TW201229072A - Crosslinkable fluororubber composition and crosslinked rubber article - Google Patents

Crosslinkable fluororubber composition and crosslinked rubber article Download PDF

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TW201229072A
TW201229072A TW100143956A TW100143956A TW201229072A TW 201229072 A TW201229072 A TW 201229072A TW 100143956 A TW100143956 A TW 100143956A TW 100143956 A TW100143956 A TW 100143956A TW 201229072 A TW201229072 A TW 201229072A
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fluoropolymer
carbon atoms
cross
fluororubber composition
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TW100143956A
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Hiroki Nagai
Takeshi Yamada
Norihide Sugiyama
Masahiro Ohkura
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Asahi Glass Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/12Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • C08L27/18Homopolymers or copolymers or tetrafluoroethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/24Crosslinking, e.g. vulcanising, of macromolecules
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/04Oxygen-containing compounds
    • C08K5/14Peroxides
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/12Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2327/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
    • C08J2327/02Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
    • C08J2327/12Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • C08K2003/2217Oxides; Hydroxides of metals of magnesium

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
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Abstract

The purpose of the present invention is to provide: a crosslinkable fluororubber composition which enables the production of a crosslinked rubber article having both excellent chemical resistance and excellent heat resistance; and a crosslinked rubber article produced using the crosslinkable fluororubber composition. A crosslinkable fluororubber composition which comprises a fluororubber and a fluoropolymer (P) that has a repeating unit derived from a fluorodiene (b) having unsaturated side chain residual performance and also has multiple polymerizable double bonds; and a crosslinked rubber article produced by crosslinking the crosslinkable fluororubber composition.

Description

201229072 六、發明說明: c發明戶斤屬之技術領域3 發明領域 本發明係有關於一種交聯性氟橡膠組成物及交聯橡膠 物品。 【先前技術3 發明背景 就將氟橡膠予以交聯而製得交聯橡膠物品之方法而 言,眾知有:(1)使用有機過氧化物,藉由加熱使自由基生 成並予以交聯之方法;(2)對氟橡膠照射放射線使自由基生 成並予以交聯之方法;及(3)使用多元醇交聯系、及多胺交 聯系等交聯劑加以交聯之方法。 在方法(1)、(2)中,為了圖謀氟橡膠之交聯特性、及製 得之交聯橡膠物品特性之提升,係使用已摻混多官能性化 合物之交聯性氟橡膠組成物作為交聯助劑。例如,就交聯 助劑而言,眾知有已摻混異三聚氰酸三烯丙酯(TAIC)之交 聯性氟橡膠組成物(參考非專利文獻1及專利文獻1)。 藉由使用TAIC作為交聯助劑,可提升氟橡膠之交聯速 度。又,使用前述交聯性氟橡膠組成物,藉由方法(1)、(2) 所製造之交聯橡膠物品,與以方法(3)所製造之交聯橡膠物 品相較之下,具有較好的耐藥性(尤其是耐胺性)。但,在前 述交聯性氟橡膠組成物中,難以製得具有顯著優異的耐熱 性之交聯橡膠物品。 先前技術文獻 201229072 專利文獻 專利文獻1 :日本特開平7_1797〇5號公報 非專利文獻 非專利文獻1:里川編,良樹脂手冊616〜622頁、及 577〜578頁(日刊工業報,1990年發行) 【發明内容3 發明概要 發明欲解決之課題 本發明之目的在於提供一種可賦予兼具良好的耐藥性 與耐熱性之交聯橡膠物品的交聯性氟橡膠組成物、及由該 交聯性氟橡膠組成物所製得之交聯橡膠物品。 用以解決課題之機構 本發明為解決前述課題,採用以下構成。 [1] 一種交聯性氟橡膠組成物,其係含有氟橡膠、及具 有多數聚合性雙鍵之下述氟聚合物(P)者,氟聚合物(P)係具 有源自於不飽和側鏈殘留性之氟二烯(b)之重複單元之氟聚 合物。 [2] 如[1]記載之交聯性氟橡膠組成物,前述氟聚合物 (P)係具有:源自於氟單烯(a)之重複單元、及源自於不飽和 側鏈殘留性之氟二烯(b)之重複單元之氟聚合物。 [3] 如[2]記載之交聯性氟橡膠組成物’前述氟單烯(a) 係選自於由四氟乙稀、氯二氣乙稀、及CF2=CFO-Rfl(式中, Rfl為碳數1-6之氟烷基、或於碳原子-碳原子間具有1個以上 趟性氧原子之碳數2~6之氟烧基)所構成之群組中之1種以上。 4 201229072 [4] 如[1]〜[3]中任一項記載之交聯性氟橡膠組成物,前 述氟二烯(b)係選自於由下述氟二烯(M)〜(b3)所構成之群組 中之1種以上。 (bl) CF2=CFO-Qfl-OCF=CF2 ; (b2) CH2=CFCF20-Qf2-0CF2CF=CH2 ; (b3) CH2=CFCF20-Qf3-0CF=CF2 ; (式中,Qfl&Qf2分別獨立為碳數3〜8之氟伸烷基、或於 碳原子-碳原子間具有1個以上醚性氧原子之碳數3〜8之氟 伸烷基。201229072 VI. Description of the Invention: c Technical Field of Invention 3 Field of the Invention The present invention relates to a crosslinkable fluororubber composition and a crosslinked rubber article. [Background of the Invention 3] In the method of crosslinking a fluororubber to obtain a crosslinked rubber article, it is known that: (1) an organic peroxide is used, and a radical is generated and crosslinked by heating. Method; (2) a method of irradiating a fluororubber to irradiate a radical to form and crosslink a radical; and (3) a method of crosslinking by using a cross-linking agent such as a polyol cross-linking and a cross-linking of a polyamine. In the methods (1) and (2), in order to constrain the crosslinking property of the fluororubber and the improvement of the properties of the obtained crosslinked rubber article, a crosslinkable fluororubber composition having a polyfunctional compound blended therein is used. Crosslinking aid. For example, a cross-linking fluororubber composition in which triallyl isocyanurate (TAIC) has been blended is known as a cross-linking aid (see Non-Patent Document 1 and Patent Document 1). By using TAIC as a crosslinking aid, the crosslinking speed of the fluororubber can be increased. Moreover, the crosslinked rubber article produced by the methods (1) and (2) is used in comparison with the crosslinked rubber article produced by the method (3), using the crosslinkable fluororubber composition. Good resistance (especially amine resistance). However, in the crosslinkable fluororubber composition described above, it is difficult to obtain a crosslinked rubber article having remarkably excellent heat resistance. CITATION LIST Patent Literature No. 201229072 Patent Document Patent Literature 1: Japanese Patent Publication No. Hei 7_1797 No. 5 Non-Patent Literature Non-Patent Document 1: Lichuan, Good Resin Handbook 616 to 622, and 577 to 578 (Japanese Journal of Industry, 1990) SUMMARY OF THE INVENTION PROBLEMS TO BE SOLVED BY THE INVENTION An object of the present invention is to provide a crosslinkable fluororubber composition capable of imparting a crosslinked rubber article having both good chemical resistance and heat resistance, and to crosslink the crosslinked fluororubber A crosslinked rubber article made of a fluororubber composition. MEANS FOR SOLVING THE PROBLEMS The present invention has the following constitutions in order to solve the above problems. [1] A crosslinkable fluororubber composition comprising a fluororubber and a fluoropolymer (P) having a plurality of polymerizable double bonds, the fluoropolymer (P) having a source derived from an unsaturated side A fluoropolymer of a repeating unit of a chain residual fluorodiene (b). [2] The cross-linkable fluororubber composition according to [1], wherein the fluoropolymer (P) has a repeating unit derived from fluoromonoolefin (a) and a residue derived from an unsaturated side chain a fluoropolymer of a repeating unit of fluorodiene (b). [3] The cross-linking fluororubber composition as described in [2], wherein the fluoromonoolefin (a) is selected from the group consisting of tetrafluoroethylene, chloroethylene, and CF2=CFO-Rfl (wherein Rfl is one or more selected from the group consisting of a fluoroalkyl group having 1 to 6 carbon atoms or a fluoroalkyl group having 2 or more carbon atoms having one or more inert oxygen atoms between carbon atoms and carbon atoms. The cross-linking fluororubber composition according to any one of [1] to [3], wherein the fluorodiene (b) is selected from the following fluorodiene (M) to (b3) One or more of the groups formed. (b1) CF2=CFO-Qfl-OCF=CF2; (b2) CH2=CFCF20-Qf2-0CF2CF=CH2; (b3) CH2=CFCF20-Qf3-0CF=CF2; (wherein, Qfl&Qf2 are independently carbon The fluoroalkyl group having 3 to 8 or the fluoroalkyl group having 3 to 8 carbon atoms having one or more etheric oxygen atoms between carbon atoms and carbon atoms.

Qf3為碳數1〜6之氟伸烷基、或於碳原子-碳原子間具有1 個以上醚性氧原子之碳數2〜6之氟伸烷基)。 [5] 如[1]〜[4]中任一項記載之交聯性氟橡膠組成物,前 述氟聚合物(P)之重量平均分子量為3,000〜50,000。 [6] 如[1]〜[5]中任一項記載之交聯性氟橡膠組成物,前 述II聚合物(P)中之聚合性雙鍵之含量為0.2〜2mmol/g。 [7] 如[1]〜[6]中任一項記載之交聯性氟橡膠組成物,其 相對於前述氟橡膠100質量份,含有前述氟聚合物(P)l〜50 質量份。 [8] 如[1]〜[7]中任一項記載之交聯性氟橡膠組成物,前 述氟橡膠係選自於由四氟乙烯/丙烯系共聚物、氟化亞乙烯 /四氟乙烯/六氟丙烯系共聚物、及四氟乙烯/全氟烷基乙烯 基醚系共聚物所構成之群組中之1種以上。 [9] 如[1]〜[8]中任一項記載之交聯性氟橡膠組成物,其 更含有有機過氧化物。 201229072 [10] —種交聯橡膠物品,其係交聯如[1]或[2]記載之交 聯性氟橡膠組成物而成者。 [11] 如[10]記載之交聯橡膠物品,其係密封材。 發明效果 本發明之交聯性氟橡膠組成物可製造兼具良好的耐藥 性與耐熱性之交聯橡膠物品。 又,由於本發明之交聯橡膠物品係將本發明之交聯性 氟橡膠組成物交聯而製造,因此兼具良好的耐藥性與耐熱 性。Qf3 is a fluorine alkyl group having 1 to 6 carbon atoms or a fluorine alkyl group having 2 or more carbon atoms having one or more etheric oxygen atoms between carbon atoms and carbon atoms. [5] The crosslinkable fluororubber composition according to any one of [1] to [4], wherein the fluoropolymer (P) has a weight average molecular weight of 3,000 to 50,000. [6] The crosslinkable fluororubber composition according to any one of [1] to [5], wherein the content of the polymerizable double bond in the above-mentioned II polymer (P) is 0.2 to 2 mmol/g. [7] The cross-linking fluororubber composition according to any one of the above-mentioned fluororubbers, wherein the fluoropolymer (P) is contained in an amount of from 1 to 50 parts by mass based on 100 parts by mass of the fluororubber. [8] The crosslinkable fluororubber composition according to any one of [1] to [7] wherein the fluororubber is selected from the group consisting of tetrafluoroethylene/propylene copolymer, vinylidene fluoride/tetrafluoroethylene One or more of the group consisting of a hexafluoropropylene copolymer and a tetrafluoroethylene/perfluoroalkyl vinyl ether copolymer. [9] The crosslinkable fluororubber composition according to any one of [1] to [8] further comprising an organic peroxide. 201229072 [10] A cross-linked rubber article which is obtained by crosslinking a cross-linking fluororubber composition as described in [1] or [2]. [11] The crosslinked rubber article according to [10], which is a sealing material. EFFECTS OF THE INVENTION The crosslinked fluororubber composition of the present invention can produce a crosslinked rubber article having both good chemical resistance and heat resistance. Further, since the crosslinked rubber article of the present invention is produced by crosslinking the crosslinkable fluororubber composition of the present invention, it has both good chemical resistance and heat resistance.

【實施方式;J 用以實施發明之形態 <交聯性氟橡膠組成物>[Embodiment] J is a form for carrying out the invention < Crosslinkable fluororubber composition >

