JPS6149338B2 - - Google Patents

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Publication number
JPS6149338B2
JPS6149338B2 JP11808377A JP11808377A JPS6149338B2 JP S6149338 B2 JPS6149338 B2 JP S6149338B2 JP 11808377 A JP11808377 A JP 11808377A JP 11808377 A JP11808377 A JP 11808377A JP S6149338 B2 JPS6149338 B2 JP S6149338B2
Authority
JP
Japan
Prior art keywords
group
parts
halogen
minutes
rubber
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
JP11808377A
Other languages
Japanese (ja)
Other versions
JPS5450550A (en
Inventor
Yoshiro Nakamura
Kunio Mori
Akira Umehara
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.)
Sankyo Kasei Co Ltd
Original Assignee
Sankyo Kasei 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 Sankyo Kasei Co Ltd filed Critical Sankyo Kasei Co Ltd
Priority to JP11808377A priority Critical patent/JPS5450550A/en
Publication of JPS5450550A publication Critical patent/JPS5450550A/en
Publication of JPS6149338B2 publication Critical patent/JPS6149338B2/ja
Granted legal-status Critical Current

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Description

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

本発明は含ハロゲンポリマーとジエン系ゴムを
同一加硫系で共加硫する方法に関する。 含ハロゲンポリマーとジエン系ゴムとの混合物
の共加硫は、ジエン系ゴムの耐油性、耐オゾン
性、耐熱性を改良できることから重要である。し
かし、含ハロゲンポリマーとジエン系ゴムとは加
硫上全く相反する反応性を有しその反応部分が異
なるため、これらの高分子混合物を同一硫系でか
つ同一条件で加硫することは困難であつた。即
ち、含ハロゲンポリマーは分子内のC―X(Xは
ハロゲンを表わす)がその反応部分であり加硫剤
の求核置換反応によつて加硫されるが、ジエン系
ゴムでは分子内のC=Cが反応部分であり加硫剤
のラジカル付加反応によつて加硫される。従つて
これらの高分子物質を同時に加硫するには同一条
件下でC−XとC=C結合に同時に反応しかつ近
似した加硫速度を有する加硫剤を用いることが必
要である。 上記のような2種の反応を1つの化合物により
起させるためには、一方の官能部がC−Xと求核
置換反応し、他方の官能部がC=Cにラジカル付
加する様な二官能性の加硫剤が望ましいが、一種
の化合物で斯かる目的を達するものは見出し得な
い。本発明者らは鋭意研究の結果、下記に詳述す
る2―置換―4.6―ジチオール―s―トリアジン
の少なくとも1種及び分子内に―N=N―基,―
S―S―基または―S―N―基を含む化合物の少
なくとも1種を共存させることにより、含ハロゲ
ンポリマーとジエン系ゴムとの混合物を同時に加
硫しうることを見出し本発明を完成するに到つ
た。 本発明に係る加硫方法を適用しうる含ハロゲン
ポリマーはポリ塩化ビニル、エビクロルヒドリン
重合体、フツ素ゴム及びクロルスルホン化ポリエ
チレンである。 またジエン系ゴムとは、ジエン構造を有する単
量体を含有する重合体および共重合体からなるゴ
ムであり、ポリブタジエンゴム、スチレン―ブタ
ジエン共重合ゴム、アクリルニトリル―ブタジエ
ンゴム、クロロプレンゴム、イソプレンゴム、プ
ロピレン―ブタジエンゴムなどを代表例として挙
げることができる。 本発明に用いる第1群の化合物は次式 〔ただし、RはSR′又はNR′,R″,R′および
R″は同一又は相異つて水素原子、アルキル基
(炭素数1〜4)又はフエニル基;Mは水素原
子、Na,K,Li,1/2Ca,1/2Mg,1/2Ba,1/2
Sr,1/2Zn,1/2Ni又は1/2Cuを表わす〕 で示される2―置換―4,6―ジチオール―s―
トリアジン誘導体である。 該トリアジンチオール誘導体の添加量は特に限
定されないが、含ハロゲンポリマーとジエン系ゴ
ムとの混合物100部(重量基準;以下同様とす
る)に対し、通常0.1〜10部、好ましくは0.5〜5
部の添加量で充分有効である。10部以上多量に添
加しても架橋密度が増大するのみで有害ではな
い。 本発明に用いる第2群の化合物、即ち分子内に
―N=N―,―S―S―基又は―N―S―基を有
する化合物とは、 NH2OCN=NCONH2 で示される化合物をいう。これらの化合物の少な
くとも1種を通常含ハロゲンポリマーとジオエン
系ゴムとの混合物100部に対し0.1〜5部添加す
る。5部より多量に添加すると含ハロゲンポリマ
ーの中には加硫しないものもある。然しながら、
CHC(エピクロルヒドリン―エチレンオキシド
共重合ゴム)の様に加硫性が高い場合には5部以
上添加しても有効であり、添加量を一義的に定め
ることはできない。 本発明において、含ハロゲンポリマーとジエン
系ゴムとの混合割合は一方の含有量が少量であつ
ても両者が混合される限り特に限定されないが、
通常重量比で1:9〜9:1の範囲で混合され
る。 本発明に用いる上記2―置換―4,6―ジチオ
ール―s―トリアジン誘導体は含ハロゲンポリマ
ーに対する架橋剤として既に使用されつつある
が、ジエン系ゴムに対しては該誘導体単独では実
質上架橋反応は進行しない。従つて含ハロゲンポ
リマーとジエン系ゴムとの混合物に該トリアジン
誘導体のみを添加した場合には、含ハロゲンポリ
マーのみ加硫されるが、ジエン系ゴムとの共加硫
は起らない。一方上記第2群の化合物はジエン系
ゴムをイオウ加硫する際の加硫助剤として用いら
れるものもあるが、一般に架橋反応が緩慢で該化
合物単独の使用では実用上有効な加硫効果は得ら
れない。 しかるに本発明に依り、上記第1群の2―置換
―4,6―ジチオール―s―トリアジン誘導体及
び第2群の―N=N―基、―S―S―基又は―N
―S―基を含む化合物を共存せしめると、その何
らかの相互作用によつてイオウと全く使用するこ
となく加硫反応は著しく促進され効率良く進行す
ると共に、優れた物性を有する共加硫物が得られ
ることが見出された。 本発明に依り、含ハロゲンポリマーとジエン系
ゴムからなる混合物を、上記第1群の化合物の少
なくとも1種及び第2群の化合物の少なくとも1
種の存在下に、一般には150〜200℃、好ましくは
160〜180℃で20〜50分加熱することによりすぐれ
た物性を有する共加硫物が得られる。 なお本発明において上記第1群及び第2群の化
合物と共に、一般に含ハロゲンポリマーおよびジ
エン系ゴムに使用される各種の添加剤を添加する
ことができる。特にMgO,CaO,ZnO,BaO,
SrOなどの金属酸化物を0.2〜10部添加すること
が好ましく、これらの添加によつて加硫反応が著
るしく促進される。また含ハロゲンポリマーに通
常添加される金属石ケン、有機スズ安定剤、エポ
キシ系安定剤、リン酸エステル系安定剤、可塑
剤、CaCO3,TiO2、カーボンなどの充填剤;ジ
エン系ゴムに添加されるステアリン酸アミン系老
化防止剤、フエノール系老化防止剤、加工助剤な
どを必要に応じ適宜配合することができる。 以下本発明を実施例によつて説明する。なお
「部」は別記しない限りすべて「重量部」を意味
するものとする。 実施例1〜3及び比較例1〜2 SBR(ニポール1502、日本ゼオン社製)及びポ
リ塩化ビニル(103EP、日本ゼオン社製)を第1
表に記載の配合割合で合計100部、安定剤フエロ
ー675C(日産フエロー社製)2部を、175℃で10
分間ロールブレンドする。これに第1表記載の
DB4部及びDM2部ならびにZnO2部、MgO5部、
ステアリン酸1部、アンテージW―300(4,
4′―ブチリデン・ビス(6―ターシヤリー、ブチ
ル―m―クレゾール,老化防止剤、川口化学工業
社製)2部を加え100℃で10分間ブレンドする。
得られた混練物を180℃で20分間プレスし、共加
