチルパーオキシ−イソプロピル)ベンゼン、m
−オクタデシルアジドホルメート、ターシヤリー
ブチルパーオキシクメン等の有機過酸化物を用い
ることができる。その他の配合剤としては、酸化
チタン(TiO2)および炭酸カルシウム等の充填
剤、亜鉛華等の顔料その他が含まれる。 本発明を実施するに際しては、上記のポリノル
ボルネン樹脂100重量部に対し、ナフテンオイル
200〜500重量部、発泡剤および架橋剤その他の配
合剤をロール、またはバンバリーミキサー等で混
練して原料コンパウンドとし、これを従来と同様
の型外発泡により発泡させればよい。その際の発
泡工程は、一挙に目的の発泡倍率を得る一段階発
泡の他、二回の発泡で目的の発泡倍率とする二段
階発泡の何れを用いてもよい。一段階発泡は高倍
率の発泡体を得るのに適し、これによれば密度
0.05g/cm3程度までの低密度発泡が可能で、より
ソフトな感触の製品が得られる。他方、二段階発
泡では密度0.2g/cm3程度までの発泡倍率しか得
られないが、この場合には反発弾性の良い製品が
得られる。 上述した本発明の製造方法によれば、後述の実
施例に示されるように、型外発泡で製造された従
来のゴム発泡体に比較して著しく柔軟性に優れた
ゴム発泡体を製造することが可能である。 以下に本発明の一実施例を説明する。 実施例 「ノーソレツクス150NA」 100重量部 (日本ゼオン社販売に係るポリノルボルネン樹
脂の商品名) ナフテンオイル 300 〃 炭酸カルシウム 300 〃 TiO2 20 〃 亜鉛華 5 〃 尿 素 2 〃 アゾジカーボンアミド 20 〃 ジクミルパーオキサイド 2 〃 上記の配合処方からなる原料組成物を熱ロール
で混練してシート状のコンパウンドを得た。この
コンパウンドシートを充填率100%でプレス型内
に充填し、下記の条件で二段階発泡を行なつたと
ころ、密度0.2g/cm3のゴム発泡体が得られた。 一次発泡;147℃×15分 二次発泡;165℃×10分 また、コンパウンドシートを下記の条件で一段
階発泡させたところ、密度0.05g/cm3のゴム発泡
体が得られた。 条件;160℃×18分 上記で製造されたものの内、二段階発泡により
得られた密度0.2g/cm3のゴム発泡体(実施例品)
と、EDPMから同様の型外発泡により製造され
たの密度0.2g/cm3のゴム発泡体とについて、
夫々弾性率および硬さを測定したところ、次表に
示す結果が得られた。この結果から、本発明の方
法で製造されたゴム発泡体は従来品に比較して著
しく柔軟性に優れていることが明らかである。
The present invention relates to a method for producing a foam made of an elastomer with rubber-like elasticity, and particularly to a method for producing a rubber foam that has a closed cell structure but has the same flexibility as an open cell foam. Related. Rubber foams made from natural rubber or various synthetic rubbers have been used for a wide variety of purposes. As a method for manufacturing these rubber foams, in addition to a method in which a diaphragm of foam formed by mechanical stirring of rubber latex is fixed with a curing agent, so-called out-of-mold foaming is widely used. In this method, a decomposable blowing agent such as azodicarbonamide, a crosslinking agent, and other compounding agents are kneaded into the rubber raw material to form a raw material compound, which is then filled into a mold with a filling rate of 100% and firmly pressed using a press. The blowing agent in the raw material compound is decomposed by closing the mold and heating it. When the mold is opened with the internal pressure increased in this manner, the raw material compound rapidly expands due to the foaming action of the decomposed gas generated from the foaming agent, yielding a rubber foam. The rubber foam produced by the above-mentioned out-of-mold foaming has finer cells and a denser structure than that obtained by mechanical foaming. In addition, in normal cases, the cell structure is almost 100% closed cells.
Due to this closed cell structure, rubber foams produced by out-of-mold foaming lack flexibility and have poor adaptability to applications such as packing, sealing materials, printing rolls, and cosmetic puffs. Therefore, when performing out-of-mold foaming, it has been conventional practice to knead oil into the raw material compound to impart flexibility to the resulting closed-cell rubber foam. However, with the conventional oil addition method, only about 100 parts by weight of oil can be mixed into 100 parts by weight of the rubber raw material, and the flexibility is almost equivalent to that of open-cell or resin foam with a high open-cell ratio. It was difficult to obtain sex. In view of the above circumstances, the inventors conducted intensive research to produce a rubber foam with excellent flexibility by out-of-mold foaming, and as a result, they used polynorbornene resin as the rubber elastomer and kneaded it into the raw material compound. When naphthenic oil is used as the oil to be mixed, the amount of
