JP2013154618A - Vulcanizing bladder for rubber product - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a vulcanizing bladder not only having excellent heat resistance, weather resistance, ozone resistance, mechanical characteristics and mold release characteristics, but having durability and the vulcanizing bladder capable of reducing the cost because of the long life by the durability and suitably used for manufacturing a rubber product, particularly a tire product by vulcanizing.SOLUTION: A vulcanizing bladder uses a rubber composition containing a copolymer of a conjugated diene compound and non-conjugated olefin in which content of cis1,4-bond in a part originating in the conjugated diene compound (conjugated diene part) is over 92%.

Description

  The present invention relates to a rubber product vulcanization bladder.

  Conventionally, for example, in a tire vulcanizing process, a raw tire is accommodated in a mold of a vulcanizer, and a vulcanizing bladder made of an elastic hollow body that is inflatable inside the raw tire is disposed inside. A technique is used in which a high-pressure vulcanizing medium is supplied and a raw tire is pressed from the inside toward the inner surface of a mold to vulcanize and mold. At this time, the rubber and sulfur molecules of the raw tire are bonded by heat and pressure applied from the bladder, and elasticity and durability are imparted to the rubber. The final shape and tread pattern of the tire are formed by the mold at this time. After the vulcanization molding, the tire is taken out from the mold to obtain a product tire. As described above, a rubber composition containing butyl rubber (IIR) has been conventionally used as a raw material for a vulcanizing bladder used in the manufacture of rubber products. This is because butyl rubber is not only excellent in chemical stability, heat resistance, weather resistance, ozone resistance, mechanical properties, saturation water vapor resistance, moldability, etc., but also in releasability from other rubbers. For example, Patent Document 1 discloses a technique of using butyl rubber in a vulcanizing bladder having a multilayer structure composed of a plurality of layers.

  On the other hand, these conventional vulcanizing bladders are repeatedly filled and exhausted by the gas, steam or hot water exhausted inside the bladder, and micro cracks are generated on the bladder surface. Had the problem of reaching the bank. In order to solve this problem, for example, natural rubber (NR), butadiene rubber (BR), styrene-butadiene rubber (SBR) is used, but heat resistance, weather resistance, ozone resistance, mechanical properties required as a bladder Characteristics and saturated water vapor resistance cannot be sufficiently obtained, and conventionally, a method of supplementing durability by mixing 0 to 20 parts by mass of chloroprene rubber with 80 to 100 parts by mass of butyl rubber has been used. .

JP-A-5-31724

  An object of the present invention is to provide a vulcanizing bladder that not only has excellent heat resistance, mechanical properties, and releasability, but also has excellent durability.

  As a result of intensive investigations to achieve the above object, the present inventor has used a rubber composition containing a copolymer of a conjugated diene compound and a non-conjugated olefin in a vulcanization bladder, thereby providing heat resistance and weather resistance. The present inventors have found that a vulcanization bladder that not only has excellent properties, ozone resistance, mechanical properties, and releasability, but also has excellent durability can be provided.

  That is, the vulcanizing bladder of the present invention is characterized by using a rubber composition containing a copolymer of a conjugated diene compound and a non-conjugated olefin.

  With this configuration, it is possible to provide a vulcanizing bladder that not only has excellent heat resistance, weather resistance, ozone resistance, mechanical properties, and releasability, but also has excellent durability.

  The cis 1,4-bond content of the conjugated diene compound-derived moiety (conjugated diene moiety) is preferably more than 92%.

  If the cis 1,4-bond content exceeds 92%, the glass transition temperature becomes low, and thus the durability of the resulting vulcanizing bladder can be further improved.

  The rubber composition preferably contains 5 parts by mass or more of a copolymer of the conjugated diene compound and the non-conjugated olefin in 100 parts by mass of the rubber component.

  With this configuration, the tensile strength and durability of the resulting vulcanizing bladder can be further improved.

  The rubber composition preferably contains 20 to 80 parts by mass of a filler with respect to 100 parts by mass of the rubber component.

  With this configuration, the obtained vulcanization bladder can be excellent in tensile strength, moldability, and bending resistance.

  According to the present invention, it is possible to provide a vulcanizing bladder that not only has excellent heat resistance, weather resistance, ozone resistance, mechanical properties, and releasability, but also has excellent durability.

  Hereinafter, the present invention will be specifically described with reference to embodiments thereof. The vulcanization bladder of the present invention is characterized by using a rubber composition containing a copolymer of a conjugated diene compound and a non-conjugated olefin.

<Copolymer of conjugated diene compound and non-conjugated olefin>
The rubber composition used in the present invention contains a copolymer of a conjugated diene compound and a non-conjugated olefin. The content is preferably 5 parts by mass or more and more preferably 10 parts by mass or more in 100 parts by mass of the rubber component from the viewpoint of tensile strength and durability of the resulting vulcanizing bladder.

  The copolymer of the conjugated diene compound and the non-conjugated olefin is not particularly limited, but the cis 1,4-bond content of the conjugated diene compound-derived portion (conjugated diene portion) is preferably more than 92%. Since the glass transition temperature of the copolymer is lowered by setting the cis 1,4-bond content of the conjugated diene compound-derived portion (conjugated diene portion) to more than 92%, the rubber composition containing the copolymer The durability of the vulcanizing bladder using can be further improved. The cis 1,4-bond content is an amount in the portion derived from the conjugated diene compound and is not a ratio to the whole copolymer.

  The non-conjugated olefin used as the monomer is a non-conjugated olefin other than the conjugated diene compound, and has excellent heat resistance and reduces the proportion of double bonds in the main chain of the copolymer and controls crystallinity. This makes it possible to increase the degree of design freedom as an elastomer.

  The non-conjugated olefin is preferably an acyclic olefin, and the non-conjugated olefin is preferably an α-olefin having 2 to 10 carbon atoms. Since the α-olefin has a double bond at the α-position of the olefin, copolymerization with the conjugated diene can be performed efficiently. Accordingly, preferred examples of non-conjugated olefins include α-olefins such as ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, and among these, ethylene, propylene and 1-butene is preferred and ethylene is more preferred. These non-conjugated olefins may be used alone or in combination of two or more. In addition, an olefin refers to the compound which is an aliphatic unsaturated hydrocarbon and has one or more carbon-carbon double bonds.

  In the copolymer of the conjugated diene compound and the non-conjugated olefin, the content of the non-conjugated olefin (part derived from the non-conjugated olefin) is preferably 10 to 50 mol%, and more preferably 15 to 20 mol%. . When the content of the non-conjugated olefin is 10 mol% or more, the weather resistance is excellent, and when the content is 50 mol% or less, the heat resistance is excellent without causing layer separation.

  The conjugated diene compound preferably has 4 to 8 carbon atoms. Specific examples of the conjugated diene compound include 1,3-butadiene, isoprene, 1,3-pentadiene, 2,3-dimethylbutadiene, and among these, 1,3-butadiene and isoprene are preferable. Moreover, these conjugated diene compounds may be used independently and may be used in combination of 2 or more type. The copolymer of the present invention can be prepared by the same mechanism using any of the specific examples of the conjugated diene compound described above.

  In addition, when a block portion composed of a monomer unit of a non-conjugated olefin is provided, it exhibits static crystallinity and can be excellent in mechanical properties such as breaking strength.

  Such a copolymer does not cause the problem of lowering the molecular weight, and its weight average molecular weight (Mw) is not particularly limited, but from the viewpoint of application to a polymer structure material, The combined polystyrene equivalent weight average molecular weight (Mw) is preferably 10,000 to 10,000,000, more preferably 10,000 to 1,000,000, and still more preferably 50,000 to 600,000. When Mw is 10,000,000 or less, moldability is not deteriorated.

  Further, the molecular weight distribution (Mw / Mn) represented by the ratio of the weight average molecular weight (Mw) and the number average molecular weight (Mn) is preferably 10 or less, and more preferably 6 or less. When the molecular weight distribution is 10 or less, the physical properties can be made uniform. Here, the average molecular weight and the molecular weight distribution can be determined using polystyrene as a standard substance by gel permeation chromatography (GPC).

  In the copolymer of the conjugated diene compound and the non-conjugated olefin of the present invention, it is preferable that the non-conjugated olefin is not continuously arranged.

Next, the manufacturing method of the copolymer of the said conjugated diene compound and a nonconjugated olefin is demonstrated in detail. However, the manufacturing method described in detail below is merely an example.
The conjugated diene compound-nonconjugated olefin copolymer includes a step of polymerizing a conjugated diene compound and a nonconjugated olefin in the presence of the polymerization catalyst or polymerization catalyst composition shown below. As a polymerization method, any method such as a solution polymerization method, a suspension polymerization method, a liquid phase bulk polymerization method, an emulsion polymerization method, a gas phase polymerization method, and a solid phase polymerization method can be used. Moreover, when using a solvent for a polymerization reaction, the solvent used should just be inactive in a polymerization reaction, For example, toluene, cyclohexane, normal hexane, mixtures thereof etc. are mentioned.

  According to the above production method, except that the polymerization catalyst or the polymerization catalyst composition is used, the monomer conjugated diene compound and the non-conjugated olefin are produced in the same manner as in the production method of the polymer using the normal coordination ion polymerization catalyst. It can be copolymerized.

