JP2001335653A - Rubber foaming composition using industrial waste rubber - Google Patents

Rubber foaming composition using industrial waste rubber

Info

Publication number
JP2001335653A
JP2001335653A JP2000156271A JP2000156271A JP2001335653A JP 2001335653 A JP2001335653 A JP 2001335653A JP 2000156271 A JP2000156271 A JP 2000156271A JP 2000156271 A JP2000156271 A JP 2000156271A JP 2001335653 A JP2001335653 A JP 2001335653A
Authority
JP
Japan
Prior art keywords
rubber
impurities
foam composition
weight
foaming 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.)
Pending
Application number
JP2000156271A
Other languages
Japanese (ja)
Inventor
Takayuki Uchiumi
隆之 内海
Hirokazu Igawa
裕和 井川
Toru Noguchi
徹 野口
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.)
Mitsuboshi Belting Ltd
Original Assignee
Mitsuboshi Belting 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 Mitsuboshi Belting Ltd filed Critical Mitsuboshi Belting Ltd
Priority to JP2000156271A priority Critical patent/JP2001335653A/en
Publication of JP2001335653A publication Critical patent/JP2001335653A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a light-weight and soft rubber foaming composition in which a natural rubber used for removing impurities in a closed kneading machine, is used as a main rubber material, and its production method. SOLUTION: This rubber composition is produced out of the natural rubber, which is used for removing impurities in a closed kneading machine, as the main rubber material. The main rubber material, in which ML(1+4) at 100 deg.C is 20 to 40, is blended with a sulfonyl hydrazide foaming agent of 3 to 5 pts.wt. as a foaming agent, a sulfenic amide vulcanization accelerator of 0.5 to 3 pts.wt. and sulfur of 0.5 to 10 pts.wt. to the above main rubber material 100 pts.wt.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は産業廃棄ゴムを主材
ゴムとして利用したゴム組成物に関するもので、更に詳
しくは密閉式混練機内の不純物除着に使用し、所定のム
ーニー粘度に調節された未加硫天然ゴムを主材ゴムとし
て利用した軽量且つ軟質なゴム発泡組成物に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a rubber composition using industrial waste rubber as a main rubber, and more particularly to a rubber composition used for desorption of impurities in a closed kneader and adjusted to a predetermined Mooney viscosity. The present invention relates to a lightweight and soft rubber foam composition using unvulcanized natural rubber as a main rubber.

【0002】[0002]

【従来の技術】従来よりゴムの製造工程は、原料ゴムと
配合剤と混練りして配合ゴムとし、この配合ゴムを所定
形状に成形加工して架橋ゴムを得る。このうち混練りと
いう作業は、原料ゴムに可塑性を与え、配合剤と混ぜ合
わせる操作方法である。
2. Description of the Related Art Conventionally, in a rubber production process, a raw rubber and a compounding agent are kneaded to form a compounded rubber, and the compounded rubber is molded into a predetermined shape to obtain a crosslinked rubber. Among these operations, kneading is an operation method for imparting plasticity to the raw rubber and mixing with the compounding agent.

【0003】この混練りの際に使用される装置としては
オープンロールと密閉式混練機が挙げられるが、大量生
産性や作業環境の面から密閉式混練機が主流となってい
る。密閉式混練機には、バンバリー型混練機や加圧ニー
ダーあるいはインターミックス等があるが、密閉式とい
う性質上、混練りしたゴムを取り出した後も内部に先に
使用した配合剤が残存し、不純物として次に練るゴムに
悪影響を与えることが問題となる。特にゴム製品の高機
能化がもとめられる近年では、不純物の混入はゴム配合
設計に多大な影響を与え、製品性能の低下を招く。
[0003] As an apparatus used for this kneading, an open roll and a closed kneader can be cited, but the closed kneader is mainly used in terms of mass productivity and work environment. The closed kneader includes a Banbury-type kneader, a pressure kneader or an intermix, etc., but due to the property of the closed type, the compounding agent used earlier remains inside even after the kneaded rubber is taken out, This has a problem that it adversely affects the rubber to be kneaded next as an impurity. In particular, in recent years in which rubber products are required to have higher functionality, the mixing of impurities has a great influence on the rubber compounding design, which leads to a reduction in product performance.

【0004】そこで従来から混練りした後、密閉式混練
機に原料ゴムを投入し、素練りを行うことで、密閉式混
練機内の不純物の除着を行う作業が通常行われている。
このゴムは繰り返し使用することが可能であるが、ある
程度以上の使用回数を経ると機械力による分子鎖の切断
が進み、ムーニー粘度が低下して混練機内にへばりつく
ために使用不可能となる。このムーニー粘度が低下した
不純物除着ゴムには、充填材、加硫剤、加硫促進剤、老
化防止剤、可塑剤等の様々な種類の配合剤が不特定量含
まれており、再利用されることなく未加硫の状態で廃棄
されていた。
[0004] Therefore, it has been customary practice to knead the raw material rubber into a closed kneader and then masticate it to remove impurities in the closed kneader.
This rubber can be used repeatedly, but after a certain number of uses, the molecular chains are cut by mechanical force, and the Mooney viscosity is reduced, so that the rubber sticks in the kneader and becomes unusable. The rubber with reduced Mooney viscosity has an unspecified amount of various types of compounding agents such as fillers, vulcanizing agents, vulcanization accelerators, antioxidants, plasticizers, etc. It was discarded in an unvulcanized state without being performed.

