Patent Application
20170313860
The present invention relates to a process for preparing a vulcanized rubber composition, the vulcanized rubber composition and a studless tire produced using the vulcanized rubber composition.
For running on ice and snow on a road, use of a studded tire and fitting of chains on tires have been employed so far, and in order to cope with an environmental problem such as a problem with a dust caused thereby, a studless tire has been developed. In order to enhance low temperature property of a studless tire, various improvements have been made from material and design points of view, and for example, a rubber composition prepared by compounding a large amount of mineral oil to a diene rubber being excellent in low temperature property, or the like has been used. However, generally as an amount of mineral oil is increased, abrasion resistance is decreased.
On an ice- and snow-covered road, as compared with a normal road surface, a friction coefficient of a tire decreases significantly and slippage is apt to occur. Therefore, not only low temperature property but also well-balanced performance on ice and snow (grip performance on ice and snow) and abrasion resistance are demanded for a studless tire. However, in many cases, performance on ice and snow is inconsistent with abrasion resistance, and it is generally difficult to improve the both properties simultaneously.
In order to improve performance on ice and snow and abrasion resistance in good balance, there is a prior art (Patent Document 1) for blending silica and a softening agent in large amounts. However, there is still a room for improvement from the viewpoint of well-balanced improvement of the both performances.
Further, a method of compounding a plurality of polymer (rubber) components (polymer blend) has been employed as a method of improving various tire performances such as low temperature property, performance on ice and snow and abrasion resistance in good balance. Specifically, a mainstream of the method is to blend some polymer components represented by a styrene-butadiene rubber (SBR), a butadiene rubber (BR), and a natural rubber (NR) as rubber components for a tire. This is a means for making good use of characteristic of each polymer component and deriving physical properties of a rubber composition which cannot be derived only by a single polymer component.
In this polymer blend, a phase structure (morphology) of each rubber component after vulcanization and a degree of distribution (localization) of a filler into each rubber phase will be important factors for deciding physical properties. Elements for deciding control of morphology and localization of a filler are very complicated, and various studies have been made in order to exhibit physical properties of a tire in good balance, but there is a room for improvement in any of the studies.
For example, Patent Document 2 discloses a technology of specifying a particle size of an island phase and a silica distribution in an sea-island matrix of a rubber composition for a tire tread comprising a styrene-butadiene rubber. However, regarding a concrete method enabling the morphology thereof to be realized, there are described only use of a master batch comprising silica and adjustment of a kneading time and a rotation torque of a rotor, and in such a method, the morphology is affected greatly by kneading and vulcanizing conditions, and therefore, stable control of the morphology is difficult. Further, the rubber component disclosed in examples is a combination of styrene-butadiene rubbers having relatively similar polarities. Therefore, it is apparent that the disclosed technology cannot be applied to the blending of rubber components having greatly different polarities, namely greatly different affinities for silica such as blending of a butadiene rubber and a natural rubber.
Particularly in the case of control of dispersion of silica between the phases using a master batch comprising silica, even if a desired morphology and silica dispersion are achieved temporarily, in many cases, the morphology and the silica dispersion change with a lapse of time and therefore, it was difficult to form a morphology being stable with a lapse of time of more than several months.
Patent Document 3 discloses a technology relating to control of a morphology and localization of silica in a compounding formulation comprising a natural rubber and a butadiene rubber. However, there is no description regarding the control of localization of silica into the butadiene rubber side in the case where the butadiene rubber which is disadvantageous to localization of silica forms a continuous phase.
A natural rubber is an important rubber component in a rubber composition for a tire, especially for a side wall because of its excellent mechanical strength, etc. However, in the case of blending with a butadiene rubber, localization of silica is apt to arise, and it is necessary to set the compounding formulation while controlling a distributing state of silica. However, so far a morphology and a distribution state of silica have not been checked sufficiently, and there was a case of a compounding formulation giving an insufficient exhibition of physical properties.
Furthermore, recently, there is a tendency of conducting modification of a natural rubber for enhancing affinity thereof for silica in order to aim at enhancement of fuel efficiency, which makes possibility of localization of silica into a natural rubber more significant.
Further, recently there are many cases of compounding a high cis butadiene rubber being excellent in abrasion resistance and low temperature grip performance. However, among diene rubbers, a high cis butadiene rubber is low in affinity particularly for silica and in a compounding system thereof with a natural rubber, there is a tendency that silica is hardly incorporated into a high cis butadiene rubber phase. Therefore, in a conventional system of compounding a high cis butadiene rubber, in some cases, a compounding formulation so as not to exhibit sufficient physical properties was employed while a morphology and a state of silica distribution were not confirmed.
In particular, in a rubber composition for a side wall, it is important to prepare a rubber composition comprising, as a continuous phase, a butadiene rubber having performance required for a side wall such as flex-crack resistance, and a technology of conducting control of silica localization on a continuous phase rubber component making a great contribution to abrasion resistance is essential.
Further, a natural rubber tends to hardly form a continuous phase as compared with a butadiene rubber, and in a compounding system where a natural rubber is blended in an amount of not more than 50 parts by mass based on 100 parts by mass of rubber components, such a tendency is further significant, and a so-called island phase is formed. Generally, a circumference of a rubber component being present in an island phase is solidified with a rubber component of a continuous phase, and therefore, there is a tendency that a hardness of the rubber component of an island phase increases and a rubber elasticity thereof is lowered. If a filler is localized, the tendency thereof increases more, and as a result, a difference in a hardness from the continuous phase rubber component increases, thereby easily causing a decrease in a rubber strength and abrasion resistance. A natural rubber is apt to have a hardness larger than a butadiene rubber even in the case of a single use thereof, and therefore, primarily it is not desirable that a difference in hardness further increases due to localization of silica. Therefore, development of a technology of not causing excessive localization of silica at a natural rubber side is important.
With respect to formation of a morphology of a plurality of polymer components in a rubber composition for a tire, only a compatible type (single phase) or in the case of incompatible type, only an sea-island phase structure, wherein a phase (island phase) of other particulate component is present in a continuous phase (sea phase), have been studied so far.
Therefore, in a system using a blend of a butadiene rubber and a natural rubber which is useful for exhibiting physical properties of a tire while polarities thereof are different from each other, development of technologies for morphology control and silica distribution to exhibit good physical properties of a rubber has been considered to be necessary.
