JP2537906B2 - Fluorine rubber composition for vulcanization adhesion - Google Patents

Fluorine rubber composition for vulcanization adhesion

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Publication number
JP2537906B2
JP2537906B2 JP62263956A JP26395687A JP2537906B2 JP 2537906 B2 JP2537906 B2 JP 2537906B2 JP 62263956 A JP62263956 A JP 62263956A JP 26395687 A JP26395687 A JP 26395687A JP 2537906 B2 JP2537906 B2 JP 2537906B2
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Japan
Prior art keywords
weight
parts
rubber
vulcanization
adhesion
Prior art date
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JP62263956A
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Japanese (ja)
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JPH01108246A (en
Inventor
直喜 森田
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EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は加硫接着剤用組成物に関し、詳しくは金属と
の接着性を改良した加硫接着用フツ素ゴム組成物に関す
る。
Description: TECHNICAL FIELD The present invention relates to a composition for vulcanizing adhesives, and more particularly to a fluororubber composition for vulcanizing adhesion with improved adhesion to metal.

〔従来技術と問題点〕[Conventional technology and problems]

ポリオール加硫系のフツ素ゴムとしては、ビニリデン
フルオライド(VdF)/ヘキサフルオロプロピレン(HF
P)系及びビニリデンフルオライド/ヘキサフルオロプ
ロピレン/テトラフルオロエチレン(TFE)系等があ
る。このポリオール加硫系のフツ素ゴムは特に高温時の
圧縮永久歪性に優れており、各種多様なゴム製品として
使用されている。その中でもゴムと金属を接着させたオ
イルシール等の複合材料として使われるケースが多い。
しかしながらフツ素ゴムは他の汎用ゴムと比較して金属
との接着性の面で劣つており、金属との接着がうまく行
なわれず製品の不良率が高い。
Vinylidene fluoride (VdF) / hexafluoropropylene (HF
P) type and vinylidene fluoride / hexafluoropropylene / tetrafluoroethylene (TFE) type. This polyol vulcanized fluororubber is particularly excellent in compression set at high temperature and is used as various rubber products. Among them, it is often used as a composite material such as an oil seal in which rubber and metal are adhered.
However, fluorine rubber is inferior to other general-purpose rubbers in terms of adhesiveness to metal, and adhesion to metal is not performed well, resulting in a high defective rate of products.

従来、プライマーを用いて低活性な酸化マグネシウム
を多量(約15重量部)配合する方法が提案(デユポンカ
タロクVT450.1)されている。しかしながら従来の市販
フツ素ゴムより高分子量のフツ素ゴムに対しては低活性
の酸化マグネシウムの配合では充分な接着性が得られな
い。
Hitherto, a method has been proposed (Dyupon Cataloc VT450.1) in which a large amount (about 15 parts by weight) of low-activity magnesium oxide is blended using a primer. However, with a fluorine rubber having a higher molecular weight than that of a conventional commercially available fluorine rubber, sufficient adhesiveness cannot be obtained by compounding low-activity magnesium oxide.

〔問題点解決の手段〕[Means for solving problems]

本発明の目的は従来の市販フツ素ゴムより耐熱性、圧
縮永久歪性耐油性等に優れた高分子量タイプのフツ素ゴ
ムと金属の加硫接着性を改良した加硫接着用フツ素ゴム
組成物を提供することにある。
The object of the present invention is to provide a fluorine rubber composition for vulcanization adhesion which has improved vulcanization adhesion between a high molecular weight fluorine rubber and a metal, which are superior in heat resistance, compression set oil resistance, etc. to conventional commercially available fluorine rubber. To provide things.

