WO2009104555A1 - 変性ジエン系ゴム及びその製造方法、並びにそれを用いたゴム組成物及びタイヤ - Google Patents
変性ジエン系ゴム及びその製造方法、並びにそれを用いたゴム組成物及びタイヤ Download PDFInfo
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- WO2009104555A1 WO2009104555A1 PCT/JP2009/052544 JP2009052544W WO2009104555A1 WO 2009104555 A1 WO2009104555 A1 WO 2009104555A1 JP 2009052544 W JP2009052544 W JP 2009052544W WO 2009104555 A1 WO2009104555 A1 WO 2009104555A1
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- diene rubber
- rubber
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- latex
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L15/00—Compositions of rubber derivatives
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
- B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
- B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
- B60C1/0016—Compositions of the tread
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08C—TREATMENT OR CHEMICAL MODIFICATION OF RUBBERS
- C08C19/00—Chemical modification of rubber
- C08C19/22—Incorporating nitrogen atoms into the molecule
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L19/00—Compositions of rubbers not provided for in groups C08L7/00 - C08L17/00
- C08L19/006—Rubber characterised by functional groups, e.g. telechelic diene polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
- C08K3/36—Silica
Definitions
- the present invention relates to a modified diene rubber, a method for producing the same, and a rubber composition and a tire using the modified diene rubber, and in particular, can be produced at a lower cost than before, and is excellent in low loss, wear resistance, and fracture resistance.
- the present invention relates to a rubber composition.
- a rubber composition used for tire treads or the like a rubber composition having a low tan ⁇ (hereinafter referred to as low loss property) and excellent in low heat generation properties is required.
- a rubber composition for a tread is required to have excellent wear resistance and fracture characteristics in addition to low loss.
- wear resistance and fracture characteristics of the rubber composition it is necessary to improve the affinity between the rubber component and the filler such as carbon black and silica in the rubber composition. It is valid.
- a modification is obtained by adding a polar group-containing monomer to natural rubber latex, graft-polymerizing the polar group-containing monomer to natural rubber molecules in natural rubber latex, and further coagulating and drying.
- natural rubber as a rubber component improves the rubber composition's affinity with the filler and improves the rubber composition's reinforcement, improving the low loss, wear resistance and fracture characteristics of the rubber composition.
- the technique to make is disclosed (refer patent document 1).
- the modified natural rubber in which the polar group is present at the molecular end is more effective for the filler than the modified natural rubber in which the polar group is present in the molecular chain. It is expected that the interaction can be enhanced, and in the technique for actually modifying the synthetic rubber described above, a higher modification effect is obtained with the terminal-modified synthetic rubber for the same reason.
- a polar group can be introduced into the main chain of the natural rubber molecule, but in this case, the position where the polar group is introduced is not limited to the molecular end.
- a metathesis catalyst and a polar group-containing olefin are used as a technique for further improving the low loss property, wear resistance and fracture property of the rubber composition by modifying the end of the main chain of the natural rubber molecule.
- a technique for introducing a polar group at the end of the main chain of a natural rubber molecule has been disclosed (see Patent Document 2).
- an object of the present invention is a modified diene rubber that can be produced at a lower cost than before and that can be used as a rubber component of the rubber composition to improve the low loss and wear resistance of the rubber composition.
- the object is to provide a method for producing the modified diene rubber.
- Another object of the present invention is to provide a rubber composition using the modified diene rubber and a tire using the rubber composition.
- the present inventor easily oxidizes the diene rubber latex and then adds a polar group-containing hydrazide compound to easily attach the polar group to the end of the molecular chain of the diene rubber. Further, it was found that low loss and wear resistance can be greatly improved by using the modified diene rubber thus obtained as a rubber component. Completed the invention.
- the modified diene rubber of the present invention is characterized in that after diene rubber latex is oxidized, a polar group-containing hydrazide compound is added to the end of the molecular chain of the diene rubber.
- the diene rubber latex is a natural rubber latex.
- the addition amount of the polar group-containing hydrazide compound is 0.01 to 5.0% by mass with respect to the rubber component in the diene rubber latex. It is characterized by.
- the polar group of the polar group-containing hydrazide compound is an amino group, imino group, nitrile group, ammonium group, imide group, amide group, hydrazo group, azo group, diazo group. And at least one selected from the group consisting of a group, a hydroxyl group, a carboxyl group, a carbonyl group, an epoxy group, an oxycarbonyl group, a nitrogen-containing heterocyclic group, an oxygen-containing heterocyclic group, a tin-containing group, and an alkoxysilyl group.
- modified diene rubber of the present invention is characterized in that the weight average molecular weight in terms of polystyrene measured by gel permeation chromatography is 200,000 or more.
- the diene rubber latex is oxidized by adding a carbonyl compound to the diene rubber latex and oxidizing it.
- the oxidation is preferably performed by air oxidation or ozone oxidation.
- the air oxidation is performed in the presence of a radical generator.
- the carbonyl compound is an aldehyde and / or a ketone.
- the radical generator is selected from the group consisting of a peroxide radical generator, a redox radical generator and an azo radical generator. .
- R is an amino group, imino group, nitrile group, ammonium group, imide group, amide group, hydrazo group, azo group, diazo group, hydroxyl group, carboxyl group, carbonyl group, epoxy group as a substituent.
- the first production method of the modified diene rubber of the present invention is to oxidize and further coagulate the diene rubber latex, add a polar group-containing hydrazide compound to the coagulated product of the obtained oxidized diene rubber latex,
- the polar group-containing hydrazide compound is added to the end of the molecular chain of the diene rubber in the coagulated product of the oxidized diene rubber latex and dried.
- the second production method of the modified diene rubber of the present invention comprises oxidizing the diene rubber latex, further coagulating and drying, adding a polar group-containing hydrazide compound to the resulting oxidized diene rubber, A group-containing hydrazide compound is subjected to an addition reaction at the end of the molecular chain of the diene rubber in the oxidized diene rubber.
- the diene rubber latex is oxidized, a polar group-containing hydrazide compound is added to the obtained oxidized diene rubber latex, and the polar group-containing hydrazide compound is added. It is characterized in that an addition reaction is carried out at the end of the molecular chain of the diene rubber in the oxidized diene rubber latex, followed by coagulation and drying.
- the rubber composition of the present invention is characterized by using the above-mentioned modified diene rubber, and the tire of the present invention is characterized by using the rubber composition for any of tire members.
- a modified diene rubber that can be produced at a lower cost than before and that can be used as a rubber component of a rubber composition to significantly improve the low loss and wear resistance of the rubber composition;
- a method for producing a modified diene rubber can be provided.
- the modified diene rubber of the present invention is characterized in that after diene rubber latex is oxidized, a polar group-containing hydrazide compound is added to the end of the molecular chain of the diene rubber.
- a polar group exists at the end of the molecular chain of the diene rubber, for example, a modified diene system in which a polar group such as the modified natural rubber described in Patent Document 1 is present in the molecular chain. It has better affinity for various fillers such as carbon black and silica than rubber.
- the rubber composition using the modified diene rubber of the present invention as a rubber component is a rubber component compared to the rubber composition using the modified diene rubber having a polar group present in the molecular chain as a rubber component.