As a result of recent global warming, there are increasing occasions to run a car with studless tires on a pavement, and therefore improvements on overall performances including dry performance and wet performance are demanded, and in particular, demand for improvement of wet performance affecting safety is strong. However, while further enhancement of performance on ice is demanded, a glass transition temperature of a rubber for a tread tends to be set lower. Therefore, it is difficult to secure wet performance simultaneously, and the present situation is such that it is difficult to improve performance on ice, wet performance and abrasion resistance in good balance using a conventional technology.
It is, therefore, an object of the present invention to provide a process for preparing a vulcanized rubber composition being capable of well-balanced improvement of performance on ice, wet performance and abrasion resistance, a vulcanized rubber composition being capable of well-balanced improvement of performance on ice, wet performance and abrasion resistance, and a studless tire comprising a tread composed of the vulcanized rubber composition.
The present invention relates to:
[1] a process for preparing a vulcanized rubber composition comprising:
(a) a step of preparing a master batch comprising a butadiene rubber and silica,
(b) a step of preparing a master batch comprising an isoprene rubber and silica,
(c) a step of kneading the master batch obtained in the step (a) and the master batch obtained in the step (b), and
(d) a step of vulcanizing a kneaded product obtained in the step (c), wherein the vulcanized rubber composition comprises:
a phase comprising the butadiene rubber and silica (BR phase), and a phase comprising the isoprene rubber and silica (IR phase),
wherein the BR phase and the IR phase are incompatible with each other,
the vulcanized rubber composition comprises a terpene resin of not less than 0.5 part by mass, preferably not less than 2 parts by mass, and preferably not more than 80 parts by mass, more preferably not more than 70 parts by mass, based on 100 parts by mass of rubber components comprising the isoprene rubber and the butadiene rubber, an abundance ratio α of silica in the BR phase 100 to 500 hours after completion of a vulcanization step satisfies the following Relation 1, and
a proportion β of the butadiene rubber satisfies the following Relation 2:
0.3≦α≦0.7 (preferably 0.5≦α≦0.6) (Relation 1)
0.4≦β≦0.8 (preferably 0.5≦β≦0.7) (Relation 2)
wherein α=Amount of silica in BR phase/(Amount of silica in BR phase+Amount of silica in IR phase) and β=Mass of butadiene rubber in vulcanized rubber composition/(Mass of butadiene rubber in vulcanized rubber composition+Mass of isoprene rubber in vulcanized rubber composition),
[2] the process for preparation of the above [1], wherein the master batch comprising a butadiene rubber and silica comprises not less than 40 parts by mass, preferably not less than 50 parts by mass, and preferably not more than 100 parts by mass, more preferably not more than 80 parts by mass of silica based on 100 parts by mass of the butadiene polymer,
[3] the process for preparation of the above [1] or [2], wherein the master batch comprising an isoprene rubber and silica comprises not less than 15 parts by mass, preferably not less than 30 parts by mass, and preferably not more than 100 parts by mass, more preferably not more than 80 parts by mass of silica based on 100 parts by mass of the isoprene rubber,
[4] the process for preparation of any one of the above [1] to [3], wherein the butadiene rubber has a cis-1,4 bond content of not less than 90%, preferably not less than 95%,
[5] the process for preparation of any one of the above [1] to [4], wherein the vulcanized rubber composition comprises 25 to 120 parts by mass, preferably 30 to 70 parts by mass of a filler and 15 to 80 parts by mass, preferably 20 to 70 parts by mass of a softening agent based on 100 parts by mass of a rubber component comprising the isoprene rubber and the butadiene rubber, and the filler comprises not less than 50% by mass, preferably not less than 70% by mass of silica based on a total amount of the filler,
[6] a vulcanized rubber composition comprising:
a phase comprising a butadiene rubber and silica (BR phase), and a phase comprising an isoprene rubber and silica (IR phase), wherein the BR phase and the IR phase are incompatible with each other,
the vulcanized rubber composition comprises a terpene resin of not less than 0.5 part by mass, preferably not less than 2 parts by mass, and preferably not more than 80 parts by mass, more preferably not more than 70 parts by mass, based on 100 parts by mass of rubber components comprising the isoprene rubber and the butadiene rubber, an abundance ratio α of silica in the BR phase 100 to 500 hours after completion of a vulcanization step satisfies the following Relation 1, and
a proportion β of the butadiene rubber satisfies the following Relation 2:
0.3≦α≦0.7 (preferably 0.5≦α≦0.6) (Relation 1)
0.4≦β≦0.8 (preferably 0.5≦β≦0.7) (Relation 2)
wherein α=Amount of silica in BR phase/(Amount of silica in BR phase+Amount of silica in IR phase) and β=Mass of butadiene rubber in vulcanized rubber composition/(Mass of butadiene rubber in vulcanized rubber composition+Mass of isoprene rubber in vulcanized rubber composition),
[7] the vulcanized rubber composition of the above [6], wherein the butadiene rubber has a cis-1,4 bond content of not less than 90%, preferably not less than 95%,
[8] the vulcanized rubber composition of the above [6] or [7], comprising 25 to 120 parts by mass, preferably 30 to 70 parts by mass of a filler and 15 to 80 parts by mass, preferably 20 to 70 parts by mass of a softening agent based on 100 parts by mass of the rubber components comprising the isoprene rubber and the butadiene rubber, wherein the filler comprises not less than 50% by mass, preferably not less than 70% by mass of silica based on the total amount of filler, and
[9] a studless tire comprising a tread composed of the vulcanized rubber composition of any one of the above [6] to [8].
According to the present invention, after an isoprene rubber and a butadiene rubber are respectively combined with silica to produce respective master batches, the obtained master batches are kneaded, thereby enabling performance on ice and abrasion resistance of an obtained vulcanized rubber composition to be improved in good balance, and by further compounding a terpene resin it is possible to enhance wet performance while maintaining compatibility of performance on ice with abrasion resistance. Further, by using this vulcanized rubber composition for a tire member such as a tread, a studless tire being excellent in these performances can be provided.
