WO2014104169A1 - Method for producing modified conjugated diene rubber - Google Patents
Method for producing modified conjugated diene rubber Download PDFInfo
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- WO2014104169A1 WO2014104169A1 PCT/JP2013/084815 JP2013084815W WO2014104169A1 WO 2014104169 A1 WO2014104169 A1 WO 2014104169A1 JP 2013084815 W JP2013084815 W JP 2013084815W WO 2014104169 A1 WO2014104169 A1 WO 2014104169A1
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- conjugated diene
- rubber
- compound
- diene rubber
- carbon atoms
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- 0 **[S+](*N(*)*)(*N(*)*)*N(*)* Chemical compound **[S+](*N(*)*)(*N(*)*)*N(*)* 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
- B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08C—TREATMENT OR CHEMICAL MODIFICATION OF RUBBERS
- C08C19/00—Chemical modification of rubber
- C08C19/30—Addition of a reagent which reacts with a hetero atom or a group containing hetero atoms of the macromolecule
- C08C19/42—Addition of a reagent which reacts with a hetero atom or a group containing hetero atoms of the macromolecule reacting with metals or metal-containing groups
- C08C19/44—Addition of a reagent which reacts with a hetero atom or a group containing hetero atoms of the macromolecule reacting with metals or metal-containing groups of polymers containing metal atoms exclusively at one or both ends of the skeleton
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L15/00—Compositions of rubber derivatives
Definitions
- the present invention relates to a method for producing a modified conjugated diene rubber, and more specifically, to produce a modified conjugated diene rubber that is excellent in processability and can provide a crosslinked rubber having low heat buildup and wear resistance. On how to do.
- the present invention also relates to a modified conjugated diene rubber obtained by this production method, a rubber composition containing the modified conjugated diene rubber, and a crosslinked rubber product thereof.
- a tire obtained from a rubber composition blended with silica is superior in low heat build-up compared to a tire obtained from a rubber composition blended with commonly used carbon black. can do.
- Patent Document 1 discloses that a conjugated diene monomer is polymerized using an organolithium catalyst in which a polyvinyl aromatic compound and lithium are prepared at a predetermined molar ratio, and the resulting polymerization active terminal has a modifier.
- a rubber composition obtained by adding a filler such as silica to a modified conjugated diene rubber obtained by reacting.
- a filler such as silica
- an alkali metalated aromatic compound having 3 or more carbon atoms directly bonded to an alkali metal atom and an aromatic ring in one molecule is used as a polymerization initiator, and at least a conjugated diene compound.
- a method for producing a radial conjugated diene polymer is disclosed in which a monomer mixture comprising is polymerized.
- the conjugated diene polymer by making the conjugated diene polymer have a radial structure, when the filler such as silica is added, the affinity with the filler is improved. The wear resistance can be improved.
- the present invention has been made in view of such a situation, and produces a modified conjugated diene rubber that is excellent in processability and can provide a rubber cross-linked product having low heat buildup and wear resistance. It aims to provide a method for
- the present inventor has obtained, as a polymerization initiator, an alkali metalated aromatic compound having three or more carbon atoms directly bonded to an alkali metal atom and an aromatic ring in one molecule. Is used to polymerize a monomer containing at least a conjugated diene compound, and a predetermined modifier is reacted with the active terminal of the resulting conjugated diene rubber, thereby providing excellent processability and low heat build-up.
- the present inventors have found that a modified conjugated diene rubber can be obtained that can provide a rubber cross-linked product having abrasion resistance, and has completed the present invention.
- At least a conjugated diene compound is used as a polymerization initiator by using an alkali metalated aromatic compound having 3 or more carbon atoms directly bonded to an alkali metal atom and an aromatic ring in one molecule.
- a compound represented by the following general formula (I) at the active end of the conjugated diene rubber having an active terminus by polymerizing a monomer comprising the first step of obtaining a conjugated diene rubber having an active terminus; And a second step of reacting with a modified conjugated diene rubber.
- X represents an atom or a reactive group capable of reacting with the active end of the conjugated diene rubber having the active end, or an active end of the conjugated diene rubber having the active end
- a hydrocarbon group containing any one of atoms and reactive groups capable of reacting, and R 1 to R 4 are each independently a chemical single bond or an alkylene group having 1 to 10 carbon atoms.
- R 5 to R 10 are each independently an alkyl group having 1 to 10 carbon atoms or an aryl group having 6 to 12 carbon atoms, and R 5 to R 10 are combinations of R 5 and R 6 , R And may be combined with each other by a combination of 7 and R 8 or a combination of R 9 and R 10 to form a ring structure together with the nitrogen atom.
- the alkali metalated aromatic compound was obtained by reacting an organic alkali metal compound with an aromatic compound having 3 or more carbon atoms in one molecule directly bonded to an aromatic ring. It is preferable.
- the aromatic compound having 3 or more carbon atoms directly bonded to the aromatic ring in one molecule is preferably an aromatic compound represented by the following general formula (II).
- R 11 to R 18 are each independently a hydrogen atom or an alkyl group having 1 to 10 carbon atoms, and 3 or more of R 11 to R 18 have 1 to And p is an integer of 0 to 5, and when p is 2 or more, 3 or more benzene rings are present regardless of the structure represented by the general formula (II). May be condensed with each other at any position.
- X is a halogen atom
- R 1 to R 4 are chemical single bonds
- R 5 to R 10. are preferably each independently an alkyl group having 1 to 5 carbon atoms.
- the amount of the compound represented by the general formula (I) used in the second step is the alkali metal atom 1 in the alkali metalated aromatic compound used in the first step.
- the amount of atoms or reactive groups capable of reacting with the active terminal of the conjugated diene rubber is preferably in an amount in the range of 0.05 to 5 moles relative to moles.
- the present invention also provides a modified conjugated diene rubber obtained by any one of the above production methods. Furthermore, according to the present invention, there is provided a rubber composition comprising 10 to 200 parts by weight of silica with respect to 100 parts by weight of a rubber component containing the modified conjugated diene rubber.
- the rubber composition of the present invention preferably contains a crosslinking agent.
- a rubber cross-linked product obtained by cross-linking the rubber composition, and a tire comprising the rubber cross-linked product.
- a modified conjugated diene rubber capable of providing a rubber cross-linked product having excellent processability and low heat buildup and wear resistance, and a rubber composition containing the modified conjugated diene rubber And a rubber cross-linked product obtained by using the rubber composition and having low heat build-up and wear resistance.
- the method for producing a modified conjugated diene rubber of the present invention uses, as a polymerization initiator, an alkali metalated aromatic compound having 3 or more carbon atoms directly bonded to an alkali metal atom and an aromatic ring in one molecule, A first step of polymerizing a monomer comprising at least a conjugated diene compound to obtain a conjugated diene rubber having an active end, and a general formula (5) described later at the active end of the conjugated diene rubber having an active end. And a second step of reacting the compound represented by:
- the 1st process in the manufacturing method of this invention is demonstrated.
- the first step uses at least an alkali metalated aromatic compound having 3 or more carbon atoms directly bonded to an alkali metal atom and an aromatic ring in one molecule as a polymerization initiator.
- This is a step of polymerizing a monomer comprising a conjugated diene compound to obtain a conjugated diene rubber having an active end.
- the polymerization initiator used in the first step of the production method of the present invention is an alkali metalated aromatic compound having 3 or more carbon atoms directly bonded to each of an alkali metal atom and an aromatic ring in one molecule.
- the alkali metal atom of the alkali metalated aromatic compound used as a polymerization initiator in the present invention is not particularly limited, but is preferably lithium, sodium, or potassium, and among these, lithium is Particularly preferred.
- the aromatic ring of the alkali metalated aromatic compound is not particularly limited as long as it is a conjugated ring having aromaticity, and specific examples include electrically neutral such as a benzene ring, a naphthalene ring, and an anthracene ring.
- An aromatic hydrocarbon ring an aromatic hydrocarbon ring having a negative charge such as a cyclopentadienyl anion ring, an indenyl anion ring or a fluorenyl anion ring; an aromatic ring containing a heteroatom such as a furan ring or a thiophene ring; And so on.
- an electrically neutral aromatic hydrocarbon ring is preferable, and a benzene ring is particularly preferable.
- An alkali metalated aromatic compound having an electrically neutral aromatic hydrocarbon ring is preferably used from the viewpoint of its stability and polymerization activity.
- the alkali metal atom is usually present in a cation state in the alkali metalated aromatic compound, and the alkali metal atom and the aromatic ring
- the carbon atom directly bonded to each of the carbon atoms is usually present in an anionic state in order to bind to the alkali metal atom in such a cation state.
- the alkali metal atom thus present in the cation state and the carbon atom present in the anion state form an ionic bond, thereby directly connecting each other. It is in a combined state.
- the conjugated diene polymer chain grows with living polymerizability from each of the carbon atoms directly bonded to three or more alkali metal atoms contained in the group compound as the polymerization starting point, the resulting conjugated diene
- the system rubber may have a radial structure.
- the alkali metalated aromatic compound used as a polymerization initiator in the present invention has a structure as long as it has three or more carbon atoms directly bonded to each of an alkali metal atom and an aromatic ring in one molecule. Is not particularly limited. For example, even if three or more carbon atoms directly bonded to an alkali metal atom are directly bonded to one aromatic ring, one carbon atom directly bonded to the alkali metal atom is one. Three or more aromatic rings directly bonded as described above may be bonded via a bonding group.
- R 19 to R 26 each independently represents a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, and an alkali metalation having 1 to 10 carbon atoms in which an alkali metal atom is bonded to the ⁇ -position. It represents any atom or group selected from alkyl groups, and three or more of R 19 to R 26 are alkali metalated alkyl groups having 1 to 10 carbon atoms in which an alkali metal atom is bonded to the ⁇ -position.
- p is an integer of 0 to 5, and when p is 2 or more, regardless of the structure represented by the general formula (1), three or more benzene rings are at arbitrary positions with respect to each other. It may be condensed. For example, when “p” is 2 or more, there are a plurality of R 19 and R 22, but a plurality of R 19 or R 22 may be the same. And it may be different.
- R 20 , R 21 , R 23 , R 24 , R 25 , and R 26 have 1 to 10 of the alkali metalated alkyl groups, and the remainder of R 20 , R 21 , R 23 , R 24 , R 25 , and R 26 is preferably a hydrogen atom.
- the alkali metalated aromatic compound in which three or more aromatic rings in which one or more carbon atoms directly bonded to an alkali metal atom are directly bonded via a bonding group is represented by the following general formula (2) Is preferably used.
- R 27 to R 31 are each independently a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, and an alkali metalation having 1 to 10 carbon atoms in which an alkali metal atom is bonded to the ⁇ -position. It represents any atom or group selected from alkyl groups, and at least one of R 27 to R 31 is an alkali metalated alkyl group having 1 to 10 carbon atoms in which an alkali metal atom is bonded to the ⁇ -position.
- A represents an arbitrary linking group, and q is an integer of 3 to 100.
- the above “independently” means that, for example, when q is 2 or more, there are a plurality of R 27 to R 31, but there are a plurality of R 27 , R 28 , R 29 , R 30 , or R 31 also means that they may be the same or different.
- the method for synthesizing an alkali metalated aromatic compound used as a polymerization initiator in the present invention is not particularly limited, but an organic alkali metal compound is added to an aromatic compound having three or more carbon atoms directly bonded to an aromatic ring in one molecule. Those obtained by reacting are preferably used.
- the alkali metal compound which has an alkyl group or an aryl group is used suitably, As the specific example, Methyl lithium, methyl sodium, methyl potassium, ethyl lithium, ethyl sodium, ethyl potassium, n-propyl lithium, isopropyl potassium, n-butyl lithium, s-butyl lithium, t-butyl lithium, n-butyl sodium, n-butyl Examples include potassium, n-pentyl lithium, n-amyl lithium, n-octyl lithium, phenyl lithium, naphthyl lithium, phenyl sodium, and naphthyl sodium. Among these, an alkali metal compound having an alkyl group is preferable, a lithium compound having an alkyl group is more preferable, and n-butyl
- a lithium compound having an alkyl group or an aryl group and potassium having an alkoxyl group may be obtained by mixing with a sodium compound.
- the potassium or sodium compound having an alkoxyl group used at this time include potassium t-butoxy and sodium t-butoxy.
- the amount of the potassium or sodium compound having an alkoxyl group is not particularly limited, but is usually 0.1 to 5.0 mol, preferably 0.2 to 3.0 mol based on the lithium compound having an alkyl group or an aryl group. Mol, more preferably 0.3 to 2.0 mol.
- An aromatic compound having three or more carbon atoms directly bonded to an aromatic ring that can be used for the synthesis of an alkali metalated aromatic compound in one molecule is an alkali metalated aromatic represented by the general formula (1).