【0005】[0005]

【発明が解決しようとする課題】しかし近年、地球環境
の保全や将来予想される化石燃料の枯渇などの観点か
ら、ゴムリサイクルは非常に期待されるものである。こ
の不純物除着作業は混練りの度に行われていることか
ら、その不純物除着ゴム廃棄量も膨大な量に達すること
に本発明者らは注目し、その利用を試みるものである。
However, in recent years, rubber recycling is highly expected from the viewpoints of preserving the global environment and depleting fossil fuels expected in the future. Since the impurity removing operation is performed at every kneading, the present inventors pay attention to the fact that the amount of waste of the impurity removing rubber reaches an enormous amount, and try to utilize the waste.

【0006】[0006]

【課題を解決するための手段】即ち、本願請求項1の発
明は、従来廃棄されていた密閉式混練機内の不純物を除
着したゴムを利用したゴム発泡組成物にある。この不純
物を除着したゴムは詳しくは100°CでのML(1+4)
が20〜40の天然ゴムであって、ムーニー粘度を該範
囲に設定することで発泡が良好なゴム発泡組成物を提供
できる。
That is, the invention of claim 1 of the present application resides in a rubber foam composition using a rubber to which impurities in a closed kneader that has been conventionally discarded are desorbed. The rubber to which this impurity has been desorbed is described in detail in ML (1 + 4) at 100 ° C.
Is 20 to 40, and by setting the Mooney viscosity in the above range, a rubber foam composition having good foaming can be provided.

【0007】本願請求項2の発明は、請求項1記載のゴ
ム発泡組成物において、主材ゴムは不純物の付着した密
閉式混練機に天然ゴムを投入し、素練りし、不純物を除
着した時点で天然ゴムを密閉式混練機から取り出すとい
うサイクルを少なくとも一回以上繰り返し、100°C
でのML(1+4)を20〜40に調節した天然ゴムであ
る。
According to a second aspect of the present invention, in the rubber foamed composition according to the first aspect, the main rubber is prepared by adding natural rubber to a closed kneader to which impurities are adhered, masticating and removing impurities. At this point, the cycle of removing natural rubber from the internal mixer is repeated at least once,
Is a natural rubber whose ML (1 + 4) is adjusted to 20-40.

【0008】本願請求項3の発明は、請求項1または2
記載のゴム発泡組成物において、加硫剤として加硫誘導
期間が長い硫黄を添加する。
[0008] The invention of claim 3 of the present application is directed to claim 1 or 2
In the rubber foam composition described above, sulfur having a long vulcanization induction period is added as a vulcanizing agent.

【0009】本願請求項4の発明は、請求項1,2また
は3記載のゴム発泡組成物において、発泡剤は分解ガス
が無害なスルホニル・ヒドラジド系発泡剤にある。
According to a fourth aspect of the present invention, in the rubber foamed composition according to the first, second or third aspect, the foaming agent is a sulfonyl hydrazide foaming agent which is harmless to a decomposition gas.

【0010】本願請求項5の発明は、請求項1,2,3
または4記載のゴム発泡組成物において、遅効性加硫促
進剤を添加する。
The invention of claim 5 of the present application is directed to claims 1, 2, 3
Alternatively, in the rubber foamed composition according to 4, a slow-acting vulcanization accelerator is added.

【0011】本願請求項6の発明は、請求項1,2,
3,4または5記載のゴム発泡組成物において、遅効性
加硫促進剤はスルフェンアミド系加硫促進剤にある。
[0011] The invention of claim 6 of the present application provides claims 1, 2, and
In the rubber foamed composition according to 3, 4, or 5, the slow-acting vulcanization accelerator is a sulfenamide-based vulcanization accelerator.

【0012】本願請求項7の発明は、密閉式混練機内の
不純物を除着したゴムを主材としたゴム発泡組成物にお
いて、主材ゴムは主材ゴムは不純物の付着した密閉式混
練機に天然ゴムを投入し、素練りし、不純物を除着した
時点で天然ゴムを密閉式混練機から取り出すというサイ
クルを少なくとも一回以上繰り返し、100°CでのM
(1+4)を20〜40に調節した天然ゴムであって、該
ゴム100重量部に対して、発泡剤としてスルホニル・
ヒドラジド系発泡剤を3〜5重量部、加硫促進剤として
スルフェンアミド系加硫促進剤を0.5〜3重量部、架
橋剤として硫黄を0.5〜10重量部添加する。
[0012] The invention according to claim 7 of the present invention relates to a rubber foamed composition mainly composed of a rubber to which impurities are removed in an internal mixer, wherein the main rubber is an internal mixer to which the impurities are attached. A cycle in which natural rubber is charged, masticated and the natural rubber is removed from the internal mixer at the time of removing impurities is repeated at least once, and M at 100 ° C.
L (1 + 4) is a natural rubber adjusted to 20 to 40, and sulfonyl.
3 to 5 parts by weight of a hydrazide-based blowing agent, 0.5 to 3 parts by weight of a sulfenamide-based vulcanization accelerator as a vulcanization accelerator, and 0.5 to 10 parts by weight of sulfur as a crosslinking agent are added.