（式中、Ｍは、ランタノイド元素、スカンジウム又はイットリウムを示し、Ｃｐ^Rは、それぞれ独立して無置換もしくは置換インデニルを示し、Ｒ^a〜Ｒ^fは、それぞれ独立して炭素数１〜３のアルキル基又は水素原子を示し、Ｌは、中性ルイス塩基を示し、ｗは、０〜３の整数を示す）で表されるメタロセン錯体、及び下記一般式（ＩＩ）：

（式中、Ｍは、ランタノイド元素、スカンジウム又はイットリウムを示し、Ｃｐ^Rは、それぞれ独立して無置換もしくは置換インデニルを示し、Ｘ'は、水素原子、ハロゲン原子、アルコキシド基、チオラート基、アミド基、シリル基又は炭素数１〜２０の炭化水素基を示し、Ｌは、中性ルイス塩基を示し、ｗは、０〜３の整数を示す）で表されるメタロセン錯体、並びに下記一般式（ＩＩＩ）：

（式中、Ｍは、ランタノイド元素、スカンジウム又はイットリウムを示し、Ｃｐ^R'は、無置換もしくは置換シクロペンタジエニル、インデニル又はフルオレニルを示し、Ｘは、水素原子、ハロゲン原子、アルコキシド基、チオラート基、アミド基、シリル基又は炭素数１〜２０の炭化水素基を示し、Ｌは、中性ルイス塩基を示し、ｗは、０〜３の整数を示し、［Ｂ］^-は、非配位性アニオンを示す）で表されるハーフメタロセンカチオン錯体からなる群より選択される少なくとも１種類の錯体を含む重合触媒組成物（以下、第一重合触媒組成物ともいう）が挙げられ、該重合触媒組成物は、更に、通常のメタロセン錯体を含む重合触媒組成物に含有される他の成分、例えば助触媒等を含んでいてもよい。ここで、メタロセン錯体は、一つ又は二つ以上のシクロペンタジエニル又はその誘導体が中心金属に結合した錯体化合物であり、特に、中心金属に結合したシクロペンタジエニル又はその誘導体が一つであるメタロセン錯体を、ハーフメタロセン錯体と称することがある。なお、重合反応系において、第一重合触媒組成物に含まれる錯体の濃度は０．１〜０．０００１ｍｏｌ／Ｌの範囲であることが好ましい。 <First polymerization catalyst composition>
The polymerization catalyst composition includes the following general formula (I):

(In the formula, M represents a lanthanoid element, scandium or yttrium, Cp ^R independently represents unsubstituted or substituted indenyl, and R ^{a to} R ^f each independently represents an alkyl having 1 to 3 carbon atoms. A group or a hydrogen atom, L represents a neutral Lewis base, w represents an integer of 0 to 3), and the following general formula (II):

(In the formula, M represents a lanthanoid element, scandium or yttrium, Cp ^R each independently represents an unsubstituted or substituted indenyl group, and X ′ represents a hydrogen atom, a halogen atom, an alkoxide group, a thiolate group, an amide group. , A silyl group or a hydrocarbon group having 1 to 20 carbon atoms, L represents a neutral Lewis base, and w represents an integer of 0 to 3), and the following general formula (III ):

(In the formula, M represents a lanthanoid element, scandium or yttrium, Cp ^R ′ represents an unsubstituted or substituted cyclopentadienyl, indenyl or fluorenyl, and X represents a hydrogen atom, a halogen atom, an alkoxide group or a thiolate group. , An amide group, a silyl group, or a hydrocarbon group having 1 to 20 carbon atoms, L represents a neutral Lewis base, w represents an integer of 0 to 3, and [B] ⁻ represents a non-coordinating group. A polymerization catalyst composition (hereinafter also referred to as a first polymerization catalyst composition) comprising at least one complex selected from the group consisting of a half metallocene cation complex represented by The product may further contain other components contained in the polymerization catalyst composition containing a normal metallocene complex, such as a promoter. Here, the metallocene complex is a complex compound in which one or more cyclopentadienyl or a derivative thereof is bonded to a central metal, and in particular, one cyclopentadienyl or a derivative thereof bonded to the central metal. A certain metallocene complex may be called a half metallocene complex. In the polymerization reaction system, the concentration of the complex contained in the first polymerization catalyst composition is preferably in the range of 0.1 to 0.0001 mol / L.

In the metallocene complexes represented by the above general formulas (I) and (II), Cp ^R in the formula is unsubstituted indenyl or substituted indenyl. Cp ^R having an indenyl ring as a basic skeleton can be represented by C ₉ H _7-X R _X or C ₉ H _11-X R _X. Here, X is an integer of 0-7 or 0-11. In addition, each R is preferably independently a hydrocarbyl group or a metalloid group. The hydrocarbyl group preferably has 1 to 20 carbon atoms, more preferably 1 to 10 carbon atoms, and still more preferably 1 to 8 carbon atoms. Specific examples of the hydrocarbyl group include a methyl group, an ethyl group, a phenyl group, and a benzyl group. On the other hand, examples of metalloid group metalloids include germyl Ge, stannyl Sn, and silyl Si, and the metalloid group preferably has a hydrocarbyl group, and the hydrocarbyl group that the metalloid group has is the same as the above hydrocarbyl group. is there. Specific examples of the metalloid group include a trimethylsilyl group. Specific examples of the substituted indenyl include 2-phenylindenyl and 2-methylindenyl. Note that the two Cp ^Rs in the general formulas (I) and (II) may be the same as or different from each other.

（式中、Ｒは水素原子、メチル基又はエチル基を示す。） In the half metallocene cation complex represented by the general formula (III), Cp ^R ′ in the formula is unsubstituted or substituted cyclopentadienyl, indenyl or fluorenyl, and among these, unsubstituted or substituted indenyl It is preferable that Cp ^R ′ having a cyclopentadienyl ring as a basic skeleton is represented by C ₅ H _5-X R _X. Here, X is an integer of 0-5. In addition, each R is preferably independently a hydrocarbyl group or a metalloid group. The hydrocarbyl group preferably has 1 to 20 carbon atoms, more preferably 1 to 10 carbon atoms, and still more preferably 1 to 8 carbon atoms. Specific examples of the hydrocarbyl group include a methyl group, an ethyl group, a phenyl group, and a benzyl group. On the other hand, examples of metalloid group metalloids include germyl Ge, stannyl Sn, and silyl Si, and the metalloid group preferably has a hydrocarbyl group, and the hydrocarbyl group that the metalloid group has is the same as the above hydrocarbyl group. is there. Specific examples of the metalloid group include a trimethylsilyl group. Specific examples of Cp ^R 'having a cyclopentadienyl ring as a basic skeleton include the following.

(In the formula, R represents a hydrogen atom, a methyl group or an ethyl group.)

In the general formula (III), Cp ^R ′ having the indenyl ring as a basic skeleton is defined in the same manner as Cp ^{R in the} general formula (I), and preferred examples thereof are also the same.

In the general formula (III), Cp ^R ′ having the fluorenyl ring as a basic skeleton can be represented by C ₁₃ H _9-X R _X or C ₁₃ H _17-X R _X. Here, X is an integer of 0-9 or 0-17. In addition, each R is preferably independently a hydrocarbyl group or a metalloid group. The hydrocarbyl group preferably has 1 to 20 carbon atoms, more preferably 1 to 10 carbon atoms, and still more preferably 1 to 8 carbon atoms. Specific examples of the hydrocarbyl group include a methyl group, an ethyl group, a phenyl group, and a benzyl group. On the other hand, examples of metalloid group metalloids include germyl Ge, stannyl Sn, and silyl Si, and the metalloid group preferably has a hydrocarbyl group, and the hydrocarbyl group that the metalloid group has is the same as the above hydrocarbyl group. is there. Specific examples of the metalloid group include a trimethylsilyl group.

  The central metal M in the general formulas (I), (II) and (III) is a lanthanoid element, scandium or yttrium. The lanthanoid elements include 15 elements having atomic numbers 57 to 71, and any of these may be used. Preferred examples of the central metal M include samarium Sm, neodymium Nd, praseodymium Pr, gadolinium Gd, cerium Ce, holmium Ho, scandium Sc, and yttrium Y.

The metallocene complex represented by the general formula (I) contains a silylamide ligand [—N (SiR ₃ ) ₂ ]. The R groups contained in the silylamide ligand (R ^{a to} R ^f in the general formula (I)) are each independently an alkyl group having 1 to 3 carbon atoms or a hydrogen atom. Moreover, it is preferable that at least one of R ^{a to} R ^f is a hydrogen atom. By making at least one of R ^{a to} R ^f a hydrogen atom, the synthesis of the catalyst is facilitated, and the bulk height around silicon is reduced, so that non-conjugated olefin is easily introduced. From the same viewpoint, it is more preferable that at least one of R ^{a to} R ^c is a hydrogen atom and at least one of R ^{d to} R ^f is a hydrogen atom. Furthermore, a methyl group is preferable as the alkyl group.

The metallocene complex represented by the general formula (II) includes a silyl ligand [—SiX ′ ₃ ]. X ′ contained in the silyl ligand [—SiX ′ ₃ ] is a group defined in the same manner as X in the general formula (III) described below, and preferred groups are also the same.

  In the general formula (III), X is a group selected from the group consisting of a hydrogen atom, a halogen atom, an alkoxide group, a thiolate group, an amide group, a silyl group, and a hydrocarbon group having 1 to 20 carbon atoms. Here, examples of the alkoxide group include aliphatic alkoxy groups such as a methoxy group, an ethoxy group, a propoxy group, an n-butoxy group, an isobutoxy group, a sec-butoxy group, and a tert-butoxy group; a phenoxy group and 2,6-dioxy -Tert-butylphenoxy group, 2,6-diisopropylphenoxy group, 2,6-dinepentylphenoxy group, 2-tert-butyl-6-isopropylphenoxy group, 2-tert-butyl-6-neopentylphenoxy group, Examples include aryloxide groups such as 2-isopropyl-6-neopentylphenoxy group, and among these, 2,6-di-tert-butylphenoxy group is preferable.

  In the general formula (III), the thiolate group represented by X includes a thiomethoxy group, a thioethoxy group, a thiopropoxy group, a thio n-butoxy group, a thioisobutoxy group, a thiosec-butoxy group, a thiotert-butoxy group and the like Group thiolate group; thiophenoxy group, 2,6-di-tert-butylthiophenoxy group, 2,6-diisopropylthiophenoxy group, 2,6-dineopentylthiophenoxy group, 2-tert-butyl-6-isopropyl Arylthiolate groups such as thiophenoxy group, 2-tert-butyl-6-thioneopentylphenoxy group, 2-isopropyl-6-thioneopentylphenoxy group, 2,4,6-triisopropylthiophenoxy group, etc. Among these, 2,4,6-triisopropylthiophenoxy group Preferred.

  In the general formula (III), examples of the amide group represented by X include aliphatic amide groups such as a dimethylamide group, a diethylamide group, and a diisopropylamide group; a phenylamide group, a 2,6-di-tert-butylphenylamide group, 2 , 6-diisopropylphenylamide group, 2,6-dineopentylphenylamide group, 2-tert-butyl-6-isopropylphenylamide group, 2-tert-butyl-6-neopentylphenylamide group, 2-isopropyl- Arylamide groups such as 6-neopentylphenylamide group and 2,4,6-tri-tert-butylphenylamide group; and bistrialkylsilylamide groups such as bistrimethylsilylamide group. Among these, bistrimethylsilylamide Groups are preferred.