- An aromatic compound for obtaining a compound, an aromatic compound represented by the following general formula (3), and an aromatic compound for obtaining an alkali metalated aromatic compound represented by the above general formula (2) An aromatic compound represented by the following general formula (4) can be exemplified.
- R 11 to R 18 are each independently a hydrogen atom or an alkyl group having 1 to 10 carbon atoms, and three or more of R 11 to R 18 have 1 to 10 carbon atoms. It is an alkyl group.
- p is an integer of 0 to 5, and when p is 2 or more, three or more benzene rings are condensed at arbitrary positions with each other regardless of the structure represented by the general formula (3). It may be what you did.
- the above “independently” means that, for example, when p is 2 or more, there are a plurality of R 11 and R 14, but a plurality of R 11 or R 14 may be the same. , Meaning it may be different.
- R 12 , R 13 , R 15 , R 16 , R 17 , and R 18 are alkyl groups having 1 to 10 carbon atoms, R 12 , It is preferable that the remainder among R 13 , R 15 , R 16 , R 17 , and R 18 is a hydrogen atom.
- R 32 to R 36 are each independently a hydrogen atom or an alkyl group having 1 to 10 carbon atoms, and one or more of R 32 to R 36 are alkyl having 1 to 10 carbon atoms. It is a group.
- A represents an arbitrary linking group, and q is an integer of 3 to 100.
- the above “independently” means that, for example, when q is 2 or more, there are a plurality of R 32 to R 36, but there are a plurality of R 32 , R 33 , R 34 , R 35 , or R 36 also means that they may be the same or different.
- aromatic compound represented by the general formula (3) examples include 1,2,3-trimethylbenzene, 1,2,4-trimethylbenzene, 1,3,5-trimethylbenzene, hexamethylbenzene, 1,2,3-triethylbenzene, 1,2,4-triethylbenzene, 1,3,5-triethylbenzene, 1,2,3-tripropylbenzene, 1,2,4-tripropylbenzene, 1,3 Benzenes having three or more alkyl groups such as 1,3,5-tributylbenzene, 1,3,5-tripentylbenzene, 2,3,5-trimethylnaphthalene, And naphthalenes having three or more alkyl groups such as 4,5-trimethylnaphthalene.
- aromatic compound represented by the general formula (4) examples include o-methylstyrene oligomer, m-methylstyrene oligomer, p-methylstyrene oligomer, p-ethylstyrene oligomer, and p-propylstyrene oligomer.
- a styrene polymer in which one or more hydrogens on the benzene ring are substituted with an alkyl group such as p-butylstyrene oligomer and p-pentylstyrene oligomer.
- the alkali metalated aromatic compound used as the polymerization initiator from the viewpoint that the resulting conjugated diene rubber has a radial structure, 3 carbon atoms directly bonded to the aromatic ring are contained in one molecule. It is preferably obtained by reacting an organic alkali metal compound with an aromatic compound having at least one, and from the viewpoint that the resulting conjugated diene rubber tends to have a more radial structure, the above general formula (3) It is especially preferable that it is a thing obtained by making an organic alkali metal compound react with the aromatic compound represented by these.
- a polymerization initiator in which three or more carbon atoms directly bonded to an alkali metal atom are directly bonded to one aromatic ring, particularly a compound represented by the above general formula (1) is polymerized. It is preferable to use it as an initiator.
- these alkali metallized aromatic compounds may be used individually by 1 type, and may be used in combination of 2 or more type.
- a method of reacting an organic alkali metal compound with an aromatic compound having 3 or more carbon atoms directly bonded to an aromatic ring in the molecule is not particularly limited, but in an inert solvent under an inert atmosphere.
- a reaction method is preferably used.
- the inert solvent used is not particularly limited as long as it can dissolve the compound to be reacted, but a hydrocarbon solvent is preferably used. Specific examples include aliphatic hydrocarbons such as n-hexane, n-heptane, and n-octane; alicyclic hydrocarbons such as cyclohexane, cyclopentane, and methylcyclohexane.
- these solvents may be used individually by 1 type, and 2 or more types may be mixed and used for them.
- the amount of the organic alkali metal compound used for the aromatic compound having 3 or more carbon atoms directly bonded to the aromatic ring in the molecule is not particularly limited, but it is directly on the aromatic ring in the aromatic compound.
- the amount is usually 0.1 to 100 mol, preferably 0.2 to 50 mol, more preferably 0.3 to 10 mol, particularly preferably 0.3 to 1.1 mol, per 1 mol of bonded carbon atoms. .
- reaction time and reaction temperature of this reaction are not particularly limited, but the reaction time is usually in the range of 1 minute to 10 days, preferably 1 minute to 5 days, and the reaction temperature is usually in the range of ⁇ 50 ° C. to 100 ° C. It is.
- an organic alkali metal compound when it is reacted with an aromatic compound having 3 or more carbon atoms bonded directly to an aromatic ring in one molecule, it has a coordination ability to an alkali metal atom for the purpose of accelerating the reaction.
- a compound may coexist.
- a Lewis base compound containing a hetero atom is preferably used, and among these, a Lewis base compound containing a nitrogen atom or an oxygen atom is particularly preferably used. .
- Lewis base compounds containing nitrogen or oxygen atoms include chain ether compounds such as diethyl ether, anisole, diphenyl ether, dimethoxybenzene, dimethoxyethane, diglyme and ethylene glycol dibutyl ether; intramolecular such as trimethylamine and triethylamine Tertiary amine compounds having one nitrogen atom in them; Cyclic ether compounds having one oxygen atom in the molecule such as tetrahydrofuran and tetrahydropyran; Nitrogen-containing heterocyclic compounds such as pyridine, lutidine and 1-methylimidazole; Bistetrahydro Cyclic ether compounds having two or more oxygen atoms in the molecule such as furylpropane; N, N, N ′, N′-tetramethylethylenediamine, dipiperidinoethane, 1,4-diazabicyclo [2.2.2 Tertiary amine compounds having two or more nitrogen atoms in the molecule such as
- the amount of the compound having the coordination ability to the alkali metal atom is not particularly limited, and may be determined according to the strength of the coordination ability.
- a compound having a coordination ability to an alkali metal atom a chain ether compound that is a relatively weak coordination ability or a tertiary amine compound having one nitrogen atom in the molecule is used.
- the amount used is usually in the range of 1 to 100 mol, preferably 5 to 50 mol, more preferably 10 to 25 mol, per mol of the alkali metal atom in the organic alkali metal compound to be reacted with the aromatic compound. .
- a cyclic ether compound or nitrogen-containing heterocyclic compound having one oxygen atom in the molecule as a compound having a coordination ability to an alkali metal atom
- the amount used is usually in the range of 1 to 100 moles, preferably 1 to 20 moles, more preferably 2 to 10 moles per mole of alkali metal atoms in the organic alkali metal compound to be reacted with the aromatic compound.
- a compound having a coordination ability to an alkali metal atom a compound having a relatively strong coordination ability, a cyclic ether compound having two or more oxygen atoms in the molecule, or two or more nitrogen atoms in the molecule
- the amount used is 1 mol of an alkali metal atom in an organic alkali metal compound to be reacted with an aromatic compound. In general, the range is 0.01 to 5 mol, preferably 0.01 to 2 mol, more preferably 0.01 to 1.5 mol.
- the reaction may not proceed.
- the compound which has the coordination ability to these alkali metal atoms may be used individually by 1 type, and may be used in combination of 2 or more type.
- the compound having a coordination ability to an alkali metal atom is a cyclic ether compound having two or more oxygen atoms in the molecule, or a tertiary amine compound having two or more nitrogen atoms in the molecule.
- the order of addition is not particularly limited.
- a compound capable of coordinating to the alkali metal atom is added to the system.
- the order in which the organic alkali metal compound is added to the system after the coexistence of the aromatic compound and the compound having the ability to coordinate to the alkali metal atom is preferred.
- the alkali metalated aromatic compound obtained in the above manner and having 3 or more carbon atoms directly bonded to the alkali metal atom and the aromatic ring in one molecule Is used as a polymerization initiator to polymerize a monomer comprising at least a conjugated diene compound, thereby obtaining a conjugated diene rubber having an active terminal.
- the conjugated diene compound is not particularly limited.
- 1,3-butadiene, isoprene or 1,3-pentadiene is preferable, and 1,3-butadiene and isoprene are particularly preferable.
- these conjugated diene compounds may be used individually by 1 type, and may be used in combination of 2 or more type.
- the conjugated diene rubber having an active end is preferably obtained by copolymerizing a monomer containing an aromatic vinyl compound in addition to the conjugated diene compound.
- the aromatic vinyl compound is not particularly limited, and for example, styrene, ⁇ -methylstyrene, 2-methylstyrene, 3-methylstyrene, 4-methylstyrene, 2-ethylstyrene, 3-ethylstyrene, 4-ethylstyrene 2,4-diisopropylstyrene, 2,4-dimethylstyrene, 4-t-butylstyrene, 5-t-butyl-2-methylstyrene, vinylnaphthalene, dimethylaminomethylstyrene, dimethylaminoethylstyrene, and the like.
- the conjugated diene rubber having an active terminal used in the present invention preferably contains 50 to 100% by weight of a conjugated diene monomer unit, particularly preferably contains 55 to 95% by weight, and an aromatic vinyl monomer. Those containing 50 to 0% by weight of monomer units are preferred, and those containing 45 to 5% by weight are particularly preferred.
- the conjugated diene rubber having an active end is optionally added to the conjugated diene compound and the aromatic vinyl compound in addition to the conjugated diene compound and aromatic vinyl compound as long as the object of the present invention is not impaired. It may be formed by copolymerizing a monomer containing a monomer.
- Examples of other monomers include ⁇ , ⁇ -unsaturated nitriles such as acrylonitrile and methacrylonitrile; unsaturated carboxylic acids or acid anhydrides such as acrylic acid, methacrylic acid, and maleic anhydride; methyl methacrylate, acrylic Unsaturated carboxylic acid esters such as ethyl acrylate and butyl acrylate; Non-conjugated dienes such as 1,5-hexadiene, 1,6-heptadiene, 1,7-octadiene, dicyclopentadiene, 5-ethylidene-2-norbornene; etc. Can be mentioned. These monomers are preferably 10% by weight or less, more preferably 5% by weight or less as monomer units in the conjugated diene rubber having an active end.
- the mode of copolymerization is not particularly limited, and any of random, block, and tapered shapes may be used. Although it is good, a random binding mode is preferable. By making it random, the resulting rubber cross-linked product is excellent in low heat build-up.
- the use ratio of the alkali metalated aromatic compound and the monomer used as the polymerization initiator to the molecular weight of the target polymer since the polymerization reaction usually proceeds with living properties, the use ratio of the alkali metalated aromatic compound and the monomer used as the polymerization initiator to the molecular weight of the target polymer.
- the amount of alkali metal in the alkali metalated aromatic compound relative to 1 mol of the monomer is usually 0.000001 to 0.1 mol, preferably 0.00001 to 0.05 mol, Particularly preferably, it is selected in the range of 0.0001 to 0.01 mol. If the amount of the alkali metalated aromatic compound used is too small, the molecular weight of the resulting conjugated diene rubber will be too high, making it difficult to handle, and the polymerization reaction may not proceed sufficiently. On the other hand, if the amount of the alkali metalated aromatic compound used is too large, the molecular weight of the resulting conjugated diene rubber will be too low, and the rubber material
- a compound having the ability to coordinate to the alkali metal atom as described above is added to the polymerization reaction system for the purpose of controlling the polymerization rate and the microstructure of the resulting conjugated diene rubber. May be.
- the amount of the compound having a coordination ability to the alkali metal atom is usually 5 mol or less, preferably 4 mol, per 1 mol of the alkali metal atom in the alkali metalated aromatic compound used as the polymerization initiator. Hereinafter, it is particularly preferably 2 mol or less. If the amount of the compound having coordination ability to these alkali metal atoms is too large, the polymerization reaction may be inhibited.
- the solution containing the compound when preparing the alkali metalated aromatic compound used as a polymerization initiator, when using the compound which has the coordination ability to an alkali metal atom, the solution containing the compound can also be used as it is.
- the obtained rubber cross-linked product can be excellent in low heat build-up, a cyclic ether compound having two or more oxygen atoms in the molecule, and a tertiary class having two or more nitrogen atoms in the molecule.
- an alkali metal compound using at least one compound selected from an amine compound and a tertiary amide compound having a nitrogen-heteroatom bond in the molecule as a polymerization initiator (the alkali metal compound here is an alkali metalation compound) Not limited to aromatic compounds, present in the reaction system and includes all alkali metal compounds that act as polymerization initiators)) in the range of 0.02 to 3.0 moles per mole of alkali metal atoms It is preferable to make it. By doing in this way, the conjugated diene rubber
- a solution polymerization method is preferably used as the polymerization mode of the monomer containing the conjugated diene compound.