【0013】[0013]

【発明の実施の形態】密閉式混練機内の不純物除着に使
用するゴムは、密閉型混練機で練ることのできるゴムで
あれば使用可能だが、本発明では、安価で、弾性が高く
除着能力に優れている天然ゴムを使用する。除着に使用
する際は、天然ゴムには基本的に配合剤は添加しない。
配合剤を添加したゴムを使用すると、本来の目的である
密閉式混練機内の不純物の除着が達せられないからであ
る。しかしムーニー粘度がある程度低下すると可塑性が
高くなって扱いにくくなることから、カーボンブラック
等の充填材を添加することもある。
BEST MODE FOR CARRYING OUT THE INVENTION The rubber used for desorption of impurities in a closed kneader can be used as long as it can be kneaded with a closed kneader. Use natural rubber which has excellent ability. When used for desorption, no compounding agent is basically added to natural rubber.
This is because the use of the rubber to which the compounding agent is added cannot achieve the original purpose of removing impurities in the internal mixer. However, if the Mooney viscosity decreases to some extent, the plasticity becomes high and it becomes difficult to handle, so that a filler such as carbon black may be added.

【0014】上記ゴムを密閉式混練機で素練りする。こ
の素練り作業により、密閉式混練機内に付着した不純物
を上記ゴムでそぎ落とし、ゴム中に練り込み、不純物を
除着する。練り条件は、混練り機の容量、形状、また不
純物の付着量等によって異なるために、その状況に応じ
た温度、時間、充填率、ロータ速度等の最適条件を選択
すべきである。
The above rubber is masticated with an internal mixer. By this kneading operation, impurities adhering to the inside of the internal mixer are removed by the rubber, kneaded into the rubber, and desorbed. The kneading conditions vary depending on the capacity and shape of the kneader, the amount of adhered impurities, and the like. Therefore, optimal conditions such as temperature, time, filling rate, and rotor speed should be selected according to the situation.

【0015】また上記ゴムは使用回数を経るごとに、分
子鎖が切断されムーニー粘度が低下する。本発明人が検
討した結果、100°CでのML(1+4)が20〜40に
なるまで使用することが好ましい。ML(1+4)が20未
満になると、密閉式混練機内にゴムがへばりつくため回
収が困難になり、一方ML(1+4)が40を超えると、高
粘度のため発泡が不十分となり、充分な軽量かつ柔軟性
を得ることができない。但し、ML(1+4)とは、JIS
K 6300の試験方法により、試料を1分間余熱し
た後毎分2回転でL字型ロータを回転させ、4分後に軸
にかかるトルクを測定し求めたムーニー粘度である。
Further, as the number of times of use of the rubber increases, the molecular chain is cut and the Mooney viscosity decreases. As a result of the study by the present inventors, it is preferable to use the ML (1 + 4) at 100 ° C. until the ML (1 + 4) becomes 20 to 40. When the ML (1 + 4) is less than 20, the rubber is stuck in the internal mixer and the recovery becomes difficult. On the other hand, when the ML (1 + 4) exceeds 40, foaming becomes insufficient due to high viscosity. Sufficient light weight and flexibility cannot be obtained. However, ML (1 + 4) is JIS
According to the test method of K6300, the Mooney viscosity was obtained by preheating the sample for 1 minute, rotating the L-shaped rotor at 2 revolutions per minute, and measuring the torque applied to the shaft after 4 minutes.

【0016】この100°CでのML(1+4)が20〜4
0になるまで使用したゴムを利用して、本発明に係るゴ
ム発泡組成物を提供する。尚、本発明に係るゴム発泡組
成物には、ゴムに通常使用できる短繊維、充填剤、可塑
剤、老化防止剤、加硫促進剤、発泡剤そして硫黄あるい
は有機過酸化物のような加硫剤等の配合剤を適宜添加す
ることが可能である。但し、このゴムには様々な配合剤
つまり不純物が混入しており、そのなかには加硫剤、加
硫促進剤も含まれていて、加硫速度が速くなる傾向にあ
る。その為、発泡剤を使用する際は、加硫誘導期間が比
較的長い硫黄架橋が好ましい。
The ML (1 + 4) at 100 ° C. is 20 to 4
The rubber foamed composition according to the present invention is provided by utilizing the rubber used until it reaches zero. In addition, the rubber foam composition according to the present invention includes a short fiber, a filler, a plasticizer, an antioxidant, a vulcanization accelerator, a foaming agent and a vulcanization such as sulfur or an organic peroxide which can be generally used for rubber. It is possible to appropriately add a compounding agent such as an agent. However, various compounding agents, that is, impurities are mixed in the rubber, and a vulcanizing agent and a vulcanization accelerator are also contained therein, and the vulcanization rate tends to be high. Therefore, when using a foaming agent, sulfur crosslinking with a relatively long vulcanization induction period is preferred.