本發明之交聯性氟橡膠組成物係含有氟橡膠、及具有多 數聚合性雙鍵之後述氟聚合物(p)作為必要成分之組成物。 [氟聚合物(PXI 氟聚合物(Ρ)在本發明之交聯性氟橡膠組成物中,係作 用為交聯助劑。亦即,氟聚合物(Ρ)係藉由以光或熱所誘發 之自由基與氟橡膠結合,而賦予屬於三維交聯物之交聯橡 膠物品。 氟聚合物(Ρ)係具有源自於不飽和側鏈殘留性之氟二烯 (b)之重複單元之氟聚合物,於分子内具有多數聚合性雙鍵 (碳-碳雙鍵)。氟聚合物(P)以具有源自於氟單烯之重複單 元、及源自於不飽和侧鏈殘留性之氟二烯(b)之重複單元之 氟聚合物為宜。 6 201229072 (氟單烯(a)) lL單烯(a)係於分子内具有丨個聚合性雙鍵之含氟化合物。 作為氟單烯(a),例如有:四氟乙烯(TFE)、三氟乙烯、 氣三氟乙烯(CTFE)、及氟化亞乙烯等氟乙烯類,以及六氟 丙烯、與以CFfCFO-R;1(式中’ Rfi為碳數卜6之氟烷基、或 於碳原子-碳原子間具有1個以上醚性氧原子之碳數2〜6之 氟烷基)表示之氟乙烯基醚(以下稱為「氟單烯(al)」)等。 在本發明中,所謂氟烷基係指烷基中有丨個以上的氫原 子被氟原子所取代之基。又,所謂於碳原子-碳原子間具有 1個以上醚性氧原子之氟烷基,係指於碳原子·碳原子間具 有1個以上醚性氧原子之烷基中有丨個以上的氫原子被氟原 子所取代之基。又,所謂全氟烷基係指烷基之全部氫原子 被氟原子所取代之基。 氟單烯(a)宜為選自於由TFE、CTFE、及氟單烯(ai)所 構成之群組中之1種以上。 若使用TFE作為氟單烯(a),可提升氟聚合物(p)之流動 性,又可製得具有特別優異之耐熱性之交聯橡膠物品。 若使用CTFE作為氟單稀(a) ’尤其在使用氟化亞乙烯共 聚系氟橡膠作為氟橡膠時’因其相溶性佳,故可提升交聯 效率。 若使用氟單烯(al)作為氟單烯(a),可使氟聚合物(p)之 黏度變低而易於交聯性氟橡膠組成物之製造。 氣半稀(al)之R之奴數以1〜5為佳,1〜3較佳。只要 之碳數在該範圍内’即可在不使氟聚合物(P)之流動性及财 201229072 熱性下降的情況下,作為氟橡膠之交聯助劑起作用。Rn之 氟伸炫基可為直鏈狀,亦可為分枝键狀。 由交聯橡膠物品之耐熱性之觀點看來,氟單烯(al)之 Rfl以烷基之氫原子全部被氟原子所取代為佳。亦即,作為 氟單烯(al),以CF2=CFO-Rfi(式中,RF1為碳數卜6之全氟烷 基、或於碳原子-碳原子間具有1個以上醚性氧原子之碳數 2〜6之全氟烷基)表示之全氟乙烯基醚(以下稱為「氟單烯 (all)」)較佳。 在更可提升氟聚合物(p)之流動性之觀點上,TFE與氟單 烯(al)之併用與單獨使用該等之情況相較之下,較為理想。 從氟聚合物(P)之流動性及交聯橡膠物品之耐熱性之觀 點看來,氟單烯(a)以全氟單體為佳,以TFE與氟單烯 較佳,以TFE之單獨使用、或TFE與氟單烯(a 11)之併用更佳。 氟*單烯(a)可僅單獨使用丨種,或可併用2種以上。 (氟二烯(b)) 氟二烯(b)係於分子内具有2個聚合性雙鍵之不飽和側 鏈殘留性之含氟化合物。亦即,氟二烯(b)係於製造氟聚合 物(P)之聚合時’2個聚合性雙鍵中之至少一部分未貢獻於聚 合反應,而在聚合後雙鍵仍殘留之化合物。具體而言,氟 二烯(b)之任一方之聚合性雙鍵中之2個碳原子,會於聚合後 形成主鏈。另一方之聚合性雙鍵中之至少一部分則未貢獻 於聚合反應’而在氟聚合物(P)中殘留作為不飽和側鏈。 藉由使用氟二烯(b),會於氟聚合物(P)中殘留不飽和側 鏈,而藉由利用該不飽和側鏈之交聯反應,可製得交聯橡 8 201229072 膠物品。 烯(b) ’例如有:由碳原子純原子構成之全 碳原子、氟科聽料構紅 又’例如可舉前述缝二烯中丨個以上之氟原 取代之氟二;^ ϋ _ μ 攸⑽十所 性之觀點看來,^ 言,從交聯橡膠物品之耐熱 ^ 玉氟一烯為佳,從氟聚合物(ρ)之流動性、 ^交聯橡膠物品之耐藥性與耐熱性之觀點看來,以 由奴,子、氟原子及氧原子構成之全氟二稀更佳。 鼠-稀(b)中連結2個聚合性雙鍵之連結鏈(碳原子 原子之合計)之原子數以5〜1〇為佳,5〜8較佳。 ” 右刚迷連結鏈之原子數在下限值以上,在製造I聚合 物(Ο之聚合反應期間’可抑制分子中料2個聚合性雙鍵反 應而引起分子内環化’且聚合性雙鍵易於作為不飽和側鏈 而殘留於氟聚合物(P)中。又,若前述連結鏈之原子數在上 限值以下’殘留於氟聚合物(P)之側鏈之聚合性雙鍵在本發 明之交聯性氟橡膠組成物之保存巾將難以引起交聯反應, 故而難以生成氟聚合物(p)之高分子量化或膠化。藉此,在 與氟橡膠揑合時,可輕㈣抑㈣聚合物(p)之流動性顯著 下降。又’連結鏈之原子數在上限值以下之氟二烯⑼可輕 易合成其本身並可高純度精製。 從防止氟聚合物(P)之流動性下降過多之觀點看來,氣 二婦⑼以不具有環結構之化合物為佳。作為氣二稀㈨,以 下述氟二稀(bl)〜(b3)較佳。 (bl) CF2=CF〇-Qf,-〇CF=CF2 ; 201229072 (b2) CH2=CFCF2〇-Qf2-〇CF2CF=CH2 ; (b3) CH2=CFCF20-Qf3-0CF=CF2。 惟,式中,Qfl與Qf2為分別獨立之碳數3〜8之氟伸烷基、 或於碳原子-碳原子間具有1個以上醚性氧原子之碳數3〜8 之氟伸烷基。The crosslinkable fluororubber composition of the present invention contains a fluororubber and a composition having a plurality of polymerizable double bonds and a fluoropolymer (p) described later as essential components. [Fluoropolymer (PXI fluoropolymer (Ρ) in the cross-linking fluororubber composition of the present invention acts as a crosslinking assistant. That is, the fluoropolymer (Ρ) is by light or heat The induced radical is combined with the fluororubber to impart a crosslinked rubber article belonging to the three-dimensional crosslinked product. The fluoropolymer (Ρ) is a repeating unit having a fluorodiene (b) derived from residual side chain residues. a fluoropolymer having a plurality of polymerizable double bonds (carbon-carbon double bonds) in a molecule. The fluoropolymer (P) has a repeating unit derived from a fluoromonoolefin and a residue derived from an unsaturated side chain. The fluoropolymer of the repeating unit of the fluorodiene (b) is preferably 6 201229072 (fluoromonoolefin (a)) lL monoolefin (a) is a fluorine-containing compound having a single polymerizable double bond in the molecule. The monoolefin (a) includes, for example, tetrafluoroethylene (TFE), trifluoroethylene, gas trifluoroethylene (CTFE), and vinyl fluoride such as vinylidene fluoride, and hexafluoropropylene, and CFfCFO-R; (In the formula, Rfi is a fluoroalkyl group of carbon number 6 or a fluoroalkyl group having 2 or more carbon atoms having 1 or more etheric oxygen atoms between carbon atoms and carbon atoms) (hereinafter referred to as "fluoromonoolefin (al)"), etc. In the present invention, the fluoroalkyl group means a group in which one or more hydrogen atoms in the alkyl group are substituted by a fluorine atom. - a fluoroalkyl group having one or more etheric oxygen atoms between carbon atoms, wherein one or more hydrogen atoms having one or more etheric oxygen atoms between carbon atoms and carbon atoms are replaced by fluorine atoms Further, the perfluoroalkyl group means a group in which all hydrogen atoms of the alkyl group are replaced by fluorine atoms. The fluoromonoolefin (a) is preferably selected from the group consisting of TFE, CTFE, and fluoromonoolefin (ai). One or more of the group is formed. If TFE is used as the fluoromonoolefin (a), the fluidity of the fluoropolymer (p) can be improved, and a crosslinked rubber article having particularly excellent heat resistance can be obtained. Use of CTFE as fluorine monosulfide (a) 'When using fluorinated vinylene copolymerized fluororubber as fluororubber, 'because of its good compatibility, it can improve the crosslinking efficiency. If fluoromonoolefin (al) is used as the fluorine single The alkene (a) can make the viscosity of the fluoropolymer (p) low and facilitate the manufacture of a crosslinkable fluororubber composition. It is preferably 1 to 5, and preferably 1 to 3. As long as the carbon number is within the range, it can be used as a fluororubber without reducing the fluidity of the fluoropolymer (P) and the heat of 201229072. The auxiliary agent acts. The fluorine extending base of Rn may be linear or branched. From the viewpoint of the heat resistance of the crosslinked rubber article, the Rfl of the fluoromonoolefin (al) is an alkyl group. It is preferred that all of the hydrogen atoms are replaced by fluorine atoms. That is, as the fluorine monoolefin (al), CF2=CFO-Rfi (wherein RF1 is a carbon number of a perfluoroalkyl group, or a carbon atom- A perfluorovinyl ether (hereinafter referred to as "fluoromonoolefin") which is a perfluoroalkyl group having 2 or more carbon atoms of one or more etheric oxygen atoms between carbon atoms is preferable. From the viewpoint of further improving the fluidity of the fluoropolymer (p), it is preferred that the combination of TFE and fluoromonene (al) is used in combination with the case of using them alone. From the viewpoint of the fluidity of the fluoropolymer (P) and the heat resistance of the crosslinked rubber article, the fluoromonoolefin (a) is preferably a perfluoromonomer, the TFE is preferably a fluoromonoolefin, and the TFE is alone. It is preferred to use or use TFE in combination with fluoromonoolefin (a 11). The fluorine*monoolefin (a) may be used alone or in combination of two or more. (Fluorodiene (b)) The fluorodiene (b) is a fluorine-containing compound having an unsaturated side chain residual property of two polymerizable double bonds in the molecule. That is, the fluorodiene (b) is a compound in which at least a part of the two polymerizable double bonds do not contribute to the polymerization reaction and the double bond remains after the polymerization in the polymerization for producing the fluoropolymer (P). Specifically, two of the polymerizable double bonds of either of the fluorodiene (b) form a main chain after polymerization. At least a part of the other polymerizable double bond does not contribute to the polymerization reaction and remains as an unsaturated side chain in the fluoropolymer (P). By using the fluorodiene (b), the unsaturated side chain remains in the fluoropolymer (P), and by using the crosslinking reaction of the unsaturated side chain, the crosslinked rubber 8 201229072 can be obtained. The olefin (b) 'is, for example, an all-carbon atom composed of a pure atom of a carbon atom, or a fluorine-based auditory composition, and a fluorine-substituted one of the above-mentioned slit diene; for example, 氟 _ μ攸(10) Ten points of view, ^, from the cross-linked rubber articles heat-resistant ^ fluorofluoro-ene is better, from the fluoropolymer (ρ) fluidity, ^ cross-linked rubber articles resistance and heat resistance From the point of view of sex, it is better to use perfluorodiazole consisting of slaves, children, fluorine atoms and oxygen atoms. In the mouse-dilute (b), the number of atoms connecting the two polymerizable double bonds (total of carbon atoms) is preferably 5 to 1 Å, and preferably 5 to 8. The number of atoms in the right chain is above the lower limit value, and in the production of the I polymer (the polymerization process can inhibit the polymerization of two polymerizable double bonds in the molecule to cause intramolecular cyclization) and the polymerizable double bond It is easy to remain in the fluoropolymer (P) as an unsaturated side chain. Further, if the number of atoms of the linking chain is less than the upper limit, the polymerizable double bond remaining in the side chain of the fluoropolymer (P) is present. The storage towel of the crosslinked fluororubber composition of the present invention is less likely to cause a crosslinking reaction, so that it is difficult to form a high molecular weight or gelation of the fluoropolymer (p), thereby being light (four) when kneaded with the fluororubber. (4) The fluidity of the polymer (p) is significantly decreased. Further, the fluorodiene (9) having a number of atoms in the chain below the upper limit can be easily synthesized and purified in high purity. From the prevention of the flow of the fluoropolymer (P) From the point of view of excessive decline in sex, it is preferable that the gas (2) is a compound having no ring structure. As the gas dilute (nine), it is preferred to use the following fluorodicarbon (b1) to (b3). (bl) CF2=CF〇 -Qf,-〇CF=CF2 ; 201229072 (b2) CH2=CFCF2〇-Qf2-〇CF2CF=CH2 ; (b3) CH2=CFCF20-Qf3-0 CF=CF2. In the formula, Qfl and Qf2 are independently a fluoroalkyl group having 3 to 8 carbon atoms, or a carbon number of 3 to 8 having one or more etheric oxygen atoms between carbon atoms and carbon atoms. Fluorine alkyl.

Qf 3為碳數1〜6之氟伸烷基、或於碳原子-碳原子間具有1 個以上醚性氧原子之碳數2〜6之氟伸烷基。 在本發明中,所謂氟伸烷基係指伸烷基中有1個以上之 氫原子被氟原子所取代之基。又,所謂於碳原子-碳原子間 具有1個以上醚性氧原子之氟伸烷基,係指於碳原子-碳原 子間具有1個以上醚性氧原子之伸烷基中有1個以上之氫原 子被氟原子所取代之基。又,所謂全氟伸烷基係指伸烷基 之全部氫原子被氟原子所取代之基。 氟二烯(bl)〜(b3)中之Qfl、、及$之氟伸烷基可具 有分枝構造。Qf 3 is a fluorine alkyl group having 1 to 6 carbon atoms or a fluorine alkyl group having 2 to 6 carbon atoms having one or more etheric oxygen atoms between carbon atoms and carbon atoms. In the present invention, the fluoroalkyl group means a group in which one or more hydrogen atoms in the alkylene group are substituted by a fluorine atom. In addition, the fluorine-extended alkyl group having one or more etheric oxygen atoms between carbon atoms and carbon atoms means one or more alkylene groups having one or more etheric oxygen atoms between carbon atoms and carbon atoms. A group in which a hydrogen atom is replaced by a fluorine atom. Further, the perfluoroalkylene group means a group in which all hydrogen atoms of the alkylene group are replaced by fluorine atoms. The Qfl, and the fluorine alkyl group in the fluorodiene (b1) to (b3) may have a branched structure.

Qfl之氟伸烷基之碳原子數以3〜6為佳。The fluorine atom of Qfl is preferably 3 to 6 carbon atoms.

