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    • 专利摘要:
    composition of rubber and pneumatic tire. the present invention is directed to a rubber composition comprising a bifunctionalized elastomer with the reaction product of 1) a live anionic elastomeric polymer activated with a functional initiator and 2) a functional polymerization terminator; and a filler selected from silica and carbon black. the invention is also directed to a pneumatic tire comprising the rubber composition.
    公开号:BR102015019831B1
    申请号:R102015019831-0
    申请日:2015-08-18
    公开日:2020-09-29
    发明作者:Paul Harry Sandstrom；Liqing Ma；Arindam Mazumdar
    申请人:The Goodyear Tire & Rubber Company；
    IPC主号:
    专利说明:

    Background of the invention
    [001] Currently, there is a growing demand for functionalized polymers. Functionalized polymers can be synthesized using various live / controlled polymerization techniques. In the process of live polymerization based on the active carbanionic center, metals from groups I and II of the periodic table are commonly used to initiate the polymerization of monomers into polymers. For example, lithium, barium, magnesium, sodium and potassium are metals that are often used in such polymerizations. Primer systems of this type are of commercial importance because they can be used to produce stereoregular polymers. For example, lithium initiators can be used to initiate the anionic polymerization of isoprene in synthetic polyisoprene rubber or to initiate the polymerization of 1,3 - butadiene in polybutadiene rubber having the desired microstructure.
    [002] The polymers formed in such polymerizations present the metal used to initiate polymerization at the growth end of the polymer chains, and are sometimes referred to as live polymers. They are called living polymers because their polymer chains, which contain the terminal metal primer, continue to grow or live until all available monomers are used. Polymers that are prepared using such metallic initiators usually have structures that are essentially linear and normally do not contain appreciable amounts of branching.
    [003] This invention details the synthesis of functionalized polymers. In general, obtaining functionalized polymers with the best performance properties in tires is highly desirable. To reduce the rolling resistance and improve the wear characteristics of the tire tread, functionalized elastomers with high physical rebound properties (low hysteresis) were used for the rubber compositions of the tire tread. However, in order to improve the skid resistance in wet tread of a tread, rubber polymers that have a low rebound property (high hysteresis), which are subjected to great energy loss, are sometimes used in such rubber compositions . To obtain such viscoelastic properties incompatible with the rubber compositions of the tire tread, blends (mixtures) of various types of natural and synthetic rubber can be used.
    [004] Functionalized rubber polymers produced by live polymerization techniques generally contain sulfur, accelerators, anti-degraders, a filler, such as carbon black, silica or starch, and other desired rubber chemicals, and are then subsequently cured or cured in the form of a useful product, such as a tire or an energy transmission belt. It has been determined that the physical properties of such cured rubbers depend on the level at which the filler is evenly dispersed through the rubber. This is related to the level of affinity that the filler has for the specific rubber polymer. This can be of practical importance in improving the physical characteristics of the rubber articles that are produced using such compositions. For example, the rolling resistance and traction characteristics of the tires can be improved by improving the affinity of carbon black and / or silica with the rubber polymer used. Therefore, it may be highly desirable to improve the affinity of a given rubber polymer with fillers, such as carbon black and silica.
    [005] In tire tread formulations, a better interaction between the filler and the rubber polymer results in less hysteresis, and, consequently, tires produced with such rubber formulations have less rolling resistance and in some cases wear of the tread. improved bearing capacity. Low tan delta values at a temperature of 60 ° C are indicative of low hysteresis, and consequently tires produced using such rubber formulations usually exhibit less rolling resistance. A better interaction between the filler and the rubber polymer in tire tread formulations also results in higher tan delta values at 0 ° C, indicating better traction characteristics.
    [006] The interaction between rubber and carbon black has been attributed to a combination of physical absorption (van der Waals strength) and chemisorption between the oxygen contained in the functional groups on the surface of carbon black and rubber (see D. Rivin , J. Aron, and A. Medalia, Rubber Chem. & Technol. 41, 330 (1968) and A. Gessler, W. Hess and A Medalia, Plast. Rubber Process, 3, 141 (1968)). Several other chemical modification techniques, especially for styrene-butadiene rubber produced by solution polymerization (S-SBR), have been described to reduce loss through hysteresis by improving filler-polymer interactions. In one of these techniques, the rubber chain end of the solution is modified with aminobenzophenone. This generally improves the interaction between the polymer and the oxygen-containing groups on the carbon black surface (see N. Nagata, Nippon Gomu Kyokaishi, 62, 630 (1989)). Tin bonding of anionic solution polymers is another commonly used chain end modification method that assists the polymer-filler interaction, presumably through the increased reaction with quinone groups on the carbon black surface. The effect of this interaction is to reduce the aggregation between the carbon black particles, which in turn improves dispersion and reduces hysteresis. Functionalization of a solution-polymerized rubber chain end using a functionalized lithium initiator can also be employed. Summary of the invention
    [007] The present invention offers the functionalization of a terminal group of live rubber polymers to improve its affinity for fillers, such as carbon black and / or silica. Such functionalized polymers can be used in the production of tires and other rubber products where an improved polymer / filler interaction is desirable. In tire tread compound compounds, this can result in minor polymeric hysteresis, which in turn can offer a lower level of rolling resistance.
    [008] The present invention is directed to a bifunctionalized elastomer comprising the reaction product of 1) a live anionic elastomeric polymer activated with a functional initiator and 2) a functional polymerization terminator, where
    [009] The live anionic elastomeric polymer activated with a functional initiator presents the formula AYLi, where Y is a divalent polymeric radical, Li is a lithium atom attached to a carbon atom of Y, and A is a radical containing amine presenting the formula X
    where R15 and R16 independently have 1 to 20 carbon atoms and each is independently an alkyl group, a cycloalkyl group, an aromatic group, a substituted alkyl group, a substituted cycloalkyl group or a substituted aromatic group, or R15 and R16 together with the nitrogen to which they are attached, comprise a heterocyclic amine group where R15 and R16 together form an alkanodiyl group of 4 to 20 carbon atoms or an alkanodiyl group of 4 to 20 carbon atoms, and R17 is a covalent group, an alkanodiyl group from 1 to 20 carbon atoms or a substituted alkanediyl group from 1 to 20 carbon atoms; and
    [010] The functional polymerization terminator has the formula I
    i. (l) where R1 is linear C1-C4 akylia, or branched C1-C4 alkanodiyl; X> X2, X3 are independently O, S, or a group of formula (II) or (III) N - R2 - P - R2 where R2 is C1-C18 straight or branched alkyl; Z is R, - OR4OU _R5__x4; R3 R4sθ0independently linear or branched C1-C18 alkyl; R5 is C1-C18 alkanodiyl or dialkyl diyl ether; X4 and halogen or a group of structure IV, V, VI, VII or VIII
    where R6, R7, R8RΘ AND RIOsθ0jnc | independently H or C1-C8 alkyl; R11 is C2-C8 alkanediyl; R12 and Rn are also H, aryl or C1-C8 alkyl; Q is N or a group of structure IX
    where R14 is C1-C8 alkyl.
