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JP5079066B2 - Rubber foam - Google Patents
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JP5079066B2 - Rubber foam - Google Patents

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JP5079066B2
JP5079066B2 JP2010224910A JP2010224910A JP5079066B2 JP 5079066 B2 JP5079066 B2 JP 5079066B2 JP 2010224910 A JP2010224910 A JP 2010224910A JP 2010224910 A JP2010224910 A JP 2010224910A JP 5079066 B2 JP5079066 B2 JP 5079066B2
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rubber
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weight
foam
ethylene
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JP2011001562A (en
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光生 松本
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Nitto Denko Corp
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Description

本発明は、熱圧縮永久歪みが少なくてシール性能の維持性に優れるエチレン・プロピレン系のゴム系発泡体に関する。   The present invention relates to an ethylene / propylene rubber foam which has a low thermal compression set and is excellent in the maintenance of sealing performance.

エチレン・プロピレン系ゴムを用いたゴム系発泡体は、優れたクッション性や圧縮性等に基づいてクッション材やパッド材、気密や止水等のシール材、断熱材や防音材などとして家電等の室内用品や自動車等の屋外用品、住宅等の建築物などの各種の分野で広く使用されており、加硫発泡の処理作業性や得られる発泡体の耐久性等の物性などの点より硫黄による加硫処理方式が一般に採られている。しかしながら従来の発泡体では、熱圧縮永久歪みが大きくて高温経験後は反発力(圧縮復元率)が大きく低下し、シール性能の低下が著しい問題点があった。   Rubber foams using ethylene / propylene rubber are used for home appliances as cushioning materials, padding materials, sealing materials such as airtightness and waterstop, heat insulation materials and soundproofing materials, etc. It is widely used in various fields such as indoor products, outdoor products such as automobiles, buildings such as houses, etc., and it depends on sulfur from the viewpoint of physical properties such as vulcanization foam processing workability and durability of the resulting foam. A vulcanization method is generally adopted. However, the conventional foam has a problem that the thermal compression set is large, the repulsive force (compression recovery rate) is greatly lowered after high temperature experience, and the sealing performance is significantly lowered.

本発明は、硫黄加硫による加硫発泡処理作業の容易性や得られる発泡体の良物性等の利点を活かしつつ、熱圧縮永久歪みが少なくてシール性能の維持性に優れるエチレン・プロピレン系ゴムを用いたゴム系発泡体の開発を課題とする。   The present invention is an ethylene / propylene rubber that has low heat compression set and is excellent in maintainability of sealing performance while taking advantage of the ease of vulcanization and foaming processing by sulfur vulcanization and the good physical properties of the resulting foam. The development of rubber-based foams using styrene is an issue.

本発明は、エチレン・プロピレン系ゴム100重量部に対して、発泡剤5〜20重量部、カーボンブラック5〜25重量部及び白色系の充填剤90〜200重量部と、硫黄とを少なくとも成分とする混和物を加硫発泡処理した発泡体からなり、圧縮率50%の状態で70℃下に22時間放置した場合の熱圧縮永久歪みが90%以下であることを特徴とするゴム系発泡体を提供するものである。   The present invention comprises 5 to 20 parts by weight of a foaming agent, 5 to 25 parts by weight of carbon black and 90 to 200 parts by weight of a white filler, and at least a component of 100 parts by weight of ethylene / propylene rubber. A rubber-based foam comprising a foam obtained by vulcanizing and foaming an admixture, and having a compression set of 50% and a thermal compression set when left at 70 ° C. for 22 hours for 90 hours or less Is to provide.

また、本発明のゴム系発泡体では、前記充填剤は、酸化亜鉛、炭酸カルシウムおよび水酸化アルミニウムからなる群から選択される少なくとも1種であることが好適である。   In the rubber foam of the present invention, it is preferable that the filler is at least one selected from the group consisting of zinc oxide, calcium carbonate, and aluminum hydroxide.

また、本発明のゴム系発泡体では、前記充填剤が、酸化亜鉛、炭酸カルシウムおよび水酸化アルミニウムであることが好適である。   In the rubber-based foam of the present invention, it is preferable that the filler is zinc oxide, calcium carbonate, and aluminum hydroxide.

また、本発明のゴム系発泡体では、混和物における硫黄の配合量がエチレン・プロピレン系ゴム100重量部あたり0.3〜0.8重量部であり、混和物がチウラム系加硫促進剤も成分とすることが好適である。   In the rubber foam of the present invention, the blending amount of sulfur in the blend is 0.3 to 0.8 parts by weight per 100 parts by weight of the ethylene / propylene rubber, and the blend is also a thiuram vulcanization accelerator. It is preferable to use it as a component.

また、本発明のゴム系発泡体では、密度が0.01〜0.3g/cmであることが好適である。 Moreover, in the rubber-type foam of this invention, it is suitable that a density is 0.01-0.3 g / cm < 3 >.

本発明によれば、硫黄加硫による加硫発泡処理作業の容易性や得られる発泡体の良物性等の利点を活かしつつ、熱圧縮永久歪みが少なくてシール性能の維持性に優れるエチレン・プロピレン系ゴムを用いたゴム系発泡体を得ることができる。従って過酸化物系等の他の加硫方式に変更する必要なく、従来の硫黄加硫方式の製造ラインをそのまま用いることができる。また前記の効果を硫黄使用量の減量で達成した場合には資源の有効活用の利点もある。   According to the present invention, ethylene propylene is excellent in maintainability of sealing performance with less heat compression set while taking advantage of the ease of vulcanization and foaming processing by sulfur vulcanization and the good physical properties of the resulting foam. A rubber-based foam using a rubber-based rubber can be obtained. Therefore, the conventional sulfur vulcanization production line can be used as it is without changing to another vulcanization method such as a peroxide type. In addition, when the above effect is achieved by reducing the amount of sulfur used, there is an advantage of effective use of resources.