The process for preparing a vulcanized rubber composition which is one embodiment of the present invention comprises (a) a step of preparing a master batch comprising a butadiene rubber (BR) and silica (BR master batch), (b) a step of preparing a master batch comprising an isoprene rubber (IR) and silica (IR master batch), (c) a step of kneading the BR master batch obtained in the step (a) and the IR master batch obtained in the step (b), and (d) a step of vulcanizing a kneaded product obtained in the step (c), and the obtained vulcanized rubber composition has predetermined properties. As mentioned above, by kneading the master batches prepared separately by kneading each rubber component with silica, the silica which is prone to be localized in an isoprene rubber can also be localized in the butadiene rubber, and it is possible to easily prepare a vulcanized rubber composition which satisfies a predetermined abundance ratio α of silica in the BR phase, and satisfies a predetermined proportion β of the butadiene rubber, thereby enabling the silica to improve performance on ice without deteriorating excellent abrasion resistance of the isoprene rubber (IR). Further, by compounding the terpene resin in any one of the steps to enable the obtained vulcanized rubber composition to comprise the terpene resin, wet performance can be enhanced while maintaining compatibility of performance on ice with abrasion resistance.
A dispersion state of silica to the rubber components in the vulcanized rubber composition can be observed with a scanning electron microscope (SEM). For example, in
The process for preparing the BR master batch is not limited particularly, and the master batch can be prepared by kneading the BR and silica. The kneading method is not limited particularly, and a kneader, which is usually used in a rubber industry, such as a Banbury mixer or an open roll can be used. The master batch can also be prepared, for example, as a wet master batch obtainable by mixing a BR latex with an aqueous dispersion of silica.
A kneading temperature in the kneading step X1 is preferably not less than 80° C., more preferably not less than 100° C., further preferably not less than 140° C. The kneading temperature of not less than 80° C. enables a reaction of a silane coupling agent with silica to be advanced sufficiently and the silica to be dispersed satisfactorily and makes performance on snow and ice and abrasion resistance be easily improved in good balance. Further, the kneading temperature in the kneading step X1 is preferably not more than 200° C., more preferably not more than 190° C., further preferably not more than 180° C. The kneading temperature of not more than 200° C. tends to inhibit an increase in a Mooney viscosity and make processability satisfactory. Further, the temperature of a kneaded product at the time of discharge from the kneader can be from 130° C. to 160° C.
A kneading time in the kneading step X1 is not limited particularly, and is usually 30 seconds or more, preferably from 1 to 30 minutes, more preferably from 3 to 6 minutes.
The BR is not limited particularly, and it is possible to use, for example, BR having a cis-1,4 bond content of less than 50% (low cis BR), BR having a cis-1,4 bond content of not less than 90% (high cis BR), a rare earth-based butadiene rubber synthesized using a rare earth element catalyst (rare earth-based BR), BR having a syndiotactic polybutadiene crystal (SPB-containing BR), modified BR (high cis modified BR, low cis modified BR) and the like. Among these, it is preferable to use at least one selected from the group consisting of a high cis BR, a low cis BR and a low cis modified BR, and use of a high cis BR is more preferable.
Examples of the high cis BR include BR730 and BR51 available from JSR Corporation, BR1220 available from ZEON CORPORATION, BR130B, BR150B and BR710 available from Ube Industries, Ltd. and the like. Among the high cis BRs, those having a cis-1,4 bond content of not less than 95% are further preferable. These may be used alone or may be used in combination of two or more thereof. When the high cis BR is compounded, low temperature property and abrasion resistance can be enhanced. Examples of the low cis BR include BR1250 available from ZEON CORPORATION and the like. These may be used alone or may be used in combination of two or more thereof.
An amount of silica to be compounded in the kneading step X1 is preferably not less than 40 parts by mass, more preferably not less than 50 parts by mass based on 100 parts by mass of the BR. When the amount of silica is not less than 40 parts by mass, a sufficient effect of localizing the silica in the BR phase tends to be obtained. Further, the amount of silica to be compounded in the kneading step X1 is preferably not more than 100 parts by mass, more preferably not more than 80 parts by mass based on 100 parts by mass of the BR. When the amount of silica is not more than 100 parts by mass, dispersion of the silica is easy, and processability can be made satisfactory.
The silica is not limited particularly, and usual ones in tire industries, for example, silica (silicic acid anhydride) prepared by a dry method, silica (hydrous silicic acid) prepared by a wet method, and the like can be used.
A nitrogen adsorption specific surface area (N2SA) of silica is preferably not less than 70 m2/g, more preferably not less than 140 m2/g. When silica has N2SA of not less than 70 m2/g, sufficient reinforcing property can be obtained and breaking resistance and abrasion resistance can be made satisfactory. The N2SA of silica is preferably not more than 220 m2/g, more preferably not more than 200 m2/g. When the N2SA of silica is not more than 220 m2/g, dispersion of the silica is easy and processability can be made satisfactory. Herein, the N2SA of silica is a value measured by a BET method in accordance with ASTM D3037-81.