    [011] The invention is also directed to a tire comprising the composition of rubber. Brief description of the figures
    [012] Figure 1 shows a graph of tan delta in relation to deformation for several rubber samples.
    [013] Figure 2 shows a graph of tan delta in relation to deformation for several rubber samples.
    [014] Figure 3 shows a graph of tan delta in relation to deformation for several rubber samples.
    [015] Figure 4 shows a graph of tan delta in relation to deformation for several rubber samples.
    [016] Figure 5 shows a graph of tan delta in relation to deformation for several rubber samples. Detailed description of the invention
    [017] A bifunctionalized elastomer is described comprising the reaction product of 1) a live anionic elastomeric polymer activated with a functional initiator and 2) a functional polymerization terminator, where
    [018] The live anionic elastomeric polymer activated with a functional initiator presents formula AYLi, where Y is a radical of divalent polymer, Li is a lithium atom attached to a carbon atom of Y and A is a radical containing amine presenting the formula X
    where R15 and R16 independently present 1 to 20 carbon atoms with each being an alkyl group, a cycloalkyl group, an aromatic group, a substituted alkyl group, a substituted cycloalkyl group, or a substituted aromatic group, or R15 and R16 together with nitrogen where both are bonded comprise a heterocyclic amine group, where R15 and R16 together form an alkanediyl group of 4 to 20 carbon atoms or a substituted alkanediyl group of 4 to 20 carbon atoms, and R17 is a covalent bond, an alkanediyl group of 1 to 20 carbon atoms or a substituted alkanediyl group of 1 to 20 carbon atoms; and 2) the functional polymerization terminator has the formula IZ
    where R1 is C1-C4 linear alkyl, or branched C1-C4 alkanediyl; X1, X2, X3 are independently O, S, or a group of formula (II) or (III) —N ~~ R2 —P - R2 where R2 is C1-C18 straight or branched alkyl; Z e, OR, or - R5 — x4; R3 R4 are independently C1-C18 straight or branched alkyl; R5 is C1-C18 alkanodiyl or dialkyl diyl ether; X4 and halogen or a group of structure IV, V, VI, VII or VIII
    where R6, R7 R8, R9 and R10 are independently H or C1-C8 alkyl; R11 is C2-C8 alkanediyl; R12 and R13 are independently H, aryl or C1-C8 alkyl; Q is N or a group of structure IX
    where R14 is C1-C8 alkyl.
    [019] A rubber composition is also described comprising the functionalized elastomer, and a tire comprising the rubber composition.
    [020] The present invention offers a way to bifunctionalize the leaving group of live rubber polymers to improve affinity for fillers, such as carbon black and / or silica, through the use of a functional polymerization initiator and a terminator functional polymerization. The process of the present invention can be used to functionalize any living polymer that is terminated with a group I or II metal from the periodic table. These polymers can be produced using techniques that are well known to those skilled in the art. Rubber polymers terminated with metals that can be functionalized with a terminator of formula I, according to this invention, can be produced using monofunctional primers, presenting the general structural formula PM, where P represents a polymeric chain and where M represents a metal group I or II.
    [021] The initiator used to begin polymerization, used in the synthesis of the live rubber polymer that is functionalized according to this invention, is generally selected from the group consisting of barium, lithium, magnesium, sodium and potassium. Lithium and magnesium are the metals most used in the synthesis of such polymers terminated with metals (live polymers). Typically, lithium initiators are preferred.
    [022] Organolithium compounds are the preferred initiators for use in such polymerizations. Organolithium compounds that are used as initiators are usually monolithic organo compounds. Organolithium compounds, which are the preferred initiators, are monofunctional compounds that can be represented by the formula: R-Li, where R represents a hydrocarbyl radical. In the present invention, the polymerization of a monomer in the presence of the initiator forms a live anionic elastomeric polymer of the formula AYLi, where Y is a divalent polymeric radical, Li is a lithium atom attached to a carbon atom of Y, and A is a amine-containing radical containing formula X

    [023] where R14 and R15 independently have 1 to 20 carbon atoms and each is independently an alkyl group, a cycloalkyl group, an aromatic group, a substituted alkyl group, a substituted cycloalkyl group or a substituted aromatic group, or R14 and R15 together with the nitrogen to which they are attached comprise a heterocyclic amine group, where R14 and R15 together form an alkanediyl group of 4 to 20 carbon atoms or a substituted alkanediyl group of 4 to 20 carbon atoms, and R16 is a covalent bond , an alkanediyl group of 1 to 20 carbon atoms or a substituted alkanediyl group of 1 to 20 carbon atoms. Therefore, the initiator has formula R-Li with R replaced by the structure of formula X. In one embodiment, the organolithium initiator is an N, N - dialkylamino alkyl lithium such as 3 - (N, N - dimethylamino) - 1 - propyl lithium, 3 - (N, N - dimethylamino) - 2 - methyl - 1 - propyl lithium, 3 - (N, N - dimethylamino) - 2,2 - dimethyl - 1 - propyl lithium, 4 - (N, N-dimethylamino ) - 1 - hexyl lithium, 8 - (N, N - dimethylamino) - 1 - propyl lithium, and the like. Correspondingly in this modality, in formula X the group structure is N, N - dialkylamino alkyl, such as 3- (N, N - dimethylamino) - 1 - propyl, 3 - (N, N - dimethylamino) - 2 - methyl - 1 - propyl, 3 - (N, N - dimethylamino) - 2.2 - dimethyl - 1 - propyl, 4 - (N, N - dimethylamino) - 1 - butyl, 5 - (N, N - dimethylamino) - 1 - pentyl, 6 - (N, N - dimethylamino) - 1 - hexyl, 8 - (N, N - dimethylamino) - 1 - propyl, and the like).
    [024] In one embodiment, the organolithium initiator is an azacycloalkyl alkyl lithium, such as 3 - piperidine - 1 - propyl lithium, 3 - pyrrolidine - 1 - propyl lithium, and the like. Likewise in this embodiment, the group structure in formula X is 3 - piperidine - 1 - propyl, 3 - pyrrolidine - 1 - propyl and the like. In one embodiment, the group is 3 - pyrrolidine - 1 - propyl and the initiator is 3 - pyrrolidine - 1 - propyl lithium.
    [025] The amount of the organolithium initiator used will vary depending on the molecular weight that is desired for the rubber polymer being synthesized, as well as the exact temperature of the polymerization that will be employed. The exact amount of the organolithium compound needed to produce a polymer of a desired molecular weight can be easily defined by those skilled in the art. However, as a general rule, the amount of 0.01 to 1 phm (parts per 100 parts by weight of the monomer) of an organolithium initiator will be used. In most cases, the amount of 0.01 to 0.1 phm of an organolithium initiator will be used, preferably 0.025 to 0.07 phm.