- the solvent used in the solution polymerization method is not particularly limited as long as it is inactive in the polymerization reaction and can dissolve the monomer and the polymerization catalyst.
- Specific examples of the solvent that can be used include aromatic hydrocarbons such as benzene, toluene, xylene, and ethylbenzene; aliphatic hydrocarbons such as n-hexane, n-heptane, and n-octane; cyclohexane, cyclopentane, and methylcyclohexane.
- ethers such as tetrahydrofuran, diethyl ether and cyclopentyl methyl ether;
- an aliphatic hydrocarbon or alicyclic hydrocarbon as a solvent because the polymerization activity becomes high.
- these solvents may be used individually by 1 type, and 2 or more types may be mixed and used for them.
- the concentration of the monomer in the polymerization solution in the solution polymerization method is not particularly limited, but is usually selected in the range of 1 to 50% by weight, preferably 2 to 45% by weight, more preferably 5 to 40% by weight. If the concentration of the monomer in the solution is too low, the productivity of the conjugated diene rubber may be deteriorated. If the concentration is too high, the viscosity of the solution may become too high and handling thereof may be difficult. is there.
- the polymerization temperature is not particularly limited, but is usually in the range of ⁇ 30 ° C. to + 200 ° C., preferably 0 ° C. to + 180 ° C.
- the polymerization time is not particularly limited, and is usually in the range of 1 minute to 100 hours.
- any of batch mode and continuous mode can be adopted.
- a conjugated diene monomer unit and an aromatic vinyl monomer unit are used.
- the batch method is preferable in that the randomness of the bond can be easily controlled.
- a conjugated diene rubber can be obtained by polymerizing a monomer containing a conjugated diene compound.
- the polymerization reaction usually proceeds with a living property, so that a polymer having an active end exists in the polymerization reaction system. Therefore, in the first step, the conjugated diene rubber obtained by the polymerization reaction has an active end.
- the compound represented by the general formula (5) described below is reacted with the active end of the conjugated diene rubber obtained by the polymerization reaction.
- a modified conjugated diene rubber is obtained.
- the conjugated diene rubber having an active end obtained in the first step in the production method of the present invention has a radial structure, a linear chain in which only one side of the polymer chain is an active end.
- the number of active ends in one molecule is large and can be efficiently modified, and as a result, the affinity with silica is further improved.
- it since it has a radial structure due to the polymerization initiator to be used, a multi-branched structure can be obtained without using a coupling agent.
- the 2nd process in the manufacturing method of the present invention is explained.
- the modified conjugated diene is produced by reacting the compound represented by the following general formula (5) with the active terminal of the conjugated diene rubber obtained in the first step.
- This is a process for obtaining a rubber.
- X reacts with an atom or a reactive group capable of reacting with the active end of the conjugated diene rubber having the active end, or with an active end of the conjugated diene rubber having the active end.
- Each of R 1 to R 4 is independently a chemical single bond or an alkylene group having 1 to 10 carbon atoms
- R 5 to R 10 are each independently an alkyl group having 1 to 10 carbon atoms or an aryl group having 6 to 12 carbon atoms
- R 5 to R 10 are a combination of R 5 and R 6 , R 7 And R 8 or a combination of R 9 and R 10 may be bonded to each other to form a ring structure together with the nitrogen atom.
- the conjugated diene rubber is modified by reacting the active terminal of the conjugated diene rubber with the compound represented by the general formula (5), so that it has an affinity for a filler such as silica.
- the modified conjugated diene rubber obtained can be excellent in processability and can give a rubber cross-linked product having low heat buildup and wear resistance.
- the atom or reactive group capable of reacting with the active terminus of the conjugated diene rubber is not particularly limited as long as it can react with the active terminus.
- a halogen atom, vinyl group, alkoxyl group, amino group or epoxy group is preferred, an epoxy group or halogen atom is more preferred, a halogen atom is further preferred, and a chlorine atom is particularly preferred.
- the hydrocarbon group containing any one of the atoms or the reactive groups is not particularly limited, but is preferably a hydrocarbon group having 1 to 10 carbon atoms. This carbon number does not include the number of carbons constituting the reactive group.
- R 1 to R 4 are each independently a chemical single bond or an alkylene group having 1 to 10 carbon atoms, preferably a chemical single bond or carbon number. It is particularly preferably a 1 to 5 alkylene group and a chemical single bond.
- R 5 to R 10 are each independently an alkyl group having 1 to 10 carbon atoms or an aryl group having 6 to 12 carbon atoms, and an alkyl group having 1 to 10 carbon atoms.
- Group more preferably an alkyl group having 1 to 5 carbon atoms, and particularly preferably a methyl group.
- X is a halogen atom
- R 1 to R 4 are all chemical single bonds.
- the usage-amount of the compound represented by the said General formula (5) is not specifically limited,
- gum per 1 mol of alkali metal atoms in the alkali metalated aromatic compound used as a polymerization initiator is used.
- the amount of atoms or reactive groups capable of reacting with is preferably 0.05 to 5 mol, more preferably 0.1 to 3 mol, more preferably 0.5 An amount of ⁇ 1.5 mol is particularly preferred.
- the usage-amount of the compound represented by the said General formula (5) may be used individually by 1 type, and may be used in combination of 2 or more type.
- the method of reacting the compound represented by the general formula (5) with the active terminal of the conjugated diene rubber obtained in the first step is not particularly limited.
- the solvent used in this case those exemplified as the solvent used for the polymerization of the conjugated diene rubber described above can be used.
- the conjugated diene rubber having an active end obtained in the first step described above is kept in the polymerization solution used for the polymerization, and is represented by the above general formula (5).
- the method of adding the compound is simple and preferable.
- the reaction temperature in the second step is not particularly limited, but is usually 0 to 120 ° C., and the reaction time is not particularly limited, but is usually 1 minute to 1 hour.
- An anti-aging agent such as a phenol-based stabilizer, a phosphorus-based stabilizer, or a sulfur-based stabilizer may be added to the modified conjugated diene rubber solution obtained as described above, if desired. What is necessary is just to determine suitably the addition amount of an anti-aging agent according to the kind etc.
- an extension oil may be blended to form an oil-extended rubber. Examples of extender oils include paraffinic, aromatic and naphthenic petroleum softeners, plant softeners, and fatty acids. When using a petroleum softener, it is preferable that the content of polycyclic aromatics extracted by the method of IP346 (the inspection method of THE INSTITUTE PETROLEUM in the UK) is less than 3%.
- the amount used is usually 5 to 100 parts by weight with respect to 100 parts by weight of the modified conjugated diene rubber.
- the modified conjugated diene rubber after the modification reaction can be obtained by removing the rubber from the solution by, for example, reprecipitation, solvent removal under heating, solvent removal under reduced pressure, or solvent removal by steam (steam stripping). It can be separated and obtained from the reaction mixture by a normal operation during separation.
- the conjugated diene compound when the conjugated diene compound is polymerized in the first step, 3 or more carbon atoms bonded directly to an alkali metal atom and an aromatic ring as a polymerization initiator in one molecule.
- the conjugated diene polymer chain is living-polymerizable with each of the carbon atoms directly bonded to three or more alkali metal atoms contained in the alkali metalated aromatic compound as the polymerization starting point. Therefore, the resulting conjugated diene rubber can have a radial structure.
- the compound represented by the general formula (5) is reacted with the active terminal of the conjugated diene rubber having such a radial structure, thereby forming the radial structure.
- a modified conjugated diene rubber having a terminal modified with the compound represented by the general formula (5) is reacted with the active terminal of the conjugated diene rubber having such a radial structure, thereby forming the radial structure.
- the modified conjugated diene rubber of the present invention thus obtained has a radial structure, and thus has an improved affinity with a filler and the like, and further modifies its active terminal.
- the compound represented by the general formula (5) as the modifier, it is possible to effectively prevent the occurrence of gelation (three-dimensional crosslinking) of the conjugated diene rubber during the modification reaction, As a result, workability can be improved.
- the modified conjugated diene rubber of the present invention is modified with the compound represented by the above general formula (5) because the active end thereof is modified with the compound represented by the above general formula (5). Can drastically improve the affinity with fillers, etc., which can further improve the low heat buildup and wear resistance when blended with silica and other fillers to make rubber cross-linked products. It is what.
- the ratio of the radial conjugated diene rubber (that is, the conjugated diene rubber having three or more branches) in the modified conjugated diene rubber obtained by the production method of the present invention is not particularly limited, but is usually 10 to 100 weights. %, Preferably 20 to 100% by weight.
- the processability of the modified conjugated diene rubber can be further improved, and the affinity with a filler such as silica can be further increased. .
- the weight average molecular weight of the modified conjugated diene rubber obtained by the production method of the present invention is not particularly limited, but is usually 1,000 to 3,000,000 as a value measured by gel permeation chromatography in terms of polystyrene.
- the range is preferably 10,000 to 2,000,000, more preferably 100,000 to 1,500,000.
- the molecular weight distribution represented by the ratio (Mw / Mn) of the weight average molecular weight (Mw) and the number average molecular weight (Mn) of the modified conjugated diene rubber obtained by the production method of the present invention is not particularly limited. Is 1.1 to 5.0, particularly preferably 1.2 to 3.0. By setting the molecular weight distribution of the modified conjugated diene rubber within the above range, the resulting rubber cross-linked product is excellent in low heat build-up.
- the Mooney viscosity (ML 1 + 4, 100 ° C.) of the modified conjugated diene rubber obtained by the production method of the present invention is not particularly limited, but is usually in the range of 20 to 150, preferably 30 to 120.
- the processability of the rubber composition becomes excellent.
- the modified conjugated diene rubber is an oil-extended rubber
- the Mooney viscosity of the oil-extended rubber is preferably in the above range.
- the vinyl bond content in the conjugated diene unit portion of the modified conjugated diene rubber obtained by the production method of the present invention is usually 1 to 80 mol%, preferably 5 to 75 mol%.
- the obtained rubber cross-linked product has excellent low heat build-up.
- the rubber composition of the present invention is a composition comprising 10 to 200 parts by weight of silica with respect to 100 parts by weight of a rubber component containing the modified conjugated diene rubber obtained by the production method of the present invention described above.
- silica used in the present invention examples include dry method white carbon, wet method white carbon, colloidal silica, and precipitated silica.
- wet method white carbon mainly containing hydrous silicic acid is preferable.
- a carbon-silica dual phase filler in which silica is supported on the carbon black surface may be used.
- These silicas can be used alone or in combination of two or more.
- nitrogen adsorption specific surface area of silica used is preferably 50 ⁇ 300m 2 / g, more preferably 80 ⁇ 220m 2 / g, particularly preferably 100 ⁇ 170m 2 / g.
- the pH of silica is preferably 5-10.
- the compounding amount of silica in the rubber composition of the present invention is 10 to 200 parts by weight, preferably 30 to 150 parts by weight, more preferably 50 to 100 parts by weight with respect to 100 parts by weight of the rubber component in the rubber composition. Part.
- the rubber composition of the present invention may further contain a silane coupling agent from the viewpoint of further improving the low heat build-up.
- a silane coupling agent examples include vinyltriethoxysilane, ⁇ - (3,4-epoxycyclohexyl) ethyltrimethoxysilane, N- ( ⁇ -aminoethyl) - ⁇ -aminopropyltrimethoxysilane, 3-octathio- 1-propyl-triethoxysilane, bis (3- (triethoxysilyl) propyl) disulfide, bis (3- (triethoxysilyl) propyl) tetrasulfide, ⁇ -trimethoxysilylpropyldimethylthiocarbamyl tetrasulfide, and ⁇ -Trimethoxysilylpropylbenzothiazyl tetrasulfide and the like.
- These silane coupling agents can be used alone
- the rubber composition of the present invention may further contain carbon black such as furnace black, acetylene black, thermal black, channel black, and graphite. Among these, furnace black is preferable. These carbon blacks can be used alone or in combination of two or more.
- the compounding amount of carbon black is usually 120 parts by weight or less with respect to 100 parts by weight of the rubber component in the rubber composition.
- the method of adding silica to the rubber component containing the modified conjugated diene rubber of the present invention is not particularly limited, and a method of adding and kneading a solid rubber component (dry kneading method) or a modified conjugated diene A method (wet kneading method) that is added to a solution containing a rubber and solidified and dried can be applied.
- the rubber composition of the present invention preferably further contains a cross-linking agent.
- the crosslinking agent include sulfur-containing compounds such as sulfur and sulfur halides, organic peroxides, quinone dioximes, organic polyvalent amine compounds, and alkylphenol resins having a methylol group. Among these, sulfur is preferably used.