- the filler is highly dispersible, and the reinforcing effect of the filler is sufficiently exerted to improve wear resistance and low loss (low heat build-up). Further, by using the rubber composition for a tire, particularly a tread of the tire, the wear resistance can be remarkably improved while significantly reducing the rolling resistance.
- the diene rubber latex used for the oxidation reaction includes natural rubber latex, polyisoprene rubber latex, styrene-butadiene copolymer rubber latex, polybutadiene rubber latex, acrylonitrile-butadiene rubber latex, chloroprene rubber. Latex.
- the diene rubber latex may be used alone or in combination of two or more.
- synthetic rubber it is possible to introduce a polar group at the end of the molecular chain during the polymerization process, but natural rubber, which is a natural product, is not possible except by a method using a metathesis catalyst.
- any of field latex, ammonia-treated latex, centrifugal concentrated latex, deproteinized latex treated with a surfactant or an enzyme, and a combination of the above can be used.
- the oxidation of the diene rubber latex can be performed by a known method.
- the diene rubber latex dissolved in an organic solvent at a ratio of 1 to 30% by mass is oxidized by air in the presence of a metal oxidation catalyst to oxidize the diene rubber latex.
- a metal oxidation catalyst to oxidize the diene rubber latex.
- suitable metal species of the metal-based oxidation catalyst used for promoting air oxidation are cobalt, copper, iron, and the like, and salts and complexes with these chlorides and organic compounds are used.
- cobalt catalysts such as cobalt chloride, cobalt acetylacetonate, and cobalt naphthenate are preferable.
- Any organic solvent may be used as long as it does not react with the rubber and is not easily oxidized and dissolves the rubber.
- Various hydrocarbon solvents, aromatic hydrocarbon solvents, organic halogens can be used.
- a system solvent or the like is preferably used.
- the hydrocarbon solvent for example, hexane, gasoline or the like can be used.
- the aromatic hydrocarbon solvent for example, toluene, xylene, benzene and the like can be used.
- organic halogen solvent for example, chloroform, dichloromethane and the like can be used. Of these, aromatic hydrocarbon-based toluene is preferably used. It is also possible to use a mixed solvent of them and alcohol.
- the diene rubber latex can be oxidized by adding a carbonyl compound to the diene rubber latex and oxidizing the diene rubber latex.
- the carbonyl compound added to the diene rubber latex is appropriately added so that it is 20 vol% (V / V%) or less, preferably 0.5 to 10 vol% with respect to the latex volume regardless of the rubber content. It is. Even if the concentration of the carbonyl compound exceeds the above range, there is no problem.
- preferable examples of the carbonyl compound include various aldehydes and ketones.
- aldehydes examples include formaldehyde, acetaldehyde, propionaldehyde, n-butyraldehyde, n-valeraldehyde, caproaldehyde, heptaldehyde, phenylacetaldehyde, benzaldehyde, tolualdehyde, nitrobenzaldehyde, salicylaldehyde, anisaldehyde, vanillin, piperonal , Methylvaleraldehyde, isocaproaldehyde, paraformaldehyde and the like.
- ketones include acetone, methyl ethyl ketone, methyl n-propyl ketone, diethyl ketone, isopropyl methyl ketone, benzyl methyl ketone, 2-hexanone, 3-hexanone, isobutyl methyl ketone, acetophenone, propiophenone, n-butyrophenone, and benzophenone. And 3-nitro-4'-methylbenzophenone.
- Oxidation can be carried out by adding the above-mentioned carbonyl compound to the diene rubber latex.
- air oxidation is performed as an oxidation method, as described in JP-A-9-136903, air oxidation is performed.
- a radical generator for example, a peroxide radical generator, a redox radical generator, an azo radical generator and the like are preferably used.
- peroxide radical generators examples include benzoyl peroxide, di-t-butyl peroxide, potassium persulfate, ammonium persulfate, hydrogen peroxide, lauroyl peroxide, diisopropyl peroxycarbonate, dicyclohexyl peroxycarbonate, etc. it can.
- redox radical generator examples include cumene hydroxyperoxide and Fe (II) salt, hydrogen peroxide and Fe (II) salt, potassium persulfate or ammonium persulfate and sodium sulfite, sodium perchlorate and sodium sulfite, cerium sulfate ( IV) and alcohols, amines or starches, peroxides such as benzoyl peroxide and lauroyl peroxide, dimethylaniline, tert-butyl hydroperoxide, tetraethylenepentamine and the like.
- azo radical generator examples include azobisisobutyronitrile, methyl azobisisobutyrate, azobiscyclohexanecarbonitrile, azobisisobutylamidine hydrochloride, 4,4′-azobis-4-cyanovaleric acid, and the like.
- the above radical generator is used by being dissolved or dispersed in the diene rubber latex.
- the amount of radical generator added is suitably 0.01 to 5% by mass, preferably 0.05 to 1% by mass, based on the diene rubber solid content. If the concentration of the radical generator is lower than the above range, the rate of air oxidation is slow and impractical. On the other hand, when the concentration of the radical generator exceeds the above range, molecular chain scission proceeds, and as the molecular weight decreases, the low loss property, wear resistance, and breaking strength of the rubber composition may deteriorate.
- the method for making the contact with air uniform is not particularly limited, for example, in addition to shaking in a shake flask, it can be easily performed by stirring, bubbling for blowing air, or the like.
- the temperature at which air oxidation proceeds is usually from room temperature to 100 ° C., but is not particularly limited.
- the reaction is usually completed in about 1 to 5 hours.
- an ozone-containing gas can be blown into a diene rubber latex, and the diene rubber latex can be oxidized by the oxidizing action of ozone.
- the decomposition reaction is accelerated by the addition of hydrogen peroxide.
- the diene rubber latex is oxidized by the above method, and then the polar group-containing hydrazide compound is added.
- a polar group-containing hydrazide compound may be added to the oxidized diene rubber latex obtained by oxidizing the diene rubber latex, or the obtained oxidized diene rubber latex is coagulated.
- a polar group-containing hydrazide compound may be added to the obtained diene rubber.
- the oxidized diene rubber latex obtained by the above method has a carbonyl group at the end of the diene rubber molecular chain.
- the polar group-containing hydrazide compound has high reactivity, and therefore, the carbonyl group at the end of the diene rubber molecule in the oxidized diene rubber latex or the oxidized diene rubber obtained by coagulating the oxidized diene rubber latex It reacts easily. Therefore, by adding a polar group-containing hydrazide compound to oxidized diene rubber latex or oxidized diene rubber, it is possible to easily and inexpensively introduce polar groups at the end of the diene rubber molecule without using an expensive catalyst. it can.
- the polar group-containing hydrazide compound is not particularly limited as long as it is a hydrazide compound having at least one polar group in the molecule.
- Preferred examples include a group, a nitrogen-containing heterocyclic group, an oxygen-containing heterocyclic group, a tin-containing group, and an alkoxysilyl group.
- These polar group-containing hydrazide compounds can be used alone or in combination of two or more.
- amino group-containing hydrazide compound examples include hydrazide compounds having at least one amino group selected from primary, secondary, and tertiary amino groups in one molecule. These amino group-containing hydrazide compounds can be used alone or in combination of two or more.