硫物を得た。加硫物試料0.2gをシクロヘキサノ
ン20mlに投入し、50℃で24時間保持した後不溶分
を測定し、その結果を第1表に記載する。 不溶率=処理後不溶分重量/処理前試料重量×100(
%)
The present invention relates to a method of co-vulcanizing a halogen-containing polymer and a diene rubber in the same vulcanization system. Co-vulcanization of a mixture of a halogen-containing polymer and a diene rubber is important because it can improve the oil resistance, ozone resistance, and heat resistance of the diene rubber. However, halogen-containing polymers and diene-based rubbers have completely contradictory reactivities during vulcanization and their reactive parts are different, so it is difficult to vulcanize these polymer mixtures using the same sulfur system and under the same conditions. It was hot. That is, in a halogen-containing polymer, C-X (X represents a halogen) in the molecule is the reactive moiety and is vulcanized by a nucleophilic substitution reaction of a vulcanizing agent, but in diene rubber, the C-X in the molecule =C is a reactive moiety and is vulcanized by radical addition reaction of a vulcanizing agent. Therefore, in order to simultaneously vulcanize these polymeric materials, it is necessary to use a vulcanizing agent that simultaneously reacts with C-X and C=C bonds under the same conditions and has similar vulcanization rates. In order to cause the above two types of reactions with one compound, it is necessary to use a difunctional compound in which one functional part undergoes a nucleophilic substitution reaction with C-X, and the other functional part undergoes a radical addition to C=C. Although a specific vulcanizing agent is desirable, no single compound has been found to achieve this goal. As a result of intensive research, the present inventors found that at least one kind of 2-substituted-4,6-dithiol-s-triazine detailed below and -N=N- group, -
The present invention was accomplished by discovering that a mixture of a halogen-containing polymer and a diene rubber can be simultaneously vulcanized by coexisting at least one compound containing an S—S— group or a —S—N— group. It has arrived. Halogen-containing polymers to which the vulcanization method of the present invention can be applied include polyvinyl chloride, shrimp chlorohydrin polymer, fluorocarbon rubber, and chlorosulfonated polyethylene. Diene rubbers are rubbers made of polymers and copolymers containing monomers having a diene structure, such as polybutadiene rubber, styrene-butadiene copolymer rubber, acrylonitrile-butadiene rubber, chloroprene rubber, and isoprene rubber. , propylene-butadiene rubber, etc. can be cited as representative examples. The first group of compounds used in the present invention has the following formula: [However, R is SR′ or NR′, R″, R′ and
R'' are the same or different hydrogen atom, alkyl group (1 to 4 carbon atoms), or phenyl group; M is hydrogen atom, Na, K, Li, 1/2Ca, 1/2Mg, 1/2Ba, 1/2
Represents Sr, 1/2Zn, 1/2Ni or 1/2Cu] 2-Substituted-4,6-dithiol-s-
It is a triazine derivative. The amount of the triazinethiol derivative added is not particularly limited, but it is usually 0.1 to 10 parts, preferably 0.5 to 5 parts, per 100 parts (by weight; the same shall apply hereinafter) of the mixture of halogen-containing polymer and diene rubber.
It is sufficiently effective with the addition amount of 50%. Adding a large amount of 10 parts or more only increases the crosslinking density and is not harmful. The second group of compounds used in the present invention, that is, compounds having -N=N-, -S-S-, or -N-S- groups in the molecule, are: NH 2 OCN=NCONH 2 , A compound represented by At least one of these compounds is usually added in an amount of 0.1 to 5 parts per 100 parts of the mixture of the halogen-containing polymer and the diene rubber. If more than 5 parts are added, some halogen-containing polymers may not be vulcanized. However,