  In the general formula (III), examples of the silyl group represented by X include trimethylsilyl group, tris (trimethylsilyl) silyl group, bis (trimethylsilyl) methylsilyl group, trimethylsilyl (dimethyl) silyl group, triisopropylsilyl (bistrimethylsilyl) silyl group, and the like. Among these, a tris (trimethylsilyl) silyl group is preferable.

  In the general formula (III), the halogen atom represented by X may be any of a fluorine atom, a chlorine atom, a bromine atom or an iodine atom, but a chlorine atom or a bromine atom is preferred. Moreover, as a C1-C20 hydrocarbon group which X represents, specifically, a methyl group, an ethyl group, n-propyl group, isopropyl group, n-butyl group, isobutyl group, sec-butyl group, tert- Linear or branched aliphatic hydrocarbon groups such as butyl group, neopentyl group, hexyl group, octyl group; aromatic hydrocarbon groups such as phenyl group, tolyl group, naphthyl group; aralkyl groups such as benzyl group, etc. Others: Examples include hydrocarbon groups containing silicon atoms such as trimethylsilylmethyl group and bistrimethylsilylmethyl group. Among these, methyl group, ethyl group, isobutyl group, trimethylsilylmethyl group and the like are preferable.

  In the general formula (III), X is preferably a bistrimethylsilylamide group or a hydrocarbon group having 1 to 20 carbon atoms.

In the general formula (III), [B] ^- The non-coordinating anion represented by, for example, a tetravalent boron anion. Specific examples of the tetravalent boron anion include tetraphenyl borate, tetrakis (monofluorophenyl) borate, tetrakis (difluorophenyl) borate, tetrakis (trifluorophenyl) borate, tetrakis (tetrafluorophenyl) borate, tetrakis ( Pentafluorophenyl) borate, tetrakis (tetrafluoromethylphenyl) borate, tetra (tolyl) borate, tetra (xylyl) borate, (triphenyl, pentafluorophenyl) borate, [tris (pentafluorophenyl), phenyl] borate, tri Decahydride-7,8-dicarbaoundecaborate and the like can be mentioned, and among these, tetrakis (pentafluorophenyl) borate is preferable.

  The metallocene complex represented by the general formulas (I) and (II) and the half metallocene cation complex represented by the general formula (III) are further 0 to 3, preferably 0 to 1 neutral. Contains Lewis base L. Here, examples of the neutral Lewis base L include tetrahydrofuran, diethyl ether, dimethylaniline, trimethylphosphine, lithium chloride, neutral olefins, neutral diolefins, and the like. Here, when the complex includes a plurality of neutral Lewis bases L, the neutral Lewis bases L may be the same or different.

  Moreover, the metallocene complex represented by the general formula (I) and the formula (II) and the half metallocene cation complex represented by the general formula (III) may exist as a monomer, a dimer or It may be present as a higher multimer.

（式中、Ｘ''はハライドを示す。） The metallocene complex represented by the general formula (I) includes, for example, a lanthanoid trishalide, scandium trishalide, or yttrium trishalide in a solvent, an indenyl salt (for example, potassium salt or lithium salt) and bis (trialkylsilyl). It can be obtained by reacting with an amide salt (for example, potassium salt or lithium salt). In addition, since reaction temperature should just be about room temperature, it can manufacture on mild conditions. The reaction time is arbitrary, but is about several hours to several tens of hours. The reaction solvent is not particularly limited, but is preferably a solvent that dissolves the raw material and the product. For example, toluene may be used. Below, the reaction example for obtaining the metallocene complex represented by general formula (I) is shown.

(In the formula, X ″ represents a halide.)

（式中、Ｘ''はハライドを示す。） The metallocene complex represented by the general formula (II) includes, for example, a lanthanoid trishalide, a scandium trishalide, or a yttrium trishalide in a solvent, an indenyl salt (for example, potassium salt or lithium salt), and a silyl salt (for example, potassium). Salt or lithium salt). In addition, since reaction temperature should just be about room temperature, it can manufacture on mild conditions. The reaction time is arbitrary, but is about several hours to several tens of hours. The reaction solvent is not particularly limited, but is preferably a solvent that dissolves the raw material and the product. For example, toluene may be used. Below, the reaction example for obtaining the metallocene complex represented by general formula (II) is shown.

(In the formula, X ″ represents a halide.)

The half metallocene cation complex represented by the general formula (III) can be obtained, for example, by the following reaction.

Here, in the compound represented by the general formula (IV), M represents a lanthanoid element, scandium or yttrium, and Cp ^R ′ independently represents unsubstituted or substituted cyclopentadienyl, indenyl or fluorenyl. , X represents a hydrogen atom, a halogen atom, an alkoxide group, a thiolate group, an amide group, a silyl group, or a hydrocarbon group having 1 to 20 carbon atoms, L represents a neutral Lewis base, and w represents 0 to 3 Indicates an integer. In the ionic compound represented by the general formula [A] ⁺ [B] ⁻ , [A] ⁺ represents a cation, and [B] ⁻ represents a non-coordinating anion.

Examples of the cation represented by [A] ⁺ include a carbonium cation, an oxonium cation, an amine cation, a phosphonium cation, a cycloheptatrienyl cation, and a ferrocenium cation having a transition metal. Examples of the carbonium cation include trisubstituted carbonium cations such as a triphenylcarbonium cation and a tri (substituted phenyl) carbonium cation. The tri (substituted phenyl) carbonyl cation is specifically exemplified by tri (methylphenyl). ) Carbonium cation and the like. Examples of amine cations include trialkylammonium cations such as trimethylammonium cation, triethylammonium cation, tripropylammonium cation, and tributylammonium cation; N, N-dimethylanilinium cation, N, N-diethylanilinium cation, N, N- N, N-dialkylanilinium cations such as 2,4,6-pentamethylanilinium cation; dialkylammonium cations such as diisopropylammonium cation and dicyclohexylammonium cation. Examples of the phosphonium cation include triarylphosphonium cations such as triphenylphosphonium cation, tri (methylphenyl) phosphonium cation, and tri (dimethylphenyl) phosphonium cation. Among these cations, N, N-dialkylanilinium cation or carbonium cation is preferable, and N, N-dialkylanilinium cation is particularly preferable.

The ionic compound represented by the general formula [A] ⁺ [B] ⁻ used for the above reaction is a compound selected and combined from the above non-coordinating anions and cations, which is N, N-dimethylaniline. Preference is given to nium tetrakis (pentafluorophenyl) borate, triphenylcarbonium tetrakis (pentafluorophenyl) borate and the like. In general formula [A] ⁺ [B] ^- ionic compounds represented by is preferably added from 0.1 to 10 mol per mol of the metallocene complex, more preferably it added about 1 molar. When the half metallocene cation complex represented by the general formula (III) is used for the polymerization reaction, the half metallocene cation complex represented by the general formula (III) may be provided as it is in the polymerization reaction system, or the compound represented by the general formula (IV) and the general formula used in the reaction [a] ⁺ [B] ^- provides an ionic compound represented separately into the polymerization reaction system, the general formula in the reaction system (III You may form the half metallocene cation complex represented by this. Further, by using a combination of the metallocene complex represented by the general formula (I) or the formula (II) and the ionic compound represented by the general formula [A] ⁺ [B] ⁻ , A half metallocene cation complex represented by the formula (III) can also be formed.

  The structures of the metallocene complexes represented by the general formulas (I) and (II) and the half metallocene cation complex represented by the general formula (III) are preferably determined by X-ray structural analysis.

  The co-catalyst that can be used in the first polymerization catalyst composition can be arbitrarily selected from components used as a co-catalyst for a polymerization catalyst composition containing a normal metallocene complex. Suitable examples of the cocatalyst include aluminoxanes, organoaluminum compounds, and the above ionic compounds. These promoters may be used alone or in combination of two or more.

  The aluminoxane is preferably an alkylaminoxan, and examples thereof include methylaluminoxane (MAO) and modified methylaluminoxane. As the modified methylaluminoxane, MMAO-3A (manufactured by Tosoh Finechem Co., Ltd.) and the like are preferable. The content of aluminoxane in the first polymerization catalyst composition is such that the element ratio Al / M between the central metal M of the metallocene complex and the aluminum element Al of the aluminoxane is about 10 to 1000, preferably about 100. It is preferable to make it.

  On the other hand, as the organoaluminum compound, the general formula AlRR′R ″ (wherein R and R ′ are each independently a C1-C10 hydrocarbon group or a hydrogen atom, and R ″ is a C1-C10 An organoaluminum compound represented by (a hydrocarbon group) is preferable. Examples of the organoaluminum compound include trialkylaluminum, dialkylaluminum chloride, alkylaluminum dichloride, and dialkylaluminum hydride. Among these, trialkylaluminum is preferable. Examples of the trialkylaluminum include triethylaluminum and triisobutylaluminum. In addition, it is preferable that it is 2-50 times mole with respect to a metallocene complex, and, as for content of the organoaluminum compound in the said polymerization catalyst composition, it is still more preferable that it is about 10 times mole.

  Further, in the above polymerization catalyst composition, the metallocene complex represented by the general formula (I) and the formula (II) and the half metallocene cation complex represented by the above general formula (III) are each used as an appropriate promoter. By combining, the amount of cis-1,4 bonds and the molecular weight of the resulting copolymer can be increased.

<Second polymerization catalyst composition>
In addition, as the polymerization catalyst composition,
Component (a): a rare earth element compound or a reaction product of the rare earth element compound and a Lewis base, the rare earth element compound or the reaction product having no bond between the rare earth element and carbon,
Component (b): includes ionic compound (b-1) composed of non-coordinating anion and cation, aluminoxane (b-2), Lewis acid, complex compound of metal halide and Lewis base, and active halogen Preferable examples include a polymerization catalyst composition (hereinafter also referred to as a second polymerization catalyst composition) containing at least one selected from the group consisting of at least one halogen compound (b-3) among organic compounds. Can
When the second polymerization catalyst composition contains at least one of an ionic compound (b-1) and a halogen compound (b-3), the polymerization catalyst composition further comprises:
(C) Component: The following general formula (X):
YR ¹ _a R ² _b R ³ _c (X)
[Wherein Y is a metal selected from Group 1, Group 2, Group 12 and Group 13 of the Periodic Table, and R ¹ and R ² are the same or different and have 1 to 10 carbon atoms. R ³ is a hydrocarbon group or a hydrogen atom, and R ³ is a hydrocarbon group having 1 to 10 carbon atoms, provided that R ³ may be the same as or different from R ¹ or R ^2, and Y is a periodic table. When it is a metal selected from Group 1, a is 1 and b and c are 0, and when Y is a metal selected from Groups 2 and 12 of the Periodic Table, a and b are 1 and c is 0, and when Y is a metal selected from Group 13 of the Periodic Table, a, b and c are 1]. It is characterized by including.