【0017】短繊維としては、ポリエステル、ポリアミ
ド、アラミド、ナイロン、ビニロン、レーヨン、綿等の
有機繊維が使用される。アラミド繊維は具体的には分子
構造中に芳香環をもつアラミド、例えば商品名コーネッ
クス、ノーネックス、ケブラー、テクノーラ、トワロン
等である。この短繊維の長さは0.1〜10mmであ
り、素繊維径が数μ〜数10μmであることが好まし
く、その添加量はゴム100重量部に対して2〜30重
量部である。
As the short fibers, organic fibers such as polyester, polyamide, aramid, nylon, vinylon, rayon, and cotton are used. The aramid fiber is specifically an aramid having an aromatic ring in the molecular structure, for example, trade names such as Conex, Nonex, Kevlar, Technora, Twaron and the like. The length of the short fiber is 0.1 to 10 mm, and the diameter of the elementary fiber is preferably several μm to several tens μm, and the addition amount thereof is 2 to 30 parts by weight based on 100 parts by weight of rubber.

【0018】可塑剤としては、鉱物油系可塑剤、植物油
系可塑剤、合成可塑剤等があり、具体的には、パラフィ
ン系オイル、芳香族系オイル、ナフテン系オイル、コー
ルタール、ステアリン酸およびその塩、菜種油、パーム
油、ヤシ油、パインタール、ロジン、ファクチス、フェ
ノールアルデヒド樹脂、低融点スチレン樹脂、液状ゴ
ム、ジオクチルフタレート、ジオクチルセバケート等が
挙げられ、このうち1種または2種以上使用することが
できる。
Examples of the plasticizer include a mineral oil-based plasticizer, a vegetable oil-based plasticizer, a synthetic plasticizer, and the like. Specifically, paraffin-based oil, aromatic oil, naphthenic oil, coal tar, stearic acid and The salt, rapeseed oil, palm oil, coconut oil, pine tar, rosin, factice, phenol aldehyde resin, low melting point styrene resin, liquid rubber, dioctyl phthalate, dioctyl sebacate, etc., and one or more of these are used can do.

【0019】発泡剤としては無機発泡剤と有機発泡剤と
に大別され、無機発泡剤としては重炭酸ナトリウム、重
炭酸アンモニウム等が挙げられる。有機発泡剤として
は、N−ニトロソ化合物、スルホニルヒドラジド類、ア
ゾ化合物等が挙げられ、さらに具体的にはP,P’−オ
キシビス(ベンゼンスルホニルヒドラジド)、アゾジカ
ルボンアミド、ジニトロソペンタメチレンテトラミン等
が使用される。なかでも好ましくは比較的加硫促進効果
が少なく、かつ分解ガスが無害なスルホニル・ヒドラジ
ド系発泡剤の使用が望ましい。その添加量はゴム100
重量部に対して3〜5重量部が好ましい。3重量部未満
だと充分な発泡が得られず、軽量化、軟質化を達成する
ことができない。一方、5重量部を越えると発泡が過多
となり、成形時に変形を起こす。
The foaming agent is roughly classified into an inorganic foaming agent and an organic foaming agent. Examples of the inorganic foaming agent include sodium bicarbonate and ammonium bicarbonate. Examples of the organic foaming agent include N-nitroso compounds, sulfonyl hydrazides, azo compounds and the like, and more specifically, P, P′-oxybis (benzenesulfonyl hydrazide), azodicarbonamide, dinitrosopentamethylenetetramine and the like. used. Among them, it is preferable to use a sulfonyl-hydrazide-based blowing agent which has a relatively small effect of accelerating vulcanization and has no harmful decomposition gas. The amount of rubber added is 100
It is preferably 3 to 5 parts by weight based on parts by weight. If the amount is less than 3 parts by weight, sufficient foaming cannot be obtained, and weight reduction and softening cannot be achieved. On the other hand, if it exceeds 5 parts by weight, foaming becomes excessive, and deformation occurs during molding.