The inventors have discovered that it is possible to add as much as 200 to 500 parts by weight of oil, and that it is possible to impart excellent flexibility to a product comparable to that of open-cell foam, and have thus arrived at the present invention. That is, the present invention prepares a raw material compound by adding and kneading 200 to 500 parts by weight of naphthenic oil, an appropriate amount of a blowing agent, a crosslinking agent, and other compounding agents to 100 parts by weight of a polynorbornene resin. After filling the compound into the mold at a filling rate of 100%, the mold is tightly closed with a press and heated to decompose the foaming agent, and then the mold is opened to expand the raw material compound to form a foam. A method for producing a rubber foam, characterized in that: The polynorbornene resin used as a rubber raw material in the present invention is a polymer obtained by polymerizing a bisdiene oligomer obtained from cyclopentadiene by a Diels-Alder reaction. The polynorbornene resin was developed by CDFCHIMIE in France, and is imported and sold in Japan by Zeon Co., Ltd. under the trade name "Nosolex". The naphthenic oil used in the present invention is composed of cyclic saturated hydrocarbons, and those having 3 to 8 carbon atoms are known, but cyclopentane having 5 carbon atoms and cyclohexane having 6 carbon atoms are the most common. As the blowing agent, crosslinking agent, and other compounding agents in the present invention, the same ones used in conventional out-of-mold foaming can be used. That is, as the blowing agent, for example, azodicarbonamide, dinitrosopentamethylenetetramine, p-toluenesulfonylhydrazine, azobisisobutyronitrile, diazoaminoazobenzene, toluenesulfonyl semicarbazide, etc. may be used. In addition, as a crosslinking agent, for example, dicumyl peroxide,
2,5-dimethyl-2,5-(tertiarybutyl)peroxide, 1,3bis(tertiarybutylperoxy-isopropyl)benzene, m
- Organic peroxides such as octadecyl azide formate, tert-butyl peroxycumene, etc. can be used. Other compounding agents include fillers such as titanium oxide (TiO 2 ) and calcium carbonate, pigments such as zinc white, and others. When carrying out the present invention, naphthene oil is added to 100 parts by weight of the above polynorbornene resin.
200 to 500 parts by weight of a blowing agent, a crosslinking agent, and other compounding agents may be kneaded using a roll or a Banbury mixer to form a raw material compound, and this may be foamed by conventional out-of-mold foaming. The foaming step at this time may be either one-stage foaming that achieves the desired expansion ratio in one step, or two-stage foaming that achieves the desired expansion ratio through two foaming steps. Single-stage foaming is suitable for obtaining foams with high expansion ratios, according to which the density
Low-density foaming of up to about 0.05g/ cm3 is possible, resulting in products with a softer feel. On the other hand, in two-stage foaming, a foaming ratio up to a density of about 0.2 g/cm 3 can only be obtained, but in this case a product with good impact resilience can be obtained. According to the above-described manufacturing method of the present invention, as shown in the examples below, a rubber foam can be manufactured that has significantly superior flexibility compared to conventional rubber foam manufactured by out-of-mold foaming. is possible. An embodiment of the present invention will be described below. Example "Nosolex 150NA" 100 parts by weight (trade name of polynorbornene resin sold by Zeon Corporation) Naphthene oil 300 〃 Calcium carbonate 300 〃 TiO 2 20 〃 Zinc white 5 〃 Urea 2 〃 Azodicarbonamide 20 〃 Zinc Milperoxide 2 A raw material composition having the above-mentioned formulation was kneaded with a heated roll to obtain a sheet-like compound. This compound sheet was filled into a press mold at a filling rate of 100%, and two-stage foaming was performed under the following conditions to obtain a rubber foam with a density of 0.2 g/cm 3 . Primary foaming: 147°C x 15 minutes Secondary foaming: 165°C x 10 minutes When the compound sheet was foamed in one step under the following conditions, a rubber foam with a density of 0.05 g/cm 3 was obtained. Conditions: 160°C x 18 minutes Among the products manufactured above, a rubber foam with a density of 0.2 g/cm 3 obtained by two-stage foaming (example product)
and a rubber foam with a density of 0.2 g/cm 3 produced from EDPM by similar out-of-mold foaming.
When the elastic modulus and hardness were measured, the results shown in the following table were obtained. From this result, it is clear that the rubber foam produced by the method of the present invention has significantly superior flexibility compared to conventional products.