- the amount of the crosslinking agent is preferably 0.1 to 15 parts by weight, more preferably 0.5 to 5 parts by weight, and particularly preferably 1 to 4 parts by weight with respect to 100 parts by weight of the rubber component in the rubber composition. It is.
- the rubber composition of the present invention includes a crosslinking accelerator, a crosslinking activator, an anti-aging agent, a filler (excluding silica and carbon black), an activator, and a process oil in accordance with conventional methods.
- a crosslinking accelerator excluding silica and carbon black
- a filler excluding silica and carbon black
- an activator excluding silica and carbon black
- a process oil in accordance with conventional methods.
- Plasticizers, lubricants, tackifiers and the like can be blended in the required amounts.
- crosslinking accelerator When sulfur or a sulfur-containing compound is used as the crosslinking agent, it is preferable to use a crosslinking accelerator and a crosslinking activator in combination.
- the crosslinking accelerator include sulfenamide-based crosslinking accelerators; guanidine-based crosslinking accelerators; thiourea-based crosslinking accelerators; thiazole-based crosslinking accelerators; thiuram-based crosslinking accelerators; dithiocarbamic acid-based crosslinking accelerators; A crosslinking accelerator; and the like. Among these, those containing a sulfenamide-based crosslinking accelerator are preferable. These crosslinking accelerators are used alone or in combination of two or more.
- the amount of the crosslinking accelerator is preferably 0.1 to 15 parts by weight, more preferably 0.5 to 5 parts by weight, and particularly preferably 1 to 4 parts by weight with respect to 100 parts by weight of the rubber component in the rubber composition. Part.
- crosslinking activator examples include higher fatty acids such as stearic acid; zinc oxide. These crosslinking activators are used alone or in combination of two or more.
- the amount of the crosslinking activator is preferably 0.05 to 20 parts by weight, particularly preferably 0.5 to 15 parts by weight based on 100 parts by weight of the rubber component in the rubber composition.
- the rubber composition of the present invention may be blended with other rubber other than the modified conjugated diene rubber obtained by the production method of the present invention described above.
- other rubbers include natural rubber, polyisoprene rubber, emulsion-polymerized styrene-butadiene copolymer rubber, solution-polymerized styrene-butadiene copolymer rubber, polybutadiene rubber (polybutadiene containing crystal fibers made of 1,2-polybutadiene polymer).
- Styrene-isoprene copolymer rubber butadiene-isoprene copolymer rubber, styrene-isoprene-butadiene copolymer rubber, acrylonitrile-butadiene copolymer rubber, acrylonitrile-styrene-butadiene copolymer rubber, and the like.
- natural rubber polyisoprene rubber, polybutadiene rubber, and solution-polymerized styrene-butadiene copolymer rubber are preferable. These rubbers can be used alone or in combination of two or more.
- the modified conjugated diene rubber obtained by the production method of the present invention preferably occupies 10 to 100% by weight, preferably 40 to 100% by weight of the rubber component in the rubber composition. Is particularly preferred.
- each component may be kneaded according to a conventional method.
- a component excluding a thermally unstable component such as a crosslinking agent or a crosslinking accelerator and a modified conjugated diene rubber are used.
- a heat-unstable component such as a crosslinking agent or a crosslinking accelerator can be mixed with the kneaded product to obtain a desired composition.
- the kneading temperature of the component excluding the thermally unstable component and the modified conjugated diene rubber is preferably 80 to 200 ° C., more preferably 120 to 180 ° C., and the kneading time is preferably 30 seconds to 30 minutes. It is.
- the kneaded product and the thermally unstable component are usually mixed after cooling to 100 ° C. or lower, preferably 80 ° C. or lower.
- the rubber cross-linked product of the present invention is obtained by cross-linking the rubber composition of the present invention described above.
- the rubber cross-linked product of the present invention uses the rubber composition of the present invention, for example, is molded by a molding machine corresponding to a desired shape, for example, an extruder, an injection molding machine, a compressor, a roll, and heated. Can be produced by carrying out a crosslinking reaction and fixing the shape as a crosslinked product.
- crosslinking may be performed after molding in advance, or crosslinking may be performed simultaneously with molding.
- the molding temperature is usually 10 to 200 ° C, preferably 25 to 120 ° C.
- the crosslinking temperature is usually 100 to 200 ° C., preferably 130 to 190 ° C.
- the crosslinking time is usually 1 minute to 24 hours, preferably 2 minutes to 12 hours, particularly preferably 3 minutes to 6 hours. .
- a heating method a general method used for crosslinking of rubber such as press heating, steam heating, oven heating, hot air heating, etc. may be appropriately selected.
- the rubber cross-linked product of the present invention thus obtained is obtained by using the modified conjugated diene rubber obtained by the above-described production method of the present invention, and therefore is excellent in low heat buildup and wear resistance. is there.
- the modified conjugated diene rubber obtained by the production method of the present invention is obtained by using the compound represented by the above general formula (5) as a modifier, and therefore, the gelation by the addition of the modifier is not necessary. Therefore, when silica as a filler is added to the modified conjugated diene rubber, the dispersibility of the silica is not lowered due to the influence of the gel content.
- the rubber cross-linked product of the present invention obtained by using the modified conjugated diene rubber obtained by the production method of the present invention has a good dispersion of silica as a filler, resulting in low heat buildup and wear resistance. It is particularly excellent in properties.
- the rubber cross-linked product of the present invention makes use of such characteristics, for example, in tires, materials for each part of the tire such as cap tread, base tread, carcass, sidewall, bead part; hose, belt, mat, anti-proof It can be used in various applications such as vibration rubber and other various industrial article materials; resin impact resistance improvers; resin film buffers; shoe soles; rubber shoes; golf balls; In particular, since the rubber cross-linked product of the present invention is excellent in low heat buildup and wear resistance, it can be suitably used as a tire material, particularly a low fuel consumption tire material.
- the molecular weight of the rubber was determined as a molecular weight in terms of polystyrene by gel permeation chromatography. Specific measurement conditions were as follows. Measuring instrument: High-performance liquid chromatograph (trade name “HLC-8220” manufactured by Tosoh Corporation) Column: A product manufactured by Tosoh Corporation and having two trade names “GMH-HR-H” connected in series was used. Detector: differential refractometer (trade name “RI-8220” manufactured by Tosoh Corporation) Eluent: Tetrahydrofuran Column temperature: 40 ° C
- a disk-shaped test piece having an outer diameter of 50 mm, an inner diameter of 15 mm, and a thickness of 10 mm was measured with a load of 1 kgf and a slip ratio of 15% using an FPS abrasion tester manufactured by Ueshima Seisakusho. About this characteristic, it showed with the index
- the ratio (molar ratio) of unsubstituted product: 1 substituted product: 2 substituted product: 3 substituted product was determined to be 3: 3: 24: 70, and the methyl group lithio of 1,3,5-trimethylbenzene was obtained.
- the conversion rate is 87%, and the average number of lithium atoms introduced into one molecule of 1,3,5-trimethylbenzene is 2.49.
- Example 1 [Production of Modified Styrene Butadiene Rubber 1] In a nitrogen atmosphere, an autoclave was charged with 800 parts of cyclohexane, 94.8 parts of 1,3-butadiene, 25.2 parts of styrene, and 0.185 parts of tetramethylethylenediamine, and then the polymerization initiator obtained in Production Example 1 0.812 parts of a solution of 1 (lithiated 1,3,5-trimethylbenzene) (the amount of tetramethylethylenediamine present in the reaction system is sufficient for lithiation of 1,3,5-trimethylbenzene). Polymerization was started at 60 ° C., with 2.0 moles per mole of n-butyllithium used.
- the obtained modified styrene butadiene rubber 1 is an elution component (peak area ratio 15.2%) having an Mn of 164,000, an Mw of 207,000, and a molecular weight distribution (Mw / Mn) of 1.27 in GPC measurement.
- Elution component (peak area ratio 14.6%) with Mn of 381,000, Mw of 386,000, molecular weight distribution (Mw / Mn), and Mn of 741,000, Mw of 784,000, molecular weight Distribution (Mw / Mn) consists of an elution component (peak area ratio 70.2%) of 1.06.
- Mn is 443,000
- Mw is 638,000
- molecular weight distribution (Mw / Mn) is 1.44.
- the modified styrene butadiene rubber 1 had a styrene unit content of 21.8% and a vinyl bond content in the butadiene unit of 60.1 mol%. Further, when 1 H-NMR of this modified styrene butadiene rubber 1 was measured, it was confirmed that a tris (dimethylamino) silyl group was introduced. The gel weight fraction of this modified styrene butadiene rubber 1 was measured according to the method described above. The results are shown in Table 1.
- the kneaded product was cooled to room temperature and then kneaded again in a Brabender type mixer at 110 ° C. for 3 minutes, and then the kneaded product was discharged from the mixer. Next, with an open roll at 50 ° C., the obtained kneaded product, 1.54 parts of sulfur, N-cyclohexyl-2-benzothiazolylsulfenamide (trade name, manufactured by Ouchi Shinsei Chemical Co., Ltd.) as a crosslinking accelerator "Noxeller CZ-G") 1.32 parts and diphenylguanidine (trade name "Noxeller D", manufactured by Ouchi Shinsei Chemical Industry Co., Ltd.), also used as a crosslinking accelerator, are kneaded and then sheet-like rubber The composition was removed.
- the obtained rubber composition is press-crosslinked at 160 ° C. for 20 minutes to obtain a crosslinked rubber, and the obtained crosslinked rubber (test piece) is evaluated for wear resistance and low heat build-up. I did it.
- the results are shown in Table 1.
- Table 1 the evaluation results of wear resistance and low heat build-up were shown as ratios when the results of Comparative Example 1 described later were set to 100, respectively.
- Example 2 [Production of modified styrene butadiene rubber 2] The blending amount of tris (dimethylamino) chlorosilane as a modifier is changed from 0.157 parts to 0.079 parts (amount to be 0.5 moles relative to 1 mole of Li contained in the polymerization initiator 1). A modified styrene butadiene rubber 2 was produced in the same manner as in Example 1 except that. The obtained modified styrene butadiene rubber 2 is an elution component (peak area ratio 15.1%) having an Mn of 161,000, an Mw of 202,000, and a molecular weight distribution (Mw / Mn) of 1.25 in GPC measurement.
- elution component peak area ratio 15.1%
- the modified styrene butadiene rubber 2 had a styrene unit content of 21.7% and a vinyl bond content in the butadiene unit of 59.9 mol%. Further, when 1 H-NMR was measured for the modified styrene butadiene rubber 2, it was confirmed that a tris (dimethylamino) silyl group was introduced. The gel weight fraction of this modified styrene butadiene rubber 2 was measured according to the method described above. The results are shown in Table 1.
- Example 1 a rubber composition and a rubber cross-linked product were obtained in the same manner as in Example 1 except that the modified styrene butadiene rubber 2 obtained above was used in place of the modified styrene butadiene rubber 1.
- Example 1 Evaluation was performed in the same manner as above. The results are shown in Table 1.
- modified styrene butadiene rubber 3 As a modifier, instead of 0.157 part of tris (dimethylamino) chlorosilane, 0.487 part of tetramethoxysilane (amount to be 4.0 moles relative to 1 mole of Li contained in the polymerization initiator 1). A modified styrene butadiene rubber 3 was produced in the same manner as in Example 1 except that it was used. The obtained modified styrene butadiene rubber 3 as a whole had a Mn of 545,000, Mw of 1,004,000, and a molecular weight distribution (Mw / Mn) of 1.84 in GPC measurement.
- the modified styrene butadiene rubber 3 had a styrene unit content of 21.7% and a vinyl bond content in the butadiene unit of 59.8 mol%. And about this modified styrene butadiene rubber 3, according to the above-mentioned method, the gel weight fraction was measured. The results are shown in Table 1.
- Example 1 a rubber composition and a rubber cross-linked product were obtained in the same manner as in Example 1 except that the modified styrene butadiene rubber 3 obtained above was used in place of the modified styrene butadiene rubber 1.
- Example 1 Evaluation was performed in the same manner as above. The results are shown in Table 1.
- the modified styrene butadiene rubber 4 had a styrene unit content of 22.3% and a vinyl bond content in the butadiene unit of 60.0 mol%. And about this modified styrene butadiene rubber 4, according to the above-mentioned method, the gel weight fraction was measured. The results are shown in Table 1.
- Example 1 a rubber composition and a rubber cross-linked product were obtained in the same manner as in Example 1 except that the modified styrene butadiene rubber 4 obtained above was used instead of the modified styrene butadiene rubber 1.
- Example 1 Evaluation was performed in the same manner as above. The results are shown in Table 1.
- the obtained modified styrene butadiene rubber 5 as a whole had a Mn of 437,000, Mw of 646,000, and molecular weight distribution (Mw / Mn) of 1.48 in GPC measurement.