In the kneading step X1, it is preferable to knead a silane coupling agent together with the silica. The silane coupling agent is not particularly limited, and any silane coupling agents which have been used in rubber industries in combination with silica can be used. Examples thereof include sulfide silane coupling agents such as bis(3-triethoxysilylpropyl)tetrasulfide, bis(2-triethoxysilylethyl)tetrasulfide, bis(3-trimethoxysilylpropyl)tetrasulfide, bis(2-trimethoxysilylethyl)tetrasulfide, bis(3-triethoxysilylpropyl)trisulfide, bis(3-trimethoxysilylpropyl)trisulfide, bis(3-triethoxysilylpropyl)disulfide, bis(3-trimethoxysilylpropyl)disulfide, 3-trimethoxysilylpropyl-N,N-dimethylthiocarbamoyl tetrasulfide, 3-triethoxysilylpropyl-N,N-dimethylthiocarbamoyl tetrasulfide, 2-triethoxysilylethyl-N,N-dimethythiocarbamoyl tetrasulfide, 2-trimethoxysilylethyl-N,N-dimethylthiocarbamoyl tetrasulfide, 3-trimethoxysilylpropylbenzothiazolyl tetrasulfide, 3-triethoxysilylpropylbenzothiazole tetrasulfide, 3-triethoxysilylpropyl methacrylate monosulfide, and 3-trimethoxysilylpropyl methacrylate monosulfide; mercapto silane coupling agents such as 3-mercaptopropyltrimethoxysilane, 3-mercaptopropyltriethoxysilane, 2-mercaptoethyltrimethoxysilane, and 2-mercaptoethyltriethoxysilane; vinyl silane coupling agents such as vinyltriethoxysilane and vinyltrimethoxysilane; amino silane coupling agents such as 3-aminopropyltriethoxysilane, 3-aminopropyltrimethoxysilane, 3-(2-aminoethyl)aminopropyltriethoxysilane, and 3-(2-aminoethyl)aminopropyltrimethoxysilane; glycidoxy silane coupling agents such as γ-glycidoxypropyltriethoxysilane, γ-glycidoxypropyltrimethoxysilane. γ-glycidoxypropylmethyldiethoxysilane, and γ-glycidoxypropylmethyldimethoxysilane; nitro silane coupling agents such as 3-nitropropyltrimethoxysilane and 3-nitropropyltriethoxysilane; chloro silane coupling agents such as 3-chloropropyltrimethoxysilane, 3-chloropropyltriethoxysilane, 2-chloroethyltrimethoxysilane, and 2-chloroethyltriethoxysilane; and the like. These silane coupling agents may be used alone or may be used in combination of two or more thereof. Among these, from the view point of good reactivity with silica, sulfide silane coupling agents are preferred, and bis(3-triethoxysilylpropyl)disulfide is particularly preferred.
When the silane coupling agent is compounded, the content thereof is preferably not less than 3 parts by mass, more preferably not less than 6 parts by mass based on 100 parts by mass of silica. The content of silane coupling agent of not less than 3 parts by mass makes it possible to obtain satisfactory breaking strength. The content of silane coupling agent based on 100 parts by mass of silica is preferably not more than 12 parts by mass, more preferably not more than 10 parts by mass. The content of silane coupling agent of not more than 12 parts by mass makes it possible to obtain an effect offsetting increase in cost.
The IR master batch can be prepared by kneading the IR and silica. The kneading method and the kneading conditions are the same as in the above-mentioned kneading step X1. Further, the IR master batch can be prepared as a wet master batch obtained by mixing an IR latex with a water dispersion of silica in the same manner as in the kneading step X1.
The isoprene rubber to be used in the present invention is not limited particularly, and usual ones which have been used in rubber industries can be used, and there are, for example, natural rubbers such as SIR20, RSS#3 and TSR20. Further, in the present invention, the isoprene rubber includes a reformed natural rubber, a modified natural rubber, a synthetic isoprene rubber and a modified synthetic isoprene rubber.
An amount of silica compounded in the kneading step X2 is preferably not less than 15 parts by mass, more preferably not less than 30 parts by mass based on 100 parts by mass of the IR. When the compounding amount of silica is not less than 15 parts by mass, a sufficient effect of dispersing the silica can be obtained. Further, the amount of silica compounded in the kneading step X2 is preferably not more than 100 parts by mass, more preferably not more than 80 parts by mass based on 100 parts by mass of the IR. When the compounding amount of silica is not more than 100 parts by mass, dispersing of the silica can be easy and processability can be satisfactory.
The silica to be used in the kneading step X2 is not limited particularly, and is as explained in the X1 kneading step.
In the kneading step X2, too, it is preferable to knead a silane coupling agent together with the silica, and the silane coupling agent is as explained in the kneading step X1.
The BR master batch obtained in the kneading step X1 and the IR master batch obtained in the kneading step X2 are kneaded. Regarding the kneading method, a kneader, which is usually used in a rubber industry, such as a Banbury mixer, an open roll or the like can be used in the same manner as in the above-mentioned kneading steps X1 and X2, and the kneading can be carried out under the conditions usually employed in a rubber industry.
A kneading temperature in the kneading step Y is preferably not less than 80° C., more preferably not less than 100° C., further preferably not less than 145° C. When the kneading temperature is not less than 80° C., a reaction of the silane coupling agent with the silica can be fully advanced, and the silica can be dispersed satisfactorily, thereby making it easy to improve performance on snow and ice and abrasion resistance in good balance. Further, the kneading temperature in the kneading step Y is preferably not more than 200° C., more preferably not more than 190° C., further preferably not more than 160° C. When the kneading temperature is not more than 200° C., there is a tendency that increase in a Mooney viscosity can be inhibited and processability can be satisfactory. Furthermore, the temperature of a kneaded product at the time of discharge from the kneader can be from 130° C. to 160° C.
A kneading time in the kneading step Y is not limited particularly, and is usually 30 seconds or more, preferably from 1 to 30 minutes, more preferably from 2 to 6 minutes.
In the process for preparing the vulcanized rubber composition of the present invention, not less than 0.5 part by mass of a terpene resin is kneaded to 100 parts by mass of the rubber component comprising the isoprene rubber and the butadiene rubber in the finally obtained vulcanized rubber composition, in the X1 kneading step, the X2 kneading step, the Y kneading step or other steps in addition to the above-mentioned materials. By compounding the terpene resin, wet performance can be improved while compatibility of performance on ice with abrasion resistance is maintained. Therefore, when the obtained rubber composition is used on tire members such as a tread (particularly a cap tread), a studless tire being excellent in a balance between these performances can be provided. The step in which the terpene resin is kneaded is not limited particularly, and the X1 kneading step or the X2 kneading step is preferable.
Herein the “terpene resin” is a resin prepared using a natural material, and generally means a resin obtained by polymerizing, as a main monomer, a terpene compound contained in a plant essential oil obtained from a leaf, a trunk or a root of a plant. The terpene compound is generally a compound having a terpene as a basic structure which is a polymer of isoprene (C5H8) classified into monoterpene (C10H16), sesquiterpene (C15H24), diterpene (C20H32) or the like. Examples thereof include α-pinene, β-pinene, dipentene, limonene, myrcene, alloocimene, ocimene, α-phellandrene, α-terpinene, γ-terpinene, terpinolene, 1,8-cineol, 1,4-cineol, α-terpineol, β-terpineol, γ-terpineol, camphene, tricyclene, sabinene, para menthe dienes, carenes and the like.