In the case of highly vulcanizable rubber such as CHC (epichlorohydrin-ethylene oxide copolymer rubber), it is effective to add 5 parts or more, and the amount to be added cannot be determined unambiguously. In the present invention, the mixing ratio of the halogen-containing polymer and diene rubber is not particularly limited as long as both are mixed even if the content of one is small.
They are usually mixed in a weight ratio of 1:9 to 9:1. The above-mentioned 2-substituted-4,6-dithiol-s-triazine derivative used in the present invention is already being used as a crosslinking agent for halogen-containing polymers, but the derivative alone does not substantially cause crosslinking reaction for diene rubber. It doesn't progress. Therefore, when only the triazine derivative is added to a mixture of a halogen-containing polymer and a diene rubber, only the halogen-containing polymer is vulcanized, but co-vulcanization with the diene rubber does not occur. On the other hand, some of the compounds in the second group mentioned above are used as vulcanization aids when sulfur vulcanization of diene rubber is carried out, but the crosslinking reaction is generally slow and the use of these compounds alone does not have a practically effective vulcanization effect. I can't get it. However, according to the present invention, the 2-substituted-4,6-dithiol-s-triazine derivatives of the first group and the -N=N- group, -S-S- group, or -N
When a compound containing an -S- group is allowed to coexist, the vulcanization reaction is significantly promoted and proceeds efficiently due to some kind of interaction between them, without using any sulfur, and a co-vulcanizate with excellent physical properties can be obtained. It was found that According to the present invention, a mixture consisting of a halogen-containing polymer and a diene rubber is mixed with at least one of the compounds of the first group and at least one of the compounds of the second group.
In the presence of seeds, generally 150-200°C, preferably
A co-vulcanizate with excellent physical properties can be obtained by heating at 160-180°C for 20-50 minutes. In the present invention, various additives generally used for halogen-containing polymers and diene rubbers can be added together with the compounds of the first and second groups. Especially MgO, CaO, ZnO, BaO,
It is preferable to add 0.2 to 10 parts of a metal oxide such as SrO, and the addition of these metals significantly accelerates the vulcanization reaction. Also, fillers such as metal soaps, organotin stabilizers, epoxy stabilizers, phosphate ester stabilizers, plasticizers, CaCO 3 , TiO 2 , and carbon, which are usually added to halogen-containing polymers; added to diene rubbers. Stearic acid amine type anti-aging agents, phenol type anti-aging agents, processing aids, etc. can be appropriately blended as necessary. The present invention will be explained below with reference to Examples. All "parts" mean "parts by weight" unless otherwise specified. Examples 1 to 3 and Comparative Examples 1 to 2 SBR (Nipole 1502, manufactured by Nippon Zeon Co., Ltd.) and polyvinyl chloride (103EP, manufactured by Nippon Zeon Co., Ltd.) were
A total of 100 parts and 2 parts of the stabilizer Ferro 675C (manufactured by Nissan Ferro Co., Ltd.) were added at the mixing ratio shown in the table for 10 minutes at 175℃.
Roll blend for a minute. Add to this the information listed in Table 1.
4 parts of DB, 2 parts of DM, 2 parts of ZnO, 5 parts of MgO,
1 part stearic acid, Antige W-300 (4,
Add 2 parts of 4'-butylidene bis (6-tertiary, butyl-m-cresol, anti-aging agent, manufactured by Kawaguchi Kagaku Kogyo Co., Ltd.) and blend for 10 minutes at 100°C.
The obtained kneaded product was pressed at 180°C for 20 minutes to obtain a co-vulcanized product. 0.2 g of the vulcanizate sample was added to 20 ml of cyclohexanone, held at 50°C for 24 hours, and the insoluble matter was measured. The results are listed in Table 1. Insoluble rate = weight of insoluble matter after treatment / weight of sample before treatment x 100 (
%)