    [026] Many types of unsaturated monomers that contain carbon-carbon double bonds can be polymerized into polymers using such metal catalysts. Rubber or elastomeric polymers can be synthesized by polymerizing diene monomers using this type of metal initiator system. The diene monomers that can be polymerized into synthetic rubber polymers can be conjugated or unconjugated diolefins. The monomers of conjugated diolefins containing 4 to 8 carbon atoms are preferred. The substituted aromatic vinyl monomers can also be copolymerized with one or more diene monomers in rubber polymers, for example, styrene-butadiene rubber (SBR). Some representative examples of conjugated diene monomers that can be polymerized in rubber polymers include 1,3 - butadiene, isoprene, 1,3 - pentadiene, 2,3 - dimethyl - 1,3 - butadiene, 2 - methyl 1,3 - pentadiene, 2,3 - dimethyl - 1,3 - pentadiene, 2 - phenyl - 1,3 - butadiene and 4,5 - diethyl - 1,3 - octadiene. Some representative examples of substituted aromatic vinyl monomers that can be used in the synthesis of rubber polymers include styrene, 1 - vinylnaphthalene, 3 - methylstyrene, 3,5 - diethylstyrene, 4 - propylstyrene, 2,4,6 - trimethylstyrene, 4 - dodecylstyrene , 3 - methyl - 5 - normal - hexylstyrene, 4 - phenylstyrene, 2 - ethyl - 4 - benzylstyrene, 3,5 - diphenylstyrene, 2,3,4,5 - tetraethylstyrene, 3 - ethyl - 1 - vinylnaphthalene, 6 - isopropyl - 1 - vinylnaphthalene, 6 - cyclohexyl - 1 - vinylnaphthalene, 7 - dodecyl - 2 - vinylnaphthalene, α - methylstyrene and the like.
    [027] Metal-terminated rubber polymers, which are functionalized with a formula I terminator according to this invention, are generally prepared by solution polymerizations using inert organic solvents, such as saturated aliphatic hydrocarbons, aromatic hydrocarbons or ethers. The solvents used in such solution polymerizations will normally contain about 4 to about 10 carbon atoms per molecule and will remain liquid under the conditions of the polymerization. Some representative examples of suitable organic solvents include pentane, isooctane, cyclohexane, normal hexane, benzene, toluene, xylene, ethylbenzene, tetrahydrofuran and the like, alone or in a mixture. For example, the solvent can be a mixture of different hexane isomers. Such solution polymerizations result in the formation of a polymer cement (a highly viscous solution of the polymer).
    [028] The metal-terminated live rubber polymers used in the practice of this invention can have any molecular weight. However, the numerical average molecular weight of the live rubber polymer will generally be within the range of about 50,000 to about 500,000. These live rubber polymers generally have numerical average molecular weights within the range of 100,000 to 250,000.
    [029] The metal-terminated live rubber polymer can be functionalized by simply adding a stoichiometric amount of a formula I terminator to a rubber polymer solution (a live polymer rubber cement). In other words, approximately 1 mol of the terminator of formula I is added per mol of the terminal metal groups in the live rubber polymer. The number of moles of the terminal metal groups in such polymers is considered to be the number of moles of the metal used in the initiator. Therefore, it is possible to add more than a stoichiometric amount of the formula I terminator. However, the use of larger amounts is not beneficial for the final polymeric properties. Despite this, in many cases, it is desirable to use a small excess of the formula I terminator to ensure that at least a stoichiometric amount is actually employed, or to control the stoichiometry of the functionalization reaction. In most, about 1.2 to about 2 moles of the formula I terminator will be used per mole of the metal terminal groups in the live polymer to be treated. In the case where functionalization of all ends of the metal-terminated chains on the rubber polymer is not desired, smaller amounts of the formula I terminator can be used.
    [030] The formula I terminator will react with the metal-terminated live rubber polymer over a wide temperature range. For practical reasons, the functionalization of such live rubber polymers will normally be carried out at a temperature within the range of 0 ° C to 150 ° C. In order to increase the reaction rates, in most cases it will be preferable to use a temperature within the range of 20 ° C to 100 ° C, preferably in the range of 50 ° C to 80 ° C. The capping reaction is very fast and only very fast reactions within the range of 0.1 to 2 hours are normally necessary. However, in some cases, the reaction time of up to about 24 h can be employed to guarantee maximum conversions.
    [031] In one of the modalities, the formula I terminator presents one of the structures shown in Table 1. Table 1

    [032] THIS: 1 - ethoxy - 2,8,9 - trioxa - 5 aza - 1 - silabicycle [3.3.3] uπdecane, or ethoxysilatran
    [033] ESTI: 1 ethoxy - 3,7,10 - trimethyl - 2,8,9 - trioxa - 5 - aza - 1 -silabicyclo [3.3.3] uπdecane, or 1 - ethoxy - 3,7,10 -trimethylsilatran
    [034] ESTM: 1 - ethoxy - 4 - methyl - 2,6,7 - trioxa - 1 -silabicycle [2.2.2] octane
    [035] BSTI: 1 - isobutyl - 3,7,10 - trimethyl - 2,8,9 - trioxa - 5 - aza -1 - silabicycle [3.3.3] uπdecane, or 1 - isobutyl - 3,7,10 - trimethylsilatran
    [036] OSTI: 1 - octyl - 3,7,10 - trimethyl - 2,8,9 - trioxa - 5 - aza - 1 -silabiciclo [3.3.3] uπdecaπo, or 1 - octyl - 3,7,10 - trimethylsilatation
    [037] CSTI: 1 - (3 - chloropropyl) - 3,7,10 - trimethyl - 2,8,9 - trioxa - 5 -aza - 1 - silabicycle [3.3.3] uπdecaπo, or 1 - (3 - choropropil ) -3,7,10 - trimethylsilatation
    [038] BIPOS: 1,2 - bis (3,7,10 - trimethyl - 2,8,9 - trioxa - 5 - aza - 1 - silabiciclo [3.3.3] uπdecaπ -1 - il) etaπo, or 1, 2 - bis (3,7,10-trimethylsilatation) ethane
    [039] BIDECS: 1.1 '(dean -1,2 -diyl) bis (3,7,10 - trimethyl - 2,8,9 -trioxa - 5 - aza - 1 - silabicycles [3.3.3] uπdection) , or 1,1 '- (dean - 1,2 - diyl) bis (3,7,10 - trimethylsilatation)
    [040] BIOCTS: 1,8 - bis (3,7,10 - trimethyl - 2,8,9 - trioxa - 5 - aza -1 - silabicycle [3.3.3] uπdecaπ - 1 - il) octane, or 1, 8 - bis (3,7,10-trimethylsilatation) octa in
    [041] DMASTI: N, N - dimethyl - 3 - (3,7,10 - trimethyl - 2,8,9 - trioxa -5 - aza - 1 - silabicycle [3.3.3] uπdecaπ - 1 - il) propane - 1 - amine
    [042] PYSTI: 3,7,10 - trimethyl - 1 - (3 - (pyrrolidin - 1 - yl) propyl) -2,8,9 - trioxa - 5 - aza - 1 - silabicycle [3.3.3]
    [043] BIMSTI: N - beπzilidene - 3 - (3,7,10 - trimethyl - 2,8,9 -trioxa -5 - aza - 1 - silabicycle [3.3.3] undecaπ - 1 - il) propane - 1 - the mine
    [044] ETTS: 1 - ethoxy - 2,8,9 - tritia - 5 - aza - 1 -silabiciclo [3.3.3] uπdecation; or 1 - ethoxy - thiosiliter
    [045] ETAS: 1 - ethoxy - 2,8,9 - trimethyl - 2,5,8,9 - tetraaza - 1 -silabicycle [3.3.3] uπdecaπo; or 1 - ethoxy - 2,8,9 - triazasilatran
    [046] EPTI: 3,7,10 - trimethyl - 1 - (3 - (oxiran - 2 - ylmethoxy) propyl) -2,8,9 - trioxa - 5 - aza - 1 - silabiciclo [3.3.3] uπdecation; or 1 - (3 - (oxiran - 2 - ylmethoxy) propyl) - 3,7,10 - trimethylsilatraπo.