- the modified styrene-butadiene rubber 5 had a styrene unit content of 22.3% and a vinyl bond content in the butadiene unit of 60.0 mol%.
- the gel weight fraction was measured. The results are shown in Table 1.
- Example 1 a rubber composition and a rubber cross-linked product were obtained in the same manner as in Example 1 except that the modified styrene butadiene rubber 5 obtained above was used instead of the modified styrene butadiene rubber 1.
- Example 1 Evaluation was performed in the same manner as above. The results are shown in Table 1.
- the obtained modified styrene butadiene rubber 6 had an overall Mn of 438,000, Mw of 626,000, and molecular weight distribution (Mw / Mn) of 1.43 in GPC measurement.
- the modified styrene butadiene rubber 6 had a styrene unit content of 21.5% and a vinyl bond content in the butadiene unit of 59.6 mol%.
- the gel weight fraction was measured. The results are shown in Table 1.
- Example 1 a rubber composition and a rubber cross-linked product were obtained in the same manner as in Example 1 except that the modified styrene butadiene rubber 6 obtained above was used in place of the modified styrene butadiene rubber 1.
- Example 1 Evaluation was performed in the same manner as above. The results are shown in Table 1.
- the obtained modified styrene butadiene rubber 7 had a Mn of 295,000, a Mw of 312,000, and a molecular weight distribution (Mw / Mn) of 1.06 in GPC measurement.
- the modified styrene butadiene rubber 7 had a styrene unit content of 21.1% and a vinyl bond content in the butadiene unit of 59.8 mol%.
- 1 H-NMR was measured for the modified styrene butadiene rubber 7, it was confirmed that a tris (dimethylamino) silyl group was introduced.
- the gel weight fraction was measured according to the method described above. The results are shown in Table 1.
- Example 1 a rubber composition and a rubber cross-linked product were obtained in the same manner as in Example 1 except that the modified styrene butadiene rubber 7 obtained above was used in place of the modified styrene butadiene rubber 1.
- Example 1 Evaluation was performed in the same manner as above. The results are shown in Table 1.
- an alkali metalated aromatic compound having 3 or more carbon atoms directly bonded to an alkali metal atom and an aromatic ring as a polymerization initiator is used, and the above general formula ( When the compound represented by 5) is used, the gel content of the modified conjugated diene rubber is not substantially contained, and the rubber cross-linked product obtained by using this has low heat build-up and resistance. It was excellent in abrasion (Examples 1 and 2).
- the resulting modified conjugated diene rubber contains a large amount of gel, is inferior in workability, and further, when a rubber cross-linked product is used.
- the results were inferior in low heat build-up and wear resistance (Comparative Example 1).
- the resulting modified conjugated diene rubber had a low gel content, but was a crosslinked rubber product. In this case, the results were inferior in low heat generation and wear resistance (Comparative Examples 2 and 3).
- the resulting modified conjugated diene rubber contains a large amount of gel, is inferior in processability, and is a crosslinked rubber product. In such a case, the result was inferior to the low exothermic property (Comparative Example 4).
- the resulting modified conjugated diene rubber does not substantially contain a gel component. The results were inferior in heat generation and wear resistance, and in particular, inferior in low heat generation (Comparative Example 5).
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Abstract
Description
本発明の製造方法においては、前記アルカリ金属化芳香族化合物が、芳香環に直接結合した炭素原子を1分子中に3個以上有する芳香族化合物に、有機アルカリ金属化合物を反応させて得られたものであることが好ましい。
本発明の製造方法においては、前記芳香環に直接結合した炭素原子を1分子中に3個以上有する芳香族化合物が、下記一般式(II)で表される芳香族化合物であることが好ましい。
本発明の製造方法においては、前記一般式(I)で表される化合物中における、Xが、ハロゲン原子であり、R1~R4が、化学的な単結合であり、R5~R10が、それぞれ独立して、炭素数1~5のアルキル基であることが好ましい。
本発明の製造方法においては、前記第2工程における、前記一般式(I)で表される化合物の使用量を、前記第1工程で用いた前記アルカリ金属化芳香族化合物中のアルカリ金属原子1モルに対し、前記共役ジエン系ゴムの活性末端と反応することができる原子または反応基の量が、0.05~5モルの範囲となる量とすることが好ましい。 In the production method of the present invention, in the first step, it is preferable to copolymerize a monomer containing an aromatic vinyl compound in addition to the conjugated diene compound.
In the production method of the present invention, the alkali metalated aromatic compound was obtained by reacting an organic alkali metal compound with an aromatic compound having 3 or more carbon atoms in one molecule directly bonded to an aromatic ring. It is preferable.
In the production method of the present invention, the aromatic compound having 3 or more carbon atoms directly bonded to the aromatic ring in one molecule is preferably an aromatic compound represented by the following general formula (II).
In the production method of the present invention, in the compound represented by the general formula (I), X is a halogen atom, R 1 to R 4 are chemical single bonds, and R 5 to R 10. Are preferably each independently an alkyl group having 1 to 5 carbon atoms.
In the production method of the present invention, the amount of the compound represented by the general formula (I) used in the second step is the alkali metal atom 1 in the alkali metalated aromatic compound used in the first step. The amount of atoms or reactive groups capable of reacting with the active terminal of the conjugated diene rubber is preferably in an amount in the range of 0.05 to 5 moles relative to moles.
さらに、本発明によれば、上記変性共役ジエン系ゴムを含むゴム成分100重量部に対して、シリカ10~200重量部を含有してなるゴム組成物が提供される。
本発明のゴム組成物は、架橋剤をさらに含有してなるものであることが好ましい。 The present invention also provides a modified conjugated diene rubber obtained by any one of the above production methods.
Furthermore, according to the present invention, there is provided a rubber composition comprising 10 to 200 parts by weight of silica with respect to 100 parts by weight of a rubber component containing the modified conjugated diene rubber.
The rubber composition of the present invention preferably contains a crosslinking agent.
本発明の変性共役ジエン系ゴムの製造方法は、重合開始剤として、アルカリ金属原子および芳香環に、直接結合した炭素原子を1分子中に3個以上有するアルカリ金属化芳香族化合物を用いて、少なくとも共役ジエン化合物を含んでなる単量体を重合し、活性末端を有する共役ジエン系ゴムを得る第1工程と、前記活性末端を有する共役ジエン系ゴムの活性末端に、後述する一般式(5)で表される化合物を反応させる第2工程と、を備える。 <Method for producing modified conjugated diene rubber>
The method for producing a modified conjugated diene rubber of the present invention uses, as a polymerization initiator, an alkali metalated aromatic compound having 3 or more carbon atoms directly bonded to an alkali metal atom and an aromatic ring in one molecule, A first step of polymerizing a monomer comprising at least a conjugated diene compound to obtain a conjugated diene rubber having an active end, and a general formula (5) described later at the active end of the conjugated diene rubber having an active end. And a second step of reacting the compound represented by:
まず、本発明の製造方法における、第1工程について説明する。本発明の製造方法における、第1工程は、重合開始剤として、アルカリ金属原子および芳香環に、直接結合した炭素原子を1分子中に3個以上有するアルカリ金属化芳香族化合物を用いて、少なくとも共役ジエン化合物を含んでなる単量体を重合し、活性末端を有する共役ジエン系ゴムを得る工程である。 <First step>
First, the 1st process in the manufacturing method of this invention is demonstrated. In the production method of the present invention, the first step uses at least an alkali metalated aromatic compound having 3 or more carbon atoms directly bonded to an alkali metal atom and an aromatic ring in one molecule as a polymerization initiator. This is a step of polymerizing a monomer comprising a conjugated diene compound to obtain a conjugated diene rubber having an active end.
なお、本発明で用いるアルカリ金属化芳香族化合物においては、前記アルカリ金属原子は、アルカリ金属化芳香族化合物内において、通常、カチオンの状態で存在しており、また、アルカリ金属原子と芳香環とのそれぞれに直接結合する炭素原子は、このようなカチオンの状態のアルカリ金属原子と結合するために、通常、アニオンの状態で存在している。そして、本発明で用いるアルカリ金属化芳香族化合物中においては、このようにカチオンの状態で存在するアルカリ金属原子と、アニオンの状態で存在する炭素原子とがイオン結合を形成し、これにより互いに直接結合した状態となっている。 The polymerization initiator used in the first step of the production method of the present invention is an alkali metalated aromatic compound having 3 or more carbon atoms directly bonded to each of an alkali metal atom and an aromatic ring in one molecule. The alkali metal atom of the alkali metalated aromatic compound used as a polymerization initiator in the present invention is not particularly limited, but is preferably lithium, sodium, or potassium, and among these, lithium is Particularly preferred. The aromatic ring of the alkali metalated aromatic compound is not particularly limited as long as it is a conjugated ring having aromaticity, and specific examples include electrically neutral such as a benzene ring, a naphthalene ring, and an anthracene ring. An aromatic hydrocarbon ring; an aromatic hydrocarbon ring having a negative charge such as a cyclopentadienyl anion ring, an indenyl anion ring or a fluorenyl anion ring; an aromatic ring containing a heteroatom such as a furan ring or a thiophene ring; And so on. Among these, an electrically neutral aromatic hydrocarbon ring is preferable, and a benzene ring is particularly preferable. An alkali metalated aromatic compound having an electrically neutral aromatic hydrocarbon ring is preferably used from the viewpoint of its stability and polymerization activity.
In the alkali metalated aromatic compound used in the present invention, the alkali metal atom is usually present in a cation state in the alkali metalated aromatic compound, and the alkali metal atom and the aromatic ring The carbon atom directly bonded to each of the carbon atoms is usually present in an anionic state in order to bind to the alkali metal atom in such a cation state. In the alkali metalated aromatic compound used in the present invention, the alkali metal atom thus present in the cation state and the carbon atom present in the anion state form an ionic bond, thereby directly connecting each other. It is in a combined state.
以下、本発明の製造方法における、第2工程について説明する。 As described above, a conjugated diene rubber can be obtained by polymerizing a monomer containing a conjugated diene compound. In the production method of the present invention, the polymerization reaction usually proceeds with a living property, so that a polymer having an active end exists in the polymerization reaction system. Therefore, in the first step, the conjugated diene rubber obtained by the polymerization reaction has an active end. In contrast, in the production method of the present invention, in the second step described later, the compound represented by the general formula (5) described below is reacted with the active end of the conjugated diene rubber obtained by the polymerization reaction. Thus, a modified conjugated diene rubber is obtained. In particular, since the conjugated diene rubber having an active end obtained in the first step in the production method of the present invention has a radial structure, a linear chain in which only one side of the polymer chain is an active end. Compared with the conjugated diene rubber, the number of active ends in one molecule is large and can be efficiently modified, and as a result, the affinity with silica is further improved. Moreover, since it has a radial structure due to the polymerization initiator to be used, a multi-branched structure can be obtained without using a coupling agent.
Hereinafter, the 2nd process in the manufacturing method of the present invention is explained.
本発明の製造方法における、第2工程は、上述した第1工程で得られた共役ジエン系ゴムの活性末端に、下記一般式(5)で表される化合物を反応させることにより、変性共役ジエン系ゴムを得る工程である。
In the second step of the production method of the present invention, the modified conjugated diene is produced by reacting the compound represented by the following general formula (5) with the active terminal of the conjugated diene rubber obtained in the first step. This is a process for obtaining a rubber.
本発明のゴム組成物は、上述した本発明の製造方法により得られる変性共役ジエン系ゴムを含むゴム成分100重量部に対して、シリカ10~200重量部を含有してなる組成物である。 <Rubber composition>
The rubber composition of the present invention is a composition comprising 10 to 200 parts by weight of silica with respect to 100 parts by weight of a rubber component containing the modified conjugated diene rubber obtained by the production method of the present invention described above.
本発明のゴム架橋物は、上述した本発明のゴム組成物を架橋してなるものである。
本発明のゴム架橋物は、本発明のゴム組成物を用い、たとえば、所望の形状に対応した成形機、たとえば、押出機、射出成形機、圧縮機、ロールなどにより成形を行い、加熱することにより架橋反応を行い、架橋物として形状を固定化することにより製造することができる。この場合においては、予め成形した後に架橋しても、成形と同時に架橋を行ってもよい。成形温度は、通常、10~200℃、好ましくは25~120℃である。架橋温度は、通常、100~200℃、好ましくは130~190℃であり、架橋時間は、通常、1分~24時間、好ましくは2分~12時間、特に好ましくは3分~6時間である。 <Rubber cross-linked product>
The rubber cross-linked product of the present invention is obtained by cross-linking the rubber composition of the present invention described above.