本発明は フツ素含量が63.5〜71重量%、極限粘度〔η〕(測定
溶媒メチルエチルケトン、測定温度35℃)が100〜250
(ml/g)、分子量5万以下のフラクシヨンの含量(M5
が5重量%以下、かつ分子量100万以上のフラクシヨン
の含量(M100)が10〜35重量%であるフツ素ゴム100重
量部、 ポリオール加硫材0.1〜10重量部、 ポリオール加硫促進剤0.05〜2重量部、 金属水酸化物1〜30重量部、 酸化マグネシウムの活性価が100(mg/g)以上であると
ころの高活性酸化マグネシウム5〜25重量部(好ましく
は10〜15重量部) からなる加硫接着用組成物を提供する。本発明に用いる
フツ素ゴムはフツ素含量が63.5〜71重量%、極限粘度数
(ml/g)が100〜250、分子量5万以下のクラクシヨンの
含量(分子量5万以下のポリマーの占める割合)(M5
が5重量%以下でありかつ分子量100万以上のフラクシ
ヨンの含量(M100)が10〜35重量%であるところのもの
である。
The present invention has a fluorine content of 63.5 to 71% by weight and an intrinsic viscosity [η] (measuring solvent methyl ethyl ketone, measuring temperature of 35 ° C.) of 100 to 250.
(Ml / g), content of fraction with molecular weight of 50,000 or less (M 5 )
Is less than 5% by weight, and the content of the fraction having a molecular weight of 1,000,000 or more (M 100 ) is 10 to 35% by weight, 100 parts by weight of fluorine rubber, 0.1 to 10 parts by weight of polyol vulcanizing material, and 0.05% of polyol vulcanization accelerator. ~ 2 parts by weight, 1 to 30 parts by weight of metal hydroxide, 5 to 25 parts by weight of highly active magnesium oxide (preferably 10 to 15 parts by weight) where the activity value of magnesium oxide is 100 (mg / g) or more A composition for vulcanization and adhesion comprising: The fluororubber used in the present invention has a fluorine content of 63.5 to 71% by weight, an intrinsic viscosity number (ml / g) of 100 to 250, and a content of claxion having a molecular weight of 50,000 or less (a ratio of a polymer having a molecular weight of 50,000 or less). (M 5 )
Is 5% by weight or less and the content (M 100 ) of the fraction having a molecular weight of 1,000,000 or more is 10 to 35% by weight.

本発明に用いるフツ素ゴムは、好ましくはビニルデン
フルオライド(VdF)単位およびヘキサフルオロプロピ
レン(HFP)単位を含有し、その和が65〜100重量%であ
り、テトラフルオロエチレン(TFE)単位を35〜0重量
%含有しビニリデンフルオライド単位とヘキサフルオロ
プロピレン単位との重量比が80:20〜40:60の範囲にあ
る。
The fluororubber used in the present invention preferably contains vinyldenfluoride (VdF) units and hexafluoropropylene (HFP) units, the sum of which is 65 to 100% by weight, and tetrafluoroethylene (TFE) units are included. It is contained in an amount of 35 to 0% by weight, and the weight ratio of vinylidene fluoride units to hexafluoropropylene units is in the range of 80:20 to 40:60.

本発明に適するフツ素ゴムおよびその製造法の詳細は
例えば特願昭62−112139号に記載されている。本発明の
フツ素ゴムの製造に適した重合法は懸濁重合法である。
本発明のフツ素ゴムを懸濁重合で製造する際の反応条件
としては例えば重合温度が50℃以上であり、触媒はジイ
ソプロピルパーオキシジカーボネートなどの炭化水素系
のパーオキシジカーボネートであり、触媒の添加方法と
しては一括仕込みを行い、重合時間は7〜18時間であ
る。重合圧力を高くすれば、重合時間は短縮することが
できる。フツ素ゴムの極限粘度数(ml/g)が100未満で
ある場合、混練作業でMgOやその他の配合物の分散性が
悪く、接着時の加硫状態が悪い為に接着不良を起こすこ
とが多い。またフツ素ゴムの極限粘度数(ml/g)が250
を越える場合、ポリマーの剛直性が増し、接着時に金属
との密着性が低下する(アンカー効果等が劣る。)こと
による接着不良が増加する。故に良好な加硫接着が得ら
れるフツ素ゴムとして極限粘度数(ml/g)が100〜250、
好ましくは120〜220であり、更にM5が5重量%以下、M
100が10〜35重量%、好ましくは15〜30重量%であるこ
とを満足すれば配合物の分散性やアンカー効果の低下の
問題が無くなり、接着性を高めることができる。
Details of the fluorine rubber suitable for the present invention and the method for producing the same are described in, for example, Japanese Patent Application No. 62-112139. A polymerization method suitable for producing the fluororubber of the present invention is a suspension polymerization method.
The reaction conditions for producing the fluororubber of the present invention by suspension polymerization include, for example, a polymerization temperature of 50 ° C. or higher, and the catalyst is a hydrocarbon-based peroxydicarbonate such as diisopropyl peroxydicarbonate. As a method of adding the above, batch charging is carried out, and the polymerization time is 7 to 18 hours. The polymerization time can be shortened by increasing the polymerization pressure. If the intrinsic viscosity number (ml / g) of fluorine rubber is less than 100, the dispersibility of MgO and other compounds during kneading may be poor, and the vulcanization state during bonding may be poor, resulting in poor adhesion. Many. In addition, the intrinsic viscosity of fluorocarbon rubber (ml / g) is 250
If it exceeds the range, the rigidity of the polymer increases, and the adhesion with the metal decreases during adhesion (the anchor effect and the like are poor), resulting in an increase in poor adhesion. Therefore, the intrinsic viscosity number (ml / g) is 100-250 as fluorocarbon rubber that can obtain good vulcanization adhesion.
It is preferably 120 to 220, M 5 is 5% by weight or less, M
When the content of 100 is 10 to 35% by weight, preferably 15 to 30% by weight, the problems of the dispersibility of the compound and the anchoring effect are eliminated, and the adhesiveness can be improved.