Qn之氟伸烷基之碳原子數以3〜6為佳。 Q1"3之氟伸烷基之碳原子數以2〜5為佳。 作為氟二烯(bl),以下述氟二烯(bll)及(bl2)為佳。 (bll) CF2=CFO-Qf,1-OCF=CF2 ; (bl2) CF2=CFOCH2-Qf12-CH2OCF=CF2。 惟,式中,為碳數3〜8之全氟伸烷基、或於碳原子-碳原子間具有1個以上醚性氧原子之碳數3〜8之全氟伸烷基。 QFI2為碳數2〜6之全氟伸烷基、或於碳原子-碳原子間具 201229072 有1個以上醚性氧原子之碳數2〜6之全氟伸烷基。 氟二烯(bll)之具體例可舉如下述化合物。 CF2=CFO(CF2)4OCF=CF2 ; CF2=CFO(CF2)5OCF=CF2 ; CF2=CFO(CF2)6OCF=CF2 ;及 CF2=CFO(CF2)4OCF(CF3)CF2OCF=CF2 等。 氟二烯(M2)之具體例可舉如下述化合物。 CF2=CFOCH2(CF2)2CH2OCF=CF2 ;及 CF2=CFOCH2(CF2)4CH2OCF=CF2 等。 作為氟二烯(b2),以下述氟二烯(b21)為佳。 (b21)CH2=CFCF20-QF21-0CF2CF=CH2。 惟,式中,QF21為碳數3〜8之全氟伸烷基、或於碳原子-碳原子間具有1個以上醚性氧原子之碳數3〜8之全氟伸烷基。 氟二烯(b21)之具體例可舉如下述化合物。 ch2=cfcf2o(cf2)2ocf2cf=ch2 ; ch2=cfcf2o(cf2)3ocf2cf=ch2 ; ch2=cfcf2o(cf2)4ocf2cf=ch2 ;及 ch2=cfcf2o(cf2)2ocf(cf3)cf2ocf2cf=ch2 等。 作為氟二烯(b3),以下述氟二烯(b31)為佳。 (b31) CH2=CFCF20-QF31-0CF=CF2。 惟,式中,QF31為碳數1〜6之全氟伸烷基、或於碳原子-碳原子間具有1個以上醚性氧原子之碳數2〜6之全氟伸烷基。 氟二烯(b31)之具體可舉例如下述化合物。 CH2=CFCF2OCF(CF3)CF2OCF=CF2 ;及 11 201229072 CH2=CFCF2OCF(CF3)CF2OCF(CF3)CF2OCF=CF2 等。 從氟聚合物(P)合成時,聚合性雙鍵具有易殘留於側鏈 之適度聚合性之觀點、及可製得具有較良好的耐熱性之交 聯橡膠物品之觀點看來,氟二烯(b)以氟二烯(bl)較佳,以 氟二烯(bll)更佳。 氟二烯(b)可僅單獨使用1種,亦可併用2種以上。 氟聚合物(P)具有以氟二烯(b)為主體之重複單元,且於 源自於氟二烯(b)之重複單元之至少一部分,殘留有具有聚 合性雙鍵之不飽和側鏈。例如,使用 cf2=cf-o-(cf2)4-o-cf=cf2作為氟二烯(b)時,製得之氟聚 合物(P)至少具有於下述式中顯示之殘留有具有聚合性雙鍵 之不飽和側鏈之重複單元。 [化1] F2 /C、c〆The number of carbon atoms of the fluorine alkyl group of Qn is preferably from 3 to 6. The carbon atom number of the fluorine alkyl group of Q1 " 3 is preferably 2 to 5. As the fluorodiene (bl), the following fluorodiene (bll) and (bl2) are preferred. (bll) CF2=CFO-Qf, 1-OCF=CF2; (bl2) CF2=CFOCH2-Qf12-CH2OCF=CF2. However, in the formula, it is a perfluoroalkylene group having 3 to 8 carbon atoms or a perfluoroalkylene group having 3 to 8 carbon atoms having one or more etheric oxygen atoms between carbon atoms and carbon atoms. QFI2 is a perfluoroalkylene group having 2 to 6 carbon atoms or a perfluoroalkylene group having 2 to 6 carbon atoms which has one or more etheric oxygen atoms between carbon atoms and carbon atoms. Specific examples of the fluorodiene (b11) include the following compounds. CF2=CFO(CF2)4OCF=CF2; CF2=CFO(CF2)5OCF=CF2; CF2=CFO(CF2)6OCF=CF2; and CF2=CFO(CF2)4OCF(CF3)CF2OCF=CF2. Specific examples of the fluorodiene (M2) include the following compounds. CF2=CFOCH2(CF2)2CH2OCF=CF2; and CF2=CFOCH2(CF2)4CH2OCF=CF2. As the fluorodiene (b2), the following fluorodiene (b21) is preferred. (b21) CH2=CFCF20-QF21-0CF2CF=CH2. However, in the formula, QF21 is a perfluoroalkylene group having 3 to 8 carbon atoms or a perfluoroalkylene group having 3 to 8 carbon atoms having one or more etheric oxygen atoms between carbon atoms and carbon atoms. Specific examples of the fluorodiene (b21) include the following compounds. Ch2=cfcf2o(cf2)2ocf2cf=ch2; ch2=cfcf2o(cf2)3ocf2cf=ch2; ch2=cfcf2o(cf2)4ocf2cf=ch2; and ch2=cfcf2o(cf2)2ocf(cf3)cf2ocf2cf=ch2 and so on. As the fluorodiene (b3), the following fluorodiene (b31) is preferred. (b31) CH2=CFCF20-QF31-0CF=CF2. In the formula, QF31 is a perfluoroalkylene group having 1 to 6 carbon atoms or a perfluoroalkylene group having 2 to 6 carbon atoms having one or more etheric oxygen atoms between carbon atoms and carbon atoms. Specific examples of the fluorodiene (b31) include the following compounds. CH2=CFCF2OCF(CF3)CF2OCF=CF2; and 11 201229072 CH2=CFCF2OCF(CF3)CF2OCF(CF3)CF2OCF=CF2. When synthesized from a fluoropolymer (P), the polymerizable double bond has a viewpoint of tending to remain moderately polymerizable in the side chain, and a crosslinked rubber article having a relatively good heat resistance can be obtained from the viewpoint of fluorodiene. (b) fluorodiene (bl) is preferred, and fluorodiene (bll) is more preferred. The fluorodiene (b) may be used alone or in combination of two or more. The fluoropolymer (P) has a repeating unit mainly composed of fluorodiene (b), and at least a part of the repeating unit derived from the fluorodiene (b), an unsaturated side chain having a polymerizable double bond remains. . For example, when cf2=cf-o-(cf2)4-o-cf=cf2 is used as the fluorodiene (b), the obtained fluoropolymer (P) has at least a residue represented by the following formula having a polymerization. Repeating unit of the unsaturated side chain of a double bond. [Chemical 1] F2 / C, c〆