The rubber cross-linked product of the present invention uses the rubber composition of the present invention, for example, is molded by a molding machine corresponding to a desired shape, for example, an extruder, an injection molding machine, a compressor, a roll, and heated. Can be produced by carrying out a crosslinking reaction and fixing the shape as a crosslinked product. In this case, crosslinking may be performed after molding in advance, or crosslinking may be performed simultaneously with molding. The molding temperature is usually 10 to 200 ° C, preferably 25 to 120 ° C. The crosslinking temperature is usually 100 to 200 ° C., preferably 130 to 190 ° C., and the crosslinking time is usually 1 minute to 24 hours, preferably 2 minutes to 12 hours, particularly preferably 3 minutes to 6 hours. .
ゴムの分子量は、ゲルパーミエーションクロマトグラフィによりポリスチレン換算分子量として求めた。具体的な測定条件は、以下のとおりとした。
測定器:高速液体クロマトグラフ(東ソー社製、商品名「HLC-8220」)
カラム:東ソー社製、商品名「GMH-HR-H」を二本直列に連結したものを用いた。
検出器:示差屈折計(東ソー社製、商品名「RI-8220」)
溶離液:テトラヒドロフラン
カラム温度:40℃ [Molecular weight of rubber]
The molecular weight of the rubber was determined as a molecular weight in terms of polystyrene by gel permeation chromatography. Specific measurement conditions were as follows.
Measuring instrument: High-performance liquid chromatograph (trade name “HLC-8220” manufactured by Tosoh Corporation)
Column: A product manufactured by Tosoh Corporation and having two trade names “GMH-HR-H” connected in series was used.
Detector: differential refractometer (trade name “RI-8220” manufactured by Tosoh Corporation)
Eluent: Tetrahydrofuran Column temperature: 40 ° C
ゴムの分岐度は、多角度光散乱光度計により測定した。具体的な測定条件は、以下のとおりとした。
ポンプ:Waters社製、商品名「MODEL515」
カラム:東ソー社製、商品名「GMH-HR-M」を三本直列に連結したものを用いた。
検出器:示差屈折計(Waters社製、商品名「RI-2414」)
検出器:多角度光散乱光度計(Wyatt Technology社製、商品名「DAWN EOS」)
溶離液:テトラヒドロフラン
カラム温度:23℃ [Branch degree of rubber]
The degree of branching of the rubber was measured with a multi-angle light scattering photometer. Specific measurement conditions were as follows.
Pump: Waters, trade name “MODEL515”
Column: A product manufactured by Tosoh Corporation and having three trade names “GMH-HR-M” connected in series was used.
Detector: Differential refractometer (manufactured by Waters, trade name “RI-2414”)
Detector: Multi-angle light scattering photometer (manufactured by Wyatt Technology, trade name “DAWN EOS”)
Eluent: Tetrahydrofuran Column temperature: 23 ° C
1H-NMRにより測定した。
測定器:JEOL社製、商品名「JNM-ECA-400WB」
測定溶媒:重クロロホルム [Rubber microstructure, rubber modification]
It was measured by 1 H-NMR.
Measuring instrument: Product name “JNM-ECA-400WB” manufactured by JEOL
Measuring solvent: deuterated chloroform
GC-MSにより測定した。
GC:アジレント・テクノロジー社製、商品名「Agilent GC 6890NGC」
MS:アジレント・テクノロジー社製、商品名「Agilent MS 5973MSD」
カラム:アジレント・テクノロジー社製、商品名「DB1701」 [Lithiation rate of polymerization initiator]
Measured by GC-MS.
GC: Product name “Agilent GC 6890NGC” manufactured by Agilent Technologies
MS: Product name “Agilent MS 5973MSD” manufactured by Agilent Technologies
Column: Product name “DB1701” manufactured by Agilent Technologies
#100メッシュカゴにゴム(重量:Wa[g])を1mm角程度に裁断して入れ、トルエン中に室温(25℃)で24時間浸漬し、引き上げた。次いで、#100メッシュカゴに残ったゴムを真空乾燥して乾燥後の重量(Wb[g])を秤量した。そして、これらの秤量値から、ゲル重量分率を、トルエン不溶分=(Wb/Wa)×100(%)により求めた。なお、ゲル重量分率が低いほど、加工性に優れるものと判断することができる。 [Gel weight fraction]
A rubber (weight: Wa [g]) was cut into a # 100 mesh basket by cutting to about 1 mm square, immersed in toluene at room temperature (25 ° C.) for 24 hours, and then pulled up. Next, the rubber remaining in the # 100 mesh basket was vacuum-dried, and the weight after drying (Wb [g]) was weighed. And the gel weight fraction was calculated | required from these weighed values by toluene insoluble content = (Wb / Wa) x100 (%). In addition, it can be judged that it is excellent in workability, so that a gel weight fraction is low.
長さ50mm、幅12.7mm、厚さ2mmのシート状の試験片について、粘弾性測定装置(レオメトリックス社製、製品名「ARES」)を用い、動的歪み2.5%、周波数10Hzの条件で60℃におけるtanδを測定した。この特性については、比較例1の測定値を100とする指数で示した。この指数が小さいものほど、低発熱性に優れる。 [Low heat generation]
For a sheet-like test piece having a length of 50 mm, a width of 12.7 mm, and a thickness of 2 mm, a viscoelasticity measuring device (manufactured by Rheometrics, product name “ARES”) is used, and the dynamic strain is 2.5% and the frequency is 10 Hz. Under the conditions, tan δ at 60 ° C. was measured. About this characteristic, it showed with the index | exponent which sets the measured value of the comparative example 1 to 100. The smaller this index, the better the low heat buildup.
外径50mm、内径15mm、厚さ10mmの円盤状の試験片について、上島製作所社製FPS摩耗試験機を用い、荷重1kgf、スリップ率15%で測定した。この特性については、比較例1の測定値を100とする指数で示した。この指数が大きいものほど、耐摩耗性に優れる。 (Abrasion resistance)
A disk-shaped test piece having an outer diameter of 50 mm, an inner diameter of 15 mm, and a thickness of 10 mm was measured with a load of 1 kgf and a slip ratio of 15% using an FPS abrasion tester manufactured by Ueshima Seisakusho. About this characteristic, it showed with the index | exponent which sets the measured value of the comparative example 1 to 100. The larger this index, the better the wear resistance.
窒素雰囲気下、ガラス反応容器に、シクロヘキサン16部、1,3,5-トリメチルベンゼン0.841部、およびテトラメチルエチレンジアミン0.813部を加えた。次に攪拌しながら、n-ブチルリチウム1.345部(n-ブチルリチウム1モル当たり前記テトラメチルエチレンジアミン0.3モルとなる)を加え、反応温度60℃にて2日間攪拌しながら反応させ、重合開始剤1の溶液(リチオ化された1,3,5-トリメチルベンゼン)18.999部を得た。次に、反応により得られたリチオ化された1,3,5-トリメチルベンゼンのリチオ化率を測定する目的で、トリメチルシリルクロライドを過剰量加えたガラス容器に、得られた反応液を数滴加え、30分間反応させた。水道水にて触媒残渣を抽出洗浄した後に溶媒を留去することで、黄色いオイル状の液体を得た。 [Production Example 1: Production of polymerization initiator 1 (lithiation of 1,3,5-trimethylbenzene)]
Under a nitrogen atmosphere, 16 parts of cyclohexane, 0.841 parts of 1,3,5-trimethylbenzene, and 0.813 parts of tetramethylethylenediamine were added to a glass reaction vessel. Next, 1.345 parts of n-butyllithium (0.3 mol of tetramethylethylenediamine per 1 mol of n-butyllithium) was added with stirring, and the reaction was conducted with stirring at a reaction temperature of 60 ° C. for 2 days. 18.999 parts of a solution of polymerization initiator 1 (lithiated 1,3,5-trimethylbenzene) were obtained. Next, for the purpose of measuring the lithiation rate of the lithiated 1,3,5-trimethylbenzene obtained by the reaction, add a few drops of the obtained reaction solution to a glass container to which an excess amount of trimethylsilyl chloride was added. , Reacted for 30 minutes. The catalyst residue was extracted and washed with tap water, and then the solvent was distilled off to obtain a yellow oily liquid.
EI-MS,m/z=120(M+)(3%),m/z=192(M+)(3%),m/z=264(M+)(24%),m/z=336(M+)(70%)。Mw=120(3%)、Mw=192(3%)、Mw=264(24%)、Mw=336(70%)。 The yellow oily liquid was subjected to gas chromatograph mass spectrometry (GC-MS). The results were as follows.
EI-MS, m / z = 120 (M +) (3%), m / z = 192 (M +) (3%), m / z = 264 (M +) (24%), m / z = 336 (M + ) (70%). Mw = 120 (3%), Mw = 192 (3%), Mw = 264 (24%), Mw = 336 (70%).
1H-NMR(CDCl3) 6.83(s,3H,Ph-H),6.73(s,1H,Ph-H),6.64(s,2H,Ph-H),6.55(s,2H,Ph-H),6.47(s,1H,Ph-H),6.39(s,3H,Ph-H),2.30(s,9H,Ph-CH3),2.28(s,6H,Ph-CH3),2.02(s,2H,Ph-CH2-SiMe3),2.26(s,3H,Ph-CH3),2.00(s,4H,Ph-CH2-SiMe3),1.98(s,6H,Ph-CH2-SiMe3)。 Next, 1 H-NMR measurement was performed on this yellow oily liquid. The results were as follows.
1 H-NMR (CDCl 3 ) 6.83 (s, 3H, Ph—H), 6.73 (s, 1H, Ph—H), 6.64 (s, 2H, Ph—H), 6.55 (S, 2H, Ph-H), 6.47 (s, 1H, Ph-H), 6.39 (s, 3H, Ph-H), 2.30 (s, 9H, Ph-CH 3 ), 2.28 (s, 6H, Ph—CH 3 ), 2.02 (s, 2H, Ph—CH 2 —SiMe 3 ), 2.26 (s, 3H, Ph—CH 3 ), 2.00 (s , 4H, Ph—CH 2 —SiMe 3 ), 1.98 (s, 6H, Ph—CH 2 —SiMe 3 ).
無置換体(1,3,5-トリメチルベンゼン)1H-NMR(CDCl3):6.83(s,3H,Ph-H),2.30(s,9H,Ph-CH3)、1置換体(1-トリメチルシリルメチル-3,5-ジメチルベンゼン)1H-NMR(CDCl3):6.73(s,1H,Ph-H),6.64(s,2H,Ph-H),2.28(s,6H,Ph-CH3),2.02(s,2H,Ph-CH2-SiMe3)、2置換体(1,3-ビス(トリメチルシリルメチル)-5-メチルベンゼン)1H-NMR(CDCl3):6.55(s,2H,Ph-H),6.47(s,1H,Ph-H),2.26(s,3H,Ph-CH3),2.00(s,4H,Ph-CH2-SiMe3)、3置換体(1,3,5-トリス(トリメチルシリルメチル)ベンゼン)1H-NMR(CDCl3):6.39(s,3H,Ph-H),1.98(s,6H,Ph-CH2-SiMe3)。 Further, each signal in 1 H-NMR was assigned by 1 H-detected multi-bond heteronuclear multiple quantum coherence spectrum-NMR (HMBC-NMR) measurement. The results were as follows.
Unsubstituted product (1,3,5-trimethylbenzene) 1 H-NMR (CDCl 3 ): 6.83 (s, 3H, Ph—H), 2.30 (s, 9H, Ph—CH 3 ), 1 Substituted substance (1-trimethylsilylmethyl-3,5-dimethylbenzene) 1 H-NMR (CDCl 3 ): 6.73 (s, 1H, Ph—H), 6.64 (s, 2H, Ph—H), 2.28 (s, 6H, Ph—CH 3 ), 2.02 (s, 2H, Ph—CH 2 —SiMe 3 ), disubstituted (1,3-bis (trimethylsilylmethyl) -5-methylbenzene) 1 H-NMR (CDCl 3 ): 6.55 (s, 2H, Ph—H), 6.47 (s, 1H, Ph—H), 2.26 (s, 3H, Ph—CH 3 ), 2 .00 (s, 4H, Ph- CH 2 -SiMe 3), 3 -substituted bodies (1,3,5-tris Trimethylsilylmethyl) benzene) 1 H-NMR (CDCl 3 ): 6.39 (s, 3H, Ph-H), 1.98 (s, 6H, Ph-CH 2 -SiMe 3).