本発明に用いる高活性酸化マグネシウムはその活性価
〔酸化マグネシウム(以下MgO)1gが吸着するヨウ素のm
g数〕が100以上であるところの高活性酸化マグネシウム
であり、非常に大きな比表面積を持ち物理的化学的に非
常に活性なものである。具体的にはキヨーワマグ150
(協和化学工業(製))等がある。高活性酸化マグネシ
ウムを使用することにより、接着が改良される要因とし
て、超微粒子のMgOである為分散性が向上し加硫時にお
ける酸性ガスの受け入れ(中和)がスムーズに行なわ
れ、金属と接着剤及び接着剤とゴム間の密着性に悪影響
を及ぼさない為であろうと考えられる。
The highly active magnesium oxide used in the present invention has an activity value of 1 g of magnesium oxide (hereinafter referred to as MgO)
g number] is 100 or more, it is a highly active magnesium oxide, has a very large specific surface area, and is very physically and chemically active. Specifically, Kiyowamag 150
(Kyowa Chemical Industry Co., Ltd.) The reason why the adhesion is improved by using high activity magnesium oxide is that it is ultrafine particles of MgO, so the dispersibility is improved and the acid gas is smoothly received (neutralized) during vulcanization. It is considered that this is because the adhesive and the adhesion between the adhesive and the rubber are not adversely affected.

配合量はフツ素ゴム100重量部に対して5〜25重量部
好ましくは10〜15重量部の範囲とすることにより、金属
との加硫接着剤を著るしく改善することができる。上記
配合量より少ない場合、加硫接着性は極端に劣り製品の
不良率が高くなる。また上記配合量より多い場合、硬度
が高くなりそれによるプレス加硫時の流れが悪くなる。
物性面では伸びがなくなり、圧縮永久歪が極端に悪くな
る。以上のことより適正配合としてはフツ素ゴム100重
量部に対して5〜25重量部好ましくは10〜15部の範囲が
加硫接着性及び加硫物性において最もバランスがとれて
いる。配合処方としては、高活性酸化マグネシウム5〜
25重量部にさらに、低活性酸化マグネシウムを混ぜ合わ
せた系でも良い。
By setting the blending amount to be in the range of 5 to 25 parts by weight, preferably 10 to 15 parts by weight, based on 100 parts by weight of fluororubber, the vulcanization adhesive with metal can be significantly improved. If the amount is less than the above amount, the vulcanization adhesion is extremely poor and the defective rate of the product is high. On the other hand, if the amount is larger than the above amount, the hardness becomes high and the flow at the time of press vulcanization becomes worse.
In terms of physical properties, elongation is lost and compression set becomes extremely poor. From the above, as a proper compounding amount, the range of 5 to 25 parts by weight, preferably 10 to 15 parts by weight, relative to 100 parts by weight of fluororubber is most balanced in vulcanization adhesiveness and vulcanized physical properties. As a compounding recipe, highly active magnesium oxide 5 to
A system in which 25 parts by weight of low activity magnesium oxide is further mixed may be used.