I 〉C(=2)4I 〉C(=2)4

V f2C, 氟聚合物(P)之重量平均分子量(以下稱為「Mw」)以 3,000〜50,000為佳,10,000~30,000較佳。若氟聚合物(?)之 Mw在下限值以上,使交聯性氟橡膠組成物硬化而製得之交 聯氟橡膠物品之耐熱性會變得較佳。又,若氟聚合物(P)之 Mw在上限值以下,製造交聯性氟橡膠組成物時,較易於混 合分散至氟橡膠。藉此,易於成形為期望之形狀,且易於 抑制因流動不均勻而使交聯橡膠物品之特性產生偏差之情 12 201229072 況°又’藉由在前述範圍内將氟聚合物設定成高Mw, 可易於製得具有較高熱穩定性之交聯橡膠物品。 而’本發明之Mw及數目平均分子量(以下稱為「Μη」) 係指使用旭硝子公司製ASAHIKLIN AK-225SEC等級1(二 氣五敦丙院與六氟異丙醇之混合溶劑(二氣五氟丙烷/六氟 異丙醇=99/1(體積比)))作為溶劑,藉由凝膠滲透層析(GPC) 以ΡΜΜΑ(聚甲基丙烯酸甲酯)換算分子量所算出者。 殘留於氟聚合物(Ρ)中之側鏈之聚合性雙鍵之含量以 0.2〜2mmol/g為佳,〇·5〜i.5mm〇i/g較佳。前述聚合性雙鍵之 含量可藉由FI9-NMR之測定加以算出。 若聚合性雙鍵之含量在下限值以上,將交聯性氟橡膠 組成物硬化時可易於充分交聯,且容易製得具有良好耐熱 性之父聯橡膠物品。又,若聚合性雙鍵之含量在上限值以 下,易於抑制硬化後因殘留於交聯橡膠物品中之未反應之 聚合性雙鍵之分解所造成的耐熱性下降,又,易於防止因 氟聚合物(P)製造時之交聯反應所造成的膠化或因高分子量 化所造成的流動性下降。 (氟聚合物(P)之合成) 氟聚合物(P)可藉由單獨聚合氟二烯(b)、或將氟單烯 與氟二烯(b)共聚合而製得,單獨聚合或共聚合時,氟二烯 (b)之聚合性雙鍵之一部分將不貢獻於反應而殘留作為側 鏈。 單獨聚合氟二烯(b)、或使氟單烯(a)與氟二烯(b)共聚合 之聚合方法並未有特別限定,可採用懸浮聚合、溶液聚合、 13 201229072 乳化聚合、及塊狀聚合等公知的聚合方法。之中,從可在以 溶劑稀釋之狀態下聚合並抑制因殘留於側鏈之聚合性雙鍵 所造成的分子間之交聯反應之觀點看來,以溶液聚合尤佳。 溶液聚合係在聚合溶劑中,於聚合起始劑單獨添加氣 二烯(b)進行聚合,或添加氟單烯(a)與氟二烯(b)進行聚合之 聚合方法。 作為溶液聚合之聚合溶劑,以生成之氟聚合物(P)可溶 解於其中之含氟溶劑為宜。含氟溶劑例如有:二氣五氟丙 院(HCFC-225) 、 CF3CH2CF2H(HFC-245fa)、 CF3CF2CH2CF2H(HFC-365mfc)、全氟己烷、全氟辛烷、全 i,(2-T^© ^Il(=-T®).CF3CF2CF2CF2CF2CF2H ^ CF3CH2OCF2CF2H 、 CF3CH2OCH2CF3 、及 CF3CF2OCF2CF2OCF2CF3 等。 在氟聚合物(P)之合成中,尤以下列方法為佳,即:不 _人使氟一晞(b)、或氟單烯(a)與氟二烯(b)之全部使用量起 反應’而將其全部使用量巾之_部分預先投人反應容器内 使聚合反應開始’然後在聚合反應之進行中,逐次添加剩 餘的氟單烯(a)及氟二烯(b)進行聚合。 藉此,較可縮窄製得之敦聚合物(p)之分子量分布及組 成分布,而易於減低氟聚合物(P)中分子量小於1〇〇〇之低分 子|成分之含量,又可提升氟聚合物之產率。前述低分 子量成分與分子量在1GGG以上之成分相較之下,每i分子之 聚合性雙鍵之含量會減少。聚合性雙鍵在用於硬化反應 時,-般會伴隨體積收縮,因此藉由減低前述低分子量成 14 201229072 ^之含置,較易使硬化反應均勻進行而製得具有良好的熱 穩疋性與尺寸穩定性之交聯橡膠物品。氟聚合物(P)中之二 述低分子量成分之含量以小於10質量%為佳,小於引 較佳。 、負里% =,在氟單烯(a)與氟二烯(b)之共聚中,除前述低分子 量成分以外’尤其以源自於IL二烯⑻之重複單元之八旦 少,眚暂μ 士 3里車父 貝貝上有可能生成非形成交聯助劑之成分。但,#曰 易地減低 刖述逐次添加氟單稀⑷及說二烯⑻之方法,可輕 疋 此種化合物之生成。 不用說,在氟二烯(b)之單獨聚合中,係使用 (b)100莫耳%。另-方面,减單稀⑷與氟二稀(b)之㈣ 中’敦單稀(a)與氟二晞(b)之莫耳比以1:99〜95:5為佳。又Λ 使用氟乙烯類作為氟單烯⑷時,氟乙烯類與氟二烯㈨:莫 耳比以⑼〜80:20較佳,3請〜㈣尤^若氟乙稀類之 饋入比例在前述上限值以下’氟聚合物(ρ)之分子量會變得 過高而易於抑制㈣性下降。又,可提升製得之交:橡: 物品之伸長度。 作為用於氟聚合物(Ρ)合成之聚合起始劑,可使用1〇小 時半衰溫度在20〜12(TC之有機過氧化物,從防止因聚合起 始劑中之氫原子之摘取反應所造成之反應率下降之觀點看 來,以含氟二醯基過氧化物等含氟過氧化物為佳。, 反應溶液中之聚合起始劑濃度以〇1〜5質量%為佳, 0.5〜2質量%較佳。 又,聚合溫度雖因聚合起始劑之1〇小時半衰溫度與單 15 201229072 體之聚合速度而異,但以2(M2(rc為佳,*〜贼較佳。 於氟聚合物(P)之合成,為了調節分子量,宜使用鍵轉 移劑。 …作為鏈轉移劑,例如有:ccl4、CH3C1、s〇2ci2、cHFci: 等乳化合物’氟院基峨、氣敎基·^等魏合物;及甲 醇、乙醇、異丙醇、己烷、二乙基醚等烴系溶劑。之中, =鏈轉移效率高且可以高產率製㈣聚合物(p)之觀點看 &quot;以S〇2Cl2、與I-(CF2)n-I(n為4或6)為佳 〇 鏈轉移劑之使用量雖因鏈轉移常數而異,但在使用 β 2 2寺相對於在氟二稀(b)單獨聚合中氣二稀⑼之使用 ^或相對於在氣單烯⑷純二_)之絲巾氣單稀(a、 ”狀二轉)之合計量,以莫耳比計在〇·謝〜(U為佳, 〇.〇5^佳。若前述莫耳比在下限值以上,較易於防止 敗聚合物(P)之分子量變得過高。又,若前述莫耳比在上限 值以下,較易於防止氟聚合物(P)之分子量過於下降。 (氟聚合物(P)之精製) 製得之氟聚合物(P)宜藉由聚合後精製分子量小於 1’〇〇〇之低分子量成分而除去。藉由精製,可減低I聚合物 (P)中之低分子量成分,因此,製得之氟聚合物可變成比 以GPC測定之Mw/Mn表現之分子量分布更狹窄分散者。藉 此,可輕易地製得具有良好的熱穩定性與尺寸穩定性之交 聯橡膠物品。 惟’氟聚合物(P)於聚合後未進行精製亦可。 作為分子量小於1,〇〇〇之低分子量成分之除去方法,例 16 201229072 如有··⑷在減壓下加熱氟聚合物(p),除去低分子量成分 之方法處於超臨界狀態之萃取_,從氟聚合物(p) 萃取低分子量成分之方法;⑺㈣聚合物(ρ)之溶液投入 不良溶劑中’使分子量在_〇以上之氟聚合物(ρ)沉殿,再 除去未沉狀低分子量齡之方法;及⑷使用膠透層析除 去低分子量成分之枝[之巾,從操作方法之簡便性、 及擴展規模之容易性之觀點看來,以方法⑷為佳且以於 方法(〇〇後實施方法(石)較佳。 方法(α )中之減壓條件以丨〜丨〇〇hPa為佳 佳’ 1〜10hPa最佳。若壓力在下限值以上, 大,亦可輕易減壓。若壓力在上限值以下 量成分之除去效率。 ’ 1〜20hPa較 即便裝置大小變 ’可提升低分子 方法(α)中之加熱溫度以1〇〇〜15〇&lt;t為佳,12〇〜15〇它 較佳。若溫度訂限似上,可啸短㈣除去低分子量 2分並提升除去效率。若溫度在上限值町,㈣抑制加 熱中產生局部膠化反應。 方法⑹錢«合物(p)域於超臨界狀態之萃取溶 劑接觸後’將氟聚合物(P)與萃取溶劑分離,藉以除去含於 氟聚合物(P)中之低分子量成分之方法。 、萃取溶_可溶解前述低分子量成分,使該低分子量 成t從氟聚合物(p)分狀制。萃取_只要斜在使用 之卒取洛劑之臨界溫度以上且低於13叱之溫度範圍,且在 料取溶叙臨界壓力以上之壓力料τ,萃取低分子量 成分者,即未有特別限定。 17 201229072 萃取溶劑例如有二氧化碳、三氟曱烷(CF3H ; R23)、及 全氟乙烷(C#6 ; R116)等碳數1〜3之氟碳化物等。之中,在 易於a又在超臨界狀態並具有良好的萃取效率之觀點上,以 二氧化碳、三氟甲烷、及全氟乙烷為佳,二氧化碳較佳。 萃取溶劑可僅單獨使用1種,亦可併用2種以上。 方法(万)中之萃取溶劑之溫度宜在使用之萃取溶劑之臨 界溫度以上且低於13〇。(3。又,萃取溶劑之壓力在該萃取溶 劑之臨界壓力以上。即,在方法(/5),以使設在低於13〇&lt;)(:之 超臨界流體之萃取溶劑與氟聚合物(p)接觸之方法為宜。 萃取浴劑之溫度只要在前述範圍内,可因應使用之萃取 溶劑適當設定。萃取溶劑之溫度下限以較臨界溫度高〇rc之 溫度較佳。萃取溶劑之溫度上限以1〇〇t:較佳,8(rc更佳。 萃取溶劑之壓力只要在前述範圍内,可因應使用之萃 取溶劑適當設定。萃取溶劑之壓力下限以較臨界壓力高 10,000Pa之壓力為佳’以較臨界壓力高川^^以之壓力較佳。 在方法(点)中’係藉由提高萃取溶劑之密度而提升低分 子量成分之萃取效率。此乃是因為萃取溶劑之密度愈高, 愈可提升與低分子里成分之萃取溶劑對應之溶解度。 萃取時之萃取溶劑之密度_即,超臨界狀態之萃取溶 劑之密度一在〇_2g/Cm3以上且在丨3g/cm3以下為佳。 又,在方法(召)中,於萃取溶劑中,亦可併用鹵化烴系 溶劑或烴系溶劑(以下稱為「添加劑㈣―)」)作為輔助 溶劑。從溶解性之觀點看來,添加劑以鹵化烴系溶劑為佳。 || 化煙系溶劑例如有:、 18 201229072 CF3CF2CHC12、CFC12CF2C卜 ecu、CF3CHFCHFCF2CF3、 及 cf3ch2ocf2cf2h 等。 煙系溶劑例如有:甲醇、乙醇、丙醇、異丙醇、及二 曱基醚等。 添加劑可單獨使用1種,亦可併用2種以上。 方法(万)係使用處於超臨界狀態之萃取溶劑進行萃取 者,所以可有效率地減低低分子量體,使製得之氟聚合物 (p)之分子量分布成狹窄分散。 方法(7 )係將不良溶劑投入氟聚合物(P)後將上清液分 離,藉以除去含於氟聚合物(P)中之低分子量成分之方法。 使用於方法(T )中之不良溶劑例如有:甲醇、己烷、及 二乙基醚等。 從易於製得具有良好的耐熱性及耐藥性之交聯橡膠物 品之觀點看來,相對於氟橡膠之100質量份,本發明之交聯 性鼠橡膠組成物中之敦聚合物(P)之含量以1〜質量份為 佳,2〜45質量份較佳,3〜40質量份更佳,若氟聚合物(p)之 含量在下限值以上,可輕易地充分形成交聯而易於製得具 有良好的耐熱性之交聯橡膠物品。若氟聚合物(p)之含量在 上限值以下,即便交聯橡膠物品中存在有源自氟聚合物(p) 之不穩定末端基(羧基等),亦可輕易抑制因該基所造成之熱 穩定性之下降。 [氟橡膠] 氟橡膠可藉由下列方法交聯,即:(1)使用有機過氧化 物,藉由加熱使自由基生成並交聯之方法;或(2)照射放射線 201229072 使自由基生成並交聯之方法。以下,有時會將方法(1)之交聯 稱為有機過氧化物交聯,將方法(2)之交聯稱為放射線交聯。 氟橡膠之氟含量以4〇質量。/〇以上為佳,5〇質量%以上較 佳,55質量%以上更佳。若氟含量在下限值以上,則易於 製得具有良好的耐熱性、耐藥性、電絕緣性、與耐蒸汽性 之父聯橡膠物品。氟橡膠之氟含量’係表示全氟原子之合 計質量相對於氟橡膠全質量之比例。 氟橡膠例如有:氟化亞乙烯/六氟丙烯系共聚物、氟化 亞乙烯/TFE/六氟丙稀系共聚物、氟化亞乙稀/CTFE系共聚 物、TFE/丙烯系共聚物、TFE/丙烯/氟化亞乙烯系共聚物、 六氟丙烯/乙烯系共聚物、TFE/全氟烷基乙烯基醚系共聚物、 及氟化亞乙稀/TFE/全氟烧基乙烯基醚系共聚物等。該等可 單獨使用1種,亦可併用2種以上。 從具有良好的耐藥性之觀點看來,氟橡膠以選自於由 TFE/丙烯系共聚物、氟化亞乙烯/TFE/六氟丙烯系共聚物、 及TFE/王氟燒基乙稀基喊系共聚物所構成之群組中之1種 以上為佳。 從具有良好的耐熱性之觀點看來,氟橡膠以將單體具 有之氫原子全部被氟原子所取代之全氟單體加以聚合而製 得之全氟彈性體尤佳。 作為全氟彈性體,以具有源自於TFE之重複單元、及源 自於CF2=CF-0-RF2(惟,式中,rF2為碳數uo之全氟烷基、 或於碳原子-碳原子間具有1個以上醚性氧原子之碳數卜汕 之王氣院基。以下稱為「全氟單體(χ)」。)之重複單元之彈 20 201229072 性體(以下稱為「彈性體(χ)」)為佳。 在彈性體(X)中,源自於全氟單體(X)之重複單元可僅為 1種,亦可為2種以上。 全氟單體(X)中iRF2之全氟烷基之碳數以1〜8為佳。RF2 之全氟烧基可為直鏈狀,亦可為分枝鏈狀。 作為全氟單體(X),以cf2=cf-o-cf3 &gt;cf2=cf-o-cf2cf3、 cf2=cf-o-cf2cf2cf3、cf2=cf-o-cf2cf(cf3)ocf2cf2cf3、 及CF2=CF-0-CF2CF2-0-CF2CF3為佳,CF2=CF-0-CF3較佳。 從具有良好的橡膠物性之觀點看來,彈性體(X)中之共 聚比率以源自於TFE之重複單元/以全氟單體(X)為主體之重 複單元=30/70〜80/20(莫耳比)為佳。 又,氟橡膠不限於全氟彈性體,聚合全氟單體時,亦 可使用利用包含少量氫原子之鏈轉移劑或共單體所製得之 彈性體。 包含氫原子之鏈轉移劑例如可舉:甲烷、乙烷、丙烷、 丁烷、戊烷、己烷、環己烷等鏈狀或環狀之飽和烴類;曱 醇、乙醇、丙醇等醇類;及三級十二烷基硫醇、正十二烷 基硫醇、正十八烷基硫醇等硫醇類等。該等鏈轉移劑可單 獨使用1種,亦可併用2種以上。 包含氫原子之共單體例如可舉:cf2=cf-o-ch2cf3、 cf2=cf-o-ch2cf2cf2cf3、cf2=cf-o-ch2(cf2cf2)2h、 CF2=CF-0-CF2CF2CH2-I 、 CF2=CF-0-CF2CF2CH2-Br 、 cf2=cf-o-cf2cf2(cf3)-o-cf2cf2ch2-i 、 及 cf2= CF-0-CF2CF2(CF3)-0-CF2CF2CH2-Br 等。該等共單體可單獨 21 201229072 使用1種’亦可併用2種以上。 使用前述鏈轉移劑及共單體之至少一方時,從交聯橡 膠物品之耐熱性及耐藥性特性之觀點看來,彈性體中之 氫原子之含量以0.5質量%以下為佳,〇 3質量%以下較佳, 〇.1質量%以下尤佳。 又,職橡膠而言,尤其在有機過氧化物交聯之情況 下’以具_原子㈣原子之至少_方之全氟彈性體(以下 亦稱為#性體⑺」)為佳,以具有礙原子之全乳彈性體較 佳具有峨原子及漠原子之至少一方之全氟彈性體係指全 I彈性體Μ原子之丨㈣上被彻、子錢原子所取代之 彈险體《具㈣原子之全氣彈性體係指錢彈性體之貌原 子之1個以上被蛾原子所取代之彈性體。 彈性體(Y)例如可舉日本特開昭仏⑵伙號公報、日本 特公昭53-4115號公報、及日本特開日召59_2〇31〇號公報中所 。己載之彈性體。具體而言,例如有:選自於由TFE及全氟單 體(X)所構成之群組中之1種以上之全氟單體,再加上共聚具 有碘原子及溴原子之至少一方之單體(以下稱為「單體(y)」) 所製得之彈性體;及在以I-RF3-I(式中,V3為碳數卜8之全 氟伸烷基、或於碳原子-碳原子間具有丨個以上醚性氧原子 之碳數1~8之全氟伸烷基)表示之化合物之存在下,使前述 單體共聚所製得之彈性體等。 單體(y)例如可舉:(^2=&lt;^-汾、(:112=(:1^?2€?2-81·、 CF2= CF-〇-CF2CF2-I ' CF2=CF-0-CF2CF2-Br CF2=CF-0-CF2CF2CH2-I、CF2=CF-0-CF2CF2CH2-Br、 22 201229072 CF2=CF-〇-CF2CF2(CF3)-〇-CF2CF2CH2-I 、及 CF2= CF-0-CF2CF2(CF3)-0-CF2CF2CH2-Br 等。 作為I-RF3-I之具體例,例如可舉:二碘二氟甲烷、1,2-二碘全氟乙烷、1,3-二碘全氟丙烷、1,4-二碘全氟丁烷、1,5-二碘全氟戊烷、1,6-二碘全氟己烷、1J-二碘全氟庚烷、及 1,8-二碘全氟辛烷等。之中,以1,4-二碘全氟丁烷、與ι,6-二碘全氟己烷為佳,1,4-二碘全氟丁烷尤佳。 彈性體(Y)中之碘原子及溴原子以鍵結於高分子末端 為佳。 從易於製得具有良好的橡膠物性與壓縮永久應變之交 聯橡膠物品之觀點看來,彈性體(Y)中之碘原子及溴原子之 合計含量以0.1〜1.5質量%為佳,0.2〜1.0質量%較佳, 0.25〜1.〇質量%尤佳。 就已上市之氟橡膠中理想者而言,諸如有:商品名 「AFLAS PFE-1100」(炮硝子公司製,TFE/全氟烷基乙烯 基醚共聚物)、商品名「AFLAS 100S」(旭硝子公司製,tfe/ 丙婦共聚物)、及商品名「AFLAS 200P」(旭;ε肖子公司製, TFE/丙烯/氟化亞乙烯共聚物)等可進行有機過氧化物交聯 之氣橡膠。 [有機過氧化物] 在藉由有機過氧化物交聯使本發明之交聯性氟橡膠組 成物硬化時,以本發明之交聯性氟橡膠組成物中含有有機 過氧化物為佳。在使交聯性氟橡膠組成物以放射線交聯而 硬化時,無須特別含有有機過氧化物。 23 201229072 有機過氧化物只要為可藉由加熱輕易使自由基生成者 即可,以半衰期為1分鐘之溫度在130〜220°C者為佳。具體 而言’諸如有:1,1-二(三級己基過氧化)_3,5,5-三曱基環己 院、2,5-二曱基己烧-2,5-二氫過氧化物、二-三級丁基過氧 化物、三級丁基異丙苯基過氧化物、二異丙苯基過氧化物、 α,α 雙(三級丁基過氧化)-對二異丙苯、2,5-二曱基_2 5_ 一(二級丁基過氧化)-己院、2,5-二甲基-2,5-二(三級丁基過 氧化)-己炔-3、一笨曱醯基過氧化物、三級丁基過氧化苯、 2,5-二甲基-2,5-二(苯曱醯基過氧化)己烷、三級丁基過氧化 馬來酸、及二級己基過氧化異丙基單碳酸酯等。之中,以 α,α’-雙(三級丁基過氧化)-對二異丙苯尤佳。 有機迴巩化物可單獨使用 ’ ^里从上〇 當本發明之交聯性氟橡膠組成物含有有機過氧化 時,有機過氧化物之含量相對於氟橡膠1〇〇質量份,以〇 ι 質量份為佳’ 0.2〜4質量份較佳,Q 5〜3f量份更佳。若有 過氧化物之含量訂限值m提升交聯效率。 過氧化物之含量在上限值以下,則易於抑制對自由基反 無貢獻之無效分解物之生成量。 [其他成分] ------人-夂應之觀點看來 膠組成物以含㈣受體為佳 酸受體例如可舉:氧化鎂、氧化辞、氫氧化約 ⑽m生亞•錯、及水滑 與氧化辞為佳。酸受體可單獨使用1種,亦可併用又 24 201229072 當本發明之交聯性橡膠組成物含有酸受體時,酸受體 之含量相對於氟橡膠100質量份,以0.1〜20質量份為佳, 0.2〜10質量份較佳。若酸受體之含量在下限值以上,易於 獲付酸受體之效果。若酸受體之含量在上限值以下,則易 於抑制會損傷交聯橡膠物品之橡膠物性。 從可提升製得之交聯橡膠物品之強度之觀點看來,本 發明之交聯性氟橡膠組成物以含有填充劑為佳。填充劑以 碳黑為佳。 碳黑只要是作為橡膠之摻混用所使用者,即無特別限 定。就具體例而言,例如有:爐黑、乙炔碳黑、熱碳黑、 槽黑、及石墨等。之中,以爐黑較佳。 破黑等級以 HAF-LS、HAF、HAF-HS、FEF、GPF、APF、 SRF-LM、SRF-HM、及MT為佳,MT尤佳。 當本發明之交聯性氟橡膠組成物含有填充劑時,填充 劑之含量相對於氟橡膠100質量份,以5〜100質量份為佳, 10〜50質量份較佳。若填充劑之含量在下限值以上,易於獲 知·填充材之效果。若填充劑之含量在上限值以下,則易於 抑制交聯橡膠物品之拉伸特性下降。又,只要填充劑之含 ®在削述範圍内’製得之交聯橡膠物品之強度與拉伸之平 衡可維持較良好的關係。 又’本發明之交聯性氟橡膠組成物亦可含有補強材、 加工助劑、滑劑、潤滑劑、難燃劑、抗靜電劑、著色劑、 及紫外線吸收劑等添加劑。 就補強材而言,例如可舉:聚四氟乙烯、乙烯/TFE共 25 201229072 聚物等氟樹脂、玻璃纖維、碳纖維、及白碳等。 當本發明之交聯性款橡膠組成物含有補強材時,補強 材之含量相對於氟橡膠100質量份計,以5〜2〇〇質量份為 佳,10〜100質量份較佳。 、 就加工助劑而言,例如可舉:高級脂肪酸之驗金屬鹽 等。之中,以硬脂酸鹽、及月桂酸鹽為佳。 當本發明之交聯性氟橡膠組成物含有加工助劑時,加 工助劑之含量相對於4橡膠1GG質量份計,則卜2()質量份 為佳,0.2〜H)質量份較佳,卜5„份更佳。若加工助劑在 下限值以上’交聯橡膠物品之張力強度會顯著下降而易 於抑制熱老化後之拉伸或張力強度之變化增大。若加工助 劑之含量在上限值以下,則易於抑制交聯橡膠物品表面產 生起霜、或使交聯橡膠物品之硬度變得過高、或使耐藥性 與耐蒸汽性下降之情況。 [交聯性氟橡膠組成物之製造方法] 本發明之父聯性氟橡膠組成物之製造方法並未有特別 限定,可採用習知的公知方法。之中,以使用雙輥機、密 閉式/¾煉機、“揉機專捏合機,將氟橡膠、I聚合物(P)、 及視需求使用之有機過氧化物、碳黑、酸受體、與其他添 加劑等予以揑合之方法為佳。又,亦可採用在將前述各成 分溶解分散至溶劑中之狀態下加以揑合調製之方法。 就前述各成分之混合順序而言,宜首先藉由發熱使難 以產生反應或分解之成分與氟橡膠充分揑合後,再將易反 應之成分或易分解之成分予以摻混並揑合。 26 201229072 例如,在使用有機過氧化物時,以爾後摻混並揑合有 機過氧化物為佳。此時,揑合之際,從不使交聯反應進行 之觀點看來,以將捏合機予以水冷維持在⑽〜丨加它之溫度 範圍内為佳。 a 以上所説明之本發明之交聯性氟橡膠組 有良好的耐藥性之氣橡膠…由於是藉由有機= 父聯或放射線交聯利用自由基進行交聯,因此可在不使氟 橡膠具有之_性下降的情況下,製得具有良好的耐藥: 之交聯橡膠物品 又 ,由於使用氟聚合物(p)作為交聯助劑 可形成充分的交聯,因此亦可達成良好的耐熱性。所以, 只要使用本發明之交聯性氣橡膠組成物,即可製得兼具良 好的对藥性與耐熱性之交聯橡膠物品。 &lt;交聯橡膠物品&gt; 本發明之交聯橡膠物品係將前述本發明之交聯性敗橡 膠組成物交聯所形成之物品。 本發明之交聯橡膠物品在汽車等輸送機械、—般機器、 用電機器、化學裝置工業、及半導體等廣泛的領域中,可 作為〇環、密封#、密合墊、油封、及軸承密封等密封材、 光圈、緩衝材、防震材、電線被覆材、工業皮帶類、管· 蛇管類、與片材類等各構件適當使用。之中,從在高溫中 具有良好的耐藥性’此外在強度、硬度、模數、與耐熱老 化性等基本特性亦有優異表現之觀點看來,以密封材為 佳,又以石油探勘用之密封材較佳。 [交聯橡膠物品之製造方法] 27 201229072 本發明之交聯橡膠物品可藉由使用本發明之交聯性氟 橡膠組成物,以有機過氧化物交聯或放射線交聯使其硬化 而成形製得。 本發明之交聯性氟橡膠組成物之成形不論在有機過氧 化物交聯及放射線交聯之任一情況,皆可採用押出成形、 射出成形、轉印成形、及壓製成形等習知的公知成形方法。 就以有機過氧化物交聯製得交聯橡膠物品之方法之具 體例而言,例如有下列方法,即:使用具有與交聯橡膠物 品1份或數份之形狀呈互補形狀之腔之模具,於該腔中填充含 有有機過氧化物之交聯性氟橡膠組成物後,加熱模具使其硬 化° 加熱溫度以130〜220。(:為佳,140〜200°C較佳,150〜200 C尤佳。 又,亦宜視需求以電、熱風、或蒸氣等作為熱源之烘 芽目等,將已以前述條件加熱交聯之交聯橡膠物品(一次交聯 物)進一步加熱使交聯進行(以下稱為「二次交聯」)。藉由 進行一次交聯’可使交聯橡膠物品中含有之有機過氧化物 之殘渣分解揮散,以減低其量。 —次父聯時之加熱溫度以150〜28〇r為佳,180。(:〜260°c 較佳,200〜250°C更佳。 —次父聯巾之加熱時間以1〜4 8小時為佳 ,2〜24小時較佳。 '沈藉由放射線交聯製得交聯橡膠物品之方法之具體例 而&amp; ’例如有下列方法’即:將本發明之交聯性i橡膠組 成物溶解分散於適當的溶射作浮溶液,並藉由將其 28 201229072 予以塗佈等而成形且使其乾燥後,照射放射線使其硬化。 就放射線而言,例如可舉:電子束、與r線等游離性 放射線。The weight average molecular weight (hereinafter referred to as "Mw") of the fluoropolymer (P) of V f2C is preferably 3,000 to 50,000, more preferably 10,000 to 30,000. When the Mw of the fluoropolymer (?) is at least the lower limit value, the heat resistance of the crosslinked fluororubber article obtained by curing the crosslinkable fluororubber composition is improved. In addition, when the Mw of the fluoropolymer (P) is at most the upper limit, when the crosslinkable fluororubber composition is produced, it is easier to mix and disperse into the fluororubber. Thereby, it is easy to form into a desired shape, and it is easy to suppress the deviation of the characteristics of the crosslinked rubber article due to flow unevenness. 12 201229072 By setting the fluoropolymer to a high Mw within the aforementioned range, Crosslinked rubber articles having higher heat stability can be easily produced. The 'Mw of the present invention and the number average molecular weight (hereinafter referred to as "Μη") refer to the use of Asahi Glass Co., Ltd. ASAHIKLIN AK-225SEC grade 1 (dioxane and hexafluoroisopropanol mixed solvent (two gas five) Fluoropropane/hexafluoroisopropanol = 99/1 (volume ratio))) was calculated as a solvent by gel permeation chromatography (GPC) in terms of molecular weight in terms of hydrazine (polymethyl methacrylate). The content of the polymerizable double bond remaining in the side chain in the fluoropolymer (yttrium) is preferably 0.2 to 2 mmol/g, more preferably 5 to 1.5 mm 〇i/g. The content of the above polymerizable double bond can be calculated by measurement by FI9-NMR. When the content of the polymerizable double bond is at least the lower limit value, the crosslinkable fluororubber composition can be easily crosslinked easily when it is cured, and it is easy to obtain a parent-linked rubber article having good heat resistance. In addition, when the content of the polymerizable double bond is at most the upper limit value, it is easy to suppress a decrease in heat resistance due to decomposition of unreacted polymerizable double bonds remaining in the crosslinked rubber article after curing, and it is easy to prevent fluorine The gelation caused by the crosslinking reaction in the production of the polymer (P) or the decrease in fluidity due to the high molecular weight. (Synthesis of fluoropolymer (P)) The fluoropolymer (P) can be obtained by polymerizing fluorodiene (b) alone or by copolymerizing fluoromonoolefin with fluorodiene (b), either alone or in combination. At the time of polymerization, a part of the polymerizable double bond of the fluorodiene (b) does not contribute to the reaction and remains as a side chain. The polymerization method in which the fluorodiene (b) is polymerized alone or the fluoromonoolefin (a) and the fluorodiene (b) are copolymerized is not particularly limited, and suspension polymerization, solution polymerization, and emulsification polymerization of 13 201229072 may be employed. A known polymerization method such as polymerization. Among them, solution polymerization is particularly preferable from the viewpoint of being polymerizable in a solvent-diluted state and suppressing the crosslinking reaction between molecules due to the polymerizable double bond remaining in the side chain. The solution polymerization is a polymerization method in which a gas-diene (b) is separately added to a polymerization initiator in a polymerization solvent, or a polymerization method in which a fluoromonoolefin (a) and a fluorodiene (b) are polymerized is added. As the polymerization solvent for solution polymerization, a fluorine-containing solvent in which the produced fluoropolymer (P) is soluble is preferable. Examples of the fluorine-containing solvent include: difluoropentafluoride (HCFC-225), CF3CH2CF2H (HFC-245fa), CF3CF2CH2CF2H (HFC-365mfc), perfluorohexane, perfluorooctane, all-i, (2-T^ © ^Il(=-T®).CF3CF2CF2CF2CF2CF2H ^ CF3CH2OCF2CF2H, CF3CH2OCH2CF3, and CF3CF2OCF2CF2OCF2CF3, etc. In the synthesis of fluoropolymer (P), the following methods are preferred, namely: no _ people make fluorine 晞 (b) Or the fluoromonoolefin (a) reacts with the total amount of fluorodiene (b) and uses all of the amount of the towel to be pre-injected into the reaction vessel to start the polymerization reaction. Then, during the polymerization reaction Adding the remaining fluoromonoolefin (a) and fluorodiene (b) one by one to carry out polymerization. Thereby, the molecular weight distribution and composition distribution of the obtained polymer (p) can be narrowed, and the fluoropolymer is easily reduced. (P) The content of the low molecular weight component of the molecular weight of less than 1 , can also increase the yield of the fluoropolymer. The polymerizable property per molecule of the low molecular weight component is compared with the component having a molecular weight of 1 GGG or more. The content of the double bond is reduced. When the polymerizable double bond is used for the hardening reaction, it is generally accompanied by volume shrinkage. Therefore, by reducing the inclusion of the low molecular weight of 14 201229072 ^, it is easier to uniformly carry out the hardening reaction to obtain a crosslinked rubber article having good thermal stability and dimensional stability. In the fluoropolymer (P) The content of the second low molecular weight component is preferably less than 10% by mass, less than preferably. 