    [047] After the functionalization reaction is complete, it will normally be desirable to "kill" any remaining chains of live polydiene. This can be achieved by adding an alcohol, such as methanol or ethanol, to the polymer cement after the functionalization reaction is completed to eliminate any live polymer that was not consumed by the reaction with the formula I terminator. The polydiene rubber with functionalized terminal group can then be recovered from the solution using standard techniques.
    [048] The functionalized polymer can be formed into a rubber composition.
    [049] The rubber composition may optionally include, in addition to the functionalized polymer, one or more elastomers or rubbers containing olefinic unsaturation. The phrases "rubber or elastomer containing olefinic unsaturation" or "diene based elastomer" include both natural rubber and its various raw and recovered forms, as well as several synthetic rubbers. In describing this invention, the terms "rubber" and "elastomer" can be used interchangeably, unless otherwise specified. The terms "rubber composition", "compound rubber" and "rubber compound" are used interchangeably to refer to rubber that has been mixed with various components and materials, and such terms are well known to those skilled in the field of mixing or rubber composition. Representative synthetic polymers are products of the homopolymerization of butadiene and its homologues and derivatives, for example, methylbutadiene, dimethylbutadiene and pentadiene, as well as copolymers such as those formed from butadiene or their counterparts or derivatives with other unsaturated monomers. Among the latter cited are acetylenes, for example, vinyl acetylene; olefins, for example, isobutylene, which is copolymerized with isoprene to form butyl rubber; vinyl compounds, for example, acrylic acid, acrylonitrile (which is polymerized with butadiene to form NBR), methacrylic acid and styrene, with the latter compound being polymerized with butadiene to form SBR, as well as vinyl esters and various unsaturated aldehydes, ketones and ethers , for example, acrolein, methyl isopropenyl ketone and vinyl ethyl ether. Specific examples of synthetic rubbers include neoprene (polychloroprene), polybutadiene (including cis - 1,4 - polybutadiene), polyisoprene (including cis - 1,4 - polyisoprene), butyl rubber, halobutyl rubber, such as chlorobutyl rubber or bromobutyl, styrene / isoprene / butadiene rubber, 1,3 - butadiene or isoprene copolymers with monomers such as styrene, acrylonitrile and methyl methacrylate, as well as ethylene / propylene terpolymers, also known as ethylene / propylene / diene monomer ( EPDM), and in particular, ethylene / propylene / dicyclopentadiene terpolymers. Additional examples of rubbers that can be used include polymers polymerized in solution with functionalized alkoxy-silyl end (SBR, PBR, IBR and SIBR), polymers with star-like branches attached to tin and silicon. The rubbers or elastomers are preferably polyisoprene (natural or synthetic), polybutadiene and SBR.
    [050] In one respect, at least one additional rubber is preferably, and most preferably at least two diene based rubbers. For example, a combination of two or more rubbers is preferably such as 1,4-polyisoprene cis rubber (natural or synthetic, although natural is preferred), 3,4 - polyisoprene rubber, rubber of styrene / isoprene / butadiene, styrene / butadiene rubbers derived from emulsion and solution polymerization, cis 1,4 - polybutadiene rubbers and butadiene / acrylonitrile copolymers prepared from emulsion polymerization.
    [051] In one aspect of this invention, a styrene / butadiene derived from emulsion polymerization (E-SBR) can be used having a relatively conventional styrene content of about 20 to about 28% bound styrene, or in some applications , an E-SBR having a medium with a relatively high content of bound styrene from about 30 to about 45%.
    [052] The expression E-SBR prepared by emulsion polymerization means that styrene and 1,3-butadiene are copolymerized as an aqueous emulsion. They are known to those skilled in the field. The content of bound styrene can vary, for example, from about 5 to about 50%. In one aspect, E-SBR may also contain acrylonitrile to form a terpolymer rubber, such as E-SBAR, in amounts, for example, from about 2 to about 30% by weight of acrylonitrile bound in the terpolymer.
    [053] Styrene / butadiene / acrylonitrile copolymer rubbers, prepared by emulsion polymerization, containing about 2 to about 40% by weight of acrylonitrile bound in the copolymer, are also considered as diene based rubbers for use in the present invention.
    [054] SBR (S-SBR) prepared by solution polymerization generally has a styrene content bound in a range of about 5 to about 50, preferably from about 9 to about 36 "%. S- SBR can be conveniently prepared, for example, by catalyzing the organo lithium in the presence of an organic hydrocarbon solvent.
    [055] In one embodiment, cis 1,4 - polybutadiene (BR) rubber can be used. Such a BR can be prepared, for example, by the polymerization of the 1,3-butadiene organic solution. BR can be conveniently characterized, for example, with a content of at least 90% cis-1,4 - polyisoprene.
    [056] Cis 1,4 - polyisoprene and cis 1,4 - polyisoprene natural rubber are well known to those skilled in the art.
    [057] The term "phr", as used in the present invention, and according to conventional practice, refers to "parts by weight of a specific material per 100 parts by weight of rubber or elastomer.