【表】 以上詳述したように、本発明によるゴム発泡体
の製造方法は、緻密な気泡構造のゴム発泡体が得
られるという型外発泡の特徴をそのまま具備する
と共に、従来の製造方法では得られなかつた優れ
た柔軟性をもつたゴム発泡体を製造できる等、顕
著な効果を奏するものである。
[Table] As detailed above, the method for producing a rubber foam according to the present invention has the characteristics of out-of-mold foaming in that a rubber foam with a dense cell structure can be obtained, and it also has the characteristics that cannot be achieved with conventional production methods. It has remarkable effects, such as being able to produce a rubber foam with excellent flexibility that has never been achieved before.

Claims (1)

【特許請求の範囲】[Claims] 1 ポリノルボルネン樹脂100重量部に対してナ
フテンオイル200〜500重量部、適量の発泡剤およ
び架橋剤その他の配合剤を添加して混練すること
により原料コンパウンドを調製し、該原料コンパ
ウンドを充填率100%で型内に充填した後、プレ
スで強固に閉型して加熱することにより発泡剤を
分解させ、続いて型を開放することにより前記原
料コンパウンドを発泡膨張させて発泡体とするこ
とを特徴とするゴム発泡体の製造方法。
1 Prepare a raw material compound by adding and kneading 200 to 500 parts by weight of naphthenic oil, appropriate amounts of blowing agents, crosslinking agents, and other compounding agents to 100 parts by weight of polynorbornene resin, and mix the raw material compound to a filling rate of 100. % in a mold, the mold is tightly closed with a press and heated to decompose the foaming agent, and then the mold is opened to expand the raw material compound to form a foam. A method for producing a rubber foam.
JP59094208A 1984-05-11 1984-05-11 Production of rubber foam Granted JPS60238333A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59094208A JPS60238333A (en) 1984-05-11 1984-05-11 Production of rubber foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59094208A JPS60238333A (en) 1984-05-11 1984-05-11 Production of rubber foam

Publications (2)

Publication Number Publication Date
JPS60238333A JPS60238333A (en) 1985-11-27
JPH0363987B2 true JPH0363987B2 (en) 1991-10-03

Family

ID=14103887

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59094208A Granted JPS60238333A (en) 1984-05-11 1984-05-11 Production of rubber foam

Country Status (1)

Country Link
JP (1) JPS60238333A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2502759B2 (en) * 1989-07-28 1996-05-29 富造 山本 Closed-cell molded article

Also Published As

Publication number Publication date
JPS60238333A (en) 1985-11-27

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