5% by weight, in the copolymerization of the fluoromonoolefin (a) and the fluorodiene (b), in addition to the low molecular weight component described above. 'In particular, the eight-denier-derived repeating unit derived from IL-diene (8) may have a component that does not form a cross-linking aid on the parent-child Babe. However, #曰易地低低刖The method of adding fluoromonoester (4) and said diene (8) one by one can lightly produce the compound. Needless to say, in the separate polymerization of fluorodiene (b), (b) 100 mol% is used. , minus thinner (4) and fluorodiuret (b) (iv) The molar ratio of 'done mono (a) to fluorodioxin (b) is preferably 1:99~95:5. As the fluoromonoolefin (4), the vinyl fluoride and the fluorodiene (nine): the molar ratio is preferably (9) to 80:20, and the ratio of the feeding ratio of the fluoroethylene to the above is preferably Below the limit, the molecular weight of the fluoropolymer (ρ) will become too high to easily suppress the decrease in (4). In addition, the resulting bond can be improved: the elongation of the article: as the fluoropolymer (Ρ) The polymerization initiator can be used at a half-life temperature of 20 to 12 (the organic peroxide of TC, from the viewpoint of preventing a decrease in the reaction rate due to the extraction reaction of hydrogen atoms in the polymerization initiator). Preferably, a fluorine-containing peroxide such as a fluorine-containing dithiol peroxide is preferred. The concentration of the polymerization initiator in the reaction solution is preferably from 1 to 5 mass%, more preferably from 0.5 to 2 mass%. Further, although the polymerization temperature varies depending on the half-life temperature of the polymerization initiator for 1 hour and the polymerization rate of the single 15 201229072 body, it is 2 (M2 (rc is preferred, *~ thief is preferred. fluoropolymer (P) In order to adjust the molecular weight, it is preferred to use a bond transfer agent. As a chain transfer agent, for example, ccl4, CH3C1, s〇2ci2, cHFci: and the like, the milk compound 'fluorine base 峨, gas 敎 base·^, etc. And hydrocarbon-based solvents such as methanol, ethanol, isopropanol, hexane, diethyl ether, etc. Among them, = chain transfer efficiency is high and can be produced in high yield (4) from the viewpoint of polymer (p) &quot; The amount of 2Cl2 and I-(CF2)nI (n is 4 or 6) is better than the chain transfer constant, but in the use of β 2 2 temple relative to the fluorine disulfide (b) alone The use of gas dilute (9) in the polymerization ^ or relative to the monotonic (a, "two-turn" of the silk scarf in the gas monoolefin (4) pure _), in terms of molar ratio in 〇·谢~(U Preferably, 〇.〇5^ is better. If the molar ratio is above the lower limit, it is easier to prevent the molecular weight of the polymer (P) from becoming too high. Moreover, if the molar ratio is below the upper limit, Easy The molecular weight of the fluoropolymer (P) is too low. (Refining the fluoropolymer (P)) The fluoropolymer (P) obtained is preferably removed by purifying a low molecular weight component having a molecular weight of less than 1 Å after polymerization. By purifying, the low molecular weight component in the I polymer (P) can be reduced, and therefore, the obtained fluoropolymer can be made to be narrower than the molecular weight distribution expressed by MPC/Mn measured by GPC. It is easy to obtain a crosslinked rubber article having good thermal stability and dimensional stability. However, the 'fluoropolymer (P) may not be purified after polymerization. As a low molecular weight component having a molecular weight of less than 1, 〇〇〇 Removal method, Example 16 201229072 If there is a method of heating a fluoropolymer (p) under reduced pressure, a method of removing a low molecular weight component is in a supercritical state, and a method of extracting a low molecular weight component from a fluoropolymer (p) (7) (4) The solution of the polymer (ρ) is put into a poor solvent, 'the fluoropolymer (ρ) having a molecular weight above 〇, and the method of removing the un-sinked low molecular weight age; and (4) using a gel permeation chromatography to remove low Branch of molecular weight component From the viewpoint of the simplicity of the operation method and the easiness of expanding the scale, it is preferable to use the method (4) and the method (the method after the subsequent method (stone) is preferable. The decompression condition in the method (α) is 丨~丨〇〇hPa is the best for Jiajia' 1~10hPa. If the pressure is above the lower limit, it can be easily decompressed. If the pressure is below the upper limit, the removal efficiency of the component is less than '1~20hPa even if the device size The heating temperature in the low molecular method (α) can be improved by 1 〇〇 15 15 〇 < t, preferably 12 〇 15 15 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 2 points and improve removal efficiency. If the temperature is in the upper limit, (4) the local gelation reaction is generated during the suppression of heating. The method (6) is a method in which the fluoropolymer (P) is separated from the extraction solvent after the contact of the extraction solvent in the supercritical state, thereby removing the low molecular weight component contained in the fluoropolymer (P). The extraction solution _ dissolves the low molecular weight component to form the low molecular weight t from the fluoropolymer (p). The extraction _ is not particularly limited as long as it is inclined above the critical temperature of the used explosive agent and is below the temperature range of 13 Torr, and the pressure τ above the critical pressure of the solvent is extracted, and the low molecular weight component is extracted. 17 201229072 The extraction solvent may, for example, be a fluorocarbon having a carbon number of 1 to 3 such as carbon dioxide, trifluorodecane (CF3H; R23) or perfluoroethane (C#6; R116). Among them, carbon dioxide, trifluoromethane, and perfluoroethane are preferred from the viewpoints of ease of a supercritical state and good extraction efficiency, and carbon dioxide is preferred. The extraction solvent may be used alone or in combination of two or more. The temperature of the extraction solvent in the process (10,000) is preferably above the critical temperature of the extraction solvent used and below 13 Torr. (3. Further, the pressure of the extraction solvent is above the critical pressure of the extraction solvent. That is, in the method (/5), the extraction solvent and the fluorine polymerization of the supercritical fluid set below 13 〇&lt;) The method of contacting the substance (p) is preferably carried out. The temperature of the extraction bath is appropriately set according to the extraction solvent to be used, and the lower limit of the temperature of the extraction solvent is preferably higher than the critical temperature by rc. The upper limit of the temperature is 1 〇〇 t: preferably, 8 (rc is better. The pressure of the extraction solvent is appropriately set in accordance with the extraction solvent used as long as it is within the above range. The lower limit of the pressure of the extraction solvent is 10,000 Pa higher than the critical pressure. It is better to use a higher critical pressure than high pressure. In the method (point), the extraction efficiency of the low molecular weight component is improved by increasing the density of the extraction solvent. This is because the density of the extraction solvent is higher. The solubility corresponding to the extraction solvent of the low molecular component can be improved. The density of the extraction solvent during extraction _ that is, the density of the extraction solvent in the supercritical state is above 〇_2g/cm3 and below 丨3g/cm3. Further, in the method (call), a halogenated hydrocarbon solvent or a hydrocarbon solvent (hereinafter referred to as "additive (4) -)") may be used in combination as an auxiliary solvent in the extraction solvent. From the viewpoint of solubility The additive is preferably a halogenated hydrocarbon solvent. || The chemical solvent is, for example, 18 201229072 CF3CF2CHC12, CFC12CF2C, ecu, CF3CHFCHFCF2CF3, and cf3ch2ocf2cf2h, etc. The flue solvent is, for example, methanol, ethanol, propanol or isopropanol. And the dimethyl ether and the like. The additives may be used singly or in combination of two or more. The method (10,000) is carried out by using an extraction solvent in a supercritical state, so that the low molecular weight body can be efficiently reduced. The molecular weight distribution of the obtained fluoropolymer (p) is narrowly dispersed. The method (7) is carried out by introducing a poor solvent into the fluoropolymer (P) and separating the supernatant to remove the fluoropolymer (P). A method of using a low molecular weight component. The poor solvent used in the method (T) is, for example, methanol, hexane, diethyl ether or the like. It is easy to obtain a crosslinked rubber material having good heat resistance and chemical resistance. From the viewpoint of the product, the content of the terpene polymer (P) in the crosslinkable squirrel rubber composition of the present invention is preferably 1 part by mass, more preferably 2 to 45 parts by mass, per 100 parts by mass of the fluororubber. More preferably, it is 3 to 40 parts by mass, and if the content of the fluoropolymer (p) is at least the lower limit value, cross-linking can be easily sufficiently formed to easily produce a crosslinked rubber article having good heat resistance. When the content of p) is at most the upper limit value, even if an unstable terminal group (carboxyl group or the like) derived from the fluoropolymer (p) is present in the crosslinked rubber article, the thermal stability due to the base can be easily suppressed. [Fluororubber] Fluororubber can be crosslinked by the following methods: (1) using organic peroxides to generate and crosslink free radicals by heating; or (2) irradiating radiation 201229072 to free radicals The method of generating and cross-linking. Hereinafter, the cross-linking of the method (1) is referred to as organic peroxide cross-linking, and the cross-linking of the method (2) is referred to as radio cross-linking. The fluorine content of the fluororubber is 4 〇. It is preferable that it is more than 5 % by mass, and more preferably 55% by mass or more. When the fluorine content is at least the lower limit value, it is easy to obtain a parent-linked rubber article having excellent heat resistance, chemical resistance, electrical insulation properties, and steam resistance. The fluorine content of the fluororubber is a ratio of the total mass of the perfluoro atoms to the total mass of the fluororubber. Examples of the fluororubber include a vinylidene fluoride/hexafluoropropylene copolymer, a vinylidene fluoride/TFE/hexafluoropropylene copolymer, a fluorinated ethylene/CTFE copolymer, and a TFE/propylene copolymer. TFE/propylene/fluorinated vinylene copolymer, hexafluoropropylene/ethylene copolymer, TFE/perfluoroalkyl vinyl ether copolymer, and fluorinated ethylene/TFE/perfluoroalkyl vinyl ether A copolymer or the like. These may be used alone or in combination of two or more. From the viewpoint of having good chemical resistance, the fluororubber is selected from the group consisting of TFE/propylene copolymer, fluorinated vinylene/TFE/hexafluoropropylene copolymer, and TFE/Wang-fluoroethylene base. It is preferred that one or more of the groups consisting of the copolymers are copolymerized. From the viewpoint of having good heat resistance, the fluororubber is preferably a perfluoroelastomer obtained by polymerizing a perfluoromonomer in which all of the hydrogen atoms of the monomer are replaced by fluorine atoms. As a perfluoroelastomer, having a repeating unit derived from TFE, and derived from CF2=CF-0-RF2 (wherein, where rF2 is a carbon number uo of a perfluoroalkyl group, or a carbon atom-carbon The carbon number of one or more etheric oxygen atoms in the atom between the atoms. The following is called "perfluoromonomer (χ)".) The repeating unit of the bomb 20 201229072 (hereinafter referred to as "elasticity" Body (χ)") is better. In the elastomer (X), the number of repeating units derived from the perfluoromonomer (X) may be one or two or more. The perfluoroalkyl group of iRF2 in the perfluoromonomer (X) preferably has 1 to 8 carbon atoms. The perfluoroalkyl group of RF2 may be linear or branched. As perfluoromonomer (X), cf2=cf-o-cf3 &gt;cf2=cf-o-cf2cf3, cf2=cf-o-cf2cf2cf3, cf2=cf-o-cf2cf(cf3)ocf2cf2cf3, and CF2= CF-0-CF2CF2-0-CF2CF3 is preferred, and CF2=CF-0-CF3 is preferred. From the viewpoint of having good rubber physical properties, the copolymerization ratio in the elastomer (X) is a repeating unit derived from TFE / a repeating unit mainly composed of a perfluoromonomer (X) = 30/70 to 80/20 (Morbi) is better. Further, the fluororubber is not limited to a perfluoroelastomer, and when a perfluoromonomer is polymerized, an elastomer obtained by using a chain transfer agent or a comonomer containing a small amount of hydrogen atoms can also be used. Examples of the chain transfer agent containing a hydrogen atom include chain or cyclic saturated hydrocarbons such as methane, ethane, propane, butane, pentane, hexane, and cyclohexane; and alcohols such as decyl alcohol, ethanol, and propanol. And thiols such as tertiary dodecyl mercaptan, n-dodecyl