- Examples of the primary amino group-containing hydrazide compound include 2-aminoacetohydrazide, 3-aminopropionic hydrazide, 4-aminobutanoic hydrazide, 2-aminobenzohydrazide, 4-aminobenzohydrazide and the like.
- secondary amino group-containing hydrazide compounds include 2- (methylamino) acetohydrazide, 2- (ethylamino) acetohydrazide, 3- (methylamino) propionic acid hydrazide, and 3- (ethylamino) propionic acid hydrazide.
- tertiary amino group-containing hydrazide compounds include N, N-disubstituted aminoalkyl hydrazide compounds and N, N-disubstituted benzohydrazide compounds.
- these compounds include 2- (dimethylamino) acetohydrazide, 2- (diethylamino) acetohydrazide, 3- (dimethylamino) propionic acid hydrazide, 3- (diethylamino) propionic acid hydrazide, and 3- (dipropylamino).
- nitrogen-containing heterocyclic group instead of an amino group.
- nitrogen-containing heterocyclic group examples include pyrrole, histidine, imidazole, triazolidine, triazole, triazine, pyridine, pyrimidine, pyrazine, indole, quinoline. , Purine, phenazine, pteridine, melamine and the like.
- the nitrogen-containing heterocycle may contain other heteroatoms in the ring.
- examples of the hydrazide compound having a pyridyl group as a nitrogen-containing heterocyclic group include isonicotinohydrazide and picolinohydrazide. These nitrogen-containing heterocyclic group-containing hydrazide compounds may be used alone or in combination of two or more.
- hydrazide compound having a nitrile group examples include 2-nitroacetohydrazide, 3-nitropropionic hydrazide, 4-nitrobutanoic hydrazide, 2-nitrobenzohydrazide, and 4-nitrobenzohydrazide. These nitrile group-containing hydrazide compounds may be used alone or in a combination of two or more.
- hydroxyl group-containing hydrazide compound examples include hydrazide compounds containing at least one primary, secondary, or tertiary hydroxyl group in one molecule.
- examples of such hydroxyl group-containing hydrazide compounds include 2-hydroxyacetohydrazide, 3-hydroxypropionic hydrazide, 4-hydroxybutanoic hydrazide, 2-hydroxybenzohydrazide, and 4-hydroxybenzohydrazide. These hydroxyl group-containing hydrazide compounds may be used alone or in a combination of two or more.
- hydrazide compound containing a carboxyl group examples include 3-carboxypropionic hydrazide, 4-carboxybutanoic hydrazide, 2-benzoic hydrazide, 4-benzoic hydrazide and the like. These carboxyl group-containing hydrazide compounds may be used individually by 1 type, and may be used in combination of 2 or more type.
- Examples of the hydrazide compound having an epoxy group include 2- (oxiran-2-yl) acetohydrazide, 3- (oxiran-2-yl) propionic acid hydrazide, and 3- (tetrahydro-2H-pyran-4-yl) propionic acid. And hydrazide.
- These epoxy group-containing hydrazide compounds may be used alone or in a combination of two or more.
- Examples of the hydrazide compound having a tin-containing group include 3- (tributyltin) propionic acid hydrazide, 3- (trimethyltin) propionic acid hydrazide, 3- (triphenyltin) propionic acid hydrazide, and 3- (trioctyltin) propionic acid.
- Hydrazide 4- (tributyltin) butanoic acid hydrazide, 4- (trimethyltin) butanoic acid hydrazide, 4- (triphenyltin) butanoic acid hydrazide, 4- (trioctyltin) butanoic acid hydrazide, 2- (tributyltin) benzohydrazide , 4- (tributyltin) benzohydrazide, 2- (trimethyltin) benzohydrazide, 4- (trimethyltin) benzohydrazide, 2- (trioctyltin) benzohydrazide, 4- (trioctyltin) benzohydrazide, etc.
- These tin-containing hydrazide compounds may be used individually by 1 type, and may be used in combination of 2 or more type.
- Examples of the hydrazide compound containing an alkoxysilyl group include 2- (trimethoxysilyl) acetohydrazide, 2- (triethoxysilyl) acetohydrazide, 3- (trimethoxysilyl) propionic acid hydrazide, 3- (triethoxysilyl) Propionic acid hydrazide, 4- (trimethoxysilyl) butanoic acid hydrazide, 4- (triethoxysilyl) butanoic acid hydrazide, 2- (trimethoxysilyl) benzohydrazide, 2- (triethoxysilyl) benzohydrazide, 4- (tri Methoxysilyl) benzohydrazide, 4- (triethoxysilyl) benzohydrazide and the like.
- These alkoxysilyl group-containing hydrazide compounds may be used individually by 1 type, and may be used in combination of 2 or more type.
- the oxidized diene rubber latex is coagulated, pulverized and crushed, and then the polar group-containing hydrazide compound is added. Thereafter, kneading is performed using, for example, a mixer, an extruder, a kneader (prebreaker), etc., and a dried modified diene rubber can be obtained.
- the oxidized diene rubber latex is coagulated, ground and dried, and then the polar group-containing hydrazide compound is added.
- a step of adding a polar group-containing hydrazide compound solution to a solid oxide diene rubber after drying by a mixer, an extruder, a kneader, etc. is preferable. It is preferable to do.
- the polar group-containing hydrazide compound is added to the oxidized diene rubber latex and water and, if necessary, an emulsifier added, and the mixture is stirred and reacted at a predetermined temperature.
- an emulsifier is added in advance to the oxidized diene rubber latex, or the polar group-containing hydrazide compound is emulsified and then added to the oxidized diene rubber latex.
- An organic peroxide can also be added as needed.
- the emulsifier that can be used is not particularly limited, and examples thereof include nonionic surfactants such as polyoxyethylene lauryl ether.
- a modified diene rubber can be obtained by coagulating and drying the modified diene rubber latex obtained by adding the polar group-containing hydrazide compound and reacting in this manner.
- the coagulant used for coagulating the oxidized diene rubber latex or the modified diene rubber latex is not particularly limited, but is not limited to acids such as formic acid and sulfuric acid, and sodium chloride. And the like.
- the oxidized diene rubber latex or the modified diene rubber latex can be dried using a dryer such as a vacuum dryer, an air dryer or a drum dryer.
- the modified diene rubber obtained as described above has the following general formula (I) at the end of the molecular chain of the diene rubber:
- R is an amino group, imino group, nitrile group, ammonium group, imide group, amide group, hydrazo group, azo group, diazo group, hydroxyl group, carboxyl group, carbonyl group, epoxy group as a substituent.
- R in the said general formula (I) originates in parts other than the hydrazide group of a polar group containing hydrazide compound as mentioned above.
- the addition amount of the polar group-containing hydrazide compound in the modified diene rubber is 0.01 to 5.5 to the rubber component in the diene rubber. 0% by mass is preferable, and 0.01 to 1.0% by mass is more preferable.
- the modified diene rubber has a weight average molecular weight in terms of polystyrene measured by gel permeation chromatography of 200,000 or more from the viewpoint of ensuring excellent low loss, wear resistance and breaking strength as a rubber composition. And more preferably 400,000 or more.