本発明によるゴム系発泡体は、エチレン・プロピレン系ゴム、発泡剤及び硫黄を少なくとも成分とする混和物を加硫発泡処理した発泡体からなり、圧縮率50%の状態で70℃下に22時間放置した場合の熱圧縮永久歪みが90%以下、就中75%以下、特に60%以下であるものからなる。   The rubber-based foam according to the present invention comprises a foam obtained by vulcanizing and foaming an ethylene / propylene-based rubber, a foaming agent, and an admixture containing at least sulfur as components, and at a compression rate of 50% for 22 hours at 70 ° C. When left standing, the heat compression set is 90% or less, especially 75% or less, particularly 60% or less.

エチレン・プロピレン系ゴムとしては、例えばエチレン・プロピレン・ジエンゴム(EPDM)やエチレン・プロピレンゴム、エチレン・プロピレンターポリマーなどの適宜なものを1種又は2種以上用いることができ、特に限定はない。圧縮性やシール性能等のゴム物性の調節性などの点よりはEPDM、就中プロピレンの共重合割合が25重量%以上、特に40〜49重量%で、5−エチリデン−2−ノルボルネンの共重合割合が4〜10重量%、特に6〜8重量%のEPDMが好ましく、またムーニー粘度が(ML1+4、100℃、以下同じ)100以下、就中10〜50、特に20〜40のエチレン・プロピレン系ゴムが好ましく用いられる。   As the ethylene / propylene rubber, one or more suitable ones such as ethylene / propylene / diene rubber (EPDM), ethylene / propylene rubber, and ethylene / propylene terpolymer can be used without any particular limitation. Copolymerization of 5-ethylidene-2-norbornene when the copolymerization ratio of EPDM and especially propylene is 25% by weight or more, especially 40 to 49% by weight in terms of controllability of rubber properties such as compressibility and sealing performance. EPDM having a proportion of 4 to 10% by weight, particularly 6 to 8% by weight, and an ethylene / propylene system having Mooney viscosity of 100 or less (ML1 + 4, 100 ° C., the same shall apply hereinafter), especially 10 to 50, especially 20 to 40 Rubber is preferably used.

発泡剤としても1種又は2種以上の適宜なものを用いることができ、特に限定はない。ちなみにその例としてはアゾジカルボンアミド(ADCA)やアゾビスイソブチロニトリルやバリウムアゾジカルボキシレートの如きアゾ系化合物、N,N'−ジニトロソペンタメチレンテトラミンやN,N'−ジメチル−N,N'−ジニトロソテレフタルアミドの如きN−ニトロソ系化合物、ベンゼンスルホニルヒドラジドやトルエンスルホニルヒドラジド、ジフェニルスルホン−3,3'−ジスルホニルヒドラジドの如きスルホニルヒドラジド系化合物があげられる。   As the foaming agent, one or more suitable ones can be used, and there is no particular limitation. Incidentally, examples include azo compounds such as azodicarbonamide (ADCA), azobisisobutyronitrile and barium azodicarboxylate, N, N′-dinitrosopentamethylenetetramine, N, N′-dimethyl-N, Examples thereof include N-nitroso compounds such as N′-dinitrosotephthalamide, and sulfonyl hydrazide compounds such as benzenesulfonyl hydrazide, toluenesulfonyl hydrazide, and diphenylsulfone-3,3′-disulfonyl hydrazide.

またトリクロロモノフルオロメタンやジクロロモノフルオロメタンの如きフッ化アルカン、4,4'−オキシビス(ベンゼンスルホニルヒドラジド)、アリルビス(スルホニルヒドラジド)の如きヒドラジン系化合物、ρ−トルイレンスルホニルセミカルバジドや4,4'−オキシビス(ベンゼンスルホニルセミカルバジド)の如きセミカルバジド系化合物、5−モルホリル−1,2,3,4−チアトリアゾールの如きトリアゾール系化合物などの有機系発泡剤もあげられる。   In addition, fluorinated alkanes such as trichloromonofluoromethane and dichloromonofluoromethane, hydrazine compounds such as 4,4′-oxybis (benzenesulfonylhydrazide), allylbis (sulfonylhydrazide), ρ-toluylenesulfonyl semicarbazide and 4,4 ′. -Organic foaming agents such as semicarbazide compounds such as oxybis (benzenesulfonyl semicarbazide) and triazole compounds such as 5-morpholyl-1,2,3,4-thiatriazole.

さらに炭酸アンモニウムや炭酸水素アンモニウム、炭酸ナトリウムや炭酸水素ナトリウム、亜硝酸アンモニウムや水素化ホウ素ナトリウム、カルシウムアジドやパラトルエンスルホニルアジドの如きアジド系化合物等の無機系発泡剤などもあげられる。就中、自己消火性による安全性や無毒性などの点よりADCAが好ましく用いられる。   Further examples include inorganic foaming agents such as ammonium carbonate, ammonium hydrogen carbonate, sodium carbonate, sodium hydrogen carbonate, ammonium nitrite, sodium borohydride, azide compounds such as calcium azide and paratoluenesulfonyl azide. In particular, ADCA is preferably used in terms of safety and non-toxicity due to self-extinguishing properties.