【0020】架橋剤として有機過酸化物を使用すること
は可能である。有機過酸化物としては、具体的にはジ−
t−ブチルパーオキサイド、ジクミルパーオキサイド、
t−ブチルクミルパーオキサイド、1.1−t−ブチル
ペロキシ−3.3.5−トリメチルシクロヘキサン、
2.5−ジ−メチル−2.5−ジ(t−ブチルペロキ
シ)ヘキサン、2.5−ジ−メチル−2.5−ジ(t−
ブチルペロキシ)ヘキサン−3、ビス(t−ブチルペロ
キシジ−イソプロピル))ベンゼン、2.5−ジ−メチ
ル−2.5−ジ(ベンゾイルペロキシ)ヘキサン、t−
ブチルペロキシベンゾアート、t−ブチルペロキシ−2
−エチル−ヘキシルカーボネートなどが用いられる。そ
の配合量は、好ましくはゴム100重量部に対して0.
2〜10重量部とする。0.2重量部未満であると架橋
が十分に行われず、10重量部を超えると十分な弾性が
得られなくなる。
It is possible to use organic peroxides as crosslinking agents. As the organic peroxide, specifically, di-
t-butyl peroxide, dicumyl peroxide,
t-butylcumyl peroxide, 1.1-t-butylperoxy-3.3.5-trimethylcyclohexane,
2.5-di-methyl-2.5-di (t-butylperoxy) hexane, 2.5-di-methyl-2.5-di (t-
Butylperoxy) hexane-3, bis (t-butylperoxydi-isopropyl)) benzene, 2.5-di-methyl-2.5-di (benzoylperoxy) hexane, t-
Butylperoxybenzoate, t-butylperoxy-2
-Ethyl-hexyl carbonate and the like are used. The compounding amount is preferably 0.1 to 100 parts by weight of rubber.
2 to 10 parts by weight. If the amount is less than 0.2 parts by weight, crosslinking is not sufficiently performed, and if it exceeds 10 parts by weight, sufficient elasticity cannot be obtained.

【0021】また、有機過酸化物による架橋効率を高め
るため公知の共架橋剤(TAIC、TAC、マレイミ
ド、キノンジオキシム、トリメチロールプロパントリメ
タクリレート、硫黄など)等を併用しても良い。
Known co-crosslinking agents (TAIC, TAC, maleimide, quinone dioxime, trimethylolpropane trimethacrylate, sulfur, etc.) and the like may be used in combination in order to increase the crosslinking efficiency with organic peroxides.

【0022】加硫促進剤としては、グアニジン系、チウ
ラム系、ジチオカルバミン酸塩系、チアゾール系、スル
フェンアミド系等の有機加硫促進剤が挙げられる。更に
具体的には、N−シクロヘキシルベンゾチアジルスルフ
ェンアミド、N,N−ジエチル・2−ベンゾチアジルス
ルフェンアミド、2−メルカプトベンゾチアゾール、2
−メルカプトチアゾリン、2−メルカプトイミダゾリ
ン、ジフェニル・グアニジン、トリフェニル・グアニジ
ン、チオハイドロピリジン、Zn−ジメチル・ジチオカ
ーバメート、Zn−ジエチル・ジチオカーバメート、テ
トラメチルチウラム・モノスルフィド、テトラメチルチ
ウラム・ジスルフィド等があげられる。これら加硫促進
剤は単独で使用してもよいし、2種以上の組み合わせで
使用してもよい。但し、該ゴムに発泡剤を添加する際
は、遅効性促進効果のある加硫促進剤を添加することが
好ましい。具体的にはスルフェンアミド系加硫促進剤が
使用が好ましい。先に述べたように、該ゴムは不純物の
なかに加硫剤や加硫促進剤といった配合剤を含むため、
加硫が速くなる傾向がある。しかしスルフェンアミド系
加硫促進剤を使用することで、加硫開始とともに起こる
急速な粘度上昇を阻止して、加硫誘導期間を長く保つと
共に、発泡剤にスルホニル・ヒドラジド系を使用した場
合は発泡剤の分解温度を低下させる効果が得られる。そ
の添加量は0.5〜3重量部が適当である。0.5重量
部未満の場合は充分な加硫誘導時間が得られず発泡不足
となり、3重量部を超えると加硫反応を阻害する。また
無水フタル酸やN−シクロヘキシルチオフタルイミド等
のスコーチリターダの使用も可能である。
Examples of the vulcanization accelerator include guanidine-based, thiuram-based, dithiocarbamate-based, thiazole-based, and sulfenamide-based organic vulcanization accelerators. More specifically, N-cyclohexylbenzothiazylsulfenamide, N, N-diethyl-2-benzothiazylsulfenamide, 2-mercaptobenzothiazole,
-Mercaptothiazoline, 2-mercaptoimidazoline, diphenyl guanidine, triphenyl guanidine, thiohydropyridine, Zn-dimethyl dithiocarbamate, Zn-diethyl dithiocarbamate, tetramethylthiuram monosulfide, tetramethylthiuram disulfide, etc. can give. These vulcanization accelerators may be used alone or in combination of two or more. However, when adding a foaming agent to the rubber, it is preferable to add a vulcanization accelerator having a slow-acting effect. Specifically, it is preferable to use a sulfenamide vulcanization accelerator. As described above, since the rubber contains a compounding agent such as a vulcanizing agent or a vulcanization accelerator among impurities,
Vulcanization tends to be faster. However, by using a sulfenamide-based vulcanization accelerator, it is possible to prevent a rapid increase in viscosity that occurs with the start of vulcanization, maintain a long vulcanization induction period, and use a sulfonyl / hydrazide-based blowing agent. The effect of lowering the decomposition temperature of the foaming agent is obtained. The addition amount is suitably 0.5 to 3 parts by weight. If the amount is less than 0.5 part by weight, sufficient vulcanization induction time cannot be obtained, resulting in insufficient foaming. If the amount exceeds 3 parts by weight, the vulcanization reaction is inhibited. It is also possible to use scorch retarders such as phthalic anhydride and N-cyclohexylthiophthalimide.