本発明の組成物に用いる加硫剤は含フツ素ポリヒドロ
キシ化合物であり、2,2−ビス(4−ヒドロキシフエニ
ル)パーフルオロプロパン〔ビスフエノールAF〕、2,2
−ビス(4−ヒドロキシフエニル)パーフルオロプロパ
ン、2−(4′−ヒドロキシフエニル)1,1,1,3,3,3−
ヘキサフルオロ−2−プロパノール、HOCH2(CF2)3CH2O
H、 HOCH2CF2CFH(CF2)3CFHCF2CH2OH、 HOCH2CH2CH2(CF2)3CH2CH2CH2OH等が例示されその中でも
ビスフエノールAFが好適である。使用量はフツ素ゴム10
0重量部当り0.1〜10重量部、好ましくは0.6〜5重量部
の割合で用いる。
The vulcanizing agent used in the composition of the present invention is a fluorine-containing polyhydroxy compound, and is 2,2-bis (4-hydroxyphenyl) perfluoropropane [bisphenol AF], 2,2
-Bis (4-hydroxyphenyl) perfluoropropane, 2- (4'-hydroxyphenyl) 1,1,1,3,3,3-
Hexafluoro-2-propanol, HOCH 2 (CF 2 ) 3 CH 2 O
H, HOCH 2 CF 2 CFH (CF 2 ) 3 CFHCF 2 CH 2 OH, HOCH 2 CH 2 CH 2 (CF 2 ) 3 CH 2 CH 2 CH 2 OH, etc. are exemplified, and among these, bisphenol AF is preferable. Fluorocarbon rubber used 10
It is used in an amount of 0.1 to 10 parts by weight, preferably 0.6 to 5 parts by weight, per 0 parts by weight.

加硫促進剤としては、第四オニウム塩化合物、第4級
ホスフオニウム塩、第4級アンモニウム塩又はイミニウ
ム塩、例えばテトラメチルアンモニウムクロリド、テト
ラエチルアンモニウムクロリド、テトラプロピルアンモ
ニアムクロリド、テトラブチルアンモニウムクロリド、
テトラブチルアンモニウムブロミド、ビス(ベンジルジ
フエニルホスフイン)イミニウムクロリド、テトラブチ
ルホスホニウムクロリド、ベンジントリフエニルホスホ
ニウムクロリド、ベンジルトリオクチルホスホニウムク
ロリドなどが適当であり、フツ素ゴム100重量部当り0.0
5〜2重量部、好ましくは0.1〜1重量部の割合で用い
る。
As the vulcanization accelerator, a quaternary onium salt compound, a quaternary phosphonium salt, a quaternary ammonium salt or an iminium salt, for example, tetramethylammonium chloride, tetraethylammonium chloride, tetrapropylammonium muchloride, tetrabutylammonium chloride,
Tetrabutylammonium bromide, bis (benzyldiphenylphosphine) iminium chloride, tetrabutylphosphonium chloride, benzintriphenylphosphonium chloride, benzyltrioctylphosphonium chloride, etc. are suitable, and 0.0 per 100 parts by weight of fluorine rubber.
It is used in an amount of 5 to 2 parts by weight, preferably 0.1 to 1 part by weight.

金属水酸化物は、酸結合剤として用いられ、マグネシ
ウム、カルシウム、亜鉛、鉛等の水酸化物が例示され、
その中で水酸化カルシウムが好適である。使用量は、フ
ツ素ゴム100重量部当り、1〜30重量部、好ましくは2
〜20重量部の割合で用いる。
The metal hydroxide is used as an acid binder, magnesium, calcium, zinc, lead and other hydroxides are exemplified,
Among them, calcium hydroxide is preferable. The amount used is 1 to 30 parts by weight, preferably 2 per 100 parts by weight of fluororubber.
Used in a proportion of up to 20 parts by weight.

本発明においては充てん剤、補強剤が用い得る。例え
ばカーボンブラツク、シリカ、クレー、タルクなどが必
要に応じて用いられる。
Fillers and reinforcing agents can be used in the present invention. For example, carbon black, silica, clay, talc, etc. are used as necessary.