    [058] The rubber composition can also include up to 70 phr of process oil. Process oil can be included in the rubber composition as an extension oil for elastomers. Process oil can also be included in the rubber composition by adding the oil directly during its formation. The process oil used can include both the extension oil present in the elastomers and the process oil added during production. Suitable process oils include several known in the art, including aromatic, paraffinic, naphthenic, vegetable oils, and with low PCA content, such as MES, TDAE, SRAE and heavy naphthenic oils. Suitable low PCA oils include those with an aromatic polycyclic content of less than 3% by weight as determined by the IP346 method. Procedures for the IP346 method can be found in Standard Methods for Analysis & Testing of Petroleum and Related Products and British Standard 2000 Parts, 2003, 62nd edition, published by the Institute of Petroleum, United Kingdom.
    [059] The rubber composition includes silica, carbon black or a combination thereof.
    [060] The composition and rubber can include from about 1 to about 150 phr of silica. In another embodiment, 10 to 100 phr of silica can be used.
    [061] The commonly used silicon pigments, which can be used in the rubber compound, include conventional pyrogenic and precipitated silicon (silica). In one embodiment, precipitated silica is used. The conventional silicon pigments employed in this invention are precipitated silicas such as, for example, those obtained by acidifying a soluble silicate, for example, sodium silicate.
    [062] Such conventional silicas can be characterized, for example, by presenting a BET surface area, as measured using nitrogen gas. In one embodiment, the BET surface area can be in the range of about 40 to about 600 m2 / g. In another embodiment, the BET surface area can be in the range of about 80 to about 300 m2 / g. The BET method of measuring surface area is described in the Journal of the American Chemical Society, volume 60, page 304 (1930).
    [063] Conventional silica can also be characterized by having an absorption value of dibutyl phthalate (DBP) in the range of about 100 to about 400, alternately from about 150 to about 300.
    [064] Conventional silica is expected to have an average particle size, for example, in the range of 0.01 to 0.05 microns, as determined by the electron microscope, although the silica particles may be even smaller, or possibly bigger.
    [065] Various commercially available silicas can be used, such as, for example only in the present invention, and without limitation, commercially available silicas from PPG Industries, under the trade name Hi-Sil with designations 210, 243, etc .; silicas available from Rhodia, with, for example, designations Z1165MP and Z165GR and silicas available from Degussa AG, with, for example, designations VN2 and VN3, etc.
    [066] The commonly used carbon blacks can be used as a conventional filler in combination with silica in an amount ranging from 1 to 150 phr. In another embodiment, 10 to 100 phr of carbon black can be used. Although carbon black can be used with silica, in one embodiment, no carbon black is used except an amount needed to provide the black load to the tire, which is 1 to 10 phr. Representative examples of such carbon blacks include N110, N121, N134, N220, N231, N234, N242, N293, N299, N315, N326, N330, N332, N339, N343, N347, N351, N358, N375, N539, N550, N582, N630, N642, N650, N683, N754, N762, N765, N774, N787, N907, N908, N990 and N991. These carbon blacks have iodine absorptions ranging from 9 to 145 g / kg and the number of BPDs varying from 34 to 150 cm3 / 100 g.
    [067] Combinations of silica and carbon black can be used in the composition. In one embodiment, the weight ratio of silica to carbon black is greater than or equal to one.
    [068] Other fillers can be used in the rubber composition including, but not limited to particulates including ultra-high molecular weight polyethylene (UHMWPE), polymeric gels with cross-linked particles including, but not limited to those described in U.S. Patent Nos. 6,242,534; 6,207,757; 6,133,364; 6,372,857; 5,395,891; or 6,127,488, and plasticized starch compound filler including, but not limited to, that described in U.S. Patent No. 5,672,639. Other fillers can be used in an amount ranging from 1 to 30 phr.
    [069] In one embodiment, the rubber composition may contain an organosilicon compound with conventional sulfur. In one embodiment, the sulfur-containing organosilicon compounds are 3,3 '- bis trimethoxy or triethoxy silylpropyl polysulfites. In one embodiment, the sulfur-containing organosilicon compounds are 3,3 '- bis triethoxysilylpropyl disulfide and / or 3,3' - bis triethoxysilylpropyl tetrasulfide.
    [070] In another embodiment, sulfur-containing organosilicon compounds include those described in U.S. Patent No. 6,608,125. In one embodiment, sulfur-containing organosilicon compounds include 3 - (octanoylthio) - 1 - propyltriethoxysilane, CH3 (CH2) ΘC (= O) - S - CH2CH2CH2Si (OCH2CH3) 3, which is commercially available as Momentive Performance Materials NXT ™ .
    [071] In another embodiment, suitable sulfur-containing organosilicon compounds include those described in U.S. Patent Publication No. 2003/0130535. In one embodiment, the sulfur-containing organosilicon compound is Degussa's Si-363.
    [072] The amount of the sulfur-containing organosilicon compound in a rubber composition will vary depending on the level of other additives that are used. In general, the amount of the compounds will vary from 0.5 to 20 phr. In one embodiment, the amount will vary from 1 to 10 phr.
    [073] It is readily understood by those skilled in the art that the composition of rubber will be formed by methods generally known in the area of rubber production, such as mixing various rubbers with sulfur-vulcanizable constituents with various commonly used additive materials, such as, for example, sulfur donors, curing aids, such as activators and retardants and process additives, such as oils, resins including taching and plasticizing resins, fillers, pigments, fatty acid, zinc oxide, waxes, antioxidants and anti-zonizer and peptizing agents. As known to those skilled in the art, depending on the purpose of using the material with vulcanized sulfur (rubbers), the additives mentioned above are selected and commonly used in conventional quantities. Representative examples of sulfur donors include elemental (free sulfur), an amine disulfide, polymeric polysulfide and sulfur olefin adducts. In one embodiment, the vulcanizing agent is elemental sulfur. The sulfur vulcanizing agent can be used in an amount ranging from 0.5 to 8 phr, alternately in a range of 1.5 to 6 phr. Typical amounts of tachyting resins, if used, comprise from about 0.5 to about 10 phr, generally from about 1 to about 5 phr. Typical amounts of process aids comprise about 1 to about 50 phr. Typical amounts of antioxidants comprise about 1 to about 5 phr. Representative antioxidants can be, for example, diphenyl - p - phenylenediamine and others, such as, for example, those described in The Vanderbilt Rubber Handbook (1978), pages 344 - 346. Typical amounts of antiozonizers comprise about 1 to 5 phr. Typical amounts of fatty acids, if used, which may include stearic acid comprise about 0.5 to about 3 phr. Typical amounts of zinc oxide comprise about 2 to about 5 phr. Typical amounts of waxes comprise about 1 to about 5 phr. Microcrystalline waxes are used. Typical amounts of peptizers comprise about 0.1 to about 1 phr. Typical peptides can be, for example, pentachlorothiophenol and dibenzamidodiphenyl disulfide.