- the rubber composition of the present invention is characterized by using the above-mentioned modified diene rubber and preferably further contains a filler.
- the blending amount of the filler is not particularly limited, but is preferably in the range of 5 to 100 parts by weight, more preferably in the range of 10 to 70 parts by weight with respect to 100 parts by weight of the modified diene rubber. . If the blending amount of the filler is less than 5 parts by mass, sufficient reinforcement may not be obtained, and if it exceeds 100 parts by mass, the workability may be deteriorated.
- Examples of the filler used in the rubber composition of the present invention include carbon black and inorganic filler.
- the inorganic filler silica and the following formula (I): nM ⁇ xSiOy ⁇ zH2O (I) [Wherein, M is a metal selected from the group consisting of aluminum, magnesium, titanium, calcium and zirconium, an oxide or hydroxide of these metals, and a hydrate thereof, or a carbonate of these metals.
- n, x, y, and z are each an integer of 1 to 5, an integer of 0 to 10, an integer of 2 to 5, and an integer of 0 to 10. Is mentioned.
- These fillers may be used individually by 1 type, and may mix and use 2 or more types.
- the carbon black examples include GPF, FEF, SRF, HAF, ISAF, and SAF grades
- examples of the silica include wet silica, dry silica, and colloidal silica.
- the inorganic compound of the above formula (I) includes alumina such as ⁇ -alumina and ⁇ -alumina (Al2O3); alumina monohydrate such as boehmite and diaspore (Al2O3 ⁇ H2O); water such as gibbsite and bayerite.
- compounding agents usually used in the rubber industry such as anti-aging agents, softeners, silane coupling agents, stearic acid, zinc Hana, a vulcanization accelerator, a vulcanizing agent, and the like can be appropriately selected and blended within a range not impairing the object of the present invention.
- compounding agents commercially available products can be suitably used.
- the rubber composition of the present invention can be produced by blending a modified diene rubber with various compounding agents appropriately selected as necessary, kneading, heating, extruding and the like.
- the tire of the present invention is characterized by using the rubber composition, and the rubber composition is preferably used for a tread.
- a tire using the rubber composition as a tread is excellent in fuel efficiency, fracture characteristics, and wear resistance.
- the tire of the present invention is not particularly limited except that the rubber composition described above is used for any of the tire members, and can be produced according to a conventional method.
- inert gas such as nitrogen, argon, helium other than normal or the air which adjusted oxygen partial pressure, can be used.
- Example 1 (Oxidized natural rubber manufacturing process)
- the field latex was centrifuged using a latex separator [manufactured by Saito Centrifugal Industries Co., Ltd.] at a rotational speed of 7500 rpm to obtain a concentrated latex having a dry rubber concentration of 60%.
- 1000 g of this concentrated latex was put into a stainless steel reaction vessel equipped with a stirrer and a temperature control jacket, and 1000 g of water was added. Thereafter, 9.0 g of potassium persulfate and 3.0 g of propionaldehyde were added and reacted with stirring at 60 ° C. for 30 hours to obtain an oxidized natural rubber latex.
- formic acid was added to adjust the pH to 4.7 to coagulate. This solid was treated 5 times with a creper and crushed through a shredder.
- Examples 2 to 7 Instead of 3.0 g of isonicotinohydrazide, 3.0 g of 3- (dimethylamino) propionic hydrazide in Example 2, 3.9 g of 4- (dimethylamino) benzohydrazide in Example 3, and 4- 3.3 g of hydroxybenzohydrazide, 3.9 g of 4-benzoic acid hydrazide in Example 5, 8.5 g of 4- (tributyltin) butanoic acid hydrazide in Example 6, and 4- (trimethoxysilyl) benzohydrazide in Example 7
- Modified natural rubbers B to G were obtained in the same manner as in Example 1 except that 0.6 g was added. Similarly to the modified natural rubber A, the addition amount of the polar group-containing hydrazide compound in the modified natural rubbers B to G was analyzed to obtain the weight average molecular weight (Mw), and the results shown in Table 1 were obtained.
- Example 8> (Oxidized natural rubber manufacturing process) The field latex was centrifuged using a latex separator [manufactured by Saito Centrifugal Industries Co., Ltd.] at a rotational speed of 7500 rpm to obtain a concentrated latex having a dry rubber concentration of 60%. 1000 g of this concentrated latex was put into a stainless steel reaction vessel equipped with a stirrer and a temperature control jacket, and 1000 g of water was added. Thereafter, 9.0 g of potassium persulfate and 3.0 g of propionaldehyde were added and reacted with stirring at 60 ° C. for 30 hours to obtain an oxidized natural rubber latex.
- a latex separator manufactured by Saito Centrifugal Industries Co., Ltd.
- Example 9 ⁇ Examples 9 and 10> Instead of 3.0 g of isonicotinohydrazide, 3.0 g of 3- (dimethylamino) propionic acid hydrazide was added in Example 9, 3.3 g of 4-hydroxybenzohydrazide was added in Example 10, and the others were the same as in the above Example. In the same manner as in Example 8, modified natural rubbers I and J were obtained. Similarly to the modified natural rubber A, the addition amount of the polar group-containing hydrazide compound in the modified natural rubbers I and J was analyzed to determine the weight average molecular weight (Mw), and the results shown in Table 1 were obtained.
- Mw weight average molecular weight
- ⁇ Comparative Example 4> The field latex was centrifuged using a latex separator [manufactured by Saito Centrifugal Industries Co., Ltd.] at a rotational speed of 7500 rpm to obtain a concentrated latex having a dry rubber concentration of 60%. 1000 g of this concentrated latex was put into a stainless steel reaction vessel equipped with a stirrer and a temperature control jacket, and 1000 g of water was added. Thereafter, 9.0 g of potassium persulfate and 3.0 g of propionaldehyde were added and reacted with stirring at 60 ° C. for 30 hours to obtain an oxidized natural rubber latex.
- a latex separator manufactured by Saito Centrifugal Industries Co., Ltd.
- oxidized natural rubber latex was treated five times with a creper, passed through a shredder and crushed, and then dried at 110 ° C. for 210 minutes with a hot air dryer to obtain oxidized natural rubber N. Further, the weight average molecular weight (Mw) of the oxidized natural rubber N was determined in the same manner as in the modified natural rubber A, and the results shown in Table 2 were obtained.
- Example 11 An oxidized styrene butadiene rubber (SBR) coagulated product was obtained in the same manner as in the oxidized natural rubber production process of Example 1 except that JSR SBR emulsion 0561 (total solid content 69%, pH 10.3) was used.
- Modified SBR1 was obtained in the same manner as in the operation method after the modification step of Example 1 except that an oxidized SBR coagulated product corresponding to a dry rubber weight of 600 g was used instead of the oxidized natural rubber coagulated product.
- the addition amount of the polar group-containing hydrazide compound was analyzed to determine the weight average molecular weight (Mw). The addition amount of the hydrazide compound was 0.50%, and the weight average molecular weight was 27. It was 30,000.