mercaptan, and n-octadecyl mercaptan. These chain transfer agents may be used singly or in combination of two or more. The comonomer containing a hydrogen atom may, for example, be cf2=cf-o-ch2cf3, cf2=cf-o-ch2cf2cf2cf3, cf2=cf-o-ch2(cf2cf2)2h, CF2=CF-0-CF2CF2CH2-I, CF2 =CF-0-CF2CF2CH2-Br, cf2=cf-o-cf2cf2(cf3)-o-cf2cf2ch2-i, and cf2=CF-0-CF2CF2(CF3)-0-CF2CF2CH2-Br. These comonomers may be used alone or in combination of two or more types. When at least one of the chain transfer agent and the comonomer is used, the content of the hydrogen atom in the elastomer is preferably 0.5% by mass or less from the viewpoint of heat resistance and chemical resistance characteristics of the crosslinked rubber article. The mass% or less is preferably ,.1 mass% or less. Further, in the case of the rubber, it is preferable to use a perfluoroelastomer (hereinafter also referred to as a "sexual body (7)" having at least _ atom (four) atoms in the case of cross-linking of the organic peroxide to have The perfluoroelastomer of the atom is preferably a perfluoroelastic system having at least one of a ruthenium atom and a desert atom, and the ruthenium of the ruthenium atom of the all-I-elastomer (4) is replaced by a ruthenium atom. The total gas elastic system refers to an elastomer in which one or more atoms of the money elastomer are replaced by moth atoms. The elastomer (Y) is disclosed in, for example, Japanese Laid-Open Patent Publication No. (2), Japanese Patent Publication No. 53-4115, and Japanese Laid-Open Patent Publication No. 59-2〇31〇. Self-loaded elastomer. Specifically, for example, one or more perfluoromonomers selected from the group consisting of TFE and perfluoromonomer (X) may be added, and at least one of an iodine atom and a bromine atom may be copolymerized. An elastomer obtained by a monomer (hereinafter referred to as "monomer (y)"); and in the case of I-RF3-I (wherein, V3 is a carbon number of a perfluoroalkyl group, or a carbon atom) An elastomer obtained by copolymerizing the above monomers in the presence of a compound represented by a perfluoroalkylene group having 1 to 8 carbon atoms and having at least one etheric oxygen atom between carbon atoms. The monomer (y) can be, for example, (^2=&lt;^-汾, (:112=(:1^?2€?2-81·, CF2=CF-〇-CF2CF2-I 'CF2=CF- 0-CF2CF2-Br CF2=CF-0-CF2CF2CH2-I, CF2=CF-0-CF2CF2CH2-Br, 22 201229072 CF2=CF-〇-CF2CF2(CF3)-〇-CF2CF2CH2-I, and CF2= CF-0 -CF2CF2(CF3)-0-CF2CF2CH2-Br, etc. Specific examples of I-RF3-I include diiododifluoromethane, 1,2-diiodoperfluoroethane, and 1,3-diiodide. Perfluoropropane, 1,4-diiodoperfluorobutane, 1,5-diiodoperfluoropentane, 1,6-diiodoperfluorohexane, 1J-diiodoperfluoroheptane, and 1,8 -diiodoperfluorooctane, etc. Among them, 1,4-diiodoperfluorobutane, and iota,6-diiodoperfluorohexane are preferred, and 1,4-diiodoperfluorobutane is preferred. The iodine atom and the bromine atom in the elastomer (Y) are preferably bonded to the end of the polymer. From the viewpoint of easily producing a crosslinked rubber article having good rubber properties and compressive permanent strain, the elastomer (Y) The total content of the iodine atom and the bromine atom is preferably 0.1 to 1.5% by mass, more preferably 0.2 to 1.0% by mass, and most preferably 0.25 to 1. 〇% by mass. For example, the product name "AFLAS PFE-1100" (TFE/perfluoroalkyl vinyl ether copolymer manufactured by Gunsko Co., Ltd.), the trade name "AFLAS 100S" (made by Asahi Glass Co., Ltd., tfe/propylene copolymer), and The product name "AFLAS 200P" (asahi, ε xiaozi company, TFE / propylene / fluorinated vinylene copolymer) can be used for organic peroxide cross-linking gas rubber. [Organic peroxide] by organic peroxidation When the cross-linking fluororubber composition of the present invention is cured by cross-linking, it is preferred that the cross-linkable fluororubber composition of the present invention contains an organic peroxide. The cross-linking fluororubber composition is cross-linked by radiation. In the case of hardening, it is not necessary to specifically contain an organic peroxide. 23 201229072 The organic peroxide is preferably a radical generator which can be easily heated by heating, and preferably has a half-life of 1 minute at a temperature of 130 to 220 ° C. Specifically, 'such as: 1,1-di (three-stage hexyl peroxidation) _3,5,5-trimethylcyclohexanyl, 2,5-dimercaptohexanol-2,5-dihydroperoxide , di-tertiary butyl peroxide, tertiary butyl cumyl peroxide, diisopropyl phenyl Oxide, α, α bis (tertiary butyl peroxy)-p-diisopropylbenzene, 2,5-dimercapto-2 5_(divalent butyl peroxy)-hexyl, 2,5-di Methyl-2,5-di(tributyl peroxide)-hexyne-3, a claudyl peroxide, tert-butyl benzoate, 2,5-dimethyl-2,5 - bis(phenylhydrazine peroxy)hexane, tertiary butyl peroxymaleic acid, and secondary hexylperoxyisopropyl monocarbonate. Among them, α,α'-bis(tri-butyl peroxide)-p-diisopropylbenzene is particularly preferred. The organic compound can be used alone. From the top, when the cross-linking fluororubber composition of the present invention contains organic peroxidation, the content of the organic peroxide is 1 part by mass relative to the fluororubber, and the mass is 〇ι. The portion is preferably '0.2 to 4 parts by mass, and more preferably Q 5 to 3f parts. If there is a peroxide content limit m, the crosslinking efficiency is increased. When the content of the peroxide is at most the upper limit value, it is easy to suppress the amount of the ineffective decomposition product which does not contribute to the radical. [Other Ingredients] ------Human-Jin Ying's point of view, it seems that the gel composition contains a (four) acceptor as a good acid acceptor, for example, magnesium oxide, oxidized, and about (10) m. Water slide and oxidation are preferred. The acid acceptor may be used singly or in combination with each other. 24 201229072 When the crosslinkable rubber composition of the present invention contains an acid acceptor, the content of the acid acceptor is 0.1 to 20 parts by mass based on 100 parts by mass of the fluororubber. Preferably, it is preferably 0.2 to 10 parts by mass. If the content of the acid acceptor is at least the lower limit value, the effect of the acid acceptor is easily obtained. When the content of the acid acceptor is at most the upper limit value, it is easy to suppress the rubber physical properties which may damage the crosslinked rubber article. The crosslinkable fluororubber composition of the present invention preferably contains a filler from the viewpoint of improving the strength of the obtained crosslinked rubber article. The filler is preferably carbon black. The carbon black is not particularly limited as long as it is used as a rubber blending user. Specific examples include furnace black, acetylene black, hot carbon black, black, and graphite. Among them, furnace black is preferred. The black level is preferably HAF-LS, HAF, HAF-HS, FEF, GPF, APF, SRF-LM, SRF-HM, and MT, and MT is particularly preferred. When the crosslinkable fluororubber composition of the present invention contains a filler, the content of the filler is preferably 5 to 100 parts by mass, more preferably 10 to 50 parts by mass, per 100 parts by mass of the fluororubber. When the content of the filler is at least the lower limit value, the effect of the filler can be easily obtained. When the content of the filler is at most the upper limit, it is easy to suppress the deterioration of the tensile properties of the crosslinked rubber article. Further, as long as the balance between the strength and the stretch of the crosslinked rubber article prepared by the inclusion of the filler in the range of the cutting agent is maintained, a good relationship can be maintained. Further, the crosslinkable fluororubber composition of the present invention may contain additives such as a reinforcing material, a processing aid, a lubricant, a lubricant, a flame retardant, an antistatic agent, a colorant, and an ultraviolet absorber. The reinforcing material may, for example, be a fluororesin such as polytetrafluoroethylene or ethylene/TFE 25 201229072 polymer, glass fiber, carbon fiber or white carbon. When the cross-linking rubber composition of the present invention contains a reinforcing material, the content of the reinforcing material is preferably 5 to 2 parts by mass, more preferably 10 to 100 parts by mass, per 100 parts by mass of the fluororubber. As the processing aid, for example, a metal salt of a higher fatty acid can be mentioned. Among them, stearate and laurate are preferred. When the crosslinkable fluororubber composition of the present invention contains a processing aid, the content of the processing aid is preferably 2 parts by mass, preferably 0.2 parts by mass to 2 parts by mass based on 4 parts by mass of the rubber. It is better if the processing aid is above the lower limit value. The tensile strength of the crosslinked rubber article will decrease significantly and it is easy to suppress the increase of the tensile or tensile strength after heat aging. When it is less than the upper limit, it is easy to suppress the occurrence of blooming on the surface of the crosslinked rubber article, or to increase the hardness of the crosslinked rubber article, or to lower the chemical resistance and the steam resistance. [Crosslinking fluororubber composition (Manufacturing method of the present invention) The method for producing the parent-linked fluororubber composition of the present invention is not particularly limited, and a conventionally known method can be employed. Among them, a double roll machine, a closed type/3⁄4 smelting machine, and a "smashing machine" are used. It is preferable to knead a fluororubber, an I polymer (P), an organic peroxide, a carbon black, an acid acceptor, and other additives as needed in a kneading machine. Further, a method of kneading and dissolving the above components in a state of being dissolved and dispersed in a solvent may be employed. In the order of mixing the above-mentioned respective components, it is preferred that the components which are difficult to react or decompose are sufficiently kneaded with the fluororubber by heat generation, and then the easily reactable component or the easily decomposable component is blended and kneaded. 26 201229072 For example, in the case of using an organic peroxide, it is preferred to blend and knead the organic peroxide. At this time, at the time of kneading, it is preferred that the kneader is water-cooled to maintain the temperature range of (10) to 丨 from the viewpoint of not allowing the crosslinking reaction to proceed. a The above-described crosslinked fluororubber group of the present invention has a good resistance to gas rubber... Since it is crosslinked by a radical by organic = parent or radiation crosslinking, the fluororubber can be prevented In the case of a decrease in the properties, a good resistance is obtained: a crosslinked rubber article, and a sufficient crosslinking can be formed by using a fluoropolymer (p) as a crosslinking assistant, so that a good crosslinking can be achieved. Heat resistance. Therefore, as long as the crosslinkable gas rubber composition of the present invention is used, a crosslinked rubber article having both good chemical properties and heat resistance can be obtained. &lt;Crosslinked rubber article&gt; The crosslinked rubber article of the present invention is an article formed by crosslinking the crosslinked rubber composition of the present invention described above. The crosslinked rubber article of the present invention can be used as an ankle ring, a seal #, a gasket, an oil seal, and a bearing seal in a wide range of fields such as automobile transportation machinery, general machinery, electric motor, chemical equipment industry, and semiconductor. It is suitable for use in various components such as sealing materials, apertures, cushioning materials, shock-proof materials, wire covering materials, industrial belts, tubes, coils, and sheets. Among them, from the viewpoint of excellent resistance at high temperatures, 'in addition to the excellent properties such as strength, hardness, modulus, and heat aging resistance, it is better to use sealing materials and oil exploration. The sealing material is preferred. [Manufacturing method of crosslinked rubber article] 27 201229072 The crosslinked rubber article of the present invention can be formed by curing the crosslinked fluororubber composition of the present invention by crosslinking with an organic peroxide or by radiation crosslinking. Got it. The formation of the crosslinkable fluororubber composition of the present invention can be known by any of the conventional organic peroxide crosslinking and radiation crosslinking, such as extrusion molding, injection molding, transfer molding, and press molding. Forming method. In the specific example of the method of crosslinking the rubber article by crosslinking with an organic peroxide, for example, there is a method of using a mold having a cavity having a shape complementary to the shape of one or several parts of the crosslinked rubber article. After filling the cavity with a crosslinkable fluororubber composition containing an organic peroxide, the mold is heated to be hardened at a heating temperature of 130 to 220. (: It is better, 140~200°C is better, 150~200 C is better. Also, it is also suitable to use electric, hot air, or steam as the heat source, etc., which will be heated and crosslinked under the aforementioned conditions. The crosslinked rubber article (primary crosslinked product) is further heated to carry out cross-linking (hereinafter referred to as "secondary cross-linking"). By performing one cross-linking, the organic peroxide contained in the cross-linked rubber article can be obtained. The residue is decomposed and volatilized to reduce its amount. - The heating temperature of the second parent is preferably 150~28〇r, 180. (: ~260°c is better, 200~250°C is better.) The heating time is preferably 1 to 48 hours, preferably 2 to 24 hours. 'Specific examples of a method for producing a crosslinked rubber article by radiation crosslinking, 'for example, the following method' is: The cross-linking i rubber composition of the present invention is dissolved and dispersed in a suitable solution as a floating solution, and is formed by applying a coating such as 28 201229072 and drying it, and then irradiating the radiation to be hardened. Either an electron beam or an arbitrary radiation such as an r line.