【0023】充填剤としては、シリカ、クレー、炭酸カ
ルシウム等の無機充填材以外にも樹脂、コルク粉等の有
機充填材があるが、特に補強性を向上させるためにはカ
ーボンブラックを添加することが望ましい。
As the filler, besides inorganic fillers such as silica, clay and calcium carbonate, there are organic fillers such as resin and cork powder. In particular, carbon black is added to improve the reinforcing property. Is desirable.

【0024】上記充填材の分散性を向上させるために、
カップリング剤を使用しても良い。具体的にはビニルト
リメトキシシラン、3−メタクリロキシプロピルトリメ
トキシシラン、3−グリドキシプロピルトリメトキシシ
ラン、3−アミノピロピルトリメトキシシラン、3−メ
ルカプトプロピルトリメトキシシラン、ビス−(3−
(トリエトキシシリル)プロピル)テトラスルフィド等
のシランカップリング剤やN,N‘−ビス(2−メチル
−2−ニトロプロピル)−1,6−ジアミノヘキサン等
があげられる。
In order to improve the dispersibility of the filler,
A coupling agent may be used. Specifically, vinyltrimethoxysilane, 3-methacryloxypropyltrimethoxysilane, 3-glycoxypropyltrimethoxysilane, 3-aminopropylpropyltrimethoxysilane, 3-mercaptopropyltrimethoxysilane, bis- (3-
Examples thereof include silane coupling agents such as (triethoxysilyl) propyl) tetrasulfide and N, N'-bis (2-methyl-2-nitropropyl) -1,6-diaminohexane.

【0025】天然ゴムは主鎖に二重結合を有するジエン
系ゴムであるために、熱酸化、オゾン劣化、そして疲労
劣化といった老化を受けやすいため、老化防止剤を添加
することが望ましい。老化防止剤は限定されるものでな
いが、アミンケトン、ジアリルアミン、p−フェニレン
ジアミン等のアミン系老化防止剤、モノフェノール、ポ
リフェノール、ハイドロキノン等のフェノール系老化防
止剤、また硫黄化合物、ホスファイト類、トリブチルチ
オウレア等の2次老化防止剤、そしてオゾン劣化防止用
ワックス等が使用できる。
Since natural rubber is a diene rubber having a double bond in its main chain, it is susceptible to aging such as thermal oxidation, ozone deterioration, and fatigue deterioration. Therefore, it is desirable to add an antioxidant. The antioxidant is not limited, but amine antioxidants such as amine ketone, diallylamine, p-phenylenediamine, phenolic antioxidants such as monophenol, polyphenol and hydroquinone, sulfur compounds, phosphites, tributyl Secondary aging inhibitors such as thiourea, and waxes for preventing ozone deterioration can be used.

【0026】また該ゴムには、該ゴム以外のエラストマ
ー成分を配合することが可能である。具体的には水素化
ニトリルゴム、エチレン−α−オレフィンエラストマ
ー、クロロプレンゴム、クロロスルファ化ポリエチレ
ン、アルキル化クロロスルファ化ポリエチレン、天然ゴ
ム、スチレン・ブタジエンゴム、あるいはオレフィン
系、エステル系、ウレタン系の熱可塑性エラストマー等
が配合できる。
The rubber may contain an elastomer component other than the rubber. Specifically, hydrogenated nitrile rubber, ethylene-α-olefin elastomer, chloroprene rubber, chlorosulfurized polyethylene, alkylated chlorosulfurized polyethylene, natural rubber, styrene / butadiene rubber, or olefin, ester, or urethane thermoplastic elastomer Etc. can be blended.

【0027】該ゴムと配合剤を混練りする手段は限定す
るものでなく、例えばバンバリーミキサー、ロール、ニ
ーダー、そして押出機等の適宜公知の手段、方法によっ
て混練することができる。また加硫方法も限定されるも
のでなく、モールド加熱、熱空気加熱、回転ドラム式加
硫機、射出成形機等の加硫装置を用いた公知の手段で加
硫される。
The means for kneading the rubber and the compounding agent is not limited, and may be kneaded by any suitable means and method such as a Banbury mixer, a roll, a kneader, and an extruder. The vulcanization method is also not limited, and vulcanization is performed by a known method using a vulcanizing apparatus such as a mold heating, a hot air heating, a rotary drum vulcanizer, and an injection molding machine.