- JSR SBR emulsion 0561 (total solid content 69%, pH 10.3) 1500 g was diluted with water to a solid content of 20%, coagulated with sulfuric acid, dehydrated and dried to obtain dry SBR1. Moreover, when the weight average molecular weight (Mw) was calculated
- Example 7 The oxidized SBR coagulated product obtained in Example 11 was directly dehydrated and dried to obtain oxidized SBR1. Moreover, when the weight average molecular weight (Mw) was calculated
- Example 12 A modified SBR2 was obtained in the same manner as in Example 8 above, except that JBR SBR emulsion 0561 (total solid content 69%, pH 10.3) was used instead of the concentrated latex of natural rubber. Similarly to the modified natural rubber A, the addition amount of the polar group-containing hydrazide compound was analyzed to determine the weight average molecular weight (Mw). The addition amount of the hydrazide compound was 0.49% and the weight average molecular weight was 24. It was 30,000.
- a rubber composition having the formulation shown in Table 3 was prepared by kneading with a plast mill, and the Mooney viscosity, tensile strength (Tb), tan ⁇ and abrasion resistance were measured for the rubber composition by the following methods. Measured and evaluated.
- the results of the rubber composition according to Formula 1 are shown in Table 4, the results of the rubber composition according to Formula 2 are shown in Table 5, and the results of the rubber composition using various SBRs as the rubber component are shown in Table 6.
- Mooney viscosity The Mooney viscosity ML1 + 4 (130 ° C) of the rubber composition was measured at 130 ° C in accordance with JIS K6300-1: 2001. A smaller Mooney viscosity indicates better processability.
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Abstract
Description
nM・xSiOy・zH2O ・・・ (I)
[式中、Mは、アルミニウム、マグネシウム、チタン、カルシウム及びジルコニウムからなる群から選ばれる金属、これらの金属の酸化物又は水酸化物、及びそれらの水和物、またはこれらの金属の炭酸塩から選ばれる少なくとも一種であり;n、x、y及びzは、それぞれ1~5の整数、0~10の整数、2~5の整数、及び0~10の整数である]で表される無機化合物が挙げられる。これら充填剤は、一種単独で用いてもよし、二種以上を混合して用いてもよい。
(酸化天然ゴム製造工程)
フィールドラテックスをラテックスセパレーター[斎藤遠心工業製]を用いて回転数7500rpmで遠心分離して、乾燥ゴム濃度60%の濃縮ラテックスを得た。この濃縮ラテックス1000gを、撹拌機及び温調ジャケットを備えたステンレス製反応容器に投入し、1000gの水を加えた。その後、過硫酸カリウム9.0g、プロピオンアルデヒド3.0gを添加し、60℃、30時間攪拌しながら反応させることで酸化天然ゴムラテックスを得た。次に、ギ酸を加えることでpHを4.7に調整し凝固させた。この固形物をクレーパーで5回処理し、シュレッダーを通してクラム化した。
得られた凝固物の乾燥ゴム含有量を求めた後、乾燥ゴム量換算で600gの凝固物とイソニコチノヒドラジド3.0gのエマルジョン溶液を混練機(プレブレーカー)内で室温にて30rpmで2分間練りこみ、均一に分散させ、乾燥した変性天然ゴムAを得た。また、該変性天然ゴムAを石油エーテルで抽出し、さらにアセトンとメタノールの2:1混合溶媒で抽出することにより、未反応のヒドラジド化合物の分離を行ったところ、抽出物の分析から未反応のヒドラジド化合物は検出されず、よって該変性天然ゴムAにおけるイソニコチノヒドラジドの付加量は天然ゴムラテックス中のゴム成分に対して0.51質量%であった。また、ゲルパーミエーションクロマトグラフィー[GPC:東ソー製HLC-8020、カラム:東ソー製GMH-XL(2本直列)、検出器:示差屈折率計(RI)]で単分散ポリスチレンを基準として、変性天然ゴムAのポリスチレン換算の重量平均分子量(Mw)を求めた。
イソニコチノヒドラジド3.0gの代わりに、実施例2では3-(ジメチルアミノ)プロピオン酸ヒドラジド3.0g、実施例3では4-(ジメチルアミノ)ベンゾヒドラジド3.9g、実施例4では4-ヒドロキシベンゾヒドラジド3.3g、実施例5では4-安息香酸ヒドラジド3.9g、実施例6では4-(トリブチルスズ)ブタン酸ヒドラジド8.5g、実施例7では4-(トリメトキシシリル)ベンゾヒドラジド5.6gを加え、それ以外は上記実施例1と同様にして変性天然ゴムB~Gを得た。また、変性天然ゴムAと同様にして、変性天然ゴムB~Gにおける極性基含有ヒドラジド化合物の付加量を分析し、重量平均分子量(Mw)を求めて、それぞれ表1に示す結果を得た。
(酸化天然ゴム製造工程)
フィールドラテックスをラテックスセパレーター[斎藤遠心工業製]を用いて回転数7500rpmで遠心分離して、乾燥ゴム濃度60%の濃縮ラテックスを得た。この濃縮ラテックス1000gを、撹拌機及び温調ジャケットを備えたステンレス製反応容器に投入し、1000gの水を加えた。その後、過硫酸カリウム9.0g、プロピオンアルデヒド3.0gを添加し、60℃、30時間攪拌しながら反応させることで酸化天然ゴムラテックスを得た。
得られた酸化天然ゴムラテックスに、予め10mLの水と90mgの乳化剤[エマルゲン1108,花王株式会社製]をイソニコチノヒドラジド3.0gに加えて乳化したものを添加し、攪拌しながら60℃で12時間反応させることで、変性天然ゴムラテックスを得た。