〔実施例〕〔Example〕

次に実施例を挙げ本発明を具体的に説明する。実施例
中各種分析方法及び物理特性の測定方法は下記の方法に
従つた。
Next, the present invention will be specifically described with reference to examples. In the examples, various analysis methods and methods for measuring physical properties were according to the following methods.

1)分析方法 フツ素ゴムの極限粘度数及び分子量分布(M5)の測定
条件は以下の通りである。
1) Analytical method The conditions for measuring the intrinsic viscosity and molecular weight distribution (M 5 ) of fluorine rubber are as follows.

(1)極限粘度数〔η〕 メチルエチルケトンを溶媒とする0.1g/100mlの濃度溶
液を毛細管粘度計を用いて35℃で測定する。
(1) Intrinsic viscosity [η] A 0.1 g / 100 ml concentration solution using methyl ethyl ketone as a solvent is measured at 35 ° C. using a capillary viscometer.

(2)分子量分布 液体クロマトグラフ : LC−3A型(島津製作所
(株)製) カラム : KF−80M(2本)+KF−8
00P(プレカラム)(昭和電工(株)製) 検出器 : ERC−7510S(エルマ光学
(株)製) インテグレーター : 7000A(システムインス
ツルメンツ社製) 展開溶媒 :テトラヒドロフラン 湿度 : 0.1重量% 温度 : 35℃ 分子量検量線用標準ポリマー:単分散ポリスチレン各種
(東洋曹達(株)製) (MW/Mn=1.2(max)) M5、M100は上記結果より算出する。
(2) Molecular weight distribution Liquid chromatograph: LC-3A type (manufactured by Shimadzu Corporation) Column: KF-80M (two) + KF-8
00P (Pre-column) (Showa Denko KK) Detector: ERC-7510S (Elma Optical Co., Ltd.) Integrator: 7000A (System Instruments) Development solvent: Tetrahydrofuran Humidity: 0.1 wt% Temperature: 35 ° C Molecular weight calibration line standard polymer: monodisperse polystyrene various (manufactured by Toyo Soda (Ltd.)) (M W / M n = 1.2 (max)) M 5, M 100 is calculated from the results.

2)接着試験方法 1.金属 テストピース(株)製テストピース ・厚さ 1mm×50mm×15mm ・ステンレス鋼 JIS G4305(SUS304) ・軟鋼 JIS G3141(SPCC B) 2.表面処理 ・ステレンス鋼 研摩無し ・軟鋼 サイドペーパー#240研摩 ・脱脂洗浄 メチルエチルケトン 3.接着剤 モニカスCF5M 横浜高分子研究所(製) 4.塗付 はけ塗り 1回 5.加硫接着条件 接着剤塗付後、室温にて乾燥させる。約30分後、接着剤
を塗付した金属の表面を上にして金型に入れ、その上に
加硫接着用組成物をおき、加硫接着させる。
2) Adhesion test method 1. Metal test piece Co., Ltd. test piece-Thickness 1mm x 50mm x 15mm-Stainless steel JIS G4305 (SUS304) -Mild steel JIS G3141 (SPCC B) 2. Surface treatment-Stellence steel No polishing- Mild steel Side paper # 240 Polishing / degreasing cleaning Methyl ethyl ketone 3. Adhesive Monikas CF5M Yokohama Polymer Research Institute (manufactured) 4. Coat / apply once 5. Vulcanization adhesion condition After application of adhesive, dry at room temperature . After about 30 minutes, the adhesive-coated metal is placed in a mold with the surface of the metal facing upward, and the vulcanization-adhesive composition is placed thereon and vulcanized and adhered.

ブレス加硫 180℃ 10分 オーブン加硫 232℃ 24時間 6.剥離試験方法および評価 (1)剥離試験方法 上記ゴム接着済み試験片のゴム部分をペチンを用いて90
°剥離する。応力集中によるゴム切れの場合は、他の部
分から同様に剥離し、さらにゴム切れの場合は、同じ方
法で繰り返し行ない、判定する。
Breath vulcanization 180 ° C 10 minutes Oven vulcanization 232 ° C 24 hours 6. Peeling test method and evaluation (1) Peeling test method The rubber part of the above rubber-bonded test piece was rubbed with pechin.
° Peel off. In the case of rubber breakage due to stress concentration, it is peeled off from other parts in the same manner, and in the case of rubber breakage, the same method is repeated to determine.