    [074] Accelerators are used to control the time and / or temperature required for vulcanization and to improve the properties of the vulcanized product. In one embodiment, a simple accelerator system can be used, that is, a primary accelerator. The primary accelerator can be used in total amounts ranging from about 0.5 to about 4, alternately from about 0.8 to about 1.5 phr. In another embodiment, combinations of a primary and secondary accelerator can be used with the secondary accelerator being used in small amounts, such as about 0.05 to about 3 phr, to activate and improve the properties of the vulcanized product. Combinations of these accelerators are expected to produce a synergistic effect on the final properties, and to be somewhat better than those produced by the use of only one accelerator. In addition, delayed-action accelerators can be used because they are unaffected by normal process temperatures, but produce satisfactory curing at normal vulcanization temperatures. Vulcanization retarders can also be used. Types of suitable accelerators that can be used in the present invention are amines, disulfides, guanidines, thiourea, thiazoles, thiuramines, sulfenamides, dithiocarbamates and xanthates. In one embodiment, the primary accelerator is a sulfenamide. If a second accelerator is used, it can be a compound of guanidine, dithiocarbamate or thiurame.
    [075] Mixing the rubber composition can be obtained by methods known to those skilled in the art. For example, components are generally mixed in at least two stages, a non-productive stage followed by a productive one. Final curing agents including sulfur vulcanizing agents are generally mixed in the final stage which is conventionally referred to as "productive", where mixing generally occurs at a temperature lower than the mixing temperature of the previous non-productive stage of the mixture. The terms "non-productive" and "productive" mix stages are well known to those skilled in the art. The rubber composition can be subjected to a thermomechanical mixing step. This step comprises mechanical work in a mixer or extruder for an adequate period of time to produce a rubber temperature between 140 ° C and 190 ° C. The appropriate duration of thermomechanical work varies as a function of operating conditions, and the volume and nature of the components. For example, thermomechanical work can be 1 to 20 minutes.
    [076] The rubber composition can be incorporated into a variety of tire rubber components. For example, this component can be a tread band (including liner and base), flank, vertex, anti-friction mesh, flank insertion, inner liner. In one embodiment, the component is a tread.
    [077] The tire of the present invention can be racing, passenger, aircraft, for use in agriculture, trucks, and the like. In one embodiment, the tire is passenger or truck. The tire can also be radial or cross-lined.
    [078] The vulcanization of the tire of the present invention is generally carried out at conventional temperatures ranging from about 100 ° C to 200 ° C. In one embodiment, vulcanization is carried out at temperatures ranging from about 110 ° C to 180 ° C. Any of the common processes and vulcanization can be used, such as heating in a press or mold, heating with superheated steam or hot air. Such tires can be produced, molded, formed and cured by various methods that are known and will become clear to those skilled in the field.
    [079] This invention is illustrated by the following examples that are merely illustrative and should not be considered as limiting the scope of the invention or the form in which it can be practiced. Unless otherwise specified, parts and percentages are given by weight. Example 1
    [080] In this example, pilot scale polymerization of a non-functionalized elastomer is illustrated. Polymerizations are produced in a 60-gallon (227.12 L) reactor at a temperature of 65 ° C. A pre-mixture of styrene and butadiene (113.5 kg, 12% by weight) was loaded into the reactor with hexane followed by the addition of a modifier (TMEDA, 39-43 ml_) and initiator (n - butyl lithium, 52-63 ml_ , 15% by weight). When the conversion was over 98%, the polymerization was terminated with isopropanol. The resulting non-functionalized elastomer was marked as a control sample 1. Example 2
    [081] In this example, pilot scale polymerization of a functionalized end elastomer obtained using a functional initiator is illustrated.
    [082] The polymerizations were carried out in a 60-gallon (227.12 L) reactor at a temperature of 65 ° C. A pre-mixture of the styrene and butadiene monomer (113.5 kg, 12% by weight) was loaded into the reactor with hexane followed by the addition of a modifier (TMEDA, 39-43 ml_) and functional initiator (3 - pyrrolidine, 1 - lithium propyl, 200-250 ml, 5.75% by weight). When the conversion was over 98%, the polymerization was terminated with isopropanol. The resulting mono-functionalized elastomer was marked as a comparative sample 2. Example 3
    [083] In this example, pilot scale polymerization of a functionalized end elastomer obtained using a functional primer is illustrated.
    [084] The functional terminator used in the polymerization was produced as follows. Trisopropanolamine (253.0 g, from Aldrich), tetraethylsilicate (289 g, from Aldrich) and potassium hydroxide (3.7 g from Aldrich) were mixed in a 1 L round-bottom flask with 3 necks, equipped with a device distillation The mixture was then heated to 85 ° C by heating mantle, and the ethanol produced from the reaction was removed under reduced pressure of 200 mmHg. After 2 hours of reaction, the pressure was set to 100 mmHg, and the mixture was heated to 120 ° C for an additional hour. The total of 230 ml of ethanol was recovered from the distillation. The crude oily product was then distilled under a pressure of ~ 2 mmHg and at a temperature of 120 ° C. A total of 305 g (88.2% yield) of white crystalline solid, 1 - ethoxy - 3,7,10 - trimethylsilatraπo (ESTI), was obtained. Analysis of 1HNMR and 13CNMR spectroscopy demonstrated more than 95% purity of the desired product, m.p. 80-83 ° C.
    [085] The polymerizations were carried out in a 60-gallon (227.12 L) reactor at a temperature of 65 ° C. A pre-mixture of the styrene and butadiene monomer (113.5 kg, 12% by weight) was loaded into the reactor with hexane as a solvent followed by the addition of a modifier (TMEDA, 39-43 mL) and initiator (n - butyl lithium, 52-63 ml, 15% by weight). When the conversion was over 98%, the polymerization was terminated with the functional terminator 1 - ethoxy - 3,7,10 - trimethylsilatraπo (ESTI). The resulting mono-functionalized elastomer was marked as a comparative sample 3. Example 4
    [086] This example illustrates the pilot scale polymerization of a bifunctionalized elastomer at both ends of the chain. The bifunctionalized elastomer was obtained using a functional initiator and a functional terminator.