【表】 SBR及びPVCは共にシクロヘキサノンに溶解
するので、共加硫物をシクロヘキサノン中で処理
した場合に、不溶率が低ければ共加硫していない
ことになる。第1表の結果によりDB及びDMを共
存させた実施例1〜3においては不溶率が高く従
つて共加硫物が得られたことは明らかである。こ
れに対しDBのみを添加した比較例1においては
PVCのみ反応するがSBRは反応しないため不溶
率は50%以下であり、DMのみ添加した比較例2
ではSBR,PVC共に殆んど反応せず不溶率は著
しく低く、何れの場合にも共加硫は実際上起つて
いないことを示している。 実施例 4〜11 CR(クロロプレンゴム、昭和ネオプレン社製
W―タイプ)及びPVC(日本ゼオン社製、
103EP)を第2表記載の配合割合で計100部に安
定剤(東京フアインケミカル社製、RP―101,ス
テアリン酸亜鉛,ステアリン酸バリウム及びステ
アリン酸カルシウム複合体)3部を加え、160℃
で10分間ロールブレンドする。これに第2表記載
の配合剤及びMgO5部、アンテージ(W―300)
2部を加えて、60〜70℃で5分間ロールブレンド
し、得られた混練物を170℃で20分間プレスして
共加硫物を得た。 共加硫物試料をテトラヒドロフラン(THFと
略記する)(PVC,CRともによく溶ける)中で、
40℃、24時間処理後の不溶率を測定した結果を第
2表に示す。何れも不溶率は高く共加硫が進んで
いることが認められる。
[Table] Both SBR and PVC dissolve in cyclohexanone, so when a co-vulcanized product is treated in cyclohexanone, if the insolubility is low, it means that they are not co-vulcanized. From the results shown in Table 1, it is clear that in Examples 1 to 3 in which DB and DM were co-existing, the insolubility was high and co-vulcanizates were obtained. On the other hand, in Comparative Example 1 in which only DB was added,
Since only PVC reacts but SBR does not, the insolubility rate is less than 50%, and Comparative Example 2 in which only DM was added
In both SBR and PVC, there was almost no reaction and the insolubility rate was extremely low, indicating that co-vulcanization did not actually occur in either case. Examples 4 to 11 CR (chloroprene rubber, W-type manufactured by Showa Neoprene Co., Ltd.) and PVC (manufactured by Nippon Zeon Co., Ltd.,
103EP) at the mixing ratio shown in Table 2, 3 parts of a stabilizer (manufactured by Tokyo Fine Chemical Co., Ltd., RP-101, zinc stearate, barium stearate, and calcium stearate complex) was added to a total of 100 parts, and the mixture was heated at 160°C.
Roll blend for 10 minutes. Add to this the compounding agents listed in Table 2, 5 parts of MgO, and Antige (W-300).
2 parts were added and roll blended at 60 to 70°C for 5 minutes, and the resulting kneaded product was pressed at 170°C for 20 minutes to obtain a co-vulcanized product. A co-vulcanizate sample was placed in tetrahydrofuran (abbreviated as THF) (PVC and CR both dissolve well).
Table 2 shows the results of measuring the insolubility after treatment at 40°C for 24 hours. In all cases, it is recognized that the insolubility rate is high and co-vulcanization is progressing.