Examples of the terpene resins include terpene resins prepared using the above-mentioned terpene compounds as a starting material, such as α-pinene resin, β-pinene resin, limonene resin, dipentene resin and β-pinene/limonene resin; aromatic modified terpene resins prepared using a terpene compound and an aromatic compound as starting materials; terpene phenolic resins prepared using a terpene compound and a phenolic compound as starting materials; hydrogenated terpene resins prepared by subjecting terpene resins to hydrogenation treatment; and the like.
Examples of the aromatic compounds as starting materials for the aromatic modified terpene resins include styrene, α-methylstyrene, vinyltoluene, divinyltoluene and the like. Further, examples of the phenolic compounds as starting materials for the terpene phenolic resins include phenol, bisphenol A, cresol, xylenol and the like.
A softening point of the terpene resin is preferably 150° C. or lower, more preferably 120° C. or lower. When the softening point of the terpene resin is 150° C. or lower, there is a tendency that the terpene resin is dispersed uniformly at the time of kneading and tackiness of the terpene resin is sufficient.
Commercially available terpene resins, for example, PX300N (available from YASUHARA CHEMICAL CO., LTD., softening point: 30° C.), PX1150N (available from YASUHARA CHEMICAL CO., LTD., softening point: 115° C.) and the like can be used suitably as the above-mentioned terpene resins.
A content of the terpene resin is 0.5 part by mass or more, preferably 2 parts by mass or more to 100 parts by mass of rubber component comprising the isoprene rubber and the butadiene rubber. When the content of the terpene resin is less than 0.5 part by mass, there is a problem that tackiness necessary for the processing is insufficient.
When the vulcanized rubber composition of the present invention is used for a tread of a tire, the content of the terpene resin is preferably not more than 80 parts by mass, more preferably not more than 70 parts by mass to 100 parts by mass of rubber component comprising the isoprene rubber and the butadiene rubber. When the rubber composition of the present invention is used for a tread of a tire, if the content of the terpene resin is not more than 80 parts by mass, tackiness and processability tend to be satisfactory.
In the process for preparing the vulcanized rubber composition of the present invention, various materials usually used in a rubber industry such as rubber components other than the IR and the BR, a filler such as carbon black, oil, wax, an antioxidant, stearic acid and zinc oxide may be kneaded as needed in the kneading step X1, the kneading step X2, the kneading step Y and other steps in addition to the above-mentioned materials.
Examples of the other rubber components include diene rubbers such as styrene-butadiene rubber.
Examples of carbon black include furnace black, acetylene black, thermal black, channel black, graphite, and the like, and these carbon blacks may be used alone or may be used in combination of two or more thereof. Among these, furnace black is preferable for the reason that low temperature property and abrasion resistance can be improved in good balance. A step of kneading carbon black is not limited particularly, and the X2-kneading is preferable for the reason that the silica is dispersed preferentially in the BR phase.
A nitrogen adsorption specific surface area (N2SA) of carbon black is preferably not less than 70 m2/g, more preferably not less than 90 m2/g from a viewpoint that sufficient reinforcing property and abrasion resistance can be obtained. Further, the N2SA of carbon black is preferably not more than 300 m2/g, more preferably not more than 250 m2/g from a viewpoint that dispersion thereof is good and heat generation hardly arises. The N2SA can be measured according to JIS K 6217-2 “Carbon black for rubber industry—Fundamental characteristics—Part 2: Determination of specific surface area—Nitrogen adsorption methods—Single-point procedures”.
When carbon black is compounded, the content thereof is preferably not less than 1 part by mass, more preferably not less than 5 parts by mass based on 100 parts by mass of the total rubber components. When the content of carbon black is not less than 1 part by mass, sufficient reinforcing property tends to be obtained. Further, the content of carbon black is preferably not more than 95 parts by mass, more preferably not more than 60 parts by mass, further preferably not more than 20 parts by mass. When the content of carbon black is not more than 95 parts by mass, good processability is obtained, heat generation can be inhibited, and abrasion resistance can be enhanced.
Oil is not limited particularly, and for example, a process oil, vegetable fats and oils, or a mixture thereof can be used. Examples of process oil include a paraffin process oil, an aromatic process oil, a naphthenic process oil, and the like. Examples of vegetable oils and fats include castor oil, cotton seed oil, linseed oil, rapeseed oil, soybean oil, palm oil, coconut oil, peanut oil, rosin, pine oil, pine tar, tall oil, corn oil, rice oil, safflower oil, sesame oil, olive oil, sunflower oil, palm kernel oil, tsubaki oil, jojoba oil, macadamia nut oil, tung oil, and the like. Among these, process oils are preferred, and particularly use of a paraffin process oil is preferred.
While oils may not be compounded, it is preferable to compound not less than 10 parts by mass of oils based on 100 parts by mass of total rubber components, from a viewpoint that performance on snow and ice required for a studless is easily exhibited. Further, the oil content is preferably not more than 55 parts by mass, more preferably not more than 40 parts by mass. When the oil content is not more than 55 parts by mass, there is a tendency that deterioration of processability, lowering of abrasion resistance and lowering of resistance to aging are prevented.
An anti-oxidant to be compounded in the present invention can be properly selected from amine, phenol and imidazole compounds, and carbamic acid metal salts. These anti-oxidants may be used alone or may be used in combination of two or more thereof. Among them, amine anti-oxidants are preferred for the reason that an ozone resistance can be improved significantly and an effect for exhibiting such a property can be maintained for a long period of time, and N-(1,3-dimethylbutyl)-N′-phenyl-p-phenylenediamine is more preferred.
When the anti-oxidant is compounded, its content is preferably not less than 0.5 part by mass, more preferably not less than 1.0 part by mass, further preferably not less than 1.2 parts by mass based on 100 parts by mass of total rubber components. When the content of anti-oxidant is not less than 0.5 part by mass, sufficient ozone resistance tends to be obtained. Further, the content of anti-oxidant is preferably not more than 8 parts by mass, more preferably not more than 4 parts by mass, further preferably not more than 2.5 parts by mass. When the content of anti-oxidant is not more than 8 parts by mass, there is a tendency that discoloration can be inhibited and bleeding can be inhibited.
Any of wax, stearic acid and zinc oxide which is used usually in rubber industries can be used suitably.