【0028】[0028]

【実施例】次に、実施例と比較例を挙げて更に具体的に
本発明の効果を説明する。 実施例1〜6、比較例1〜3 表2に示すムーニー粘度になるまで使用した夫々の不純
物除着天然ゴムに、表1に示す配合剤を添加し、バンバ
リーミキサーにて混練りした。尚、発泡剤については表
2に示す所定量を添加した。得られた上記ゴム組成物を
圧延し、150°Cで20分加硫した。
Next, the effects of the present invention will be described more specifically with reference to examples and comparative examples. Examples 1 to 6 and Comparative Examples 1 to 3 The compounding ingredients shown in Table 1 were added to each of the impurity-desorbed natural rubbers used until reaching the Mooney viscosity shown in Table 2, and kneaded with a Banbury mixer. In addition, about the foaming agent, the predetermined amount shown in Table 2 was added. The obtained rubber composition was rolled and vulcanized at 150 ° C. for 20 minutes.

【0029】[0029]

【表1】 [Table 1]

【0030】得られた上記加硫発泡ゴムシートについ
て、発泡成形性を評価し、比重と硬度を測定した。また
最大衝撃値の測定については、該加硫シートを厚さ2m
mの合板(表皮材)上に固定した後、高さ10cmから
荷重120g、直径30mmの金属球を落下させた。該
加硫シートを通じて下板に伝播した衝撃レベルを、合板
に取り付けた加速度ピックアップで測定し、高速フーリ
エ変換分析器(FFTアナライザー)で解析し最大衝撃
値を測定した。結果を表2に併記する。
With respect to the obtained vulcanized foamed rubber sheet, foam moldability was evaluated, and specific gravity and hardness were measured. For the measurement of the maximum impact value, the vulcanized sheet was 2 m thick.
After fixing on a plywood (skin material) of m, a metal ball having a load of 120 g and a diameter of 30 mm was dropped from a height of 10 cm. The impact level transmitted to the lower plate through the vulcanized sheet was measured by an acceleration pickup attached to the plywood, and analyzed by a high-speed Fourier transform analyzer (FFT analyzer) to measure the maximum impact value. The results are also shown in Table 2.

【0031】[0031]

【表2】 [Table 2]

【0032】上記表2の結果から、実施例1〜6の10
0°CでのML(1+4)が20〜40の不純物除着ゴムを
使用したゴム発泡組成物は、軽量かつ軟質だが、他方1
00°CでのML(1+4)が上記範囲外の比較例1,2は
硬度、比重共に高い。また、スルフェンアミド系加硫促
進剤を添加した実施例では、チアゾール系加硫促進剤を
添加した実施例2に比べ発泡が良く成形性の面で優れて
いる。但し、発泡剤を6重量部添加した実施例6は発泡
が過多となって、比重、硬度ともに低いものの成形性が
悪い。また、発泡剤を添加していない比較例3では比
重、硬度とも高く、目的の物性が得られない。
From the results shown in Table 2 above, 10
The rubber foam composition using the desorbing rubber having an ML (1 + 4) of 20 to 40 at 0 ° C. is lightweight and soft,
Comparative Examples 1 and 2 in which the ML (1 + 4) at 00 ° C. is out of the above range are high in both hardness and specific gravity. Further, in the example in which the sulfenamide-based vulcanization accelerator was added, foaming was good and the formability was excellent as compared with Example 2 in which the thiazole-based vulcanization accelerator was added. However, in Example 6 in which 6 parts by weight of the foaming agent was added, foaming was excessive, and although the specific gravity and hardness were low, the moldability was poor. In Comparative Example 3, in which no foaming agent was added, both the specific gravity and the hardness were high, and the desired physical properties could not be obtained.

【0033】[0033]

【発明の効果】以上のように本発明の請求項の発明によ
り、産業廃棄ゴムの有効利用と軽量かつ軟質なゴム発泡
組成物及びその製造方法の提供が可能になる。またスル
ホニル・ヒドラジド系発泡剤を使用することで更に環境
観点からも好ましく、特定の加硫促進剤の配合によりそ
の発泡性は優れたものになる。
As described above, according to the invention of the present invention, it is possible to effectively use industrial waste rubber, and to provide a lightweight and soft rubber foam composition and a method for producing the same. The use of a sulfonyl / hydrazide-based blowing agent is more preferable from an environmental point of view, and the addition of a specific vulcanization accelerator makes the foaming property excellent.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C08L 7/00 C08L 7/00 // C08L 7:00 7:00 Fターム(参考) 4F074 AA06 AB00 BA17 BA18 BB01 BB05 BB27 BB29 CA21 CA22 CC27X 4F301 AA04 AB01 BA22 CA04 CA09 CA32 CA71 4J002 AC011 DA048 EV216 EV277 FD148 FD157 FD326 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C08L 7/00 C08L 7/00 // C08L 7:00 7:00 F term (Reference) 4F074 AA06 AB00 BA17 BA18 BB01 BB05 BB27 BB29 CA21 CA22 CC27X 4F301 AA04 AB01 BA22 CA04 CA09 CA32 CA71 4J002 AC011 DA048 EV216 EV277 FD148 FD157 FD326