発泡剤の使用量は、エチレン・プロピレン系ゴム100重量部あたり5〜20重量部、特に10〜15重量部が好ましい。なお用いる発泡剤は、加熱膨脹性の物質がマイクロカプセル内に封入された熱膨脹性微粒子などであってもよい。その熱膨脹性微粒子にはマイクロスフェア(商品名、松本油脂社製)などの市販物もある。   The amount of the blowing agent used is preferably 5 to 20 parts by weight, particularly 10 to 15 parts by weight per 100 parts by weight of the ethylene / propylene rubber. The foaming agent used may be heat-expandable fine particles in which a heat-expandable substance is enclosed in microcapsules. The thermally expandable fine particles include commercially available products such as microspheres (trade name, manufactured by Matsumoto Yushi Co., Ltd.).

加硫剤としては、上記したように加硫発泡処理作業の容易性や得られる発泡体の耐久性等の物性などの点より硫黄が用いられる。その使用量は、従来よりも少ない量、就中エチレン・プロピレン系ゴム100重量部あたり0.3〜0.8重量部、特に0.4〜0.6重量部の使用量とすることが好ましい。斯かる少な目の使用量とすることにより本発明の目的である熱圧縮永久歪みの少ない発泡体が得られやすい。これは硫黄の少な目の使用量がポリスルフィド結合の生成を抑制するためであると考えられる。   As described above, sulfur is used as the vulcanizing agent in view of the physical properties such as the ease of the vulcanization foaming work and the durability of the obtained foam. The amount used is preferably less than the conventional amount, especially 0.3 to 0.8 parts by weight, especially 0.4 to 0.6 parts by weight per 100 parts by weight of ethylene / propylene rubber. . By setting the amount to be used in such a small amount, it is easy to obtain a foam having a small thermal compression set, which is an object of the present invention. This is thought to be because a small amount of sulfur used suppresses the formation of polysulfide bonds.

すなわち硫黄による加硫処理では、モノスルフィド結合やジスルフィド結合、ポリスルフィド結合にて架橋構造が形成されるが、その場合に架橋構造がポリスルフィド化するほど結合エネルギーが小さくなる。従ってモノスルフィド結合やジスルフィド結合による架橋構造をリッチに生成させ、ポリスルフィド結合による架橋構造の生成を抑制するほど結合エネルギーの大きい架橋構造が形成されて架橋物の熱安定性が向上し、その耐熱性の向上で熱圧縮永久歪みの少ない発泡体が得られることとなり、硫黄の使用量を少なくすることでそのポリスルフィド結合の生成が抑制されると考えられる。硫黄使用量の減量は資源の有効活用の点よりも利点がある。   That is, in the vulcanization treatment with sulfur, a crosslinked structure is formed by monosulfide bonds, disulfide bonds, and polysulfide bonds. In this case, the bond energy becomes smaller as the crosslinked structure becomes polysulfide. Therefore, a cross-linked structure with a monosulfide bond or a disulfide bond is generated in a rich manner, and a cross-linked structure with a large binding energy is formed to suppress the formation of a cross-linked structure with a polysulfide bond, thereby improving the thermal stability of the cross-linked product and its heat resistance. It is considered that a foam with less heat compression set can be obtained by improving the amount of polysulfide bonds by reducing the amount of sulfur used. Reduction of sulfur usage is more advantageous than efficient use of resources.

本発明による発泡体を形成するための混和物の調製は、少なくともエチレン・プロピレン系ゴム、発泡剤及び硫黄からなる配合成分を、例えばバンバリーミキサやニーダ、インターミックスの如きインターナルミキサ類等の混練機を介して混合する方式などの適宜な方式で混合することにより行うことができる。その場合、加硫が進行する程度に温度上昇する混合方式は好ましくなく、必要に応じ加硫剤や発泡剤等を他成分混合後に加える多段階の混合方式を採ることもできる。   Preparation of an admixture for forming a foam according to the present invention is performed by kneading at least a compounding component comprising an ethylene / propylene rubber, a foaming agent and sulfur, for example, an internal mixer such as a Banbury mixer, a kneader, or an intermix. It can be carried out by mixing by an appropriate method such as a method of mixing via a machine. In that case, a mixing method in which the temperature rises to such an extent that vulcanization proceeds is not preferable, and a multi-stage mixing method in which a vulcanizing agent, a foaming agent, or the like is added after mixing other components as necessary can be adopted.

混和物の調製に際しては加硫処理や発泡処理の促進、混和物の粘度や得られる発泡体の物性の調節などを目的に従来に準じた適宜な配合剤の1種又は2種以上を必要に応じて添加することができる。ちなみに加硫処理の促進を目的に用いる加硫促進剤の例としては、テトラメチルチウラムモノスルフィドやテトラメチルチウラムジスルフィド、テトラエチルチウラムジスルフィドやジペンタメチレンチウラムテトラスルフィドの如きチウラム類があげられる。   When preparing an admixture, one or more suitable compounding agents according to the prior art are required for the purpose of accelerating the vulcanization treatment and foaming treatment, adjusting the viscosity of the admixture and the physical properties of the resulting foam, etc. Can be added accordingly. Incidentally, examples of the vulcanization accelerator used for the purpose of promoting the vulcanization treatment include thiurams such as tetramethylthiuram monosulfide, tetramethylthiuram disulfide, tetraethylthiuram disulfide and dipentamethylenethiuram tetrasulfide.