The second polymerization catalyst composition used in the method for producing the copolymer needs to contain the component (a) and the component (b), where the polymerization catalyst composition is the ionic compound (b). -1) and at least one of the above halogen compounds (b-3),
(C) Component: The following general formula (X):
YR ¹ _a R ² _b R ³ _c (X)
[Wherein Y is a metal selected from Group 1, Group 2, Group 12 and Group 13 of the Periodic Table, and R ¹ and R ² are the same or different and have 1 to 10 carbon atoms. R ³ is a hydrocarbon group or a hydrogen atom, and R ³ is a hydrocarbon group having 1 to 10 carbon atoms, provided that R ³ may be the same as or different from R ¹ or R ^2, and Y is a periodic table. When it is a metal selected from Group 1, a is 1 and b and c are 0, and when Y is a metal selected from Groups 2 and 12 of the Periodic Table, a and b are 1 and c is 0, and when Y is a metal selected from Group 13 of the Periodic Table, a, b and c are 1]. It is necessary to include. Since the ionic compound (b-1) and the halogen compound (b-3) have no carbon atom to be supplied to the component (a), the carbon source for the component (a) is the above ( c) A component is required. In addition, even if the said polymerization catalyst composition is a case where the said aluminoxane (b-2) is included, this polymerization catalyst composition can contain the said (c) component. The second polymerization catalyst composition may contain other components, such as a promoter, contained in a normal rare earth element compound-based polymerization catalyst composition. In the polymerization reaction system, the concentration of the component (a) contained in the second polymerization catalyst composition is preferably in the range of 0.1 to 0.0001 mol / l.

  The component (a) used in the second polymerization catalyst composition is a rare earth element compound or a reaction product of the rare earth element compound and a Lewis base. Here, the reaction of the rare earth element compound and the rare earth element compound with a Lewis base is performed. The object does not have a bond between rare earth element and carbon. When the rare earth element compound and the reactant do not have a rare earth element-carbon bond, the compound is stable and easy to handle. Here, the rare earth element compound is a compound containing a lanthanoid element or scandium or yttrium composed of the elements of atomic numbers 57 to 71 in the periodic table. Specific examples of the lanthanoid element include lanthanium, cerium, praseodymium, neodymium, promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, and lutetium. In addition, the said (a) component may be used individually by 1 type, and may be used in combination of 2 or more type.

The rare earth element compound is preferably a divalent or trivalent salt or complex compound of a rare earth metal, and one or more coordinations selected from a hydrogen atom, a halogen atom and an organic compound residue. More preferably, the rare earth element compound contains a child. Furthermore, the reaction product of the rare earth element compound or the rare earth element compound and a Lewis base is represented by the following general formula (XI) or (XII):
M ¹¹ X ¹¹ ₂ · L ¹¹ w (XI)
M ¹¹ X ¹¹ ₃ · L ¹¹ w (XII)
[Wherein, M ¹¹ represents a lanthanoid element, scandium or yttrium, and X ¹¹ independently represents a hydrogen atom, a halogen atom, an alkoxide group, a thiolate group, an amide group, a silyl group, an aldehyde residue, a ketone residue. A group, a carboxylic acid residue, a thiocarboxylic acid residue or a phosphorus compound residue, L ¹¹ represents a Lewis base, and w represents 0 to 3].

  Specific examples of the group (ligand) bonded to the rare earth element of the rare earth element compound include a hydrogen atom; a methoxy group, an ethoxy group, a propoxy group, an n-butoxy group, an isobutoxy group, a sec-butoxy group, a tert- Aliphatic alkoxy groups such as butoxy group; phenoxy group, 2,6-di-tert-butylphenoxy group, 2,6-diisopropylphenoxy group, 2,6-dineopentylphenoxy group, 2-tert-butyl-6- Isopropylphenoxy group, 2-tert-butyl-6-neopentylphenoxy group, 2-isopropyl-6-neopentylphenoxy group; thiomethoxy group, thioethoxy group, thiopropoxy group, thio n-butoxy group, thioisobutoxy group, thio aliphatic thiolate groups such as sec-butoxy group and thio-tert-butoxy group; Noxy group, 2,6-di-tert-butylthiophenoxy group, 2,6-diisopropylthiophenoxy group, 2,6-dineopentylthiophenoxy group, 2-tert-butyl-6-isopropylthiophenoxy group, 2 Arylthiolate groups such as -tert-butyl-6-thioneopentylphenoxy, 2-isopropyl-6-thioneopentylphenoxy, 2,4,6-triisopropylthiophenoxy; dimethylamide, diethylamide, diisopropyl Aliphatic amide group such as amide group; phenylamide group, 2,6-di-tert-butylphenylamide group, 2,6-diisopropylphenylamide group, 2,6-dineopentylphenylamide group, 2-tert- Butyl-6-isopropylphenylamide group, 2-tert-butyl Arylamide groups such as ru-6-neopentylphenylamide group, 2-isopropyl-6-neopentylphenylamide group, 2,4,6-tert-butylphenylamide group; bistrialkylsilylamides such as bistrimethylsilylamide group Groups: silyl groups such as trimethylsilyl group, tris (trimethylsilyl) silyl group, bis (trimethylsilyl) methylsilyl group, trimethylsilyl (dimethyl) silyl group, triisopropylsilyl (bistrimethylsilyl) silyl group; fluorine atom, chlorine atom, bromine atom, iodine And halogen atoms such as atoms. Furthermore, residues of aldehydes such as salicylaldehyde, 2-hydroxy-1-naphthaldehyde, 2-hydroxy-3-naphthaldehyde; 2′-hydroxyacetophenone, 2′-hydroxybutyrophenone, 2′-hydroxypropiophenone, etc. Hydroxyphenone residues of: acetylacetone, benzoylacetone, propionylacetone, isobutylacetone, valerylacetone, ethylacetylacetone, etc. diketone residues; isovaleric acid, caprylic acid, octanoic acid, lauric acid, myristic acid, palmitic acid, Stearic acid, isostearic acid, oleic acid, linoleic acid, cyclopentanecarboxylic acid, naphthenic acid, ethylhexanoic acid, bivaric acid, versatic acid [trade name of Shell Chemical Co., Ltd., mixture of isomers of C10 monocarboxylic acid Synthetic acids comprised of, carboxylic acid residues such as phenylacetic acid, benzoic acid, 2-naphthoic acid, maleic acid, succinic acid; hexanethioic acid, 2,2-dimethylbutanethioic acid, decanethioic acid, thiobenzoic acid Thiocarboxylic acid residues such as dibutyl phosphate, dipentyl phosphate, dihexyl phosphate, diheptyl phosphate, dioctyl phosphate, bis (2-ethylhexyl phosphate), bis (1-methylheptyl phosphate), dilauryl phosphate Dioleyl phosphate, diphenyl phosphate, bis (p-nonylphenyl) phosphate, bis (polyethylene glycol-p-nonylphenyl) phosphate, (butyl) phosphate (2-ethylhexyl), phosphoric acid (1-methylheptyl) ) (2-ethylhexyl), phosphoric acid esters such as phosphoric acid (2-ethylhexyl) (p-nonylphenyl) Residues; monobutyl 2-ethylhexylphosphonate, mono-2-ethylhexyl 2-ethylhexylphosphonate, mono-2-ethylhexyl phenylphosphonate, mono-p-nonylphenyl 2-ethylhexylphosphonate, mono-2-ethylhexyl phosphonate, Phosphonic acid ester residues such as mono-1-methylheptyl phosphonate, mono-p-nonylphenyl phosphonate, dibutylphosphinic acid, bis (2-ethylhexyl) phosphinic acid, bis (1-methylheptyl) phosphinic acid, di Laurylphosphinic acid, dioleylphosphinic acid, diphenylphosphinic acid, bis (p-nonylphenyl) phosphinic acid, butyl (2-ethylhexyl) phosphinic acid, (2-ethylhexyl) (1-methylheptyl) phosphinic acid, (2-ethylhexyl) Phosphinic acids such as (p-nonylphenyl) phosphinic acid, butylphosphinic acid, 2-ethylhexylphosphinic acid, 1-methylheptylphosphinic acid, oleylphosphinic acid, laurylphosphinic acid, phenylphosphinic acid, p-nonylphenylphosphinic acid Can also be mentioned. In addition, these ligands may be used individually by 1 type, and may be used in combination of 2 or more type.

In the component (a) used in the second polymerization catalyst composition, examples of the Lewis base that reacts with the rare earth element compound include tetrahydrofuran, diethyl ether, dimethylaniline, trimethylphosphine, lithium chloride, neutral olefins, Diolefins and the like. Here, when the rare earth element compound reacts with a plurality of Lewis bases (in the formulas (XI) and (XII), when w is 2 or 3), the Lewis base L ¹¹ is the same or different. It may be.

  The component (b) used in the second polymerization catalyst composition is at least one compound selected from the group consisting of an ionic compound (b-1), an aluminoxane (b-2) and a halogen compound (b-3). is there. In addition, it is preferable that content of the sum total of (b) component in said 2nd polymerization catalyst composition is 0.1-50 times mole with respect to (a) component.