(2)評価 接着の評価は次のように行つた。(2) Evaluation The adhesion was evaluated as follows.

以上のような評価をし、それにM−RC−Rの%表示も
あわせて示した。
The above evaluation was performed, and the% display of M-RC-R was also shown.

M :金属と接着剤間の剥離 RC:ゴム部と接着剤間の剥離 R :ゴム部の剥離 総合評価(n=4試験片)は次のようにあらわした。M: Peeling between metal and adhesive RC: Peeling between rubber part and adhesive R: Peeling of rubber part The comprehensive evaluation (n = 4 test pieces) is shown as follows.

◎ 優 ○ 良 △ 可 × 不可 実施例1 電磁誘導式かきまぜ機を備えた内容積約15lのオート
クレープを窒素ガスで十分に掃気し、減圧−N2充てんを
3回繰り返して、窒素置換したのち、減圧状態で、脱酸
素した純粋5800g、1,1,2−トリクロロ−1,2,2−トリフ
ルオロエタン(以下フロン113という)2670g及び懸濁安
定剤としてのメチルセルロース(粘度50cp)2.9gを仕込
み、500rpmでかきまぜながら、温度50℃に保つた。次い
でVdF26.4重量%、HFP68.1重量%、及びTFE5.5重量から
成る混合モノマーを仕込ガスとして、13Kg/m2−Gとな
るまで仕込んだ。次に触媒として、ジイソプロピルパー
オキシジカーボネート10.5重量%を含有したフロン113
溶液を51g仕込み重合を開始させた。重合により圧力が1
2.5Kg/m2−Gまで低下するのでVdF55.3重量%、HFP28.3
重量%、TFE16.4重量%から成る混合モノマーを追添ガ
スとして追添し、再び圧力を13Kg/cm2−Gに戻した。こ
のような操作を繰り返し9時間重合反応を行なつた。重
合反応終了後、残存する混合モノマーを掃気し、得られ
た懸濁液を遠心分離機で脱水し、十分水洗したのち、10
0℃で真空乾燥して約8Kgのゴムを得た。得られたフツ素
ゴムを19FNMRにより分析したところ、VdF単位55.1重量
%、HFP単位29.1重量%、TFE単位15.8重量%であり、
〔η〕は228であつた。
◎ Excellent ○ Good △ Yes × No Example 1 An autoclave with an internal volume of about 15 l equipped with an electromagnetic induction stirrer was thoroughly scavenged with nitrogen gas, and after decompression-N 2 filling was repeated 3 times to replace nitrogen. , Deoxidized pure 5800 g, 1,1,2-trichloro-1,2,2-trifluoroethane (hereinafter referred to as CFC 113) 2670 g, and methyl cellulose (viscosity 50 cp) 2.9 g as a suspension stabilizer under reduced pressure The temperature was maintained at 50 ° C while charging and stirring at 500 rpm. Then, a mixed monomer consisting of 26.4% by weight of VdF, 68.1% by weight of HFP, and 5.5% by weight of TFE was charged as a charging gas to 13 Kg / m 2 -G. Next, as a catalyst, Freon 113 containing 10.5% by weight of diisopropyl peroxydicarbonate was used.
51 g of the solution was charged and the polymerization was started. 1 pressure due to polymerization
Since drops to 2.5Kg / m 2 -G VdF55.3 wt%, HFP28.3
A mixed monomer consisting of 1% by weight of TFE and 16.4% by weight of TFE was added as an additional gas, and the pressure was returned to 13 kg / cm 2 -G again. Such an operation was repeated to carry out a polymerization reaction for 9 hours. After the completion of the polymerization reaction, the remaining mixed monomer was scavenged, the resulting suspension was dehydrated with a centrifuge, washed thoroughly with water, and then washed with 10
It was vacuum dried at 0 ° C. to obtain about 8 kg of rubber. When the obtained fluorine rubber was analyzed by 19 FNMR, it was found that the VdF unit was 55.1% by weight, the HFP unit was 29.1% by weight, and the TFE unit was 15.8% by weight.
The [η] was 228.