次に、上記変性天然ゴムラテックスにギ酸を加えpHを4.7に調整し、変性天然ゴムラテックスを凝固させた。このようにして得られた固形物をクレーパーで5回処理し、シュレッダーに通してクラム化した後、熱風式乾燥機により110℃で210分間乾燥して変性天然ゴムHを得た。また、変性天然ゴムAと同様にして、変性天然ゴムHにおける極性基含有ヒドラジド化合物の付加量を分析し、重量平均分子量(Mw)を求めて、それぞれ表1に示す結果を得た。
イソニコチノヒドラジド3.0gの代わりに、実施例9では3-(ジメチルアミノ)プロピオン酸ヒドラジド3.0g、実施例10では4-ヒドロキシベンゾヒドラジド3.3g、を加え、それ以外は上記実施例8と同様にして変性天然ゴムI、Jを得た。また、変性天然ゴムAと同様にして、変性天然ゴムI、Jにおける極性基含有ヒドラジド化合物の付加量を分析し、重量平均分子量(Mw)を求めて、それぞれ表1に示す結果を得た。
(天然ゴムラテックスの変性反応工程)
フィールドラテックスを、ラテックスセパレーター(斎藤遠心工業製)を用いて回転数7500rpmで遠心分離することで、乾燥ゴム濃度あ60%の濃縮ラテックスを得た。この濃縮ラテックス1000gを、撹拌機及び温調ジャケットを備えたステンレス製反応容器に投入し、予め10mLの水と90mgの乳化剤「エマルゲン1108」(花王株式会社製)をN,N-ジエチルアミノエチルメタクリレート3.0gに加えて乳化したものを990mLの水と共に添加し、窒素置換しながら30分間撹拌した。次いで、tert-ブチルハイドロパーオキサイド1.2g、テトラエチレンペンタミン1.2gを加え、40℃で1時間反応させることで、変性天然ゴムラテックスを得た。
次に、上記変性天然ゴムラテックスにギ酸を加えpHを4.7に調整し、変性天然ゴムラテックスを凝固させた。このようにして得られた固形物をクレーパーで5回処理し、シュレッダーに通してクラム化した後、熱風式乾燥機により110℃で210分間乾燥して変性天然ゴムKを得た。このようにして得られた変性天然ゴムKの質量から、添加したN,N-ジエチルアミノエチルメタクリレートの転化率が100%であることが確認された。また、該変性天然ゴムKを石油エーテルで抽出し、更にアセトンとメタノールの2:1混合溶媒で抽出することで、ホモポリマーの分離を試みたが、抽出物を分析したところホモポリマーは検出されず、添加した単量体の100%が天然ゴム分子に導入されていることが確認された。また、変性天然ゴムAと同様にして、変性天然ゴムKの重量平均分子量(Mw)を求めて、表2に示す結果を得た。
極性基含有単量体としてN,N-ジエチルアミノエチルメタクリレート3.0gの代わりに、比較例2では2-ヒドロキシエチルメタクリレートを2.1g、比較例3では4-ビニルピリジンを1.7g加える以外は、上記比較例1と同様にして変性天然ゴムL、Mを得た。また、変性天然ゴムKと同様にして、変性天然ゴムL、Mを分析したところ、それぞれ添加した極性基含有単量体の100%が天然ゴム分子に導入されていることが確認された。また、変性天然ゴムAと同様にして、変性天然ゴムL、Mの重量平均分子量(Mw)を求めて、表2に示す結果を得た。
フィールドラテックスをラテックスセパレーター[斎藤遠心工業製]を用いて回転数7500rpmで遠心分離して、乾燥ゴム濃度60%の濃縮ラテックスを得た。この濃縮ラテックス1000gを、撹拌機及び温調ジャケットを備えたステンレス製反応容器に投入し、1000gの水を加えた。その後、過硫酸カリウム9.0g、プロピオンアルデヒド3.0gを添加し、60℃、30時間攪拌しながら反応させることで酸化天然ゴムラテックスを得た。次に、上記酸化天然ゴムラテックスにギ酸を加えpHを4.7に調整し、酸化天然ゴムラテックスを凝固させた。このようにして得られた固形物をクレーパーで5回処理し、シュレッダーに通してクラム化した後、熱風式乾燥機により110℃で210分間乾燥して酸化天然ゴムNを得た。また、変性天然ゴムAと同様にして、酸化天然ゴムNの重量平均分子量(Mw)を求めて、表2に示す結果を得た。
フィールドラテックスにギ酸を加えpHを4.7に調整し、フィールドラテックスを凝固させた。このようにして得られた固形物をクレーパーで5回処理し、シュレッダーに通してクラム化した後、熱風式乾燥機により110℃で210分間乾燥して天然ゴムOを得た。また、変性天然ゴムAと同様にして、酸化天然ゴムNの重量平均分子量(Mw)を求めて、表2に示す結果を得た。
JSR製SBRエマルジョン 0561(全固形分69%、pH10.3)を用いた以外は上記実施例1の酸化天然ゴム製造工程と同様にして、酸化スチレンブタジエンゴム(SBR)凝固物を得た。酸化天然ゴム凝固物の代わりに乾燥ゴム重量600g相当の酸化SBR凝固物を用いた以外は上記実施例1の変性工程以後の操作方法と同様にして、変性SBR1を得た。また、変性天然ゴムAと同様にして、極性基含有ヒドラジド化合物の付加量を分析し、重量平均分子量(Mw)を求めたところ、ヒドラジド化合物の付加量は0.50%、重量平均分子量は27.3万であった。
JSR製SBRエマルジョン 0561(全固形分69%、pH10.3)1500gを水で固形分20%に希釈し、硫酸を用いて凝固し、脱水乾燥して乾燥SBR1を得た。また、変性天然ゴムAと同様にして、重量平均分子量(Mw)を求めたところ、重量平均分子量は45.2万であった。
実施例11で得られた酸化SBR凝固物をそのまま脱水乾燥して、酸化SBR1を得た。また、変性天然ゴムAと同様にして、重量平均分子量(Mw)を求めたところ、重量平均分子量は26.1万であった。
JSR製SBRエマルジョン 0561(全固形分69%、pH10.3)を天然ゴムの濃縮ラテックスの代わりに用いた以外は上記実施例8と同様にして変性SBR2を得た。また、変性天然ゴムAと同様にして、極性基含有ヒドラジド化合物の付加量を分析し、重量平均分子量(Mw)を求めたところ、ヒドラジド化合物の付加量は0.49%、重量平均分子量は24.3万であった。
JIS K6300-1:2001に準拠して、130℃にてゴム組成物のムーニー粘度ML1+4(130℃)を測定した。ムーニー粘度が小さい程、加工性に優れることを示す。
上記ゴム組成物を145℃で33分間加硫して得た加硫ゴムに対し、JIS K6251-2004に準拠して引張試験を行い、引張強さ(Tb)を測定した。引張強さが大きい程、耐破壊性が良好であることを示す。
上記ゴム組成物を145℃で33分間加硫して得た加硫ゴムに対し、粘弾性測定装置[レオメトリックス社製]を用い、温度50℃、歪み5%、周波数15Hzで損失正接(tanδ)を測定した。tanδが小さい程、低ロス性に優れることを示す。
上記ゴム組成物を145℃で33分間加硫して得た加硫ゴムに対し、ランボーン型摩耗試験機を用い、室温におけるスリップ率60%での摩耗量を測定し、実施例13~21及び比較例8~11においては比較例11の摩耗量の逆数を100として指数表示し、実施例22~30及び比較例12~16においては比較例16の摩耗量の逆数を100として指数表示し、実施例31、32及び比較例17、18においては比較例17の摩耗量の逆数を100として指数表示し、実施例33、34及び比較例19、20においては比較例19の摩耗量の逆数を100として指数表示した。指数値が大きい程、摩耗量が少なく、耐摩耗性に優れることを示す。
*2 東ソー・シリカ(株)製, 商標:ニプシルAQ.
*3 デグッサ社製, 商標Si69, ビス(3-トリエトキシシリルプロピル)テトラスルフィド.
*4 N-(1,3-ジメチルブチル)-N'-フェニル-p-フェニレンジアミン.
*5 N,N'-ジシクロヘキシル-2-ベンゾチアゾリルスルフェンアミド.
*6 ジフェニルグアニジン.
*7 ジベンゾチアジルジスルフィド.
*8 N-t-ブチル-2-ベンゾチアゾリルスルフェンアミド.