  The ionic compound represented by the above (b-1) is composed of a non-coordinating anion and a cation, and reacts with a reaction product of the rare earth element compound or its Lewis base as the component (a) to be cationic. Examples thereof include ionic compounds capable of generating a transition metal compound. Here, as the non-coordinating anion, for example, tetraphenyl borate, tetrakis (monofluorophenyl) borate, tetrakis (difluorophenyl) borate, tetrakis (trifluorophenyl) borate, tetrakis (tetrafluorophenyl) borate, tetrakis ( Pentafluorophenyl) borate, tetrakis (tetrafluoromethylphenyl) borate, tetra (tolyl) borate, tetra (xylyl) borate, (triphenyl, pentafluorophenyl) borate, [tris (pentafluorophenyl), phenyl] borate, tri Decahydride-7,8-dicarboundecaborate and the like can be mentioned. On the other hand, examples of the cation include a carbonium cation, an oxonium cation, an ammonium cation, a phosphonium cation, a cycloheptatrienyl cation, and a ferrocenium cation having a transition metal. Specific examples of the carbonium cation include trisubstituted carbonium cations such as triphenylcarbonium cation and tri (substituted phenyl) carbonium cation, and more specifically, as tri (substituted phenyl) carbonyl cation, Examples include tri (methylphenyl) carbonium cation, tri (dimethylphenyl) carbonium cation, and the like. Specific examples of ammonium cations include trialkylammonium cations such as trimethylammonium cation, triethylammonium cation, tripropylammonium cation, and tributylammonium cation (for example, tri (n-butyl) ammonium cation); N, N-dimethylanilinium N, N-dialkylanilinium cation such as cation, N, N-diethylanilinium cation, N, N-2,4,6-pentamethylanilinium cation; dialkylammonium cation such as diisopropylammonium cation and dicyclohexylammonium cation Is mentioned. Specific examples of the phosphonium cation include triarylphosphonium cations such as triphenylphosphonium cation, tri (methylphenyl) phosphonium cation, and tri (dimethylphenyl) phosphonium cation. Accordingly, the ionic compound is preferably a compound selected and combined from the above-mentioned non-coordinating anions and cations, specifically, N, N-dimethylanilinium tetrakis (pentafluorophenyl) borate, triphenylcarbohydrate. Preferred is nitrotetrakis (pentafluorophenyl) borate. Moreover, these ionic compounds can be used individually by 1 type, or 2 or more types can be mixed and used for them. In addition, it is preferable that it is 0.1-10 times mole with respect to (a) component, and, as for content of the ionic compound in the said 2nd polymerization catalyst composition, it is still more preferable that it is about 1 time mole.

  The aluminoxane represented by the above (b-2) is a compound obtained by bringing an organoaluminum compound and a condensing agent into contact with each other. For example, the aluminoxane represented by the general formula: (—Al (R ′) O—) A chain aluminoxane or cyclic aluminoxane having a unit (wherein R ′ is a hydrocarbon group having 1 to 10 carbon atoms, and some of the hydrocarbon groups may be substituted with a halogen atom and / or an alkoxy group) The degree of polymerization of the unit is preferably 5 or more, and more preferably 10 or more. Here, specific examples of R ′ include a methyl group, an ethyl group, a propyl group, and an isobutyl group. Among these, a methyl group is preferable. Examples of the organoaluminum compound used as an aluminoxane raw material include trialkylaluminums such as trimethylaluminum, triethylaluminum, and triisobutylaluminum, and mixtures thereof, and trimethylaluminum is particularly preferable. For example, an aluminoxane using a mixture of trimethylaluminum and tributylaluminum as a raw material can be preferably used. The content of the aluminoxane in the second polymerization catalyst composition is such that the element ratio Al / M of the rare earth element M constituting the component (a) and the aluminum element Al of the aluminoxane is about 10 to 1000. It is preferable to do.

  The halogen compound represented by (b-3) is composed of at least one of a Lewis acid, a complex compound of a metal halide and a Lewis base, and an organic compound containing an active halogen. By reacting with a certain rare earth element compound or a reaction product thereof with a Lewis base, a cationic transition metal compound, a halogenated transition metal compound, or a compound in which the transition metal center is deficient in charge can be generated. In addition, it is preferable that content of the sum total of the halogen compound in the said 2nd polymerization catalyst composition is 1-5 times mole with respect to (a) component.

As the Lewis acid, boron-containing halogen compounds such as B (C ₆ F ₅ ) ₃ and aluminum-containing halogen compounds such as Al (C ₆ F ₅ ) ₃ can be used. A halogen compound containing an element belonging to the group V, VI or VIII can also be used. Preferably, aluminum halide or organometallic halide is used. Moreover, as a halogen element, chlorine or bromine is preferable. Specific examples of the Lewis acid include methyl aluminum dibromide, methyl aluminum dichloride, ethyl aluminum dibromide, ethyl aluminum dichloride, butyl aluminum dibromide, butyl aluminum dichloride, dimethyl aluminum bromide, dimethyl aluminum chloride, diethyl aluminum bromide, diethyl Aluminum chloride, dibutylaluminum bromide, dibutylaluminum chloride, methylaluminum sesquibromide, methylaluminum sesquichloride, ethylaluminum sesquibromide, ethylaluminum sesquichloride, dibutyltin dichloride, aluminum tribromide, antimony trichloride, antimony pentachloride, phosphorus trichloride , Pentachloride , Tin tetrachloride, titanium tetrachloride, tungsten hexachloride, etc., among which diethylaluminum chloride, ethylaluminum sesquichloride, ethylaluminum dichloride, diethylaluminum bromide, ethylaluminum sesquibromide, ethylaluminum dibromide preferable.

  The metal halide constituting the complex compound of the above metal halide and Lewis base includes beryllium chloride, beryllium bromide, beryllium iodide, magnesium chloride, magnesium bromide, magnesium iodide, calcium chloride, calcium bromide, iodine. Calcium chloride, barium chloride, barium bromide, barium iodide, zinc chloride, zinc bromide, zinc iodide, cadmium chloride, cadmium bromide, cadmium iodide, mercury chloride, mercury bromide, mercury iodide, manganese chloride, Manganese bromide, manganese iodide, rhenium chloride, rhenium bromide, rhenium iodide, copper chloride, copper iodide, silver chloride, silver bromide, silver iodide, gold chloride, gold iodide, gold bromide, etc. Of these, magnesium chloride, calcium chloride, barium chloride, manganese chloride, zinc chloride, and copper chloride are preferred. , Magnesium chloride, manganese chloride, zinc chloride, copper chloride being particularly preferred.

  Moreover, as a Lewis base which comprises the complex compound of the said metal halide and a Lewis base, a phosphorus compound, a carbonyl compound, a nitrogen compound, an ether compound, alcohol, etc. are preferable. Specifically, tributyl phosphate, tri-2-ethylhexyl phosphate, triphenyl phosphate, tricresyl phosphate, triethylphosphine, tributylphosphine, triphenylphosphine, diethylphosphinoethane, diphenylphosphinoethane, acetylacetone, benzoylacetone , Propionitrile acetone, valeryl acetone, ethyl acetylacetone, methyl acetoacetate, ethyl acetoacetate, phenyl acetoacetate, dimethyl malonate, diethyl malonate, diphenyl malonate, acetic acid, octanoic acid, 2-ethyl-hexanoic acid, olein Acid, stearic acid, benzoic acid, naphthenic acid, versatic acid, triethylamine, N, N-dimethylacetamide, tetrahydrofuran, diphenyl ether, 2-ethyl-hexyl alcohol Examples include oleyl alcohol, stearyl alcohol, phenol, benzyl alcohol, 1-decanol, and lauryl alcohol. Among these, tri-2-ethylhexyl phosphate, tricresyl phosphate, acetylacetone, 2-ethylhexanoic acid, versatic acid, 2 -Ethylhexyl alcohol, 1-decanol and lauryl alcohol are preferred.

The Lewis base is reacted at a ratio of 0.01 to 30 mol, preferably 0.5 to 10 mol, per mol of the metal halide. When the reaction product with the Lewis base is used, the metal remaining in the polymer can be reduced.
Examples of the organic compound containing the active halogen include benzyl chloride.

The component (c) used in the second polymerization catalyst composition is represented by the following general formula (X):
YR ¹ _a R ² _b R ³ _c (X)
[Wherein Y is a metal selected from Group 1, Group 2, Group 12 and Group 13 of the Periodic Table, and R ¹ and R ² are the same or different and have 1 to 10 carbon atoms. R ³ is a hydrocarbon group or a hydrogen atom, and R ³ is a hydrocarbon group having 1 to 10 carbon atoms, provided that R ³ may be the same as or different from R ¹ or R ^2, and Y is a periodic table. When it is a metal selected from Group 1, a is 1 and b and c are 0, and when Y is a metal selected from Groups 2 and 12 of the Periodic Table, a and b are 1 and c is 0, and when Y is a metal selected from Group 13 of the Periodic Table, a, b and c are 1]. Yes, the following general formula (Xa):
AlR ¹ R ² R ³ (Xa)
[Wherein, R ¹ and R ² are the same or different and each represents a hydrocarbon group having 1 to 10 carbon atoms or a hydrogen atom, and R ³ is a hydrocarbon group having 1 to 10 carbon atoms, provided that R ³ represents the above It may be the same as or different from R ¹ or R ² ]. Examples of the organoaluminum compound of the formula (X) include trimethylaluminum, triethylaluminum, tri-n-propylaluminum, triisopropylaluminum, tri-n-butylaluminum, triisobutylaluminum, tri-t-butylaluminum, tripentylaluminum, Trihexyl aluminum, tricyclohexyl aluminum, trioctyl aluminum; diethyl aluminum hydride, di-n-propyl aluminum hydride, di-n-butyl aluminum hydride, diisobutyl aluminum hydride, dihexyl aluminum hydride, diisohexyl hydride Aluminum, dioctyl aluminum hydride, diisooctyl aluminum hydride; ethyl aluminum dihydride, n-propyl aluminum Hydride, include isobutyl aluminum dihydride and the like, among these, triethylaluminum, triisobutylaluminum, hydrogenated diethylaluminum, hydrogenated diisobutylaluminum are preferred. The organoaluminum compound as component (c) described above can be used alone or in combination of two or more. In addition, it is preferable that it is 1-50 times mole with respect to (a) component, and, as for content of the organoaluminum compound in said 2nd polymerization catalyst composition, it is still more preferable that it is about 10 times mole.

<Polymerization catalyst and third polymerization catalyst composition>
The polymerization catalyst is for polymerization of a conjugated diene compound and a non-conjugated olefin, and has the following formula (A):
R _a MX _b QY _b (A)
[In the formula, each R independently represents an unsubstituted or substituted indenyl, the R is coordinated to M, M represents a lanthanoid element, scandium or yttrium; 20 represents a hydrocarbon group, X is μ-coordinated to M and Q, Q represents a group 13 element of the periodic table, and Y independently represents a hydrocarbon group having 1 to 20 carbon atoms or A hydrogen atom, wherein Y is coordinated to Q and a and b are 2].