    [087] The polymerizations were carried out in a 60-gallon (227.12 L) reactor at a temperature of 65 ° C. A pre-mixture of the styrene and butadiene monomer (113.5 kg, 12% by weight) was loaded into the reactor with hexane as a solvent followed by the addition of a modifier (TMEDA, 39-43 ml_) and initiator (3 - pyrrolidine - 1 - lithium propyl, 200-250 ml, 5.75% by weight). When the conversion was over 98%, the polymerization was completed with the functional terminator 1 - ethoxy - 3,7,10 - trimethylsilatran (ESTI). The resulting bifunctionalized elastomer was marked as a sample of the invention 4. Example 5
    [088] The polymers of examples 1-4 were characterized using different techniques, for example, size exclusion chromatography (SEC) for molecular weight determination, differential scanning calorimetry (DSC, inflection at 10 ° C / min) for determination of Tg, IR for determination of cis, trans styrene and vinyl content, and measurements of Mooney viscosity with the results provided in tables 2 and 3. Sample 1, the non-functional SBR of example 1, was marked as control. Sample 2, the monofunctionalized SBR from example 2 obtained using a functional primer, was marked as comparative. Sample 3, the monofunctionalized SBR of example 3 obtained using a functional terminator, was marked as comparative. Sample 4, the bifunctionalized SBR of example 4 obtained using a functional initiator and a functional terminator, represents the present invention. Table 2
    1 Non-functionalized SBR, from example 1 2 Functionalized SBR starting with pyrrolidine propyl lithium (PPL), from example 2 3 Functionalized SBR ending with 1 - ethoxy - 3,7,10 - trimethylsilatran (ESTI), from example 3. 4 Functionalized SBR started with PPL and ended with ESTI, from example 4. Table 3
    1 Viña content expressed as a percentage by weight based on the weight of the total polymer. Example 6
    [089] This example illustrates the use of a rubber compound of a functionalized SBR according to the present invention. The rubber compounds were produced using SBR shown in table 2. Each of the rubber compounds had 70 parts by weight, per 100 parts by weight of rubber (phr) of SBR, 30 phr of polybutadiene, 65 phr of silica and standard quantities other additives, including curing agents. The quantities of these agents were adjusted to maintain a constant cross-linking level, as indicated by the 300% module. The same amount of curing agent was used in samples 2, 3 and 4 while the amount was slightly increased for the non-functionalized SBR of sample 1. All other additives were used in identical amounts in all samples. The rubber compounds were mixed in a standard 3 L mixer with Banbury® rotor. Each SBR sample was mixed with additives in a three-stage mixture.
    [090] The compounds were tested for various physical properties, as provided in table 4. As noted in table 4 and figure 1, sample 4 containing the SBR of the present invention, demonstrated unexpectedly greater resistance to bearing compared to samples 2 and 3, as reflected in the tangent delta measured at 60 ° C and 5% deformation. The lower value of the tangent delta of sample 4 indicates better rolling resistance and suggests a better interaction of the bifunctionalized elastomer of sample 4 with silica, compared to the monofunctionalized elastomers of samples 2 and 3.
    [091] The mixed compounds were tested for viscoelastic properties with the results provided in table 4. Tan delta as indicated was determined using an Alpha Technologies Rubber Process Analyzer (RPA). A description of RPA 2000, its capacity, sample preparation, tests and subtests can be found in these references. HA Pawlowski and J S Dick, Rubber World, June 1992; J S Dick and HA Pawlowski, Rubber World, January 1997; and J S Dick and J A Pawlowski, Rubber & Plastics News, April 26 and May 10, 1993.
    [092] The determination of the tear resistance property is carried out for adhesion of one sample to another sample of the same material. A description can be found in ASTM D4393, except that the 2.5 cm sample width is used and a 5 mm wide Mylar clear plastic window is inserted between the two test samples. It is a measurement of interfacial adhesion (tensile strength expressed in N / mm) between two layers of the same tested compound that was co-cured together with the Mylar film window. The purpose of Mylar's film window is to delimit the width of the peeled area.
    [093] Viscoelastic properties (Tan Delta) were measured using an Alpha Technologies Rubber Process Analyzer (RPA). A description of RPA 2000, its capacity, sample preparation, tests and subtests can be found in these references. HA Pawlowski and J S Dick, Rubber World, June 1992; J S Dick and HA Pawlowski, Rubber World, January 1997; and J S Dick and J A Pawlowski, Rubber & Plastics News, April 26 and May 10, 1993.
    [094] The voltage data was measured according to Instron Corporation's automatic test system equipment. Such equipment can determine the final tension, final elongation, modules, etc. The data reported in the table is produced by processing the ring tension test station which is an Instron 4201 load structure.
    [095] Wear data was measured according to the DIN 53516 abrasion resistance test procedure using a Zwick drum abrasion unit, model 6102 with Newton 2.5 force. DIN standards are German tests. The results of DIN abrasion are described as values related to a control of the rubber composition used by the laboratory.
    [096] Alternatively, the Grosch abrasion rate was processed on a LAT-100 friction device and is measured in terms of mg / km of the rubbed rubber. The rubber test sample is placed at a sliding angle under constant load (newtons) as it travels a certain distance on a rotating abrasive wheel (wheel from HB Scheifmittel GmbH). Frictional forces, both lateral and circumferential, produced by the rubbed sample can be measured together with the load (newtons) using a triaxial load cell. The surface temperature of the abrasive wheel is monitored during the test and recorded as an average temperature. In practice, the low abrasion gravity test can be performed, for example, with a load of 20 N, with a slip angle of 2 degrees and a disc speed of 40 kph (kilometers per hour) with a sample stroke of 7,500 m. A medium abrasion gravity test can be carried out, for example, with a load of 40 N with a slip angle of 6 degrees and a disk speed of 20 hph and a sample stroke path of 1,000 m. A high abrasion gravity test can be carried out, for example, with a load of 70 N and a sliding angle of 12 degrees and a disk speed of 20 kph, and a sample stroke of 250 m. Table 4

    * Functionality: NF = not functionalized; Fl = functionalized initiator; FT = functionalized terminator. Example 7
    [097] The procedure of example 6 was repeated to produce compounds containing 60 phr of SBR, 40 phr of polybutadiene and 95 phr of silica. All other conditions were maintained according to example 6. The results of physical tests on the compounds (marked samples No. 5-8), as shown in Table 5 and Figure 2, demonstrated resistance to the upper bearing of the functionalized polymer of the present invention ( sample No. 8) compared to samples 6 and 7, as reflected in the delta tangent measured at 60C and 5% deformation. The value of the minor delta tangent in sample 8 indicates better rolling resistance, and suggests a better interaction of the bifunctionalized elastomer of sample 8 with silica compared to the monofunctionalized elastomers of samples 6 and 7. Table 5

    * Functionality: NF = not functionalized; Fl = functionalized initiator; FT = functionalized terminator. Example 8
    [098] The procedure of example 6 was repeated to produce compounds containing 50 phr of SBR, 50 phr of natural rubber and 60 phr of silica, with the exception of the SBR composition with about 18% styrene, 10% vinyl and a Tg of about -72 ° C. All other conditions were maintained according to example 6. The results of the physical tests on the compounds (marked samples No. 9-12), as shown in table 6 and in figure 3, demonstrated superior resistance to the functionalized polymer bearing of the present invention ( sample No. 12) compared to samples 10 and 11, as reflected in the delta tangent measured at 60C and 5% deformation. The value of the minor delta tangent of sample 12 indicates better rolling resistance, and suggests better interaction of the bifunctionalized elastomer of sample 12 with silica compared to the monofunctionalized elastomers of samples 10 and 11. Table 6
    * Functionality: NF = not functionalized; FI = functionalized initiator; FT = functionalized terminator. Example 9
    [099] The procedure of example 8 was repeated to produce compounds containing 50 phr of SBR, 50 phr of natural rubber, 30 phr of silica, and 30 phr of carbon black. All other conditions were maintained according to example 8. The results of the physical tests on the compounds (samples marked No. 13-16), as shown in Table 7 and Figure 4, demonstrated superior resistance to the functionalized polymer bearing of the present invention ( sample No. 16), and for the polymer functionalized only with the functional initiator (sample No. 14) compared to sample 15, as reflected in the delta tangent measured at 60C and 5% deformation. These results suggest a weak interaction of the bifunctionalized elastomer with the silica and carbon black filler, compared to the data in examples 6-8. Apparently, the interaction with the carbon black is predominantly due to the functional initiator, although the initiator and the functional terminator improve the interaction of the bifunctionalized elastomer with silica. Table 7

    * Functionality: NF = not functionalized; Fl = functionalized initiator; FT = functionalized terminator. Example 10
    [0100] The procedure of example 8 was repeated to produce the compound containing 50 phr of SBR, 50 phr of natural rubber and 60 phr of carbon black, without silica. All other conditions were maintained according to example 8. The results of the physical tests on the compounds (marked samples No. 5-8), as shown in table 8 and figure 5 demonstrate improved rolling resistance for the polymer with functionalized initiator (sample 18 ) and no improvement for the polymer with functionalized terminator (sample 19), suggesting little or no benefit from the bifunctionalized elastomer in all carbon black rubber compounds. Table 8

    * Functionality: NF = not functionalized; Fl = functionalized initiator; FT = functionalized terminator.