またN−シクロヘキシル−2−ベンゾチアゾールスルフェンアミドやN−オキシジエン−2−ベンゾチアゾールスルフェンアミド、N,N−ジイソプロピル−2−ベンゾチアゾールスルフェンアミドの如きスルフェンアミド類、2−メルカプトベンゾチアゾールやジベンゾチアジルジスルフィドの如きチアゾール類、ジフェニルグアニジンやジフェニルグアニジンフタレートの如きグアニジン類、アセトアルデヒド−アニリン反応物やアセトアルデヒドアンモニアの如きアルデヒドアミン類やアルデヒドアンモニア類、2−メルカプトイミダゾリンの如きイミダゾリン類、チオカルバニリドやジエチルチオユリアの如きチオユリア類、ジメチルジチオカルバミン酸亜鉛やジエチルジチオカルバミン酸亜鉛の如きジチオ酸塩類、ジブチルキサントゲン酸亜鉛の如きザンテート類、亜鉛華なども加硫促進剤の例としてあげられる。   Further, sulfenamides such as N-cyclohexyl-2-benzothiazole sulfenamide, N-oxydiene-2-benzothiazole sulfenamide, N, N-diisopropyl-2-benzothiazole sulfenamide, 2-mercaptobenzothiazole And thiazoles such as dibenzothiazyl disulfide, guanidines such as diphenylguanidine and diphenylguanidine phthalate, aldehyde amines and aldehyde ammonia such as acetaldehyde-aniline reactant and acetaldehyde ammonia, imidazolines such as 2-mercaptoimidazoline, thiocarbanilide, Thioureas such as diethylthiourea, dithioacid salts such as zinc dimethyldithiocarbamate and zinc diethyldithiocarbamate, dibutylxan Such xanthates Gen zinc, zinc flower be cited as examples of the vulcanization accelerator.

加硫促進剤は1種又は2種以上を用いることができ、就中、硫黄供給能を有してそれ自体も加硫剤として機能しうるチウラム類が熱圧縮永久歪みの少ない発泡体を得る点より好ましく用いられる。加硫促進剤の使用量は、エチレン・プロピレン系ゴム100重量部あたり0.1〜10重量部、就中0.5〜8重量部、特に3〜6重量部が好ましい。なお加硫促進剤の使用に際しては加硫促進助剤も併用することができる。   One or two or more vulcanization accelerators can be used, and in particular, thiurams which have a sulfur supply ability and can function as a vulcanizing agent themselves provide a foam having a low thermal compression set. It is preferably used from the point. The amount of the vulcanization accelerator used is preferably 0.1 to 10 parts by weight, especially 0.5 to 8 parts by weight, particularly 3 to 6 parts by weight, per 100 parts by weight of the ethylene / propylene rubber. When using a vulcanization accelerator, a vulcanization accelerator aid can be used in combination.

発泡処理の促進を目的に用いる発泡助剤の例としては、サリチル酸系やフタル酸系、ステアリン酸系やシュウ酸系、安息香酸系の如き有機酸系化合物、尿素やその誘導体の如き尿素系化合物などがあげられ、就中、尿素が好ましく用いられる。発泡助剤は1種又は2種以上を用いることができ、その配合で発泡剤の分解温度を低下させて発泡処理を促進しうると共に、気泡の均一化などにも有効である。発泡助剤の使用量は、エチレン・プロピレン系ゴム100重量部あたり0.1〜10重量部、就中0.5〜8重量部、特に1〜5重量部が好ましい。   Examples of foaming aids used for the purpose of promoting foaming treatment include salicylic acid-based, phthalic acid-based, stearic acid-based, oxalic acid-based, organic acid-based compounds such as benzoic acid-based compounds, and urea-based compounds such as urea and its derivatives. In particular, urea is preferably used. One or two or more foaming aids can be used, and the blending of the foaming aid can lower the decomposition temperature of the foaming agent to promote foaming treatment, and is also effective for uniformizing bubbles. The amount of the foaming aid used is preferably 0.1 to 10 parts by weight, especially 0.5 to 8 parts by weight, particularly 1 to 5 parts by weight per 100 parts by weight of the ethylene / propylene rubber.

また、本発明の混和物にはカーボンブラックを添加する。カーボンブラックは、補強剤等として機能して得られる発泡体の熱圧縮永久歪みの低減に有用である。補強効果等の点よりはジブチルフタレート吸収量が0.5〜1.3ml/g、就中0.6〜1.1ml/gのカーボンブラックが好ましく用いられる。カーボンブラックの使用量は、適度な補強効果の発現性などの点よりエチレン・プロピレン系ゴム100重量部あたり5〜25重量部、特に10〜20重量部が好ましい。その使用量が過多では補強効果が強くなりすぎて得られる発泡体の発泡倍率が低下しやすくなる。   Carbon black is added to the blend of the present invention. Carbon black is useful for reducing the thermal compression set of a foam obtained by functioning as a reinforcing agent or the like. Carbon black having a dibutyl phthalate absorption of 0.5 to 1.3 ml / g, especially 0.6 to 1.1 ml / g, is preferably used in view of the reinforcing effect and the like. The amount of carbon black used is preferably 5 to 25 parts by weight, particularly 10 to 20 parts by weight, per 100 parts by weight of the ethylene / propylene rubber, from the standpoint of appropriate reinforcement effect. If the amount used is excessive, the reinforcing effect becomes too strong, and the foaming ratio of the foam obtained is likely to be lowered.

混和物の粘度やそれによる加工性、得られる発泡体の物性の調節などを目的に添加されることのあるその他の配合剤の例としては、充填剤や軟化剤ないし可塑剤、難燃剤や老化防止剤、酸化防止剤や顔料、着色剤や防カビ剤などをあげることができる。   Examples of other compounding agents that may be added for the purpose of adjusting the viscosity of the admixture and the resulting processability and the physical properties of the resulting foam include fillers, softeners or plasticizers, flame retardants and aging. Examples thereof include an inhibitor, an antioxidant and a pigment, a colorant and an antifungal agent.