［式中、Ｍ¹は、ランタノイド元素、スカンジウム又はイットリウムを示し、Ｃｐ^Rは、それぞれ独立して無置換もしくは置換インデニルを示し、Ｒ^a及びＲ^bは、それぞれ独立して炭素数１〜２０の炭化水素基を示し、該Ｒ^a及びＲ^bは、Ｍ¹及びＡｌにμ配位しており、Ｒ^c及びＲ^dは、それぞれ独立して炭素数１〜２０の炭化水素基又は水素原子を示す］で表されるメタロセン系複合触媒が挙げられる。 In a preferred example of the metallocene composite catalyst, the following formula (XV):

[ ^Wherein , M ¹ represents a lanthanoid element, scandium or yttrium, Cp ^R independently represents an unsubstituted or substituted indenyl group, and R ^a and R ^b each independently have 1 to 20 carbon atoms. R ^a and R ^b are μ-coordinated to M ¹ and Al, and R ^c and R ^d each independently represents a hydrocarbon group having 1 to 20 carbon atoms or a hydrogen atom. Metallocene composite catalysts represented by

  The third polymerization catalyst composition includes the metallocene composite catalyst and a boron anion.

<Metalocene composite catalyst>
Hereinafter, the metallocene composite catalyst will be described in detail. The metallocene composite catalyst includes a lanthanoid element, a rare earth element of scandium or yttrium, and a Group 13 element of the periodic table, and has the following formula (A):
R _a MX _b QY _b (A)
[In the formula, each R independently represents an unsubstituted or substituted indenyl, the R is coordinated to M, M represents a lanthanoid element, scandium or yttrium; 20 represents a hydrocarbon group, X is μ-coordinated to M and Q, Q represents a group 13 element of the periodic table, and Y independently represents a hydrocarbon group having 1 to 20 carbon atoms or A hydrogen atom, wherein Y is coordinated to Q, and a and b are 2.] By using the metallocene polymerization catalyst, a copolymer of a conjugated diene compound and a non-conjugated olefin can be produced. In addition, by using the metallocene composite catalyst, for example, a catalyst previously combined with an aluminum catalyst, the amount of alkylaluminum used at the time of copolymer synthesis can be reduced or eliminated. If a conventional catalyst system is used, it is necessary to use a large amount of alkylaluminum at the time of copolymer synthesis. For example, in the conventional catalyst system, it is necessary to use 10 equivalents or more of alkylaluminum with respect to the metal catalyst. If the metallocene composite catalyst is used, an excellent catalytic action can be obtained by adding about 5 equivalents of alkylaluminum. Is demonstrated.

  In the metallocene composite catalyst, the metal M in the formula (A) is a lanthanoid element, scandium, or yttrium. The lanthanoid elements include 15 elements having atomic numbers 57 to 71, and any of these may be used. Preferred examples of the metal M include samarium Sm, neodymium Nd, praseodymium Pr, gadolinium Gd, cerium Ce, holmium Ho, scandium Sc, and yttrium Y.

  In the formula (A), each R is independently an unsubstituted indenyl or a substituted indenyl, and the R is coordinated to the metal M. Specific examples of the substituted indenyl group include 1,2,3-trimethylindenyl group, heptamethylindenyl group, 1,2,4,5,6,7-hexamethylindenyl group, and the like. It is done.

  In the above formula (A), Q represents a group 13 element in the periodic table, and specific examples include boron, aluminum, gallium, indium, thallium and the like.

  In the above formula (A), each X independently represents a hydrocarbon group having 1 to 20 carbon atoms, and X is μ-coordinated to M and Q. Here, as a C1-C20 hydrocarbon group, methyl group, ethyl group, propyl group, butyl group, pentyl group, hexyl group, heptyl group, octyl group, decyl group, dodecyl group, tridecyl group, tetradecyl group , Pentadecyl group, hexadecyl group, heptadecyl group, stearyl group and the like. Note that the μ coordination is a coordination mode having a crosslinked structure.

  In the formula (A), each Y independently represents a hydrocarbon group having 1 to 20 carbon atoms or a hydrogen atom, and the Y is coordinated to Q. Here, as a C1-C20 hydrocarbon group, methyl group, ethyl group, propyl group, butyl group, pentyl group, hexyl group, heptyl group, octyl group, decyl group, dodecyl group, tridecyl group, tetradecyl group , Pentadecyl group, hexadecyl group, heptadecyl group, stearyl group and the like.

In the above formula (XV), the metal M ¹ is a lanthanoid element, scandium or yttrium. The lanthanoid elements include 15 elements having atomic numbers 57 to 71, and any of these may be used. Preferred examples of the metal M ¹ include samarium Sm, neodymium Nd, praseodymium Pr, gadolinium Gd, cerium Ce, holmium Ho, scandium Sc, and yttrium Y.

In the above formula (XV), Cp ^R is unsubstituted indenyl or substituted indenyl. Cp ^R having an indenyl ring as a basic skeleton can be represented by C ₉ H _7-X R _X or C ₉ H _11-X R _X. Here, X is an integer of 0-7 or 0-11. In addition, each R is preferably independently a hydrocarbyl group or a metalloid group. The hydrocarbyl group preferably has 1 to 20 carbon atoms, more preferably 1 to 10 carbon atoms, and still more preferably 1 to 8 carbon atoms. Specific examples of the hydrocarbyl group include a methyl group, an ethyl group, a phenyl group, and a benzyl group. On the other hand, examples of metalloid group metalloids include germyl Ge, stannyl Sn, and silyl Si, and the metalloid group preferably has a hydrocarbyl group, and the hydrocarbyl group that the metalloid group has is the same as the above hydrocarbyl group. is there. Specific examples of the metalloid group include a trimethylsilyl group. Specific examples of the substituted indenyl include 2-phenylindenyl and 2-methylindenyl. Incidentally, the two Cp ^R in the formula (XV) may each be the same or different from each other.

In the above formula (XV), R ^A and R ^B each independently represent a hydrocarbon group having 1 to 20 carbon atoms, said R ^A and R are coordinated μ to M ¹及A ^l. Here, as a C1-C20 hydrocarbon group, methyl group, ethyl group, propyl group, butyl group, pentyl group, hexyl group, heptyl group, octyl group, decyl group, dodecyl group, tridecyl group, tetradecyl group , Pentadecyl group, hexadecyl group, heptadecyl group, stearyl group and the like. Note that the μ coordination is a coordination mode having a crosslinked structure.

In the above formula (XV), R ^C and R ^D are each independently a hydrocarbon group having 1 to 20 carbon atoms or a hydrogen atom. Here, as a C1-C20 hydrocarbon group, methyl group, ethyl group, propyl group, butyl group, pentyl group, hexyl group, heptyl group, octyl group, decyl group, dodecyl group, tridecyl group, tetradecyl group , Pentadecyl group, hexadecyl group, heptadecyl group, stearyl group and the like.

（式中、Ｍ²は、ランタノイド元素、スカンジウム又はイットリウムを示し、Ｃｐ^Rは、それぞれ独立して無置換もしくは置換インデニルを示し、Ｒ^E〜Ｒ^Jは、それぞれ独立して炭素数１〜３のアルキル基又は水素原子を示し、Ｌは、中性ルイス塩基を示し、ｗは、０〜３の整数を示す）で表されるメタロセン錯体を、ＡｌＲ^KＲ^LＲ^Mで表される有機アルミニウム化合物と反応させることで得られる。なお、反応温度は室温程度にすればよいので、温和な条件で製造することができる。また、反応時間は任意であるが、数時間〜数十時間程度である。反応溶媒は特に限定されないが、原料及び生成物を溶解する溶媒であることが好ましく、例えばトルエンやヘキサンを用いればよい。なお、上記メタロセン系複合触媒の構造は、¹Ｈ−ＮＭＲやＸ線構造解析により決定することが好ましい。 The metallocene composite catalyst is, for example, in a solvent in the following formula (XVI):

(In the formula, M ² represents a lanthanoid element, scandium or yttrium, Cp ^R each independently represents an unsubstituted or substituted indenyl group, and R ^{E to} R ^J each independently represents a group having 1 to 3 carbon atoms. an alkyl group or a hydrogen atom, L is a neutral Lewis base, w is, the metallocene complex represented by an integer of 0 to 3), an organoaluminum compound represented by AlR ^K R ^L R ^M It is obtained by reacting with. In addition, since reaction temperature should just be about room temperature, it can manufacture on mild conditions. The reaction time is arbitrary, but is about several hours to several tens of hours. The reaction solvent is not particularly limited, but is preferably a solvent that dissolves the raw material and the product. For example, toluene or hexane may be used. The structure of the metallocene composite catalyst is preferably determined by ¹ H-NMR or X-ray structural analysis.

In the metallocene complex represented by the above formula (XVI), Cp ^R is unsubstituted indenyl or substituted indenyl, and has the same meaning as Cp ^R in the above formula (XV). In the above formula (XVI), the metal M ² is a lanthanoid element, scandium or yttrium, and has the same meaning as the metal M ¹ in the above formula (XV).

The metallocene complex represented by the above formula (XVI) contains a silylamide ligand [—N (SiR ₃ ) ₂ ]. The R groups (R ^{E to} R ^J groups) contained in the silylamide ligand are each independently an alkyl group having 1 to 3 carbon atoms or a hydrogen atom. Moreover, it is preferable that at least one of R ^{E to} R ^J is a hydrogen atom. By making at least one of R ^{E to} R ^J a hydrogen atom, the catalyst can be easily synthesized. Furthermore, a methyl group is preferable as the alkyl group.

  The metallocene complex represented by the above formula (XVI) further contains 0 to 3, preferably 0 to 1, neutral Lewis bases L. Here, examples of the neutral Lewis base L include tetrahydrofuran, diethyl ether, dimethylaniline, trimethylphosphine, lithium chloride, neutral olefins, neutral diolefins, and the like. Here, when the complex includes a plurality of neutral Lewis bases L, the neutral Lewis bases L may be the same or different.

  Moreover, the metallocene complex represented by the above formula (XVI) may exist as a monomer, or may exist as a dimer or a multimer higher than that.

On the other hand, the organoaluminum compound used for the production of the metallocene composite catalyst is represented by AlR ^K R ^L R ^M , where R ^K and R ^L are each independently a monovalent carbon atom having 1 to 20 carbon atoms. R ^M is a hydrogen group or a hydrogen atom, and R ^M is a monovalent hydrocarbon group having 1 to 20 carbon atoms, provided that R ^M may be the same as or different from R ^K or R ^L described above. Examples of the monovalent hydrocarbon group having 1 to 20 carbon atoms include methyl group, ethyl group, propyl group, butyl group, pentyl group, hexyl group, heptyl group, octyl group, decyl group, dodecyl group, tridecyl group and tetradecyl group. , Pentadecyl group, hexadecyl group, heptadecyl group, stearyl group and the like.