該フツ素ゴムを下記の押出機、押出条件で、加熱混練
して押出し、ホツトカツターでカツテイング後放冷し、
ペレツト状とした。
The fluorocarbon rubber was extruded by heating and kneading under the following extruder and extrusion conditions, and then allowed to cool after cutting with a hot cutter,
It was made into a pellet shape.

〔押出機〕(Extruder)

日本製鋼株式会社製 型式:TEX44PS−30AW−2V(2軸) 〔押出条件〕 加熱温度 170℃ スクリユー回転数 300rpm 試料供給速度 30Kg/hr 得られたペレツト状フツ素ゴムの〔η〕は169、
は23.9×104は2.2、M5は2.0重量%、M100
は13.3重量%であり、ムーニー粘度〔ML1+10(121
℃)〕は102であつた。
Nippon Steel Co., Ltd. Model: TEX44PS-30AW-2V (biaxial) [Extrusion conditions] Heating temperature 170 ℃ Screen rotation speed 300rpm Sample feeding rate 30Kg / hr [η] of the obtained pelletized fluororubber is 169, n
Is 23.9 × 10 4 , w / n is 2.2, M 5 is 2.0% by weight, M 100
Is 13.3% by weight, and the Mooney viscosity [ML 1 + 10 (121
° C)] was 102.

実施例2 仕込モノマー組成がVdF5.4重量%、HGP90.6重量%。T
FE4.0重量%、追添モノマー組成がVdF39.4重量%、HFP3
8.8重量%、TFE21.8重量%重合時間を11時間とした以外
は実施例1と同様に行なつた。得られたフツ素ゴムの
〔η〕は143、は16.1×104は2.7、M5
は4.9%、M100は10.2%であり、ムーニー粘度〔ML1+10
(121℃)〕は143であつた。
Example 2 The composition of the charged monomer was VdF 5.4% by weight and HGP 90.6% by weight. T
FE4.0% by weight, added monomer composition is VdF39.4% by weight, HFP3
The procedure of Example 1 was repeated except that the polymerization time of 8.8% by weight and TFE21.8% by weight was 11 hours. [Η] of the obtained fluororubber was 143, n was 16.1 × 10 4 , w / n was 2.7, M 5
Is 4.9%, M 100 is 10.2%, and Mooney viscosity [ML 1 + 10
(121 ° C.)] was 143.

実施例3 実施例1と同様な方法で純粋フロン113及び懸濁安定
剤を仕込み、500rpmでかきまぜながら温度を50℃に保つ
た。次いで、VdF16.9重量%、HFP83.1重量%から成る混
合モノマーを仕込モノマーとして15.0Kg/m2−Gとなる
まで仕込み、次に触媒としてジイソプロピルパーオキシ
ジカーボネート10.5重量%を含有したフロン113溶液51g
を仕込み重合を開始させた。この際、重合により圧力が
14.5Kg/m2−Gまで低下するのでVdF51.7重量%、HFP48.
3重量%から成る混合ガスを追添モノマーとして追添し
再び圧力を15Kg/m2−Gにした。かかる操作を重合反応
中繰り返し15時間重合を行い、約5Kgのフツ素ゴムを得
た。このフツ素ゴムの組成はVdF単位52.0重量%、HFP単
位48.0重量%であり、〔η〕は151、は17.9×104
は3.2、M5は4.3%、M100は19.6%であり、ム
ーニー粘度〔ML1+10(121℃)〕は133であつた。
Example 3 Pure freon 113 and a suspension stabilizer were charged in the same manner as in Example 1, and the temperature was kept at 50 ° C. while stirring at 500 rpm. Then, a mixed monomer consisting of 16.9% by weight of VdF and 83.1% by weight of HFP was charged as a charging monomer to 15.0 Kg / m 2 -G, and then CFC containing 10.5% by weight of diisopropyl peroxydicarbonate as a catalyst. 51 g of solution
Was charged to start the polymerization. At this time, the pressure is increased by the polymerization.
Since drops to 14.5Kg / m 2 -G VdF51.7 wt%, HFP48.
A mixed gas consisting of 3% by weight was added as an additional monomer, and the pressure was adjusted to 15 kg / m 2 -G again. This operation was repeated during the polymerization reaction for 15 hours for polymerization to obtain about 5 kg of fluororubber. The composition of this fluororubber was VdF unit 52.0% by weight, HFP unit 48.0% by weight, [η] was 151, and n was 17.9 × 10 4 ,
w / n was 3.2, M 5 was 4.3%, M 100 was 19.6%, and Mooney viscosity [ML 1 + 10 (121 ° C.)] was 133.