Claims (16)
- ジエン系ゴムラテックスを酸化した後、極性基含有ヒドラジド化合物をジエン系ゴムの分子鎖の末端に付加させてなることを特徴とする変性ジエン系ゴム。
- 前記ジエン系ゴムラテックスが天然ゴムラテックスであることを特徴とする請求項1記載の変性ジエン系ゴム。
- 前記極性基含有ヒドラジド化合物の付加量が、前記ジエン系ゴムラテックス中のゴム成分に対して0.01~5.0質量%であることを特徴とする請求項1記載の変性ジエン系ゴム。
- 前記極性基含有ヒドラジド化合物の極性基がアミノ基、イミノ基、ニトリル基、アンモニウム基、イミド基、アミド基、ヒドラゾ基、アゾ基、ジアゾ基、ヒドロキシル基、カルボキシル基、カルボニル基、エポキシ基、オキシカルボニル基、含窒素複素環基、含酸素複素環基、スズ含有基及びアルコキシシリル基からなる群から選ばれる少なくとも一つであることを特徴とする請求項1記載の変性ジエン系ゴム。
- ゲル浸透クロマトグラフィーで測定したポリスチレン換算重量平均分子量が200,000以上であることを特徴とする請求項1記載の変性ジエン系ゴム。
- 前記ジエン系ゴムラテックスの酸化を、ジエン系ゴムラテックスにカルボニル化合物を添加し、酸化することによって行うことを特徴とする請求項1記載の変性ジエン系ゴム。
- 前記酸化を、空気酸化又はオゾン酸化によって行うことを特徴とする請求項1記載の変性ジエン系ゴム。
- 前記空気酸化をラジカル発生剤の存在下で行うことを特徴とする請求項7記載の変性ジエン系ゴム。
- 前記カルボニル化合物が、アルデヒド類及び/又はケトン類であることを特徴とする請求項6記載の変性ジエン系ゴム。
- 前記ラジカル発生剤が過酸化物系ラジカル発生剤、レドックス系ラジカル発生剤及びアゾ系ラジカル発生剤からなる群から選ばれることを特徴とする請求項8記載の変性ジエン系ゴム。
- ジエン系ゴムラテックスを酸化し、更に凝固し、得られた酸化ジエン系ゴムラテックスの凝固物に極性基含有ヒドラジド化合物を添加し、該極性基含有ヒドラジド化合物を該酸化ジエン系ゴムラテックスの凝固物中のジエン系ゴムの分子鎖の末端に付加反応させ、更に乾燥することを特徴とする変性ジエン系ゴムの製造方法。
- ジエン系ゴムラテックスを酸化し、更に凝固及び乾燥し、得られた酸化ジエン系ゴムに極性基含有ヒドラジド化合物を添加し、該極性基含有ヒドラジド化合物を該酸化ジエン系ゴム中のジエン系ゴムの分子鎖の末端に付加反応させることを特徴とする変性ジエン系ゴムの製造方法。
- ジエン系ゴムラテックスを酸化し、得られた酸化ジエン系ゴムラテックスに極性基含有ヒドラジド化合物を添加し、該極性基含有ヒドラジド化合物を該酸化ジエン系ゴムラテックス中のジエン系ゴムの分子鎖の末端に付加反応させ、更に凝固及び乾燥することを特徴とする変性ジエン系ゴムの製造方法。
- 請求項1~11のいずれか1項に記載の変性ジエン系ゴムを用いたゴム組成物。
- 請求項15記載のゴム組成物をタイヤ部材のいずれかに用いたタイヤ。
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| EP09712057.0A EP2248833B1 (en) | 2008-02-18 | 2009-02-16 | Modified diene rubber, method for producing the same, rubber composition using the same, and tire |
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| PCT/JP2009/052544 Ceased WO2009104555A1 (ja) | 2008-02-18 | 2009-02-16 | 変性ジエン系ゴム及びその製造方法、並びにそれを用いたゴム組成物及びタイヤ |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US8389641B2 (ja) |
| EP (1) | EP2248833B1 (ja) |
| JP (1) | JP5582786B2 (ja) |
| CN (1) | CN102099380B (ja) |
| MY (1) | MY150517A (ja) |
| WO (1) | WO2009104555A1 (ja) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011026379A (ja) * | 2009-07-22 | 2011-02-10 | Bridgestone Corp | タイヤ |
| JP2014534995A (ja) * | 2011-10-28 | 2014-12-25 | コンパニー ゼネラール デ エタブリッスマン ミシュラン | エラストマーマトリックス中で充填剤の極めて良好な分散を有するエラストマー組成物 |
| JP2015034224A (ja) * | 2013-08-08 | 2015-02-19 | 東洋ゴム工業株式会社 | 変性天然ゴム及びそれを用いたゴム組成物 |
| JP2017078126A (ja) * | 2015-10-21 | 2017-04-27 | 株式会社ブリヂストン | ゴム組成物、トレッドゴム及び重荷重用タイヤ |
| WO2019156094A1 (ja) * | 2018-02-07 | 2019-08-15 | 株式会社ブリヂストン | ゴム組成物及びタイヤ |
| JP2023063829A (ja) * | 2021-10-25 | 2023-05-10 | Toyo Tire株式会社 | 末端変性ジエン系ポリマー、及びその製造方法 |
| US11655357B2 (en) | 2019-12-13 | 2023-05-23 | Toyo Tire Corporation | Modified natural rubber, rubber composition using the rubber, and pneumatic tire using the composition |
| US11897971B2 (en) | 2018-11-19 | 2024-02-13 | Toyo Tire Corporation | Modified natural rubber, rubber composition using same, and method for producing modified natural rubber |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009108204A (ja) * | 2007-10-30 | 2009-05-21 | Bridgestone Corp | 変性天然ゴム及びその製造方法、並びにそれを用いたゴム組成物及びタイヤ |
| US20130303681A1 (en) * | 2012-05-09 | 2013-11-14 | Bridgestone Corporation | Natural rubber, rubber composition containing natural rubber, and the production process of the same, and tire |
| EP2848647B1 (en) * | 2012-05-09 | 2017-08-30 | Bridgestone Corporation | Natural rubber, rubber composition comprising natural rubber and method for producing same, and tire |
| WO2016069536A1 (en) * | 2014-10-29 | 2016-05-06 | Arkema Inc. | Peroxide vulcanization of rubber latexes |
| FR3029523B1 (fr) * | 2014-12-05 | 2017-01-20 | Michelin & Cie | Procede de preparation d'un caoutchouc naturel modifie au moyen d'un agent de modification |
| WO2016093129A1 (ja) * | 2014-12-10 | 2016-06-16 | 株式会社ブリヂストン | ゴム組成物及びゴム組成物の製造方法 |
| ES2971953T3 (es) * | 2018-06-06 | 2024-06-10 | Bridgestone Corp | Composición de caucho y neumático |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0827315A (ja) * | 1994-07-15 | 1996-01-30 | Bridgestone Corp | ゴム組成物の混練り方法 |
| JPH0881505A (ja) | 1994-09-14 | 1996-03-26 | Kao Corp | 解重合天然ゴムおよびその製造方法 |
| JPH09136903A (ja) | 1995-11-10 | 1997-05-27 | Kao Corp | 解重合天然ゴムの製造方法 |
| JPH10330549A (ja) * | 1997-04-02 | 1998-12-15 | Bridgestone Corp | 空気入りタイヤ |
| JP2001172435A (ja) * | 1999-12-16 | 2001-06-26 | Bridgestone Corp | ゴム組成物の製造方法及び空気入りタイヤ |
| JP2001261707A (ja) | 2000-03-23 | 2001-09-26 | Okayama Prefecture | 天然ゴムの解重合方法 |
| WO2004106397A1 (en) | 2003-06-02 | 2004-12-09 | Bridgestone Corporation | Modified natural rubber or modified natural rubber latex, and rubber composition and pneumatic tire |
| JP2004359717A (ja) * | 2003-06-02 | 2004-12-24 | Bridgestone Corp | 変性天然ゴムおよびその製造方法 |