A vulcanizing agent and a vulcanization accelerator as required are kneaded with the kneaded product obtained in the above-mentioned Y-kneading in the kneading step F to obtain a kneaded product (un-vulcanized rubber composition). Then, this un-vulcanized rubber composition is molded into a required form, which is laminated as a tire member, followed by vulcanization in accordance with a known method to obtain the vulcanized rubber composition of the present invention.
In the kneading step F, the kneading is started from about 50° C. when the kneader is cold and from about 80° C. when the kneader is used continuously, and can be performed until the temperature of a kneaded product at the time of discharge from the kneader reaches 95° C. to 110° C.
A vulcanizing temperature is preferably not less than 120° C., more preferably not less than 140° C., and is preferably not more than 200° C., more preferably not more than 180° C., from a viewpoint that the effect of the present invention can be obtained satisfactorily. A vulcanizing time is preferably from 5 to 30 minutes from a viewpoint that the effect of the present invention can be obtained satisfactorily.
A vulcanizing agent is not limited particularly, and those usually used in rubber industries can be used, and sulfur atom-containing vulcanizing agents are preferred and a sulfur powder is used particularly preferably.
A vulcanization accelerator also is not limited particularly, and those usually used in rubber industries can be used.
The vulcanized rubber composition obtained by the above-mentioned process for preparing the vulcanized rubber composition of the present invention comprises the phase comprising a butadiene rubber and silica (BR phase), and the phase comprising an isoprene rubber and silica (IR phase), and the BR phase and the IR phase are incompatible with each other. Herein, “incompatible” means, for example, that an averaged equivalent circle radius of a discontinuous phase in the section of the vulcanized rubber composition is 100 nm or more, and can be easily evaluated, for example, by an image taken with a scanning electron microscope (SEM).
Further, in the vulcanized rubber composition obtained by the process for preparing the vulcanized rubber composition of the present invention, since the abundance ratio α of silica in the BR phase satisfies the following Relation 1, abrasion resistance of the vulcanized rubber composition is enhanced, and when the vulcanized rubber composition is used for a tread, performance on ice is also enhanced. Herein “the abundance ratio α of silica in the BR phase” is an index indicating how much amount of silica among the total amount of silica in the rubber composition is present in the BR phase 100 to 500 hours after completion of the vulcanization step.
0.3≦α≦0.7 (Relation 1)
wherein, α=Amount of silica in BR phase/(Amount of silica in BR phase+Amount of silica in IR phase).
Specifically, for example, the vulcanized rubber composition is subjected to surface shaping to obtain a sample. In a photograph of a scanning electron microscope (SEM) from one sample, ten regions of 2 μm×2 μm which do not overlap each other are selected. In each region, an area of silica per unit area and an area of silica in the BR phase per unit area are measured to calculate the abundance ratio α of silica in the BR phase. When it can be confirmed that a difference between a maximum value and a minimum value of the γ in the ten regions is within 10%, an average of the γ in the ten regions is specified as α.
The abundance ratio α of silica in the BR phase is not less than 0.3, preferably not less than 0.5. When the abundance ratio α of silica in the BR phase is less than 0.3, there is a tendency that abrasion resistance and performance on ice cannot be expected to be improved and are rather deteriorated. The abundance ratio α of silica in the BR phase is not more than 0.7, preferably not more than 0.6. When the abundance ratio α of silica in the BR phase is more than 0.7, there is a tendency that particularly abrasion resistance cannot be expected to be improved and is rather deteriorated.
The vulcanized rubber composition obtained by the process for preparing the vulcanized rubber composition of the present invention is one in which the proportion β of the butadiene rubber satisfies the following Relation 2:
0.4≦β≦0.8 (Relation 2)
wherein β=Mass of butadiene rubber in vulcanized rubber composition/(Mass of butadiene rubber in vulcanized rubber composition+Mass of isoprene rubber in vulcanized rubber composition). The mass of the butadiene rubber in the vulcanized rubber composition and the mass of the isoprene rubber in the vulcanized rubber composition correspond to the contents of the respective rubbers compounded when preparing the vulcanized rubber composition.
The proportion β of the butadiene rubber is not less than 0.4, preferably not less than 0.5. When the proportion β of the butadiene rubber is less than 0.4, there is a tendency that enhancement of the obtained performance on ice cannot be expected. Further the proportion β of the butadiene rubber is not more than 0.8, preferably not more than 0.7. When the proportion β of the butadiene rubber exceeds 0.8, the content of isoprene rubber becomes smaller and there is a tendency that sufficient breaking strength and abrasion resistance cannot be obtained.
In the vulcanized rubber composition obtained by the process for preparing the vulcanized rubber composition of the present invention, the total content of the butadiene rubber and the isoprene rubber in the total rubber components is preferably not less than 70% by mass, more preferably not less than 80% by mass, further preferably 90% by mass, particularly preferably 100% by mass. As the total content of the butadiene rubber and the isoprene rubber is higher, low temperature property is excellent and required performance on snow and ice can be exhibited. Therefore, it is preferable to use rubber components consisting of the butadiene rubber and the isoprene rubber.
By the above-mentioned process for preparing the vulcanized rubber composition of the present invention, silica which is easily localized in IR can be also localized in the BR, thereby making it possible to disperse silica in the whole vulcanized rubber composition. Thus, performance on ice can be improved by silica without impairing good abrasion resistance of the isoprene rubber, and these performances can be obtained in good balance.
A vulcanized rubber composition according to another embodiment of the present invention is a vulcanized rubber composition having the phase comprising the butadiene rubber and silica (BR phase) and the phase comprising the isoprene rubber and silica (IR phase), wherein the BR phase and the IR phase are incompatible with each other, the vulcanized rubber composition comprises the terpene resin of not less than 0.5 part by mass, based on 100 parts by mass of rubber components comprising the isoprene rubber and the butadiene rubber, an abundance ratio α of silica in the BR phase 100 to 500 hours after completion of the vulcanization step satisfies the following Relation 1, and the proportion β of the butadiene rubber satisfies the following Relation 2:
0.3≦α≦0.7 (Relation 1)
0.4≦β≦0.8 (Relation 2)
wherein α=Amount of silica in BR phase/(Amount of silica in BR phase+Amount of silica in IR phase) and β=Mass of butadiene rubber in vulcanized rubber composition/(Mass of butadiene rubber in vulcanized rubber composition+Mass of isoprene rubber in vulcanized rubber composition), and the vulcanized rubber composition can be prepared, for example, by the above-mentioned process for preparing the vulcanized rubber composition of the present invention.