また、本発明の混和物には、充填剤を添加する。充填剤としては、白色系の充填剤が挙げられる。そのような充填剤の具体例としては、炭酸カルシウムや炭酸マグネシウムの如き炭酸塩類、湿式や乾式のシリカ、タルクやクレー、ウォラストナイトやベントナイト、アルミニウムシリケートの如き各種ケイ酸塩類、酸化亜鉛や酸化アルミニウム、酸化チタンや酸化マグネシウムの如き酸化金属類、雲母粉やアルミニウム粉、それらをカップリング剤等で表面処理したものなどがあげられる。   Moreover, a filler is added to the blend of the present invention. An example of the filler is a white filler. Specific examples of such fillers include carbonates such as calcium carbonate and magnesium carbonate, wet and dry silica, talc and clay, wollastonite and bentonite, various silicates such as aluminum silicate, zinc oxide and oxide. Examples thereof include aluminum, metal oxides such as titanium oxide and magnesium oxide, mica powder and aluminum powder, and those obtained by surface treatment with a coupling agent or the like.

本発明において、充填剤として、上記したカーボンブラックの添加による黒色化を抑制する点より、白色系の充填剤が用いられる。充填剤として、特に、酸化亜鉛、炭酸カルシウムや水酸化アルミニウムが好ましく用いられる。充填剤の使用量は、混和物における押出し成形性等の加工性の改善効果や得られる発泡体における柔軟性の維持性などの点よりエチレン・プロピレン系ゴム100重量部あたり90〜200重量部であり、就中95〜190重量部、特に100〜180重量部が好ましい。   In the present invention, a white filler is used as the filler from the viewpoint of suppressing blackening due to the addition of the above-described carbon black. In particular, zinc oxide, calcium carbonate, and aluminum hydroxide are preferably used as the filler. The filler is used in an amount of 90 to 200 parts by weight per 100 parts by weight of ethylene / propylene rubber from the viewpoint of improving processability such as extrudability in the blend and maintaining flexibility in the resulting foam. In particular, 95 to 190 parts by weight, particularly 100 to 180 parts by weight is preferable.

一般に混和物の成形性の調節などに有用な軟化剤ないし可塑剤の具体例としては、パラフィン系やナフテン系等のプロセスオイル、流動パラフィンやその他のパラフィン類、ワックス類や潤滑油類、シリコーンオイルや液状ポリブテン等の合成高分子系軟化剤、アロマ類やアスファルト類、アマニ油等の乾性油類や動植物油類、石油系オイル類や各種の低分量ポリマー類、フタル酸系やアジピン酸系、セバシン酸系やリン酸系等のエステル系可塑剤類、ステアリン酸やそのエステル類、アルキルスルホン酸エステル類や粘着付与剤などがあげられる。   Specific examples of softeners or plasticizers that are generally useful for adjusting the moldability of admixtures include paraffinic and naphthenic process oils, liquid paraffin and other paraffins, waxes and lubricating oils, and silicone oils. And synthetic polymer softeners such as liquid polybutene, aromas and asphalts, drying oils such as linseed oil, animal and vegetable oils, petroleum oils and various low-volume polymers, phthalic acid and adipic acid, Examples thereof include ester plasticizers such as sebacic acid and phosphoric acid, stearic acid and esters thereof, alkylsulfonic acid esters and tackifiers.

加工性の点よりは特にパラフィン系プロセスオイルが好ましく用いられる。軟化剤ないし可塑剤の使用量は、混和物における押出し成形性等の加工性の改善効果や得られる発泡体における成分揮発による耐熱性の低下を防止する点より、エチレン・プロピレン系ゴム100重量部あたり20〜55重量部、就中25〜50重量部、特に30〜40重量部が好ましい。   In particular, paraffinic process oil is preferably used from the viewpoint of processability. The amount of the softener or plasticizer used is 100 parts by weight of ethylene / propylene rubber from the viewpoint of improving the processability such as extrudability in the blend and preventing the heat resistance from being reduced due to component volatilization in the resulting foam. 20 to 55 parts by weight, especially 25 to 50 parts by weight, especially 30 to 40 parts by weight are preferred.

上記した難燃剤や老化防止剤、酸化防止剤や顔料、着色剤や防カビ剤等のその他の配合剤には、前記した水酸化アルミニウムや水酸化マグネシウム、エチレンビスペンタブロモジフェニルの如き難燃剤などの従来に準じた適宜なものを用いうる。また難燃性の向上の点よりは引火点の高い配合剤を用いることが有利である。なお上記した酸化亜鉛は安定剤として、ステアリン酸やそのエステル類は滑剤などとしても有用であり、従って各種の安定剤や滑剤も配合しうる成分の例としてあげられる。   Other flame retardants such as the above-mentioned flame retardants, anti-aging agents, antioxidants and pigments, colorants and anti-mold agents, such as aluminum hydroxide, magnesium hydroxide, ethylene bispentabromodiphenyl, etc. An appropriate one according to the conventional method can be used. In addition, it is advantageous to use a compounding agent having a high flash point rather than improving flame retardancy. The zinc oxide described above is useful as a stabilizer, and stearic acid and its esters are useful as a lubricant. Therefore, examples of components in which various stabilizers and lubricants can be blended are listed.