| JP2007204637A (ja) | 2006-02-02 | 2007-08-16 | Bridgestone Corp | 変性天然ゴム及びその製造方法、並びにそれを用いたゴム組成物及びタイヤ |
| JP2007277310A (ja) * | 2006-04-03 | 2007-10-25 | Bridgestone Corp | ゴム組成物及びそれを用いた空気入りタイヤ |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA931299A (en) * | 1970-09-25 | 1973-07-31 | Polysar Limited | Terminally reactive polymers |
| DD138070A1 (de) | 1974-09-20 | 1979-10-10 | Peter Knoth | Verfahren zur polymerisation von konjugierten dienen zu"lebenden"polymeren |
| DE69424455T2 (de) * | 1993-03-02 | 2001-01-18 | Bridgestone Corp., Tokio/Tokyo | Methode zur Herstellung eines mit viskositätsstabilisierenden Verbindungen behandelten Naturkautschukes |
| DE69827906T2 (de) * | 1997-04-02 | 2005-05-19 | Bridgestone Corp. | Kautschukzusammensetzung und reifen |
| AU2002210988A1 (en) * | 2000-11-07 | 2002-05-21 | Bridgestone Corporation | Natural rubber produced from latex and composition comprising the same |
| US7879952B2 (en) * | 2005-12-28 | 2011-02-01 | Bridgestone Corporation | Functionalized polymers |
| JP2009108204A (ja) * | 2007-10-30 | 2009-05-21 | Bridgestone Corp | 変性天然ゴム及びその製造方法、並びにそれを用いたゴム組成物及びタイヤ |
-
2009
- 2009-02-16 MY MYPI20103862 patent/MY150517A/en unknown
- 2009-02-16 JP JP2009554302A patent/JP5582786B2/ja not_active Expired - Fee Related
- 2009-02-16 CN CN200980112949.8A patent/CN102099380B/zh not_active Expired - Fee Related
- 2009-02-16 WO PCT/JP2009/052544 patent/WO2009104555A1/ja not_active Ceased
- 2009-02-16 US US12/918,218 patent/US8389641B2/en not_active Expired - Fee Related
- 2009-02-16 EP EP09712057.0A patent/EP2248833B1/en not_active Not-in-force
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0827315A (ja) * | 1994-07-15 | 1996-01-30 | Bridgestone Corp | ゴム組成物の混練り方法 |
| JPH0881505A (ja) | 1994-09-14 | 1996-03-26 | Kao Corp | 解重合天然ゴムおよびその製造方法 |
| JPH09136903A (ja) | 1995-11-10 | 1997-05-27 | Kao Corp | 解重合天然ゴムの製造方法 |
| JPH10330549A (ja) * | 1997-04-02 | 1998-12-15 | Bridgestone Corp | 空気入りタイヤ |
| JP2001172435A (ja) * | 1999-12-16 | 2001-06-26 | Bridgestone Corp | ゴム組成物の製造方法及び空気入りタイヤ |
| JP2001261707A (ja) | 2000-03-23 | 2001-09-26 | Okayama Prefecture | 天然ゴムの解重合方法 |
| WO2004106397A1 (en) | 2003-06-02 | 2004-12-09 | Bridgestone Corporation | Modified natural rubber or modified natural rubber latex, and rubber composition and pneumatic tire |
| JP2004359717A (ja) * | 2003-06-02 | 2004-12-24 | Bridgestone Corp | 変性天然ゴムおよびその製造方法 |
| JP2007204637A (ja) | 2006-02-02 | 2007-08-16 | Bridgestone Corp | 変性天然ゴム及びその製造方法、並びにそれを用いたゴム組成物及びタイヤ |
| JP2007277310A (ja) * | 2006-04-03 | 2007-10-25 | Bridgestone Corp | ゴム組成物及びそれを用いた空気入りタイヤ |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011026379A (ja) * | 2009-07-22 | 2011-02-10 | Bridgestone Corp | タイヤ |
| US10519299B2 (en) | 2011-10-28 | 2019-12-31 | Compagnie Generale Des Etablessements Michelin | Elastomer composition having a very good dispersion of the charge in the elastomer matrix |
| JP2014534995A (ja) * | 2011-10-28 | 2014-12-25 | コンパニー ゼネラール デ エタブリッスマン ミシュラン | エラストマーマトリックス中で充填剤の極めて良好な分散を有するエラストマー組成物 |
| US10059833B2 (en) | 2011-10-28 | 2018-08-28 | Compagnie Generale Des Etablissements Michelin | Elastomer composition having a very good dispersion of the charge in the elastomer matrix |
| JP2015034224A (ja) * | 2013-08-08 | 2015-02-19 | 東洋ゴム工業株式会社 | 変性天然ゴム及びそれを用いたゴム組成物 |
| JP2017078126A (ja) * | 2015-10-21 | 2017-04-27 | 株式会社ブリヂストン | ゴム組成物、トレッドゴム及び重荷重用タイヤ |
| WO2019156094A1 (ja) * | 2018-02-07 | 2019-08-15 | 株式会社ブリヂストン | ゴム組成物及びタイヤ |
| JPWO2019156094A1 (ja) * | 2018-02-07 | 2021-02-04 | 株式会社ブリヂストン | ゴム組成物及びタイヤ |
| JP7271445B2 (ja) | 2018-02-07 | 2023-05-11 | 株式会社ブリヂストン | ゴム組成物及びタイヤ |
| US11897971B2 (en) | 2018-11-19 | 2024-02-13 | Toyo Tire Corporation | Modified natural rubber, rubber composition using same, and method for producing modified natural rubber |
| US11655357B2 (en) | 2019-12-13 | 2023-05-23 | Toyo Tire Corporation | Modified natural rubber, rubber composition using the rubber, and pneumatic tire using the composition |
| JP2023063829A (ja) * | 2021-10-25 | 2023-05-10 | Toyo Tire株式会社 | 末端変性ジエン系ポリマー、及びその製造方法 |
| JP7713851B2 (ja) | 2021-10-25 | 2025-07-28 | Toyo Tire株式会社 | 末端変性ジエン系ポリマー、及びその製造方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| EP2248833A4 (en) | 2011-06-15 |
| MY150517A (en) | 2014-01-30 |
| CN102099380A (zh) | 2011-06-15 |
| EP2248833B1 (en) | 2014-03-26 |
| US20110003911A1 (en) | 2011-01-06 |
| JP5582786B2 (ja) | 2014-09-03 |
| US8389641B2 (en) | 2013-03-05 |
| JPWO2009104555A1 (ja) | 2011-06-23 |
| EP2248833A1 (en) | 2010-11-10 |
| CN102099380B (zh) | 2014-03-12 |
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