The explanation made herein on the vulcanized rubber composition is applicable to not only the above-mentioned vulcanized rubber composition according to one embodiment of the present invention but also the vulcanized rubber composition obtained by the above-mentioned process for preparing the vulcanized rubber composition according to one embodiment of the present invention, and the statements made herein in the explanation on the process for preparing the vulcanized rubber composition according to one embodiment of the present invention relating to compounding ratios of various materials, properties of the obtained vulcanized rubber composition and the like are also applicable to the above-mentioned vulcanized rubber composition according to one embodiment of the present invention.
In the vulcanized rubber composition of the present invention, the butadiene rubber forms a sea phase and the isoprene rubber forms an island phase and the abundance ratio of silica in the butadiene rubber is 30% or more. When sufficient localization of silica in the butadiene rubber is not seen, namely when the abundance ratio of silica in the BR phase is less than 0.3, since a hardness of the isoprene rubber as such tends to be larger than that of the butadiene rubber, a further difference in hardness arises due to location of silica and lowering of abrasion resistance tends to be seen.
It is preferable that the vulcanized rubber composition of the present invention comprises 25 to 120 parts by mass of a filler and 15 to 80 parts by mass of a softening agent based on 100 parts by mass of rubber components comprising the isoprene rubber and the butadiene rubber.
A content of filler is preferably not less than 25 parts by mass, more preferably not less than 30 parts by mass based on 100 parts by mass of rubber components. When the filler content is not less than 25 parts by mass, there is a tendency that abrasion resistance and breaking resistance become satisfactory. Also, the filler content is preferably not more than 120 parts by mass, more preferably not more than 70 parts by mass. When the filler content is not more than 120 parts by mass, there is a tendency that processability and workability are enhanced and lowering of low temperature property due to an increased amount of filler is prevented. Examples of the filler include silica, carbon black, aluminum hydroxide and the like, and it is preferable that silica is blended in an amount of preferably not less than 50% by mass, more preferably not less than 70% by mass based on the total amount of filler.
The total silica content is preferably not less than 25 parts by mass, more preferably not less than 38 parts by mass, based on 100 parts by mass of the rubber components. When the total silica content is not less than 25 parts by mass, there is a tendency that abrasion resistance and breaking resistance become satisfactory. Further, the total silica content is preferably not more than 100 parts by mass, more preferably not more than 80 parts by mass, based on 100 parts by mass of the rubber components. When the total silica content is not more than 100 parts by mass, there is a tendency that processability and workability are enhanced and lowering of low temperature property due to an increased amount of silica is prevented.
A content of the softening agent is preferably not less than 15 parts by mass, more preferably not less than 20 parts by mass based on 100 parts by mass of the rubber components. When the content of the softening agent is not less than 15 parts by mass, there is a tendency that performance on snow and ice required for a studless tire is exhibited and wet performance is enhanced. Also, the content of the softening agent is preferably not more than 80 parts by mass, more preferably not more than 70 parts by mass. When the content of the softening agent is not more than 80 parts by mass, there is a tendency that lowering of processability, lowering of abrasion resistance and deterioration of resistance to aging are prevented. Examples of the softening agent include an aromatic oil, a naphthenic oil, a paraffinic oil, a terpene resin, and the like.
The vulcanized rubber composition according to one embodiment of the present invention and the vulcanized rubber composition obtained by the process for preparing the vulcanized rubber composition according to one embodiment of the present invention can be used for tire application, for example, tire members such as a tread, a carcass, a side wall and a bead as well as other industrial products such as a vibration proof rubber, a belt and a hose. Particularly, from the viewpoint of satisfactory performance on ice and abrasion resistance, the vulcanized rubber composition is used suitably on a tread, and in the case of a tread of two-layer structure comprising a cap tread and a base tread, is suitably used on the cap tread.
The studless tire of the present invention can be produced by a usual method using the vulcanized rubber composition according to one embodiment of the present invention. Namely the rubber composition of the present invention is extrusion-processed into a shape of a tread of a tire in its unvulcanized state, and further, the obtained extruded product is laminated with other tire parts to form an unvulcanized tire on a tire molding machine by a usual forming method. The studless tire of the present invention can be produced by heating and pressurizing this unvulcanized tire in a vulcanizer.
The present invention is explained below by means of Examples, but is not limited to only the Examples.
Various kinds of chemicals used in Examples and Comparative Examples are collectively shown below.
Butadiene rubber (BR1): BR730 available from JSR Corporation (cis-1,4 content: 95%)
Butadiene rubber (BR2): BR1250 available from ZEON CORPORATION (cis-1,4 content: 45%)
Isoprene rubber (IR1): Natural rubber (NR) (RSS#3)
Isoprene rubber (IR2): Natural rubber (NR) (TSR20)
Carbon black: DIABLACK I (ISAF carbon, N2SA: 114 m2/g, average particle size: 23 nm) available from Mitsubishi Chemical Corporation
Silica: ULTRASIL (registered trade mark) VN3 (N2SA: 175 m2/g) available from EVONIK INDUSTRIES AG
Silane coupling agent: Si266 available from EVONIK INDUSTRIES AG
Terpene resin: Terpene resin PX300N available from YASUHARA CHEMICAL CO., LTD. (softening point: 30° C.)
Mineral oil: PS-32 (paraffinic process oil) available from Idemitsu Kosan Co., Ltd.
Stearic acid: Stearic acid “Kiri” available from NOF CORPORATION
Zinc oxide: Zinc oxide II available from MITSUI MINING & SMELTING CO., LTD.
(N-(1,3-dimethylbutyl)-N-phenyl-p-phenylenediamine) available from OUCHI SHINKO CHEMICAL INDUSTRIAL CO., LTD.
Wax: Ozoace wax available from NIPPON SEIRO CO., LTD.
Sulfur: Sulfur powder available from TSURUMI CHEMICAL INDUSTRY CO., LTD.