混和物には更に、得られる発泡体の強度等の調節を目的に非ゴム系ポリマーやエチレン・プロピレン系ゴム以外のゴム系ポリマーを1種又は2種以上配合することもできる。その非ゴム系ポリマーやゴム系ポリマーについては適宜なものを用いることができ、特に限定はない。ちなみにその非ゴム系ポリマーの例としては、ポリ(メタ)アクリル酸アルキルエステルの如きアクリル系ポリマーやポリエチレン、ポリプロピレンやエチレン・酢酸ビニル共重合体、ポリ酢酸ビニルやポリアミド、ポリエステルやウレタン系ポリマー、スチレン系ポリマーやシリコーン系ポリマー、エポキシ系樹脂などがあげられる。その使用量は、発泡体のゴム的性質を維持する点などよりエチレン・プロピレン系ゴムの50重量%以下、就中30重量%以下、特に15重量%以下が好ましい。   The blend may further contain one or more rubber polymers other than non-rubber polymers and ethylene / propylene rubbers for the purpose of adjusting the strength and the like of the resulting foam. Any suitable non-rubber polymer or rubber polymer can be used without any particular limitation. Incidentally, examples of non-rubber polymers include acrylic polymers such as poly (meth) acrylic acid alkyl esters, polyethylene, polypropylene, ethylene / vinyl acetate copolymers, polyvinyl acetate and polyamide, polyesters and urethane polymers, styrene. Examples thereof include silicone polymers, silicone polymers, and epoxy resins. The amount used is preferably 50% by weight or less, more preferably 30% by weight or less, and particularly preferably 15% by weight or less of the ethylene / propylene rubber from the viewpoint of maintaining the rubbery properties of the foam.

一方、前記したエチレン・プロピレン系ゴム以外のゴム系ポリマーの例としては、ブテン−1の如きα−オレフィン・ジシクロペンタジエンやエチリデンノルボルネンの如き非共役二重結合を有する環状又は非環状のポリエンを成分とするゴム系共重合体やシリコーンゴム、フッ素ゴムやアクリルゴム、ポリウレタン系ゴムやポリアミド系ゴム、天然ゴムやポリイソブチレン、ポリイソプレンやブチルゴム、ニトリルブチルゴムやスチレン・ブタジエンゴム、スチレン・ブタジエン・スチレンゴムやスチレン・イソプレン・スチレンゴム、スチレン・エチレン・ブタジエンゴムやスチレン・エチレン・ブチレン・スチレンゴム、スチレン・イソプレン・プロピレン・スチレンゴムなどがあげられる。エチレン・プロピレン系ゴム以外のゴム系ポリマーの配合量は、前記非ゴム系ポリマーの場合に準じうる。   On the other hand, examples of rubber-based polymers other than the above-described ethylene / propylene rubber include cyclic or non-cyclic polyenes having non-conjugated double bonds such as α-olefins such as butene-1, dicyclopentadiene and ethylidene norbornene. Rubber copolymer, silicone rubber, fluorine rubber, acrylic rubber, polyurethane rubber, polyamide rubber, natural rubber, polyisobutylene, polyisoprene, butyl rubber, nitrile butyl rubber, styrene-butadiene rubber, styrene-butadiene-styrene Examples thereof include rubber, styrene / isoprene / styrene rubber, styrene / ethylene / butadiene rubber, styrene / ethylene / butylene / styrene rubber, and styrene / isoprene / propylene / styrene rubber. The compounding amount of the rubber polymer other than the ethylene / propylene rubber can be the same as that of the non-rubber polymer.

本発明によるゴム系発泡体の形成は、上記した混和物を加熱して発泡処理と加硫処理を加えることにより行うことができ、その加硫発泡処理は同時に行うこともできるし、別工程にて行うこともできる。そのゴム系発泡体の形成に際しては必要に応じ混和物を例えばシート等の所定の形態に成形して、その成形体を加熱処理して加硫発泡体とすることもできる。その場合に成形体は、適宜な方式にて任意な形態に成形したものであってよく、その形態について特に限定はない。   Formation of the rubber-based foam according to the present invention can be performed by heating the above-mentioned mixture and adding a foaming treatment and a vulcanization treatment, and the vulcanization foaming treatment can be performed simultaneously or in a separate process. Can also be done. In forming the rubber-based foam, if necessary, the blend may be formed into a predetermined form such as a sheet, and the molded body may be heat-treated to obtain a vulcanized foam. In that case, the molded body may be molded into an arbitrary form by an appropriate method, and the form is not particularly limited.

従って加硫発泡処理の対象物は、混和物を例えばミキシングロールやカレンダーロールや押出成形等による適宜な方式でシート状やその他の形態に成形したものであってもよいし、所定の型を介して射出成形やプレス成形等による適宜な方式で凹凸等を有する所定の形態に成形したものなどであってもよい。その場合に凹凸形状を有する発泡体の形成では、成形シートを凹凸を有する型の上に配置して加熱し、その型の凹凸に前記シートを形成する混和物を流動侵入させて加硫発泡処理する方式なども採ることができる。   Therefore, the object of vulcanization and foaming treatment may be a mixture obtained by molding the admixture into a sheet or other form by an appropriate method such as a mixing roll, a calender roll, or extrusion molding, or through a predetermined mold. Further, it may be formed into a predetermined form having irregularities by an appropriate method such as injection molding or press molding. In that case, in the formation of a foam having a concavo-convex shape, a molded sheet is placed on a mold having a concavo-convex shape and heated, and the mixture forming the sheet flows into the concavo-convex shape of the mold and vulcanized and foamed. It is also possible to adopt a method to do so.

前記の型を介した方式は、ヒダ構造を有する複雑で深い凹凸構造を有する型の場合にもその凹凸形状を精度よく形成できる利点などを有している。よって成形体の寸法は任意であり、目的とする発泡体の形態などに応じて適宜に決定することができる。シート等の場合、その厚さは100mm以下、就中1μm〜80mm、特に10μm〜50mmが一般的である。   The method using the mold has an advantage that the uneven shape can be accurately formed even in the case of a mold having a complex deep uneven structure having a corrugated structure. Therefore, the size of the molded body is arbitrary, and can be appropriately determined according to the form of the target foam. In the case of a sheet or the like, the thickness is generally 100 mm or less, in particular, 1 μm to 80 mm, particularly 10 μm to 50 mm.