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 密閉式混練機内の不純物を除着したゴム
を主材としたゴム発泡組成物であって、主材ゴムは10
0°CでのML(1+4)が20〜40の天然ゴムであるこ
とを特徴とするゴム発泡組成物。
1. A rubber foam composition containing a rubber as a main material to which impurities in an internal mixer are removed, wherein the main rubber is 10%.
A rubber foam composition characterized by being a natural rubber having a ML (1 + 4) of 20 to 40 at 0 ° C.
【請求項2】 主材ゴムは、(イ)不純物の付着した密
閉式混練機に天然ゴムを投入し、(ロ)素練りし、
(ハ)不純物を除着した時点で天然ゴムを密閉式混練機
から取り出し、という(イ)〜(ハ)のサイクルを少な
くとも一回以上繰り返して、100°CでのML(1+4)
を20〜40に調節した天然ゴムである請求項1記載の
ゴム発泡組成物。
2. The main rubber is (a) natural rubber is charged into an internal mixer kneaded with impurities, and (b) masticated,
(C) When the impurities are desorbed, the natural rubber is taken out of the internal mixer, and the cycle of (a) to (c) is repeated at least once, and the ML (1 + 4) at 100 ° C.
The rubber foam composition according to claim 1, wherein the rubber foam composition is a natural rubber whose is adjusted to 20 to 40.
【請求項3】 加硫剤として硫黄が添加されている請求
項1または2記載のゴム発泡組成物。
3. The rubber foam composition according to claim 1, wherein sulfur is added as a vulcanizing agent.
【請求項4】 発泡剤は、スルホニル・ヒドラジド系発
泡剤である請求項1,2または3記載のゴム発泡組成物
4. The rubber foam composition according to claim 1, wherein the foaming agent is a sulfonyl hydrazide foaming agent.
【請求項5】 遅効性加硫促進剤が添加されている請求
項1,2,3または4記載のゴム発泡組成物。
5. The rubber foam composition according to claim 1, wherein a slow-acting vulcanization accelerator is added.
【請求項6】 遅効性加硫促進剤は、スルフェンアミド
系加硫促進剤である請求項1,2,3,4または5記載
のゴム発泡組成物。
6. The rubber foam composition according to claim 1, wherein the slow-acting vulcanization accelerator is a sulfenamide vulcanization accelerator.
【請求項7】 密閉式混練機内の不純物を除着したゴム
を主材としたゴム発泡組成物において、主材ゴムは
(イ)不純物の付着した密閉式混練機に天然ゴムを投入
し、(ロ)素練りし、(ハ)不純物を除着した時点で天
然ゴムを密閉式混練機から取り出し、という(イ)〜
(ハ)のサイクルを少なくとも一回以上繰り返して、1
00°CでのML(1+4)を20〜40に調節した天然ゴ
ムであって、該ゴム100重量部に対して、発泡剤とし
てスルホニル・ヒドラジド系発泡剤を3〜5重量部、加
硫促進剤としてスルフェンアミド系加硫促進剤を0.5
〜3重量部、架橋剤として硫黄を0.5〜10重量部添
加したことを特徴とするゴム発泡組成物。
7. A rubber foamed composition mainly composed of a rubber to which impurities have been desorbed in an internal mixer, (a) natural rubber is charged into an internal mixer to which impurities are attached, and B) masticating, and (c) removing the natural rubber from the internal kneading machine when the impurities are desorbed.
By repeating the cycle of (c) at least once or more, 1
A natural rubber whose ML (1 + 4) at 00 ° C is adjusted to 20 to 40, and 3 to 5 parts by weight of a sulfonyl / hydrazide foaming agent as a foaming agent is added to 100 parts by weight of the rubber. As a sulfur accelerator, a sulfenamide-based vulcanization accelerator of 0.5
1 to 3 parts by weight, and 0.5 to 10 parts by weight of sulfur as a crosslinking agent.
JP2000156271A 2000-05-26 2000-05-26 Rubber foaming composition using industrial waste rubber Pending JP2001335653A (en)

Priority Applications (1)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publication Number Publication Date
JP2001335653A true JP2001335653A (en) 2001-12-04

Family

ID=18661083

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2001335653A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112300462A (en) * 2020-11-26 2021-02-02 义乌市大胜橡塑制品有限公司 Disposable foaming pad and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112300462A (en) * 2020-11-26 2021-02-02 义乌市大胜橡塑制品有限公司 Disposable foaming pad and preparation method thereof

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