游離性放射線之照射量以1〜300kGy為佳,l〇〜2〇〇kG 較佳。 實施例 以下,將以實施例詳細説明本發明’惟,本發明不受 限於以下記載。 [GPC分析] 以本實施例所製得之氟聚合物(P)之Μη及Mw係依照曰 本特開2001-208736號公報中記載之方法,在下述條件下以 GPC所測定。 移動相:旭硝子公司製,ASAHIKLINAK-225SEC等級 U二氣五氟丙烷與六氟異丙醇之混合溶劑(二氣五氟丙烷/ 六氟異丙醇=99/1(體積比)))。 分析管柱:將PLgel MIXED-E管柱(Polymer Laboratories公司製)2管串聯者。 分子量測定用標準試料:PMMA(聚甲基丙烯酸甲酯)。 移動相流速:l.OmL/分。 管柱溫度:37°C。 檢測器:蒸發光散射檢測器。 [使用原料] 本實施例中所使用之成分如下。 (1)氟橡膠 29 201229072 氟橡膠(Yl) : TFE/全氟烷基乙烯基醚系共聚物之彈性 體(過氧化物交聯型),商品名「AFLAS PFE-1100」(旭硝子 公司製,氟含量:72質量%)。 (2)交聯助劑 氟聚合物(P1): 將内容積1L(公升)之附攪拌機之不鏽鋼製高壓爸予以 除氣後,於該高壓爸中壓入氟單烯(a)之TFE 17g、氟二烯(b) 之全氟丁烯二乙烯基醚(以下稱為「C4DVE」)76g、S02C12 3.0g、AK225cb(旭硝子公司製)725g、及含有聚合起始劑之 (C3F7COO)2 6.8g之AK225cb溶液227g,一邊加以攪拌並同 時一邊使高壓蚤内升溫至40°C。爾後,以TFE之追加饋入量 為29g、且C4DVE之追加饋入量為44g的方式,將壓力保持 在0.2MPa逐次添加TFE及C4DVE,進行4小時聚合反應。之 後,冷卻至室溫,並將未反應之TFE予以排淨後,將内容物 取出放到内容積2L之玻璃燒杯中。 接下來,進行攪拌並投入甲醇500g,使所生成之氟聚 合物析出,並除去上清液藉以除去低分子量成分後,再溶 解至AK225cb中,製得氟聚合物溶液1。接著,水洗氟聚合 物溶液1使下層分離,再使用細孔徑lem之PTFE(聚四氟乙 烯)製之膜過濾機加以過濾,藉以製得大致透明的氟聚合物 溶液2。再來’使用蒸發器從該氟聚合物溶液2蒸餾除去溶 劑後’以100°C真空乾燥2小時,藉以製得無色透明的高黏 度液狀之氟聚合物(Pl)52g。 藉由GPC測定所製得之氟聚合物(P1)之平均分子量發 30 201229072 現,Mw為22,800,Μη為7,300。 又,藉由19F-NMR測定氟聚合物(P1)之組成及聚合性雙 鍵之含量發現,源自於TFE之重複單元與源自於C4DVE之 重複單元之莫耳比為69/31,聚合性雙鍵之含量為 1.18mmol/g。 氟聚合物(P2): 於内容積500mL之附有攪拌機與冷卻器之玻璃製燒瓶 中,加入C4DVE497g、I(CF2)6I 2_5g、及聚合起始劑之 V-601(和光純藥工業製)0.7g,使溶液氮氣起泡1〇分鐘,進行 攪拌並同步以水浴使燒瓶内升溫到70°C。將内溫保持在70 °C並聚合反應使進行25小時。爾後,冷卻至室溫後將内容 物溶至C6F13H中,取出放至内容積2L之玻璃燒杯中。 接下來,進行攪拌並投入甲醇374g,使所生成之敦聚 合物析出,並除去上清液藉以除去低分子量成分。以5〇。匚 真空乾燥12小時,藉以製得無色透明的高黏度液狀之氟聚 合物(P2)124g。 藉由GPC測定所製得之氟聚合物(P2)之平均分子量發 現,Mw為25,700,Μη為6,800。 又,藉由19F-NMR測定氟聚合物(Ρ2)之聚合性雙鍵之含 量發現,聚合性雙鍵之含量為2.68mmol/g。 TAIC :異三聚氰酸三烯丙酯。 (3)有機過氧化物 PERBUTYL P: 〇:,〇:’-雙(三級丁基過氧化)_對二異丙 苯(商品名「Perkadox 14」、曰油公司製)。 31 201229072 (4) 酸受體 KYOWAMAG#150 :氧化鎂(協和化學工業公司製)。 (5) 填充劑 MT碳:碳黑(等級:MT碳、CANCARB公司製)。 (6) 加工助劑 NONSOUL SN-1 :硬月旨酸鈉(日油公司製)。 [例1] 藉由雙軸輥將含氟橡膠(Yl)l〇〇質量份' PERHEXA 25B(曰本油脂公司製)1質量份、氟聚合物(Ρ1)33·8質量份、 ΜΤ碳10質量份、及KYOWAMAG#150 3質量份予以揑合, 藉以製得交聯性氟橡膠組成物(i)。以17 0 °C之熱壓2 0分鐘將 所製得之交聯性氟橡膠組成物⑴成形呈縱長lOOmmx橫寬 lOOmmx厚度2mm之片材狀(一次交聯)。將所製得之片材進 一步放入250°C之吉爾式供箱(Geer Oven)中2小時,進行二 次交聯後製得片材。 以第3號啞鈴從所製得之片材打穿試料後,測定硬度 (HS)、張力強度(TB)、拉伸(EB)、及100%張力應力(M100) 進行常態物性評估,再測定以吉爾式烘箱進行250°C熱處理 70小時後之硬度(HS)、張力強度(tb)、及拉伸(EB)並評估 而才熱老化性。 [例2] 除使用TAIC 5質量份來取代氟聚合物(ρι)33 8質量份 作為交聯助劑’且未使用KY〇WAMAG#150以外,以同於 例1的方式製作片材並測定特性。 32 201229072 [例3] 除使用TAIC 5質量份來取代氟聚合物(Pl)33.8質量份作 為交聯助劑以外,以同於例1的方式製作片材並測定特性。 [例4] 除使用氟聚合物(P2)21.3質量份來取代氟聚合物 (Ρ1)33·8質量份作為交聯助劑以外,以同於例1的方式製作 片材並測定特性。 [例5] 除使用氟聚合物(Ρ2)14.2質量份來取代氟聚合物 (Ρ1)33·8質量份作為交聯助劑以外,以同於例1的方式製作 片材並測定特性。 例[1]、[4]及[5]為實施例,例[2]及[3]為比較例。 [測定方法] (1) 硬度(HS) 依據JIS Κ6253-1997,藉由在23°c之橡膠硬度計型Α硬 度試驗測定硬度(HS)。 就片材之硬度而言,以60〜95°為適當。 (2) 張力強度(TB) 依據JIS K6251-2004,在23°C測定張力強度(TB)。 就片材之張力強度(TB)而言,以lOMPa以上為適當。 (3) 拉伸(EB) 依據JIS K6251-2004,在23°C 測定拉伸(EB)。 就片材之拉伸(EB)而言,以130%以上為適當。 (4) 100%張力應力(模數) 33 201229072 依據JIS K6251-2004,在23°C 測定 100%張力應力(Μιοο)。 就片材之100%張力應力(M100)而言,以3〜17MPa為適 當。 (5) 空氣加熱老化試驗(硬度變化率) 以吉爾式烘箱在250 °C熱處理70小時後,依據Jis K6253-1997,藉由在23°C之橡膠硬度計型A硬度試驗測定石更 度(HS),並與(1)之硬度作比較,求算變化率。 (6) 空氣加熱老化試驗(張力強度變化率) 以吉爾式烘箱在250°C熱處理70小時後,依 K6251-2〇04,在23°C測定張力強度(TB),並與(2)之張力強 度作比較,求算變化率。 (7) 空氣加熱老化試驗(拉伸變化率) 以吉爾式烘箱在2501熱處理70小時後,依據JIS K6251-2004 ’在23°C測定拉伸(EB),並與(3)之拉伸作比較, 來求算變化率。 於表1顯示例[1]〜例[5]中用於片材製作之各個材料之 組成(質量份)、及上述特性之評估測定結果。 34 201229072 表1 例1 例2 例3 例4 例5 氟橡膠 氟橡膠(Y1) 100 100 100 100 100 交聯助劑 氟聚合物(P1) 33.8 - - - - 氟聚合物(P2) - - - 21.3 14.2 TAIC - 5 5 - - 有機過氧化物 PERBUTYL P 1 1 1 1 1 酸受體 KYOWAMAG#150 3 - 3 3 3 填充劑 MT碳 10 10 10 10 10 加工助劑 NONSOUL SN-1 1 1 1 1 1 硬度(HS)[°] 86 72 74 82 77 張力強度(TB)[MPa] 24.9 24.9 23.9 25.2 24.0 拉伸(EB)[%] 140 200 187 159 180 __ 100%張力應力[MPa] 12.6 7.5 8.5 15.4 10.1 空氣加熱老化試驗 (在250〇C進行 70小時) 硬度變化率[%] -1 0 0 -2 -2 張力強度變化率[%] +4 -13 -20 -3 -5 拉伸變化率[%] +19 +47 +6 +12 +27 如表1顯示’作為交聯助劑使用氟聚合物(P1及P2)之例 1、例4及例5之片材,與作為交聯助劑使用TAIC之例2、及 例3之片材相較之下’較可抑制縮小空氣加熱老化試驗之張 力強度變化率,且耐熱性較佳。 產業上之可利用性 藉由使用本發明之交聯性氟橡膠組成物,可製得兼具 良好的耐藥性(尤其是耐胺性)與耐熱性之交聯橡膠物品,可 用於〇環、片材、密合墊、油封、軸承密封等密封材等,尤 以作為石油探勘用之密封材有所助益。 而,於此引用於2〇10年11月3〇日提出申請之日本專利 申請2〇10-266864號之說明書、專利申請範圍、及摘要之全 部内容’納入作為本發明之說明書之揭示者。 35 201229072 I:圖式簡單說明3 (無) 【主要元件符號說明】 (無) 36The irradiation amount of the free radiation is preferably 1 to 300 kGy, and preferably 1 〇 2 〇〇 kG. EXAMPLES Hereinafter, the present invention will be described in detail by way of examples. However, the invention should not be construed as limited. [GPC analysis] Μη and Mw of the fluoropolymer (P) obtained in the present Example were measured by GPC under the following conditions in accordance with the method described in JP-A-2001-208736. Mobile phase: Asahi Glass Co., Ltd., ASAHIKLINAK-225SEC grade U mixed solvent of pentafluoropropane and hexafluoroisopropanol (difluoropentafluoropropane / hexafluoroisopropanol = 99/1 (volume ratio)). Analytical column: A PLgel MIXED-E column (manufactured by Polymer Laboratories Co., Ltd.) was connected in series. Standard sample for molecular weight measurement: PMMA (polymethyl methacrylate). Mobile phase flow rate: 1.0 mL / min. Column temperature: 37 ° C. Detector: Evaporative light scattering detector. [Use Raw Material] The components used in the examples were as follows. (1) Fluororubber 29 201229072 Fluororubber (Yl): an elastomer (peroxide crosslinked type) of TFE/perfluoroalkyl vinyl ether copolymer, trade name "AFLAS PFE-1100" (made by Asahi Glass Co., Ltd.) Fluorine content: 72% by mass). (2) Cross-linking aid fluoropolymer (P1): After degassing the high-pressure dad of stainless steel with a volume of 1 L (liter), the fluoromonoolefin (a) TFE 17g is pressed into the high pressure dad. PFadiene (b) perfluorobutene divinyl ether (hereinafter referred to as "C4DVE") 76g, S02C12 3.0g, AK225cb (made by Asahi Glass Co., Ltd.) 725g, and (C3F7COO)2 6.8 containing a polymerization initiator 227 g of the AK225cb solution of g was heated while stirring to 40 ° C while stirring. Then, TFE and C4DVE were sequentially added at a pressure of 0.2 MPa so that the additional feed amount of TFE was 29 g and the additional feed amount of C4DVE was 44 g, and the polymerization reaction was carried out for 4 hours. Thereafter, the mixture was cooled to room temperature, and the unreacted TFE was drained, and the contents were taken out and placed in a glass beaker having an inner volume of 2 L. Subsequently, 500 g of methanol was added thereto, and the produced fluoropolymer was precipitated, and the supernatant liquid was removed to remove the low molecular weight component, and then dissolved in AK225cb to obtain a fluoropolymer solution 1. Next, the fluoropolymer solution 1 was washed with water to separate the lower layer, and then filtered using a membrane filter made of PTFE (polytetrafluoroethylene) having a pore diameter of lem to obtain a substantially transparent fluoropolymer solution 2. Then, the solvent was distilled off from the fluoropolymer solution 2 using an evaporator, and then vacuum-dried at 100 ° C for 2 hours to obtain 52 g of a colorless transparent high-viscosity liquid fluoropolymer (P1). The average molecular weight of the fluoropolymer (P1) obtained by GPC measurement was 30 201229072. Mw was 22,800 and Μη was 7,300. Further, by measuring the composition of the fluoropolymer (P1) and the content of the polymerizable double bond by 19F-NMR, it was found that the molar ratio derived from the repeating unit derived from TFE and the repeating unit derived from C4DVE was 69/31, and polymerization was carried out. The content of the double bond was 1.18 mmol/g. Fluoropolymer (P2): V-601 (manufactured by Wako Pure Chemical Industries, Ltd.) containing C4DVE 497g, I(CF2)6I 2_5g, and a polymerization initiator in a glass flask containing 500 ml of an internal volume and a stirrer and a cooler. 0.7 g, the solution nitrogen was bubbled for 1 minute, stirred and simultaneously heated to 70 ° C in a water bath with a water bath. The internal temperature was maintained at 70 ° C and the polymerization was allowed to proceed for 25 hours. Thereafter, after cooling to room temperature, the contents were dissolved in C6F13H, and taken out to a glass beaker having an inner volume of 2 L. Next, stirring was carried out and 374 g of methanol was introduced to precipitate the resulting polymer, and the supernatant was removed to remove low molecular weight components. Take 5 〇.真空 Drying under vacuum for 12 hours gave 124 g of a colorless, transparent, highly viscous liquid fluoropolymer (P2). The average molecular weight of the fluoropolymer (P2) obtained by GPC measurement revealed Mw of 25,700 and Μη of 6,800. Further, the content of the polymerizable double bond of the fluoropolymer (?2) was measured by 19F-NMR to find that the content of the polymerizable double bond was 2.68 mmol/g. TAIC: Triallyl isocyanurate. (3) Organic peroxide PERBUTYL P: 〇:, 〇: '-bis (tertiary butyl peroxy) _ p-diisopropylbenzene (trade name "Perkadox 14", manufactured by Oyster Sauce Co., Ltd.). 31 201229072 (4) Acid acceptor KYOWAMAG #150 : Magnesium oxide (manufactured by Kyowa Chemical Industry Co., Ltd.). (5) Filler MT carbon: carbon black (grade: MT carbon, manufactured by CANCARB). (6) Processing aid NONSOUL SN-1 : Sodium sulphate (made by Nippon Oil Co., Ltd.). [Example 1] A fluorine-containing rubber (Y1), a mass fraction of PERHEXA 25B (manufactured by Sakamoto Oil Co., Ltd.), 1 part by mass, a fluoropolymer (Ρ1), 33·8 parts by mass, and a ruthenium carbon 10, were prepared by a biaxial roll. The mass fraction and 3 parts by mass of KYOWAMAG #150 were kneaded to obtain a crosslinkable fluororubber composition (i). The crosslinked fluororubber composition (1) thus obtained was formed into a sheet shape (primary cross-linking) having a length of 100 mm x a width of 100 mm and a thickness of 2 mm at a hot pressure of 170 ° C for 20 minutes. The obtained sheet was further placed in a Geer Oven at 250 ° C for 2 hours, and a second cross-linking was carried out to obtain a sheet. After the sample was punched from the prepared sheet with the No. 3 dumbbell, the hardness (HS), tensile strength (TB), tensile (EB), and 100% tensile stress (M100) were measured for normal physical property evaluation, and then measured. The hardness (HS), tensile strength (tb), and elongation (EB) after heat treatment at 250 ° C for 70 hours in a Gil oven were evaluated and evaluated for heat aging. [Example 2] A sheet was produced in the same manner as in Example 1 except that 5 parts by mass of TAIC was used instead of fluoropolymer (ρι) 33 8 parts by mass as a crosslinking aid' and KY〇WAMAG #150 was not used. characteristic. 32 201229072 [Example 3] A sheet was produced in the same manner as in Example 1 except that 5 parts by mass of TAIC was used instead of 33.8 parts by mass of the fluoropolymer (Pl) as a crosslinking assistant, and the properties were measured. [Example 4] A sheet was produced in the same manner as in Example 1 except that 21.3 parts by mass of the fluoropolymer (P2) was used instead of the fluoropolymer (?1) of 33.8 parts by mass as a crosslinking assistant, and the properties were measured. [Example 5] A sheet was produced in the same manner as in Example 1 except that 14.2 parts by mass of a fluoropolymer (?2) was used instead of the fluoropolymer (?1) 333.8 parts by mass as a crosslinking assistant, and the properties were measured. Examples [1], [4], and [5] are examples, and examples [2] and [3] are comparative examples. [Measurement method] (1) Hardness (HS) The hardness (HS) was measured by a rubber hardness tester hardness test at 23 ° C in accordance with JIS Κ 6253-1997. In terms of the hardness of the sheet, it is suitably 60 to 95°. (2) Tensile strength (TB) The tensile strength (TB) was measured at 23 ° C according to JIS K6251-2004. The tensile strength (TB) of the sheet is preferably 10 MPa or more. (3) Stretching (EB) The stretching (EB) was measured at 23 ° C according to JIS K6251-2004. The sheet stretching (EB) is preferably 130% or more. (4) 100% tensile stress (modulus) 33 201229072 100% tensile stress (Μιοο) was measured at 23 ° C according to JIS K6251-2004. For the 100% tensile stress (M100) of the sheet, it is appropriate to use 3 to 17 MPa. (5) Air heating aging test (hardness change rate) After heat treatment at 250 °C for 70 hours in a Gil oven, the stone hardness was determined by a rubber hardness tester A hardness test at 23 ° C according to Jis K6253-1997. HS), and compared with the hardness of (1), calculate the rate of change. (6) Air heating aging test (tension rate change rate) After heat treatment at 250 ° C for 70 hours in a Gil oven, the tensile strength (TB) is measured at 23 ° C according to K6251-2〇04, and (2) The tensile strength is compared and the rate of change is calculated. (7) Air heating aging test (tensile change rate) After heat treatment in a Gil oven for 250 hours at 2501, the tensile (EB) was measured at 23 ° C according to JIS K6251-2004, and the stretching was performed with (3) Compare, to calculate the rate of change. Table 1 shows the composition (parts by mass) of each material used for sheet production in Examples [1] to [5], and the evaluation results of the above characteristics. 34 201229072 Table 1 Example 1 Example 2 Example 3 Example 4 Example 5 Fluororubber fluororubber (Y1) 100 100 100 100 100 Crosslinking aid fluoropolymer (P1) 33.8 - - - - Fluoropolymer (P2) - - - 21.3 14.2 TAIC - 5 5 - - Organic peroxide PERBUTYL P 1 1 1 1 1 Acid acceptor KYOWAMAG#150 3 - 3 3 3 Filler MT carbon 10 10 10 10 10 Processing aid NONSOUL SN-1 1 1 1 1 1 Hardness (HS) [°] 86 72 74 82 77 Tensile strength (TB) [MPa] 24.9 24.9 23.9 25.2 24.0 Tensile (EB) [%] 140 200 187 159 180 __ 100% tensile stress [MPa] 12.6 7.5 8.5 15.4 10.1 Air heating aging test (70 hours at 250 ° C) Hardness change rate [%] -1 0 0 -2 -2 Tensile strength change rate [%] +4 -13 -20 -3 -5 Tensile change rate [%] +19 +47 +6 +12 +27 As shown in Table 1, 'The fluoropolymers (P1 and P2) used as cross-linking aids, the sheets of Examples 4 and 5, and the cross-linking aid In the case of the TAIC, the sheets of Example 2 and Example 3 were used to suppress the change in the tensile strength of the reduced air heat aging test, and the heat resistance was better. INDUSTRIAL APPLICABILITY By using the crosslinkable fluororubber composition of the present invention, a crosslinked rubber article having both good chemical resistance (especially amine resistance) and heat resistance can be obtained, which can be used for an anthracene ring. Sealing materials such as sheets, gaskets, oil seals, bearing seals, etc., especially for the sealing materials used in petroleum exploration. The entire contents of the specification, the scope of the patent application, and the abstract of the Japanese Patent Application No. Hei. No. Hei. 35 201229072 I: Simple description of the diagram 3 (none) [Description of main component symbols] (none) 36