  Specific examples of the organoaluminum compound include trimethylaluminum, triethylaluminum, tri-n-propylaluminum, triisopropylaluminum, tri-n-butylaluminum, triisobutylaluminum, tri-t-butylaluminum, tripentylaluminum, Hexyl aluminum, tricyclohexyl aluminum, trioctyl aluminum; diethyl aluminum hydride, di-n-propyl aluminum hydride, di-n-butyl aluminum hydride, diisobutyl aluminum hydride, dihexyl aluminum hydride, diisohexyl aluminum hydride , Dioctylaluminum hydride, diisooctylaluminum hydride; ethylaluminum dihydride, n-propylaluminium Dihydride, isobutyl aluminum dihydride and the like. Among these, triethylaluminum, triisobutylaluminum, hydrogenated diethylaluminum, hydrogenated diisobutylaluminum are preferred. These organoaluminum compounds can be used alone or in combination of two or more. In addition, the amount of the organoaluminum compound used for the production of the metallocene composite catalyst is preferably 1 to 50 times mole, more preferably about 10 times mole relative to the metallocene complex.

<Third polymerization catalyst composition>
The polymerization catalyst composition contains the metallocene composite catalyst and a boron anion, and further contains other components such as a cocatalyst contained in the polymerization catalyst composition containing a normal metallocene catalyst. Etc. are preferably included. The metallocene composite catalyst and boron anion are also referred to as a two-component catalyst. According to the third polymerization catalyst composition, since the boron anion is further contained in the same manner as the metallocene composite catalyst, the content of each monomer component in the copolymer can be arbitrarily controlled. Become.

  In the third polymerization catalyst composition, specific examples of the boron anion constituting the two-component catalyst include a tetravalent boron anion. For example, tetraphenylborate, tetrakis (monofluorophenyl) borate, tetrakis (difluorophenyl) borate, tetrakis (trifluorophenyl) borate, tetrakis (tetrafluorophenyl) borate, tetrakis (pentafluorophenyl) borate, tetrakis (tetrafluoromethyl) Phenyl) borate, tetra (tolyl) borate, tetra (xylyl) borate, (triphenyl, pentafluorophenyl) borate, [tris (pentafluorophenyl), phenyl] borate, tridecahydride-7,8-dicarboundecaborate Among these, tetrakis (pentafluorophenyl) borate is preferable.

  In addition, the said boron anion can be used as an ionic compound combined with the cation. Examples of the cation include a carbonium cation, an oxonium cation, an amine cation, a phosphonium cation, a cycloheptatrienyl cation, and a ferrocenium cation having a transition metal. Examples of the carbonium cation include trisubstituted carbonium cations such as a triphenylcarbonium cation and a tri (substituted phenyl) carbonium cation. The tri (substituted phenyl) carbonyl cation is specifically exemplified by tri (methylphenyl). ) Carbonium cation and the like. Examples of amine cations include trialkylammonium cations such as trimethylammonium cation, triethylammonium cation, tripropylammonium cation, and tributylammonium cation; N, N-dimethylanilinium cation, N, N-diethylanilinium cation, N, N- N, N-dialkylanilinium cations such as 2,4,6-pentamethylanilinium cation; dialkylammonium cations such as diisopropylammonium cation and dicyclohexylammonium cation. Examples of the phosphonium cation include triarylphosphonium cations such as triphenylphosphonium cation, tri (methylphenyl) phosphonium cation, and tri (dimethylphenyl) phosphonium cation. Among these cations, N, N-dialkylanilinium cation or carbonium cation is preferable, and N, N-dialkylanilinium cation is particularly preferable. Therefore, as the ionic compound, N, N-dimethylanilinium tetrakis (pentafluorophenyl) borate, triphenylcarbonium tetrakis (pentafluorophenyl) borate and the like are preferable. In addition, it is preferable to add 0.1-10 times mole with respect to the said metallocene type composite catalyst, and, as for the ionic compound which consists of a boron anion and a cation, it is still more preferable to add about 1 time mole.

  In the third polymerization catalyst composition, it is necessary to use the metallocene composite catalyst and the boron anion, but a reaction system for reacting the metallocene catalyst represented by the formula (XVI) with an organoaluminum compound. If a boron anion is present, the metallocene composite catalyst of the above formula (XV) cannot be synthesized. Therefore, for the preparation of the third polymerization catalyst composition, it is necessary to synthesize the metallocene composite catalyst in advance, isolate and purify the metallocene composite catalyst, and then combine with the boron anion.

Examples of the third polymerization catalyst co-catalyst which can be used in the compositions, for example, other organic aluminum compound represented by AlR ^K R ^L R ^M described above, aluminoxane can be preferably used. The aluminoxane is preferably an alkylaminoxan, and examples thereof include methylaluminoxane (MAO) and modified methylaluminoxane. As the modified methylaluminoxane, MMAO-3A (manufactured by Tosoh Finechem Co., Ltd.) and the like are preferable. These aluminoxanes may be used alone or in combination of two or more.

  In the method for producing a copolymer, as described above, polymerization is carried out in the same manner as in the method for producing a polymer using a normal coordination ion polymerization catalyst, except that the polymerization catalyst or the polymerization catalyst composition is used. be able to. Here, in the copolymer production method, for example, (1) a component of the polymerization catalyst composition is separately provided in a polymerization reaction system including a conjugated diene compound as a monomer and a non-conjugated olefin other than the conjugated diene compound. The polymerization catalyst composition may be used in the reaction system, or (2) a polymerization catalyst composition prepared in advance may be provided in the polymerization reaction system. Moreover, (2) includes providing a metallocene complex (active species) activated by a cocatalyst. In addition, the usage-amount of the metallocene complex contained in a polymerization catalyst composition has the preferable range of 0.0001-0.01 times mole with respect to the sum total of nonconjugated olefins other than a conjugated diene compound and this conjugated diene compound.

  In the method for producing a copolymer, the polymerization may be stopped using a polymerization terminator such as methanol, ethanol, or isopropanol.

  In the method for producing a copolymer, the polymerization reaction of the conjugated diene compound and the non-conjugated olefin is preferably performed in an atmosphere of an inert gas, preferably nitrogen gas or argon gas. The polymerization temperature of the polymerization reaction is not particularly limited, but is preferably in the range of −100 ° C. to 200 ° C., for example, and can be about room temperature. If the polymerization temperature is raised, the cis-1,4 selectivity of the polymerization reaction may be lowered. Moreover, since the pressure of the said polymerization reaction fully takes in a conjugated diene compound and a nonconjugated olefin in a polymerization reaction system, the range of 0.1-10.0 MPa is preferable. The reaction time of the polymerization reaction is not particularly limited and is preferably in the range of 1 second to 10 days, for example, but can be appropriately selected depending on conditions such as the type of monomer to be polymerized, the type of catalyst, and the polymerization temperature.

  In the method for producing the copolymer, when the conjugated diene compound is polymerized with a non-conjugated olefin other than the conjugated diene compound, the pressure of the non-conjugated olefin is preferably 0.1 MPa to 10 MPa. When the pressure of the non-conjugated olefin is 0.1 MPa or more, the non-conjugated olefin can be efficiently introduced into the reaction mixture. Moreover, even if the pressure of the non-conjugated olefin is increased too much, the effect of efficiently introducing the non-conjugated olefin reaches a peak, and therefore the pressure of the non-conjugated olefin is preferably 10 MPa or less.

In the method for producing the copolymer, when the conjugated diene compound is polymerized with a non-conjugated olefin other than the conjugated diene compound, the concentration of the conjugated diene compound at the start of polymerization (mol / l) and the concentration of the non-conjugated olefin (Mol / l) means the following formula:
Non-conjugated olefin concentration / conjugated diene compound concentration ≧ 1.0
It is preferable to satisfy the relationship:
Non-conjugated olefin concentration / conjugated diene compound concentration ≧ 1.3
And more preferably the following formula:
Non-conjugated olefin concentration / conjugated diene compound concentration ≧ 1.7
Satisfy the relationship. By setting the value of the concentration of the non-conjugated olefin / the concentration of the conjugated diene compound to 1 or more, the non-conjugated olefin can be efficiently introduced into the reaction mixture.

<Rubber component>
The rubber composition used in the vulcanizing bladder of the present invention can contain other rubber as a rubber component in addition to the copolymer of the conjugated diene compound and the non-conjugated olefin. Other rubber components are not particularly limited. For example, butyl rubber, halogenated butyl rubber, chloroprene rubber, butadiene rubber, halogenated butadiene rubber, ethylene-propylene rubber, fluorine rubber, acrylic rubber, natural rubber, isoprene rubber, styrene- Examples thereof include butadiene rubber, acrylonitrile-butadiene rubber, and silicone rubber. Among these, butyl rubber and halogenated butyl rubber are preferable from the viewpoints of heat resistance, mechanical properties, and releasability of the resulting vulcanizing bladder.

<Filler>
The rubber composition used for the vulcanization bladder of the present invention can contain a filler. Examples of the filler include, but are not limited to, carbon black, wet silica, calcium carbonate, aluminum hydroxide, aluminum oxide, magnesium oxide, montmorillonite, mica, smectite, organic montmorillonite, organic mica, and organic smectite. . Among these, carbon black is preferable from the viewpoint of durability of the resulting vulcanizing bladder. These fillers may be used individually by 1 type, and may use 2 or more types. Moreover, it is preferable that it is 20-80 mass parts with respect to 100 mass parts of rubber components, and, as for content of the said filler, it is still more preferable that it is 30-70 mass parts. When the filler content is 20 parts by mass or more with respect to 100 parts by mass of the rubber component, the tensile strength of the resulting vulcanizing bladder is good, and when it is 80 parts by mass or less, molding processability and bending resistance are improved. It is good and does not cause deterioration in durability.

<Zinc flower>
The rubber composition used for the vulcanization bladder of the present invention can contain zinc white (ZnO). The zinc white content is preferably 0.5 to 8 parts by mass, more preferably 2 to 7 parts by mass with respect to 100 parts by mass of the rubber component. When the content of zinc white is 0.5 parts by mass or more with respect to 100 parts by mass of the rubber component, vulcanization can be promoted sufficiently, and when it is 8 parts by mass or less, workability is also good.