    [0101] In summary, the data in the examples illustrates that the bifunctionalized elastomer of the present invention demonstrates improved rolling resistance when used in a rubber compound with a silica filler or with a mixture of silica and carbon black when compared to elastomer functionalized by the terminator or the elastomer functionalized by the initiator. However, no benefit of the bifunctionalized elastomer is seen in rubber compounds containing carbon black filler, without silica, as functionalization due to the functional terminator apparently has little interaction with carbon black. These results support the use of the bifunctionalized elastomer in the rubber compound with silica or mixture of silica and carbon black, especially with a weight ratio of silica to carbon black greater than or equal to one.
    [0102] Although certain representative modalities and details have been demonstrated only to illustrate the present invention, it will be clear to those skilled in the art that various changes and modifications can be made without departing from the scope of the invention.
    权利要求:
    Claims (15)
    [0001]
    1. Rubber composition comprising: a bifunctionalized elastomer comprising the reaction product of 1) a live anionic elastomeric polymer activated with a functional initiator and 2) a functional polymerization terminator, CHARACTERIZED by the fact that the live anionic elastomeric polymer activated with a functional initiator has formula AYLi, where Y is a divalent polymer radical, Li is a lithium atom attached to a carbon atom of Y, and A is an amine containing radical presenting formula X
    [0002]
    2. Rubber composition, according to claim 1, CHARACTERIZED by the fact that the filler comprises from 10 phr to 100 phr of silica.
    [0003]
    3. Rubber composition according to claim 1 or 2, CHARACTERIZED by the fact that the rubber composition comprises carbon black and silica, and in which the weight ratio of silica to carbon black is greater than or equal the one.
    [0004]
    Rubber composition according to any one of claims 1 to 3, CHARACTERIZED by the fact that also at least one additional elastomer based on diene selected from the group consisting of styrene-butadiene rubber, polybutadiene, natural and poly rubber synthetic isoprene.
    [0005]
    Rubber composition according to any one of claims 1 to 4, CHARACTERIZED by the fact that the live anionic elastomer is derived from at least one diene monomer and optionally at least one aromatic vinyl monomer.
    [0006]
    Rubber composition according to any one of claims 1 to 5, CHARACTERIZED by the fact that the live anionic elastomer is derived from at least one of isoprene and butadiene, and optionally of styrene.
    [0007]
    Rubber composition according to any one of claims 1 to 6, CHARACTERIZED by the fact that the live anionic elastomer is derived from butadiene and styrene.
    [0008]
    Rubber composition according to any one of claims 1 to 7, CHARACTERIZED by the fact that the polymerization terminator of formula I: (i) ESTI, 1-ethoxy-3,7,10-trimethylsilatran; or (ii) CSTI, 1- (3-chloropropyl) -3,7,10-trimethylsilatran; or (iii) BSTI, 1 -isobutyl-3,7,10-trimethylsilatran; or (iv) OSTI, 1-octyl-3,7,10-trimethylsilatran; or (v) BIPOS, 1,2-bis (3,7,10-trimethylsilatran) ethane.
    [0009]
    Rubber composition according to any one of claims 1 to 8, CHARACTERIZED by the fact that the polymerization terminator of formula I is selected from the group consisting of the following structures:
    [0010]
    10. Rubber composition, according to claims 1 to 9, CHARACTERIZED by the fact that the polymerization terminator of formula I has the structure:
    [0011]
    11. Rubber composition according to any one of claims 1 to 10, CHARACTERIZED by the fact that the polymerization terminator of formula I has the structure:
    [0012]
    12. Rubber composition according to any one of claims 1 to 11, CHARACTERIZED by the fact that the structure of formula X is selected from the group consisting of 3 - (N, N - dimethylamino) - 1 - propyl; 3 - (N, N - dimethylamino) - 2 - methyl - 1 - propyl; 3 - (N, N - dimethylamino) - 2,2 - dimethyl - 1 - propyl; 4 - (N, N-dimethylamino) - 1 - butyl; 5 - (N, N - dimethylamino) - 1 - pentyl; 6 - (N, N - dimethylamino) - 1 - hexyl; 8 - (N, N - dimethylamino) - 1 - propyl.
    [0013]
    13. Rubber composition according to any one of claims 1 to 12, CHARACTERIZED by the fact that the structure of formula X is selected from the group consisting of 3 - piperidine - 1 - propyl and 3 - pyrrolidine - 1 - propyl.
    [0014]
    14. Pneumatic CHARACTERIZED by the fact that it contains the rubber composition as defined in any one of claims 1 to 13.
    [0015]
    15. Pneumatic, according to claim 14, CHARACTERIZED by the fact that the rubber composition is comprised in the tire tread.
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    法律状态:
    2016-03-29| B03A| Publication of a patent application or of a certificate of addition of invention [chapter 3.1 patent gazette]|
    2018-09-18| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|
    2019-12-31| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|
    2020-05-12| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|
    2020-09-29| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 18/08/2015, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    US14/463,187|US9090730B1|2014-08-19|2014-08-19|Rubber composition and pneumatic tire|
    US14/463,187|2014-08-19|
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