Vulcanization accelerator NS: NOCCELER NS (N-tert-butyl-2-benzothiazolylsulfenamide) available from OUCHI SHINKO CHEMICAL INDUSTRIAL CO., LTD.
Vulcanization accelerator DPG: NOCCELER D (1,3-diphenylguanidine) available from OUCHI SHINKO CHEMICAL INDUSTRIAL CO., LTD.
According to the formulation shown in step (I) of Tables 1 to 3, rubber components, silica and other materials were kneaded for three minutes with a 1.7 liter Banbury mixer at the compound temperature at the time of discharge from the mixer of 150° C. to obtain each of kneaded product comprising the butadiene rubber and silica (BR master batches) and kneaded product comprising the isoprene rubber and silica (IR master batches). Next, the both of the obtained kneaded products and other materials in accordance with the formulation shown in step (II) of Tables 1 to 3 were kneaded for two minutes at the compound temperature at the time of discharge from the mixer of 150° C. to obtain a kneaded product. To the obtained kneaded product were added sulfur and a vulcanization accelerator in accordance with the formulation shown in step (III) of Tables 1 to 3, followed by 5-minute kneading at a temperature of 150° C. using an open roll to obtain an un-vulcanized rubber composition. In the case where no compounding amount is described in the step (I) of Tables 1 to 3, only the step (II) was carried out.
Each of the obtained un-vulcanized rubber compositions was press-vulcanized for 12 minutes at 170° C. using a 0.5 mm thick metal mold to obtain each of vulcanized rubber compositions.
Further, each of the obtained vulcanized rubber compositions was formed into a shape of a cap tread which was then laminated with other tire members, followed by 15-minute vulcanization at 170° C. to produce a studless tire for test (tire size: 195/65R15).
The obtained vulcanized rubber compositions and test studless tires were stored at room temperature, and 200 hours after completion of vulcanization (about one week later), the following tests were performed to evaluate abrasion resistance, wet grip performance, performance on ice and localization of silica. Further, with respect to the vulcanized rubber compositions, a state thereof 200 hours after completion of vulcanization was compared with a state thereof one year after completion of vulcanization, and stability over time of a dispersed state of silica was evaluated. Each of test results is shown in Tables 1 to 3.
An abrasion loss of each vulcanized rubber composition was measured with a Lambourn abrasion testing machine being available from IWAMOTO Quartz GlassLabo Co., Ltd. under the conditions of a surface rotation speed of 50 m/min, a load of 3.0 kg, an amount of falling sand of 15 g/min, and a slip ratio of 20%, and a reciprocal of the abrasion loss was obtained. A reciprocal of the abrasion loss of Comparative Example 1 is assumed to be 100, and reciprocals of other abrasion losses are indicated by indexes. The larger the index is, the more excellent the abrasion resistance is.
Each of the test tires were mounted on all wheels of a vehicle (a 2000 cc domestic FF car), and a braking distance from an initial speed of 100 km/h was measured on a wet asphalt road surface. The result is indicated by an index. The larger the index is, the more excellent the wet skid performance (wet grip performance) is. The index is calculated by the following equation.
(Index of wet grip performance)=(Braking distance of Reference Comparative Example)/(Braking distance of each compounding formulation)×100
In-vehicle running on ice surface was carried out under the following conditions using studless tires of Examples and Comparative Examples, and performance on ice was evaluated. The test was performed at the test course of Sumitomo Rubber Industries, Ltd. in Nayoro, Hokkaido, and air temperature on snow was −2° C. to −6° C. The test tires were mounted on a 2000 cc domestic FR car, and a lock brake was applied at a speed of 30 km/hr. A stopping distance required for stopping the car after putting on the lock brake was measured, and was indicated by a value calculated by the following equation based on the distance of Comparative Example 1.
(Performance on ice)=(Stopping distance of Comparative Example 1)/(Stopping distance of each compounding formulation)×100
A vulcanized rubber composition was subjected to surface shaping and observed with a scanning electron microscope (SEM). The morphology of each phase could be confirmed by comparison of a contrast. As a result, in Examples and Comparative Examples, it was confirmed that the phase comprising the butadiene rubber (BR phase) and the phase comprising the isoprene rubber (IR phase) are incompatible with each other. The BR phase formed a sea phase and the IR phase formed an island phase, and in Examples, silica was dispersed in both of the BR phase and the IR phase.
Silica can be observed in the form of particulate. In an SEM photograph of one sample, ten regions of 2 μm×2 μm each which do not overlap each other were selected. In each region, an area of silica per unit area of each phase was measured, and an abundance ratio γ of the silica of the BR phase was calculated. After confirming that a difference between the maximum ratio and the minimum ratio among the ratios γ of the ten regions is within 10%, an average of the ratios γ in the ten regions was obtained and indicated by α.
With respect to the same vulcanized rubber composition, an abundance ratio α of silica in the BR phase in a state one year after completion of vulcanization was measured in the same manner as above. Then, a rate of change of the abundance ratio α of silica in the BR phase in a state one year after completion of vulcanization to an abundance ratio α of silica in the BR phase in a state 200 hours after completion of vulcanization was determined.
Rate of change (%)=|α(one year after)−α(200 hours after)|/α(200 hours after)×100
The stability over time of a dispersed state of silica of each of Examples and Comparative Examples was evaluated in accordance with the following criteria for evaluation. The smaller the rate of change is, the more satisfactory the evaluation result is.
A: Rate of change being within 10%.
B: Rate of change exceeding 10% and not more than 30%.
C: Rate of change exceeding 30%.
From the results shown in Tables 1 to 3, it is seen that by the process of preparing the two kinds of master batches, one comprising the BR and another one comprising the IR, wherein each of the master batches comprises silica, and then kneading the master batches, the vulcanized rubber composition having a satisfactory abundance ratio α of silica in the BR phase can be prepared, and stability of dispersion of silica is satisfactory. Further, it is seen that the vulcanized rubber composition having such a satisfactory abundance ratio α of silica in the BR phase can improve abrasion resistance and performance on ice in good balance. Further, it is seen that the wet grip performance can be enhanced while maintaining compatibility of performance on ice with abrasion resistance by compounding the terpene resin.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2014-232215 | Nov 2014 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2015/082010 | 11/13/2015 | WO | 00 |