<Sulfur>
Moreover, the rubber composition used for the vulcanizing bladder of the present invention may contain 0.1 to 10 parts by mass of sulfur with respect to 100 parts by mass of the rubber component, and preferably 0.2 to 5 parts by mass. . When the sulfur content is 0.1 parts by mass or more with respect to 100 parts by mass of the rubber component, a sufficient crosslinking density as a vulcanized rubber can be formed, and when it is 10 parts by mass or less, the elasticity of the rubber composition The rate does not become too high and can be easily removed from the mold during the production of the vulcanizing bladder.

<Other ingredients>
In addition to the above components, the rubber composition used in the vulcanizing bladder of the present invention contains known compounding agents such as heat resistance improvers, flame retardants, heat conduction imparting agents, vulcanization accelerators, and vulcanization accelerators. An agent, a processing aid and the like can be appropriately blended depending on the purpose.

  The vulcanizing bladder of the present invention is not particularly limited and has a known structure and can be produced by a usual method. For example, a rubber composition obtained by blending a copolymer of a conjugated diene compound and a non-conjugated olefin and the above components, kneading, heating, extruding, etc., was molded into the shape of a vulcanizing bladder. Thereafter, it can be vulcanized and manufactured.

  The kneading conditions are not particularly limited, and various conditions such as the input volume to the kneading apparatus, the rotational speed of the rotor, the ram pressure, the kneading temperature, the kneading time, the type of the kneading apparatus, and the like depending on the purpose Can be selected as appropriate. Moreover, as a kneading apparatus, the Banbury mixer, intermix, kneader etc. which are normally used for kneading | mixing of a rubber composition are mentioned, for example.

  There is no restriction | limiting in particular as said heating conditions, It can select suitably according to the objective about various conditions, such as heating temperature, heating time, and a heating apparatus. Moreover, as a heating apparatus, the roll machine etc. which are normally used for the heating of a rubber composition are mentioned, for example.

  The conditions for the extrusion are not particularly limited, and various conditions such as an extrusion time, an extrusion speed, an extrusion apparatus, and an extrusion temperature can be appropriately selected according to the purpose. Moreover, as an extrusion apparatus, the extruder etc. which are normally used for extrusion of a rubber composition are mentioned, for example. In addition, extrusion temperature can be suitably determined according to the objective.

  There is no restriction | limiting in particular as said molding and vulcanization conditions, It can select suitably according to the objective about various conditions, such as an apparatus and a system. As an apparatus for performing vulcanization, for example, a molding vulcanizer using a mold usually used for vulcanizing a rubber composition may be used. The temperature at the time of vulcanization is usually about 100 to 190 ° C.

  The vulcanizing bladder of the present invention contains a copolymer of a conjugated diene compound and a non-conjugated olefin, and is not only excellent in heat resistance, weather resistance, ozone resistance, mechanical properties, releasability, but also durable. Excellent in properties. Therefore, since the vulcanizing bladder of the present invention has a long life, the cost can be reduced, and a rubber product, particularly a tire product can be efficiently produced.

  EXAMPLES Hereinafter, although this invention is demonstrated concretely based on an Example, this invention is not limited to these Examples.

<Production example of copolymer of conjugated diene compound and non-conjugated olefin>
After adding 325 mL of a toluene solution containing 13.58 g (0.25 mol) of 1,3-butadiene to a sufficiently dried 400 mL pressure-resistant glass reactor, ethylene was introduced at 0.4 MPa. On the other hand, in a glove box under a nitrogen atmosphere, bis (2-phenylindenyl) gadolinium bis (dimethylsilylamide) [(2-PhC ₉ H ₆ ) 2GdN (SiHMe ₂ ) ₂ ] 18.0 μmol in a glass container, 36.0 μmol of dimethylanilinium tetrakis (pentafluorophenyl) borate (Me ₂ NHPhB (C ₆ F ₅ ) ₄ ) and 0.90 mmol of diisobutylaluminum hydride were charged and dissolved in 10 ml of toluene to obtain a catalyst solution. Thereafter, the catalyst solution was taken out from the glove box, an amount of 17.5 μmol in terms of gadolinium was added to the monomer solution, and polymerization was performed at room temperature for 180 minutes. After the polymerization, 1 mL of 2,2′-methylene-bis (4-ethyl-6-tert-butylphenol) (NS-5) 5% by mass isopropanol solution was added to stop the reaction, and a copolymer with a large amount of methanol was added. Was separated and vacuum-dried at 70 ° C. to obtain a copolymer A. The yield of the obtained copolymer A was 12.00 g.

  Regarding the copolymer A obtained as described above, the weight average molecular weight (Mw), the molecular weight distribution (Mw / Mn), the cis-1,4 bond content, and the ethylene content were measured and evaluated by the following methods. .

-Weight average molecular weight (Mw) and molecular weight distribution (Mw / Mn)
Using gel permeation chromatography [GPC: Tosoh HLC-8121GPC / HT, column: Tosoh GMH _HR- H (S) HT × 2, detector: differential refractometer (RI)], measuring temperature 140 The weight average molecular weight (Mw) and molecular weight distribution (Mw / Mn) in terms of polystyrene of the polymer were determined on the basis of monodisperse polystyrene at ° C.
The weight average molecular weight (Mw) of the copolymer A was 338,000, and the molecular weight distribution (Mw / Mn) was 1.9.

-Cis-1,4 bond content The microstructure of the butadiene moiety in the copolymer was measured with a ¹ H-NMR spectrum (amount of 1,2-vinyl bonds) and a ¹³ C-NMR spectrum (with a cis-1,4 bond). It was determined from the integral ratio of the trans-1,4 bond content ratio). The calculated value of cis-1,4 bond content (%) of copolymer A was 98%.

-Ethylene content The content (mol%) of the ethylene part in the copolymer was determined by the ¹³ C-NMR spectrum (100 ° C, d-tetrachloroethane standard: 73.8 ppm) as a whole of the ethylene-bonded component (28.5- 30.0 ppm) and the integral ratio of the entire butadiene bond component (26.5-27.5 ppm + 31.5-32.5 ppm). The content of the ethylene portion of the copolymer A was 11 mol%.

(Examples and Comparative Examples)
In the composition shown in Table 1 below, a rubber composition before crosslinking was prepared using a Banbury mixer, and the resulting unvulcanized rubber composition was vulcanized at 150 ° C. for 15 minutes using a high-temperature press, A vulcanized rubber sheet having a thickness of 1 mm was produced. Using this vulcanized rubber sheet, tensile strength (Tb), elongation at break (Eb), and heat resistance (Tb change rate, Eb change rate) were evaluated by the following methods. About hardness, it measured based on JISK6301 (type A). Further, a separately molded unvulcanized rubber composition was vulcanized by a conventional method to produce a vulcanizing bladder used for manufacturing a tire. Using this vulcanizing bladder, the releasability and durability were evaluated by the following methods. The measurement and evaluation results are shown in Table 1.

"Evaluation method"
・ Tensile strength (Tb), elongation at break (Eb)
Using Instron-1125, temperature: 20-24 ° C., pulling speed: 300 mm / min, shape: DIN3, strain reading: tensile strength (Tb) and cutting of each vulcanized rubber sheet under the conditions of automatic measurement The time elongation (Eb) was measured. Larger values indicate better tensile strength and elongation at break.

・ Hardness (Hd)
It measured based on JISK6301 (type A). It shows that it is excellent in hardness, so that a value is large.

・ Tb change rate, Eb change rate In the oven, heat treatment was performed at 160 ° C. for 96 hours, the tensile strength (Tb) and tensile elongation (Eb) before and after the treatment were measured by the above method, and the change rate was calculated. . The smaller the decrease, the better the heat resistance.

・ Releasability Using the obtained vulcanizing bladder, tires of size PSR215 / 60R15.5 were vulcanized under normal conditions, and the vulcanization bladder and the vulcanized tire were easily separated. Was visually evaluated. On the basis of Comparative Example 1, it was marked as ◎ when better than Comparative Example 1, 〇 when equal, and × when defective.

-Durability Using the obtained vulcanizing bladder, vulcanization of tires of size PSR215 / 60R15.5 was repeated under normal conditions until the bladder punctured, and the service life was evaluated. On the basis of Comparative Example 1, it was marked as ◎ when better than Comparative Example 1, 〇 when equal, and × when defective.

* 1 Made by JSR, Butyl268
* 2 Showa Neoprene, Neoprene W
* 3 Toast Carbon, Seast 9
* 4 Made by Hakusuitec Co., Ltd., No. 3 zinc white * 5 Made by Ouchi Shinsei Chemical, Noxeller CZ
* 6 Powder sulfur produced by Hosoi Chemical Co., Ltd.

  As is apparent from the results in Table 1, the vulcanization bladders (Examples 1 and 2) including the rubber composition containing the copolymer of the conjugated diene compound and the non-conjugated olefin are sufficiently good in heat resistance, machine Characteristics (tensile strength, elongation at break, hardness), releasability, and durability are superior to those of the comparative example not including the copolymer. It could be confirmed.

On the other hand, Comparative Example 1 using a rubber composition containing 100 parts by mass of butyl rubber has a tensile strength (Tb) as compared with Example 1 using a rubber composition containing 100 parts by mass of Copolymer A. It was inferior in hardness (Hd) and durability.
Comparative Example 2 using a rubber composition containing 90 parts by mass of butyl rubber and 10 parts by mass of chloroprene rubber is similar to Example 2 using a rubber composition containing 90 parts by mass of butyl rubber and 10 parts by mass of copolymer A. In comparison, the tensile strength (Tb), hardness (Hd), heat resistance (Tb change rate), and durability were inferior.

Claims (4)

  A vulcanizing bladder comprising a rubber composition containing a copolymer of a conjugated diene compound and a non-conjugated olefin.   The vulcanization bladder according to claim 1, wherein the cis 1,4-bond content of the conjugated diene compound-derived portion (conjugated diene portion) is more than 92%.   The vulcanizing bladder according to claim 1 or 2, wherein the rubber composition contains a copolymer of a conjugated diene compound and a non-conjugated olefin in an amount of 5 parts by mass or more per 100 parts by mass of the rubber component.   The said rubber composition contains 20-80 mass parts of fillers with respect to 100 mass parts of rubber components, The bladder for vulcanization | cure as described in any one of Claims 1-3 characterized by the above-mentioned.