【表】 実施例 12〜23 NBR(日本ゼオン社製、ニポール1041)、PVC
(日本ゼオン社製、ゼオン121)及び安定剤として
RP101ターシヤリー・ブチルカテコール(TBCと
略記する)、及び4,4′―チオビス(6―ターシ
ヤリー・ブチル―m―クレゾール(川口化学工業
社製、アンテージRC)をそれぞれ第3表記載の
配合割合で下記の如くしてブレンドする。 NBRを2インチロールに巻きつけ、これに微
粒粉末PVCと安定剤を加えて90℃で15分間ロー
ルブレンドする。斯くして得られたブレンド物10
部に、更に第3表記載の配合剤を加えて更にロー
ルブレンドしてブレンドシートとする。 このシートを170℃で30分間プレスして厚さ0.1
mmと1mmの共加硫物シートを得る。0.1mmのシー
トにつきTHF不溶率と膨潤度の、1mmシートに
つき物性の測定を行いその結果を第4表に示す。
[Table] Examples 12 to 23 NBR (manufactured by Nippon Zeon Co., Ltd., Nipole 1041), PVC
(Nippon Zeon Co., Ltd., Zeon 121) and as a stabilizer
RP101 tertiary butylcatechol (abbreviated as TBC) and 4,4′-thiobis(6-tertiary butyl-m-cresol (manufactured by Kawaguchi Kagaku Kogyo Co., Ltd., Antage RC) are each mixed in the following proportions as shown in Table 3. Blend as follows. Wrap NBR on a 2-inch roll, add fine powder PVC and stabilizer to it, and roll blend at 90°C for 15 minutes. The blend 10 thus obtained
The ingredients listed in Table 3 are further added to the mixture, and the mixture is further roll blended to form a blend sheet. This sheet was pressed at 170℃ for 30 minutes to a thickness of 0.1
Co-vulcanizate sheets of mm and 1 mm are obtained. The THF insolubility and swelling degree of a 0.1 mm sheet and the physical properties of a 1 mm sheet were measured and the results are shown in Table 4.