〔変性スチレンブタジエンゴム1の製造〕
窒素雰囲気下、オートクレーブに、シクロヘキサン800部、1,3-ブタジエン94.8部、スチレン25.2部、およびテトラメチルエチレンジアミン0.185部を仕込んだ後、製造例1で得られた重合開始剤1の溶液(リチオ化された1,3,5-トリメチルベンゼン)0.812部を添加し(反応系中に存在するテトラメチルエチレンジアミンの量は、1,3,5-トリメチルベンゼンのリチオ化に用いたn-ブチルリチウム1モル当たり2.0モルである)、60℃で重合を開始した。60分間重合反応を継続し、重合転化率が95%~100%の範囲になったことを確認してから、変性剤としてのトリス(ジメチルアミノ)クロロシラン(上記一般式(5)において、X=Cl、R1~R4=化学的な単結合、R5~R10=CH3)0.157部(重合開始剤1中に含有されるLi1モルに対して、1.0モルとなる量)を添加し、30分間反応させた後、重合停止剤としてメタノール0.064部を添加して重合体を含有する溶液を得た。 [Example 1]
[Production of Modified Styrene Butadiene Rubber 1]
In a nitrogen atmosphere, an autoclave was charged with 800 parts of cyclohexane, 94.8 parts of 1,3-butadiene, 25.2 parts of styrene, and 0.185 parts of tetramethylethylenediamine, and then the polymerization initiator obtained in Production Example 1 0.812 parts of a solution of 1 (lithiated 1,3,5-trimethylbenzene) (the amount of tetramethylethylenediamine present in the reaction system is sufficient for lithiation of 1,3,5-trimethylbenzene). Polymerization was started at 60 ° C., with 2.0 moles per mole of n-butyllithium used. The polymerization reaction was continued for 60 minutes, and after confirming that the polymerization conversion was in the range of 95% to 100%, tris (dimethylamino) chlorosilane (in the general formula (5), X = Cl, R 1 to R 4 = chemical single bond, R 5 to R 10 = CH 3 ) 0.157 parts (amount that is 1.0 mol with respect to 1 mol of Li contained in the polymerization initiator 1) ) And reacted for 30 minutes, and then 0.064 part of methanol was added as a polymerization terminator to obtain a solution containing a polymer.
次に、容量250mlのブラベンダータイプミキサー中で、上記にて得られた変性スチレンブタジエンゴム1 100部を30秒素練りし、次いでシリカ(ローディア社製、商品名「Zeosil1115MP」)50部、プロセスオイル(新日本石油社製、商品名「アロマックス T-DAE」)20部、およびシランカップリング剤:ビス(3-(トリエトキシシリル)プロピル)テトラスルフィド(デグッサ社製、商品名「Si69」)6.0部を添加して、110℃を開始温度として1.5分間混練後、シリカ(ローディア社製、商品名「Zeosil1115MP」)25部、酸化亜鉛3部、ステアリン酸2部および老化防止剤としてのN-フェニル-N’-(1,3-ジメチルブチル)-p-フェニレンジアン(大内新興化学工業社製、商品名「ノクラック6C」)2部を添加し、さらに2.5分間混練し、ミキサーから混練物を排出させた。混練終了時の混練物の温度は150℃であった。そして、混練物を、室温まで冷却した後、再度ブラベンダータイプミキサー中で、110℃を開始温度として3分間混練した後、ミキサーから混練物を排出させた。次いで、50℃のオープンロールで、得られた混練物と、硫黄1.54部、架橋促進剤としてのN-シクロヘキシル-2-ベンゾチアゾリルスルフェンアミド(大内新興化学工業社製、商品名「ノクセラーCZ-G」)1.32部、および同じく架橋促進剤としてのジフェニルグアニジン(大内新興化学工業社製、商品名「ノクセラーD」)1.32部を混練した後、シート状のゴム組成物を取り出した。そして、得られたゴム組成物を、160℃で20分間プレス架橋することで、ゴム架橋物を得て、得られたゴム架橋物(試験片)について、耐摩耗性および低発熱性の評価を行なった。結果を表1に示す。なお、表1中においては、耐摩耗性および低発熱性の評価結果は、後述する比較例1の結果を、それぞれ100とした場合における比率で示した。 (Preparation of rubber composition)
Next, 100 parts of the modified styrene butadiene rubber 1 obtained above was masticated for 30 seconds in a Brabender type mixer having a capacity of 250 ml, and then 50 parts of silica (trade name “Zeosil 1115MP”, manufactured by Rhodia), 20 parts of oil (trade name “Aromax T-DAE” manufactured by Nippon Oil Corporation) and silane coupling agent: bis (3- (triethoxysilyl) propyl) tetrasulfide (trade name “Si69” manufactured by Degussa) ) After adding 6.0 parts and kneading at 110 ° C. for 1.5 minutes, 25 parts of silica (trade name “Zeosil 1115MP” manufactured by Rhodia), 3 parts of zinc oxide, 2 parts of stearic acid and anti-aging N-Phenyl-N '-(1,3-dimethylbutyl) -p-phenylenedian (Ouchi Shinsei Chemical Industry Co., Ltd.) , Was added trade name "Nocrac 6C") 2 parts, and further kneaded for 2.5 minutes to discharge the kneaded product from the mixer. The temperature of the kneaded product at the end of kneading was 150 ° C. The kneaded product was cooled to room temperature and then kneaded again in a Brabender type mixer at 110 ° C. for 3 minutes, and then the kneaded product was discharged from the mixer. Next, with an open roll at 50 ° C., the obtained kneaded product, 1.54 parts of sulfur, N-cyclohexyl-2-benzothiazolylsulfenamide (trade name, manufactured by Ouchi Shinsei Chemical Co., Ltd.) as a crosslinking accelerator "Noxeller CZ-G") 1.32 parts and diphenylguanidine (trade name "Noxeller D", manufactured by Ouchi Shinsei Chemical Industry Co., Ltd.), also used as a crosslinking accelerator, are kneaded and then sheet-like rubber The composition was removed. Then, the obtained rubber composition is press-crosslinked at 160 ° C. for 20 minutes to obtain a crosslinked rubber, and the obtained crosslinked rubber (test piece) is evaluated for wear resistance and low heat build-up. I did it. The results are shown in Table 1. In Table 1, the evaluation results of wear resistance and low heat build-up were shown as ratios when the results of Comparative Example 1 described later were set to 100, respectively.
〔変性スチレンブタジエンゴム2の製造〕
変性剤としてのトリス(ジメチルアミノ)クロロシランの配合量を0.157部から、0.079部(重合開始剤1中に含有されるLi1モルに対して、0.5モルとなる量)に変更した以外は、実施例1と同様にして、変性スチレンブタジエンゴム2の製造を行った。得られた変性スチレンブタジエンゴム2は、GPC測定において、Mnが161,000、Mwが202,000、分子量分布(Mw/Mn)が1.25の溶出成分(ピーク面積比15.1%)、Mnが373,000、Mwが378,000、分子量分布(Mw/Mn)が1.01の溶出成分(ピーク面積比16.4%)、およびMnが723,000、Mwが763,000、分子量分布(Mw/Mn)が1.06の溶出成分(ピーク面積比68.5%)からなるものであり、全体としてMnが430,000、Mwが615,000、分子量分布(Mw/Mn)が1.43のものであった。また、多角度光散乱測定により、高分子側のピークの分岐度が高い事が確認された。さらに、この変性スチレンブタジエンゴム2のスチレン単位の含有量は21.7%、ブタジエン単位中のビニル結合含有量は59.9モル%であった。また、この変性スチレンブタジエンゴム2について、1H-NMRを測定したところ、トリス(ジメチルアミノ)シリル基が導入されていることが確認された。この変性スチレンブタジエンゴム2について、上記した方法にしたがい、ゲル重量分率を測定した。結果を表1に示す。 [Example 2]
[Production of modified styrene butadiene rubber 2]
The blending amount of tris (dimethylamino) chlorosilane as a modifier is changed from 0.157 parts to 0.079 parts (amount to be 0.5 moles relative to 1 mole of Li contained in the polymerization initiator 1). A modified styrene butadiene rubber 2 was produced in the same manner as in Example 1 except that. The obtained modified styrene butadiene rubber 2 is an elution component (peak area ratio 15.1%) having an Mn of 161,000, an Mw of 202,000, and a molecular weight distribution (Mw / Mn) of 1.25 in GPC measurement. Elution component (peak area ratio 16.4%) with Mn of 373,000, Mw of 378,000, molecular weight distribution (Mw / Mn), and Mn of 723,000, Mw of 763,000, molecular weight Distribution (Mw / Mn) is composed of 1.06 elution component (peak area ratio 68.5%), Mn is 430,000, Mw is 615,000 as a whole, and molecular weight distribution (Mw / Mn) is It was 1.43. Moreover, it was confirmed by the multi-angle light scattering measurement that the degree of branching of the peak on the polymer side is high. The modified styrene butadiene rubber 2 had a styrene unit content of 21.7% and a vinyl bond content in the butadiene unit of 59.9 mol%. Further, when 1 H-NMR was measured for the modified styrene butadiene rubber 2, it was confirmed that a tris (dimethylamino) silyl group was introduced. The gel weight fraction of this modified styrene butadiene rubber 2 was measured according to the method described above. The results are shown in Table 1.
〔変性スチレンブタジエンゴム3の製造〕
変性剤として、トリス(ジメチルアミノ)クロロシラン0.157部の代わりに、テトラメトキシシラン0.487部(重合開始剤1中に含有されるLi1モルに対して、4.0モルとなる量)を用いたこと以外は、実施例1と同様にして、変性スチレンブタジエンゴム3の製造を行った。得られた変性スチレンブタジエンゴム3は、GPC測定において、全体としてMnが545,000、Mwが1,004,000、分子量分布(Mw/Mn)が1.84のものであった。また、この変性スチレンブタジエンゴム3のスチレン単位の含有量は21.7%、ブタジエン単位中のビニル結合含有量は59.8モル%であった。そして、この変性スチレンブタジエンゴム3について、上記した方法にしたがい、ゲル重量分率を測定した。結果を表1に示す。 [Comparative Example 1]
[Production of modified styrene butadiene rubber 3]
As a modifier, instead of 0.157 part of tris (dimethylamino) chlorosilane, 0.487 part of tetramethoxysilane (amount to be 4.0 moles relative to 1 mole of Li contained in the polymerization initiator 1). A modified styrene butadiene rubber 3 was produced in the same manner as in Example 1 except that it was used. The obtained modified styrene butadiene rubber 3 as a whole had a Mn of 545,000, Mw of 1,004,000, and a molecular weight distribution (Mw / Mn) of 1.84 in GPC measurement. The modified styrene butadiene rubber 3 had a styrene unit content of 21.7% and a vinyl bond content in the butadiene unit of 59.8 mol%. And about this modified styrene butadiene rubber 3, according to the above-mentioned method, the gel weight fraction was measured. The results are shown in Table 1.
〔変性スチレンブタジエンゴム4の製造〕
変性剤として、トリス(ジメチルアミノ)クロロシラン0.157部の代わりに、トリメチルクロロシラン0.087部(重合開始剤1中に含有されるLi1モルに対して、1.0モルとなる量)を用いたこと以外は、実施例1と同様にして、変性スチレンブタジエンゴム4の製造を行った。得られた変性スチレンブタジエンゴム4は、GPC測定において、全体としてMnが440,000、Mwが629,000、分子量分布(Mw/Mn)が1.43のものであった。また、この変性スチレンブタジエンゴム4のスチレン単位の含有量は22.3%、ブタジエン単位中のビニル結合含有量は60.0モル%であった。そして、この変性スチレンブタジエンゴム4について、上記した方法にしたがい、ゲル重量分率を測定した。結果を表1に示す。 [Comparative Example 2]
[Production of Modified Styrene Butadiene Rubber 4]
As a modifier, instead of 0.157 part of tris (dimethylamino) chlorosilane, 0.087 part of trimethylchlorosilane (amount to be 1.0 mole with respect to 1 mole of Li contained in the polymerization initiator 1) is used. A modified styrene butadiene rubber 4 was produced in the same manner as in Example 1 except that it was. The obtained modified styrene butadiene rubber 4 as a whole had Mn of 440,000, Mw of 629,000, and molecular weight distribution (Mw / Mn) of 1.43 in GPC measurement. The modified styrene butadiene rubber 4 had a styrene unit content of 22.3% and a vinyl bond content in the butadiene unit of 60.0 mol%. And about this modified styrene butadiene rubber 4, according to the above-mentioned method, the gel weight fraction was measured. The results are shown in Table 1.