実施例4〜9、比較例1〜5 実施例1で得られたフツ素ゴムおよび比較例としてテ
クノフロンFOR−45Bi(モンテジソン社製2元共重合フ
ツ素ゴム〔η〕=80(mg/g)M5=20(%)M100=16
(%))を用いた例も併わせて、表1、表2に示す配合
処方で、ロールにより混練しゴムと金属の加硫接着性を
評価した。結果を第3表、第4表に示した。
Examples 4 to 9 and Comparative Examples 1 to 5 The fluorocarbon rubbers obtained in Example 1 and Technoflon FOR-45Bi (a binary copolymer fluorocarbon rubber manufactured by Montedison Co. [η] = 80 (mg / g) as comparative examples. ) M 5 = 20 (%) M 100 = 16
(%)) Was also used, and the compounding prescriptions shown in Tables 1 and 2 were used to knead with a roll to evaluate the vulcanization adhesion of rubber and metal. The results are shown in Tables 3 and 4.

〔発明の効果〕 以上のように、高活性酸化マグネシウムを配合するこ
とで、高分子量フツ素ゴムと金属の加硫接着性が著るし
く向上した。
[Effects of the Invention] As described above, the vulcanization adhesiveness between the high molecular weight fluorine rubber and the metal was remarkably improved by incorporating the highly active magnesium oxide.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】フツ素含量が63.5〜71重量%、極限粘度
〔η〕(測定溶媒メチルエチルケトン、測定温度35℃)
が100〜250(ml/g)、分子量5万以下のフラクシヨンの
含量(M5)が5重量%以下、かつ分子量100万以上のフ
ラクシヨンの含量(M100)が10〜35重量%であるフツ素
ゴム100重量部、 ポリオール加硫剤0.1〜10重量部、 ポリオール加硫促進剤0.05〜2重量部、 金属水酸化物1〜30重量部、 酸化マグネシウムの活性価が100(mg/g)以上であると
ころの高活性酸化マグネシウム5〜25重量部 からなる加硫接着用組成物。
1. A fluorine content of 63.5 to 71% by weight, an intrinsic viscosity [η] (measuring solvent methyl ethyl ketone, measuring temperature 35 ° C.)
Of 100 to 250 (ml / g), the content of the fraction having a molecular weight of 50,000 or less (M 5 ) is 5% by weight or less, and the content of the fraction having a molecular weight of 1 million or more (M 100 ) is 10 to 35% by weight. Base rubber 100 parts by weight, polyol vulcanizing agent 0.1 to 10 parts by weight, polyol vulcanization accelerator 0.05 to 2 parts by weight, metal hydroxide 1 to 30 parts by weight, magnesium oxide activity value of 100 (mg / g) or more A vulcanizing and bonding composition comprising 5 to 25 parts by weight of highly active magnesium oxide.
JP62263956A 1987-10-21 1987-10-21 Fluorine rubber composition for vulcanization adhesion Expired - Lifetime JP2537906B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62263956A JP2537906B2 (en) 1987-10-21 1987-10-21 Fluorine rubber composition for vulcanization adhesion

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Application Number Priority Date Filing Date Title
JP62263956A JP2537906B2 (en) 1987-10-21 1987-10-21 Fluorine rubber composition for vulcanization adhesion

Publications (2)

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JPH01108246A JPH01108246A (en) 1989-04-25
JP2537906B2 true JP2537906B2 (en) 1996-09-25

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Country Link
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Publication number Priority date Publication date Assignee Title
JP4978081B2 (en) * 2006-06-30 2012-07-18 日立電線株式会社 Modified fluororesin composition and molded body using the same
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