上記した加硫発泡処理は、用いた発泡剤や加硫剤などによる発泡温度や加硫開始温度などにより従来に準じた適宜な条件で行うことができる。一般的な処理温度は、450℃以下、就中100〜350℃、特に120〜300℃である。斯かる加硫発泡処理で混和物が軟化して発泡剤が膨脹し発泡構造を形成しつつ加硫が進行して目的の加硫発泡体が形成される。その場合に発泡処理は、発泡倍率の調節などを目的に加圧下で行うこともでき加圧条件は、従来に準じることができる。また加硫発泡処理は、発泡処理と加硫処理を異なる温度条件で行うこともでき、適宜な処理条件を採ることができる。   The vulcanization foaming treatment described above can be performed under appropriate conditions according to the prior art depending on the foaming temperature, the vulcanization start temperature, and the like by the used foaming agent or vulcanizing agent. Typical processing temperatures are 450 ° C. or less, especially 100 to 350 ° C., particularly 120 to 300 ° C. By such vulcanization and foaming treatment, the admixture is softened and the foaming agent expands to form a foamed structure, and vulcanization proceeds to form the desired vulcanized foam. In this case, the foaming treatment can be performed under pressure for the purpose of adjusting the foaming ratio and the pressurizing conditions can be the same as in the past. Moreover, the vulcanization | foaming process can also perform a foaming process and a vulcanization process on different temperature conditions, and can take an appropriate process condition.

形成する加硫発泡体の発泡倍率(発泡前後の密度比)は、使用目的などに応じて適宜に決定することができる。一般には1.1〜25倍、就中1.5〜20倍の発泡倍率とされるが通例、0.01〜0.5g/cm、就中0.05〜0.4g/cm、特に0.1〜0.3g/cmの密度とした発泡体が各種の用途に好ましく用いうる。なお発泡倍率は、上記した発泡剤の配合量や加硫発泡の処理時間や温度などにより制御することができる。また発泡倍率の調節などにより、得られる発泡体の独立や連続、それらの混在等の発泡構造を制御することができる。 The expansion ratio (density ratio before and after foaming) of the vulcanized foam to be formed can be appropriately determined according to the purpose of use. Generally, the foaming ratio is 1.1 to 25 times, especially 1.5 to 20 times, but usually 0.01 to 0.5 g / cm 3 , especially 0.05 to 0.4 g / cm 3 , In particular, a foam having a density of 0.1 to 0.3 g / cm 3 can be preferably used for various applications. The expansion ratio can be controlled by the blending amount of the above-described foaming agent, the processing time and temperature of vulcanization foaming, and the like. In addition, by adjusting the expansion ratio, the foam structure such as the independent and continuous foams and the mixture thereof can be controlled.

本発明によるゴム系発泡体は、例えばクッション材やパッド材、気密や防水等の各種目的のシール材、断熱材、防音や制振等の振動低減材などの従来に準じた各種の用途に好ましく用いることができる。   The rubber-based foam according to the present invention is preferably used in various conventional applications such as cushion materials, pad materials, sealing materials for various purposes such as airtightness and waterproofing, heat insulating materials, vibration reducing materials such as soundproofing and vibration damping. Can be used.

実施例1
ムーニー粘度30のEPDM100部(重量部、以下同じ)、カーボンブラック10部、酸化亜鉛5部、ステアリン酸2部、プロセスオイル30部、重炭酸カルシウム150部及び水酸化アルミニウム30部をバンバリーミキサにて混練後、それにADCA10部、尿素(発泡助剤)2部、硫黄0.5部、チアゾール系加硫促進剤0.8部、及びジチオカルバミン酸塩系加硫促進剤1.0部を加えてミキシングロールにより混練して混和物を得、それを押出し機で成形して厚さ4.5mm、幅150mmの未加硫シートを得、それを乾燥機内で100℃にて40分間予熱後15分間かけて160℃に昇温しその温度で15分間加熱して加硫発泡処理し、発泡シートを得た。
Example 1
100 parts of EPDM having a Mooney viscosity of 30 (parts by weight, the same applies hereinafter), carbon black 10 parts, zinc oxide 5 parts, stearic acid 2 parts, process oil 30 parts, calcium bicarbonate 150 parts and aluminum hydroxide 30 parts in a Banbury mixer After kneading, add 10 parts ADCA, 2 parts urea (foaming aid), 0.5 part sulfur, 0.8 part thiazole vulcanization accelerator, and 1.0 part dithiocarbamate vulcanization accelerator to mix. The mixture is kneaded with a roll to obtain an admixture, which is molded with an extruder to obtain an unvulcanized sheet having a thickness of 4.5 mm and a width of 150 mm, preheated in a dryer at 100 ° C. for 40 minutes, and then applied for 15 minutes. The temperature was raised to 160 ° C. and heated at that temperature for 15 minutes for vulcanization and foaming to obtain a foamed sheet.

実施例2
チウラム系加硫促進剤を3部追加配合したほかは実施例1に準じて混和物を得、それを未加硫シートに成形した後そのシートを乾燥機内で100℃にて25分間予熱後15分間かけて160℃に昇温しその温度で15分間加熱して加硫発泡処理し、発泡シートを得た。
Example 2
Except for the addition of 3 parts of thiuram vulcanization accelerator, an admixture was obtained according to Example 1, formed into an unvulcanized sheet, and then the sheet was preheated in a dryer at 100 ° C. for 25 minutes and then 15 The temperature was raised to 160 ° C. over a period of 15 minutes, and heated at that temperature for 15 minutes for vulcanization and foaming treatment to obtain a foamed sheet.