Claims (1)

201229072 七、申請專利範圍: L —種交聯性氟橡膠組成物,其係含有氟橡膠、及具有多 數聚合性制之下述氟时物(P)者, 氟聚合物(P):具有源自於不飽和側鏈殘留性之氟二 烯(b)之重複單元者。 2_如申請專利範圍第1項之交聯性氟橡膠組成物,其中前 述氟聚合物(P)係具有:源自於氟單烯(a)之重複單元、 及源自於不飽和側鏈殘留性之氟二烯(b)之重複單元者。 3♦如申請專利範圍第2項之交聯性氟橡膠組成物,其中前 述氟單烯(a)係選自於由四氟乙烯、氯三氟乙烯、及 CF2=CFO-Rn(式中,Rf丨為碳數卜6之氟烷基、或於碳原 子-碳原子間具有1個以上醚性氧原子之碳數2~6之氟烷 基)所構成之群組中之1種以上。 4·如申睛專利範圍第1至3項中任一項之交聯性I橡膠組 成物’其中前述氟二烯(b)係選自於由下述氟二烯 (bl)〜(b3)所構成之群組中之1種以上: (bl) CF2=CF〇-Qfl.〇cF=CF2 ; (b2) CHfCFCFA-QtOCFzCFsC% ; (b3) CH2=CFCF2〇-Qf3-OCF=CF2 ; (式中’(^及卩17分別獨立為碳數3〜8之氟伸烷基、 或於碳原子-碳原子間具有1個以上醚性氧原子之碳數 3〜8之氟伸烷基; Qf3為碳數1〜6之氟伸烷基,或於碳原子-碳原子間具 有1個以上醚性氡原子之碳數2〜6之氟伸院基)。 37 201229072 5. 如申請專利範圍第1至4項中任一項之交聯性氟橡膠組 成物,其中前述氟聚合物(P)之重量平均分子量為3,000〜 50,000。 6. 如申請專利範圍第1至5項中任一項之交聯性氟橡膠組 成物,其中前述氟聚合物(P)中之聚合性雙鍵之含量為 0.2〜2mmol/g。 7. 如申請專利範圍第1至6項中任一項之交聯性氟橡膠組 成物,其相對於前述氟橡膠100質量份,含有前述氟聚 合物(P)l〜50質量份。 8. 如申請專利範圍第1至7項中任一項之交聯性氟橡膠組 成物,其中前述氟橡膠係選自於由四氟乙烯/丙烯系共 聚物、氟化亞乙烯/四氟乙稀/六氟丙稀系共聚物、及四 氟乙烯/全氟烷基乙烯基醚系共聚物所構成之群組中之 1種以上。 9. 如申請專利範圍第1至8項中任一項之交聯性氟橡膠組 成物,其更含有有機過氧化物。 10. —種交聯橡膠物品,其係交聯如申請專利範圍第1或2項 之交聯性氟橡膠組成物而成者。 11. 如申請專利範圍第10項之交聯橡膠物品,其係密封材。 38 201229072 四、指定代表圖: (一) 本案指定代表圖為:第( )圖。(無) (二) 本代表圖之元件符號簡單說明: 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式: (無) 2201229072 VII. Patent application scope: L—a cross-linking fluororubber composition containing fluororubber and the following fluorine-containing compound (P) having a majority of polymerizable properties, fluoropolymer (P): having a source Repetitive unit of fluorodiene (b) from the residual side chain of unsaturated. The cross-linking fluororubber composition of claim 1, wherein the fluoropolymer (P) has a repeating unit derived from fluoromonoolefin (a) and derived from an unsaturated side chain Repetitive unit of residual fluorodiene (b). 3) The cross-linkable fluororubber composition according to claim 2, wherein the fluoromonoolefin (a) is selected from the group consisting of tetrafluoroethylene, chlorotrifluoroethylene, and CF2=CFO-Rn (wherein Rf丨 is at least one selected from the group consisting of a fluoroalkyl group of carbon number 6 or a fluoroalkyl group having 2 or more carbon atoms having one or more etheric oxygen atoms between carbon atoms and carbon atoms. 4. The crosslinkable I rubber composition of any one of claims 1 to 3 wherein the fluorodiene (b) is selected from the group consisting of fluorodiene (b1) to (b3) One or more of the group consisting of: (bl) CF2=CF〇-Qfl.〇cF=CF2; (b2) CHfCFCFA-QtOCFzCFsC%; (b3) CH2=CFCF2〇-Qf3-OCF=CF2 ; Wherein (^ and 卩17 are each independently a fluoroalkyl group having 3 to 8 carbon atoms; or a fluoroalkyl group having 3 to 8 carbon atoms having one or more etheric oxygen atoms between carbon atoms and carbon atoms; Qf3 It is a fluorine alkyl group having 1 to 6 carbon atoms, or a carbon number of 2 to 6 having one or more etheric sulfonium atoms between carbon atoms and carbon atoms. 37 201229072 5. The cross-linking fluororubber composition according to any one of items 1 to 4, wherein the fluoropolymer (P) has a weight average molecular weight of 3,000 to 50,000. 6. The method of any one of claims 1 to 5 A crosslinkable fluororubber composition in which the content of the polymerizable double bond in the fluoropolymer (P) is 0.2 to 2 mmol/g. 7. Crosslinkability as claimed in any one of claims 1 to 6. Fluororubber composition, relative to The cross-linking fluororubber composition of any one of the above-mentioned fluoropolymers, wherein the fluororubber is contained in an amount of from 1 to 50 parts by weight of the fluoropolymer (P). Selected from the group consisting of a tetrafluoroethylene/propylene copolymer, a vinylidene fluoride/tetrafluoroethylene/hexafluoropropylene copolymer, and a tetrafluoroethylene/perfluoroalkyl vinyl ether copolymer A cross-linking fluororubber composition according to any one of claims 1 to 8, which further contains an organic peroxide. 10. A cross-linked rubber article, the system Cross-linking is the result of applying the cross-linking fluororubber composition of the first or second patent scope. 11. If the cross-linked rubber article of claim 10 is a sealing material, it is a sealing material. : (1) The representative representative of the case is: ( ) (No) (2) The symbol of the symbol of the representative figure is simple: 5. If there is a chemical formula in this case, please disclose the chemical formula that best shows the characteristics of the invention: ) 2
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