〔変性スチレンブタジエンゴム5の製造〕
変性剤として、トリス(ジメチルアミノ)クロロシラン0.157部の代わりに、両末端アミノ変性ポリオルガノシロキサン(信越シリコーン社製、商品名「KF-8012」)1.756部(重合開始剤1中に含有されるLi1モルに対して、0.5モルとなる量)を用いたこと以外は、実施例1と同様にして、変性スチレンブタジエンゴム5の製造を行った。得られた変性スチレンブタジエンゴム5は、GPC測定において、全体としてMnが437,000、Mwが646,000、分子量分布(Mw/Mn)が1.48のものであった。また、この変性スチレンブタジエンゴム5のスチレン単位の含有量は22.3%、ブタジエン単位中のビニル結合含有量は60.0モル%であった。そして、この変性スチレンブタジエンゴム5について、上記した方法にしたがい、ゲル重量分率を測定した。結果を表1に示す。 [Comparative Example 3]
[Production of Modified Styrene Butadiene Rubber 5]
As a modifier, instead of 0.157 part of tris (dimethylamino) chlorosilane, 1.756 parts of both-terminal amino-modified polyorganosiloxane (manufactured by Shin-Etsu Silicone Co., Ltd., trade name “KF-8012”) (in polymerization initiator 1) A modified styrene butadiene rubber 5 was produced in the same manner as in Example 1 except that 0.5 mol) was used with respect to 1 mol of Li contained. The obtained modified styrene butadiene rubber 5 as a whole had a Mn of 437,000, Mw of 646,000, and molecular weight distribution (Mw / Mn) of 1.48 in GPC measurement. The modified styrene-butadiene rubber 5 had a styrene unit content of 22.3% and a vinyl bond content in the butadiene unit of 60.0 mol%. And about this modified styrene butadiene rubber 5, according to the above-mentioned method, the gel weight fraction was measured. The results are shown in Table 1.
〔変性スチレンブタジエンゴム6の製造〕
変性剤として、トリス(ジメチルアミノ)クロロシラン0.157部の代わりに、下記式(6)で表される側鎖グリシドキシ変性ポリオルガノシロキサン0.086部(重合開始剤1中に含有されるLi1モルに対して、0.1モルとなる量)を濃度22%のキシレン溶液の状態で用いたこと以外は、実施例1と同様にして、変性スチレンブタジエンゴム6の製造を行った。得られた変性スチレンブタジエンゴム6は、GPC測定において、全体としてMnが438,000、Mwが626,000、分子量分布(Mw/Mn)が1.43のものであった。また、この変性スチレンブタジエンゴム6のスチレン単位の含有量は21.5%、ブタジエン単位中のビニル結合含有量は59.6モル%であった。そして、この変性スチレンブタジエンゴム6について、上記した方法にしたがい、ゲル重量分率を測定した。結果を表1に示す。
[Production of modified styrene butadiene rubber 6]
As a modifier, instead of 0.157 part of tris (dimethylamino) chlorosilane, 0.086 part of a side chain glycidoxy-modified polyorganosiloxane represented by the following formula (6) (1 mol of Li contained in the polymerization initiator 1) The modified styrene butadiene rubber 6 was produced in the same manner as in Example 1 except that 0.1 mol) was used in the form of a 22% concentration xylene solution. The obtained modified styrene butadiene rubber 6 had an overall Mn of 438,000, Mw of 626,000, and molecular weight distribution (Mw / Mn) of 1.43 in GPC measurement. The modified styrene butadiene rubber 6 had a styrene unit content of 21.5% and a vinyl bond content in the butadiene unit of 59.6 mol%. And about this modified styrene butadiene rubber 6, according to the above-mentioned method, the gel weight fraction was measured. The results are shown in Table 1.
〔変性スチレンブタジエンゴム7の製造〕
窒素雰囲気下、オートクレーブに、シクロヘキサン800部、1,3-ブタジエン94.8部、スチレン25.2部、およびテトラメチルエチレンジアミン0.232部とを仕込んだ後、n-ブチルリチウム0.051部を添加し、60℃で重合を開始した。60分間重合反応を継続し、重合転化率が95%から100%の範囲になったことを確認してから、変性剤としてのトリス(ジメチルアミノ)クロロシラン0.157部を添加し、30分間反応させた後、重合停止剤としてメタノール0.064部を添加して重合体を含有する溶液を得た。 [Comparative Example 5]
[Production of Modified Styrene Butadiene Rubber 7]
In a nitrogen atmosphere, an autoclave was charged with 800 parts of cyclohexane, 94.8 parts of 1,3-butadiene, 25.2 parts of styrene, and 0.232 parts of tetramethylethylenediamine, and 0.051 part of n-butyllithium was added. The polymerization was started at 60 ° C. The polymerization reaction was continued for 60 minutes, and after confirming that the polymerization conversion was in the range of 95% to 100%, 0.157 part of tris (dimethylamino) chlorosilane as a modifier was added and reacted for 30 minutes. Then, 0.064 parts of methanol was added as a polymerization terminator to obtain a solution containing a polymer.
また、変性剤として、トリメチルクロロシランや両末端アミノ変性ポリオルガノシロキサンを用いた場合には、得られる変性共役ジエン系ゴムは、ゲル分の含有量が低いものであったが、ゴム架橋物とした場合に、低発熱性および耐摩耗性に劣る結果となった(比較例2,3)。
さらに、変性剤として、側鎖グリシドキシ変性ポリオルガノシロキサンを用いた場合には、得られる変性共役ジエン系ゴムは、ゲル分を多く含むものとなり、加工性に劣り、さらには、ゴム架橋物とした場合に、低発熱性に劣る結果となった(比較例4)。
また、重合開始剤として、n-ブチルリチウムを用いた場合には、得られる変性共役ジエン系ゴムは、ゲル分を実質的に含有しないものであったが、ゴム架橋物とした場合に、低発熱性および耐摩耗性に劣り、とりわけ、低発熱性に極めて劣る結果となった(比較例5)。 On the other hand, when tetramethoxysilane is used as a modifier, the resulting modified conjugated diene rubber contains a large amount of gel, is inferior in workability, and further, when a rubber cross-linked product is used. The results were inferior in low heat build-up and wear resistance (Comparative Example 1).
In addition, when trimethylchlorosilane or both-terminal amino-modified polyorganosiloxane was used as a modifier, the resulting modified conjugated diene rubber had a low gel content, but was a crosslinked rubber product. In this case, the results were inferior in low heat generation and wear resistance (Comparative Examples 2 and 3).
Furthermore, when a side-chain glycidoxy-modified polyorganosiloxane is used as a modifier, the resulting modified conjugated diene rubber contains a large amount of gel, is inferior in processability, and is a crosslinked rubber product. In such a case, the result was inferior to the low exothermic property (Comparative Example 4).
In addition, when n-butyllithium is used as a polymerization initiator, the resulting modified conjugated diene rubber does not substantially contain a gel component. The results were inferior in heat generation and wear resistance, and in particular, inferior in low heat generation (Comparative Example 5).
Claims (11)
- 重合開始剤として、アルカリ金属原子および芳香環に、直接結合した炭素原子を1分子中に3個以上有するアルカリ金属化芳香族化合物を用いて、少なくとも共役ジエン化合物を含んでなる単量体を重合し、活性末端を有する共役ジエン系ゴムを得る第1工程と、
前記活性末端を有する共役ジエン系ゴムの活性末端に、下記一般式(I)で表される化合物を反応させる第2工程と、を備える変性共役ジエン系ゴムの製造方法。
And a second step of reacting a compound represented by the following general formula (I) with an active terminal of the conjugated diene rubber having the active terminal.
- 前記第1工程において、前記共役ジエン化合物に加えて芳香族ビニル化合物を含んでなる単量体を共重合する請求項1に記載の変性共役ジエン系ゴムの製造方法。 The method for producing a modified conjugated diene rubber according to claim 1, wherein, in the first step, a monomer comprising an aromatic vinyl compound in addition to the conjugated diene compound is copolymerized.
- 前記アルカリ金属化芳香族化合物が、芳香環に直接結合した炭素原子を1分子中に3個以上有する芳香族化合物に、有機アルカリ金属化合物を反応させて得られたものである請求項1または2に記載の変性共役ジエン系ゴムの製造方法。 The alkali metalated aromatic compound is obtained by reacting an organic alkali metal compound with an aromatic compound having 3 or more carbon atoms directly bonded to an aromatic ring in one molecule. A process for producing the modified conjugated diene rubber described in 1.
- 前記芳香環に直接結合した炭素原子を1分子中に3個以上有する芳香族化合物が、下記一般式(II)で表される芳香族化合物である請求項3に記載の変性共役ジエン系ゴムの製造方法。
- 前記一般式(I)で表される化合物中における、Xが、ハロゲン原子であり、R1~R4が、化学的な単結合であり、R5~R10が、それぞれ独立して、炭素数1~5のアルキル基である請求項1~4のいずれかに記載の変性共役ジエン系ゴムの製造方法。 In the compound represented by the general formula (I), X is a halogen atom, R 1 to R 4 are chemical single bonds, and R 5 to R 10 are each independently a carbon atom. The method for producing a modified conjugated diene rubber according to any one of claims 1 to 4, which is an alkyl group of 1 to 5.
- 前記第2工程における、前記一般式(I)で表される化合物の使用量を、前記第1工程で用いた前記アルカリ金属化芳香族化合物中のアルカリ金属原子1モルに対し、前記共役ジエン系ゴムの活性末端と反応することができる原子または反応基の量が、0.05~5モルの範囲となる量とする請求項1~5のいずれかに記載の変性共役ジエン系ゴムの製造方法。 In the second step, the amount of the compound represented by the general formula (I) is used with respect to 1 mol of the alkali metal atom in the alkali metalated aromatic compound used in the first step. The method for producing a modified conjugated diene rubber according to any one of claims 1 to 5, wherein the amount of atoms or reactive groups capable of reacting with the active terminal of the rubber is in an amount ranging from 0.05 to 5 mol. .
- 請求項1~6のいずれかに記載の製造方法により得られる変性共役ジエン系ゴム。 A modified conjugated diene rubber obtained by the production method according to any one of claims 1 to 6.
- 請求項7に記載の変性共役ジエン系ゴムを含むゴム成分100重量部に対して、シリカ10~200重量部を含有してなるゴム組成物。 A rubber composition comprising 10 to 200 parts by weight of silica with respect to 100 parts by weight of a rubber component containing the modified conjugated diene rubber according to claim 7.
- 架橋剤をさらに含有してなる請求項8に記載のゴム組成物。 The rubber composition according to claim 8, further comprising a crosslinking agent.
- 請求項9に記載のゴム組成物を架橋してなるゴム架橋物。 A crosslinked rubber product obtained by crosslinking the rubber composition according to claim 9.
- 請求項10に記載のゴム架橋物を含んでなるタイヤ。 A tire comprising the rubber cross-linked product according to claim 10.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1555729A (en) * | 1976-06-17 | 1979-11-14 | Charbonnages Ste Chimique | Bifunctional and trifunctional organo-lithium initiators and their use |
WO2010131646A1 (en) * | 2009-05-11 | 2010-11-18 | 日本ゼオン株式会社 | Method for producing radial conjugated diene polymer |
JP2012256789A (en) * | 2011-06-10 | 2012-12-27 | Taiyo Yuden Co Ltd | Active material for electrochemical device, and electrochemical device using the same |
WO2013100022A1 (en) * | 2011-12-28 | 2013-07-04 | 日本ゼオン株式会社 | Method for producing modified conjugated diene rubber |
-
2013
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1555729A (en) * | 1976-06-17 | 1979-11-14 | Charbonnages Ste Chimique | Bifunctional and trifunctional organo-lithium initiators and their use |
WO2010131646A1 (en) * | 2009-05-11 | 2010-11-18 | 日本ゼオン株式会社 | Method for producing radial conjugated diene polymer |
JP2012256789A (en) * | 2011-06-10 | 2012-12-27 | Taiyo Yuden Co Ltd | Active material for electrochemical device, and electrochemical device using the same |
WO2013100022A1 (en) * | 2011-12-28 | 2013-07-04 | 日本ゼオン株式会社 | Method for producing modified conjugated diene rubber |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016104628A1 (en) * | 2014-12-25 | 2016-06-30 | 住友化学株式会社 | Modified conjugated diene polymer, and polymer composition containing said polymer |
CN107001491A (en) * | 2014-12-25 | 2017-08-01 | 住友化学株式会社 | Modified conjugated diene polymer and the polymer composition containing the polymer |
JPWO2016104628A1 (en) * | 2014-12-25 | 2017-10-05 | 住友化学株式会社 | Modified conjugated diene polymer and polymer composition containing the polymer |
US10118973B2 (en) | 2014-12-25 | 2018-11-06 | Sumitomo Chemical Company, Limited | Modified conjugated diene polymer, and polymer composition containing said polymer |
WO2018181161A1 (en) * | 2017-03-31 | 2018-10-04 | 日本ゼオン株式会社 | Method for producing modified conjugated diene-based rubber |
JPWO2018181161A1 (en) * | 2017-03-31 | 2020-02-06 | 日本ゼオン株式会社 | Method for producing modified conjugated diene rubber |
JP7010285B2 (en) | 2017-03-31 | 2022-01-26 | 日本ゼオン株式会社 | Method for manufacturing modified conjugated diene rubber |
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