比較例1
硫黄の配合量を1.5部としたほかは実施例1に準じて混和物を得、それを未加硫シートに成形した後そのシートを乾燥機内で100℃にて15分間予熱後15分間かけて160℃に昇温しその温度で15分間加熱して加硫発泡処理し、発泡シートを得た。
Comparative Example 1
An admixture was obtained according to Example 1 except that the amount of sulfur was changed to 1.5 parts. After forming the mixture into an unvulcanized sheet, the sheet was preheated at 100 ° C. for 15 minutes in a dryer and then 15 minutes. The temperature was raised to 160 ° C. and heated at that temperature for 15 minutes for vulcanization and foaming treatment to obtain a foamed sheet.

比較例2
硫黄の配合量を1.0部としたほかは実施例1に準じて混和物を得、それを未加硫シートに成形した後そのシートを乾燥機内で100℃にて25分間予熱後15分間かけて160℃に昇温しその温度で15分間加熱して加硫発泡処理し、発泡シートを得た。
Comparative Example 2
An admixture was obtained in the same manner as in Example 1 except that the amount of sulfur was 1.0 part. After forming the mixture into an unvulcanized sheet, the sheet was preheated in a dryer at 100 ° C. for 25 minutes and then 15 minutes. The temperature was raised to 160 ° C. and heated at that temperature for 15 minutes for vulcanization and foaming treatment to obtain a foamed sheet.

評価試験
実施例、比較例で得た発泡シートについて、その密度を調べると共に熱圧縮永久歪みを調べた。なお熱圧縮永久歪みは、JIS K 6262に準拠した試験機に直径29mm、厚さ10±0.15mm(t)の試験片を平行金属板間に厚さ5.0mm(t)のスペーサを介しサンドイッチしてボルトで締め付けて圧縮率50%の状態とし、それを50℃又は70℃の恒温槽中に22時間放置したのち圧縮装置より試験片を取り出して室温下に30分間放置し、その試験片の厚さをJIS K 6262に準拠した測厚器にて測定し、その値(t)より次式にて熱圧縮永久歪みを算出した。
熱圧縮永久歪み(%)=(t−t)/(t−t)×100
前記の結果を次表1に示した。
Evaluation test About the foam sheet obtained by the Example and the comparative example, while examining the density, it investigated the thermal compression set. The thermal compression set is a spacer having a diameter of 29 mm and a thickness of 10 ± 0.15 mm (t 0 ) on a test machine conforming to JIS K 6262 with a thickness of 5.0 mm (t 2 ) between parallel metal plates. Sandwiched between the two and tightened with a bolt to a compression rate of 50%, left in a constant temperature bath at 50 ° C. or 70 ° C. for 22 hours, then removed from the compression device and left at room temperature for 30 minutes, The thickness of the test piece was measured with a thickness measuring instrument based on JIS K 6262, and the thermal compression set was calculated from the value (t 1 ) according to the following equation.
Thermal compression set (%) = (t 0 -t 1 ) / (t 0 -t 2 ) × 100
The results are shown in Table 1 below.

Figure 0005079066
Figure 0005079066

表1より硫黄の配合量を少なくした実施例で熱圧縮永久歪みが少なくなっており、チウラム系加硫促進剤を併用した実施例2で熱圧縮永久歪みが顕著に少なくなっていることがわかる。   It can be seen from Table 1 that the thermal compression set is reduced in the example in which the amount of sulfur is reduced, and the thermal compression set is significantly reduced in Example 2 in combination with the thiuram vulcanization accelerator. .

Claims (4)

エチレン・プロピレン系ゴム100重量部に対して、発泡剤5〜20重量部、カーボンブラック5〜25重量部及び白色系の充填剤90〜200重量部と、硫黄とを少なくとも成分とする混和物を加硫発泡処理した発泡体からなり、圧縮率50%の状態で70℃下に22時間放置した場合の熱圧縮永久歪みが90%以下であり、
密度が0.01〜0.3g/cm であることを特徴とするゴム系発泡体。
A blend comprising 5 to 20 parts by weight of a foaming agent, 5 to 25 parts by weight of carbon black and 90 to 200 parts by weight of a white filler and 100 parts by weight of sulfur with respect to 100 parts by weight of ethylene / propylene rubber. consists vulcanized foam treated foam, heat compression set if left 22 hours under 70 ° C. in a state of compression ratio 50% Ri der 90% or less,
Rubber foam density wherein 0.01 to 0.3 g / cm 3 der Rukoto.
前記充填剤は、酸化亜鉛、炭酸カルシウムおよび水酸化アルミニウムからなる群から選択される少なくとも1種であることを特徴とする、請求項1に記載のゴム系発泡体。 The rubber foam according to claim 1, wherein the filler is at least one selected from the group consisting of zinc oxide, calcium carbonate, and aluminum hydroxide. 前記充填剤が、酸化亜鉛、炭酸カルシウムおよび水酸化アルミニウムであることを特徴とする、請求項1または2に記載のゴム系発泡体。 The rubber-based foam according to claim 1 or 2, wherein the filler is zinc oxide, calcium carbonate, and aluminum hydroxide. 混和物における硫黄の配合量がエチレン・プロピレン系ゴム100重量部あたり0.3〜0.8重量部であり、混和物がチウラム系加硫促進剤も成分とすることを特徴とする、請求項1〜3のいずれか一項に記載のゴム系発泡体 The amount of sulfur in the admixture is 0.3 to 0.8 parts by weight per 100 parts by weight of the ethylene / propylene rubber, and the admixture also contains a thiuram vulcanization accelerator as a component. The rubber-based foam as described in any one of 1-3 .
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