【表】【table】

【表】【table】

【表】 実施例24〜27及び比較例1〜2 第5表に記載の配合割合で実施例12〜23と同様
にして作成したブレンドシートを170℃で45分間
プレスして厚さ1mmの共加硫物シートを得、これ
らの試料の永久歪と耐油性を測定した結果を第5
表に示す。
[Table] Examples 24 to 27 and Comparative Examples 1 to 2 Blend sheets prepared in the same manner as Examples 12 to 23 with the blending ratios listed in Table 5 were pressed at 170°C for 45 minutes to form a 1 mm thick sheet. Vulcanizate sheets were obtained, and the results of measuring the permanent set and oil resistance of these samples were reported in the fifth section.
Shown in the table.

【表】 実施例 28〜31 第6表中のA群の配合を80〜100℃で30分間ブ
レンドし、NBRコンパウンドを調製する。 一方、第6表中のB群の配合をPVCの場合170
℃,10分、他は80℃30分間ブレンドして、含塩素
ゴムコンパウンドとする。さらに、両者を170℃
で20分(PVCのとき)又は100℃で30分間ブレン
ドして、共ブレンド物を得る。これを170℃で40
分間加熱して共加硫物を得た。 共加硫物試料をTHF(NBR及び含ハロゲンポ
リマーはよくとける)中で40℃48時間処理後の不
溶率を測定した結果を第6表に示す。
[Table] Examples 28-31 NBR compounds are prepared by blending the formulations of Group A in Table 6 at 80-100°C for 30 minutes. On the other hand, in the case of PVC, the composition of Group B in Table 6 is 170
℃ for 10 minutes, and others at 80℃ for 30 minutes to make a chlorine-containing rubber compound. Furthermore, both were heated to 170℃.
Blend for 20 minutes at 100°C (for PVC) or 30 minutes at 100°C to obtain a co-blend. This was heated to 170℃ for 40 minutes.
A co-vulcanizate was obtained by heating for a minute. Table 6 shows the results of measuring the insolubility of co-vulcanizate samples after treating them at 40° C. for 48 hours in THF (NBR and halogen-containing polymers dissolve easily).

【表】【table】

【表】【table】

【表】 加硫物中のゴム含量
[Table] Rubber content in vulcanizate

Claims (1)

【特許請求の範囲】 1 ポリ塩化ビニル、クロルスルホン化ポリエチ
レン又はフツ素ゴムとジエン系ゴムからなる混合
物を (1) 次式 〔ただし、RはSR′又はNR′R″,R′および
R″は同一又は相異つて水素原子、アルキル基
(炭素数1〜4)又はフエニル基;Mは水素原
子、Ma,K,Li,1/2Ca、1/2Mg,1/2Ba,1/
2Sr,1/2Zn,1/2Ni又は1/2Cuを表わす〕 で示される2―置換―4,6―ジチオール―s
―トリアジン誘導体の少なくとも1種及び (2) NH2OCN=NCONH2 及び からなる群から選ばれた分子内に―N=N―,
―S―基又は―N―S―基を含む化合物の少な
くとも1種 の存在下に加熱することを特徴とする含ハロゲン
ポリマーとジエン系ゴムの共加硫方法。
[Scope of Claims] 1 A mixture of polyvinyl chloride, chlorosulfonated polyethylene, or fluororubber and diene rubber is represented by (1) the following formula: [However, R is SR′ or NR′R″, R′ and
R'' are the same or different hydrogen atom, alkyl group (1 to 4 carbon atoms), or phenyl group; M is hydrogen atom, Ma, K, Li, 1/2Ca, 1/2Mg, 1/2Ba, 1/
2-substituted-4,6-dithiol-s represented by 2Sr, 1/2Zn, 1/2Ni or 1/2Cu]
-At least one triazine derivative and (2) NH 2 OCN=NCONH 2 , as well as -N=N-, in a molecule selected from the group consisting of
A method for co-vulcanizing a halogen-containing polymer and a diene rubber, the method comprising heating in the presence of at least one compound containing an -S- group or an -N-S- group.
JP11808377A 1977-09-30 1977-09-30 Coovulcanizing method of halogenncontaing polymer and diene rubber Granted JPS5450550A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11808377A JPS5450550A (en) 1977-09-30 1977-09-30 Coovulcanizing method of halogenncontaing polymer and diene rubber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11808377A JPS5450550A (en) 1977-09-30 1977-09-30 Coovulcanizing method of halogenncontaing polymer and diene rubber

Publications (2)

Publication Number Publication Date
JPS5450550A JPS5450550A (en) 1979-04-20
JPS6149338B2 true JPS6149338B2 (en) 1986-10-29

Family

ID=14727566

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11808377A Granted JPS5450550A (en) 1977-09-30 1977-09-30 Coovulcanizing method of halogenncontaing polymer and diene rubber

Country Status (1)

Country Link
JP (1) JPS5450550A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5943045A (en) * 1982-09-06 1984-03-09 Shin Etsu Chem Co Ltd Vinyl chloride resin composition
JPS62179560A (en) * 1986-02-03 1987-08-06 Nippon Zeon Co Ltd Rubber mixture
EP1748054A4 (en) * 2004-05-17 2008-11-19 Daikin Ind Ltd Thermoplastic polymer composition
JP4867311B2 (en) * 2004-11-24 2012-02-01 ダイソー株式会社 Composition for vulcanized rubber and vulcanized product thereof

Also Published As

Publication number Publication date
JPS5450550A (en) 1979-04-20

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