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WO2020262373A1 - Rubber composition for tire and pneumatic tire obtained using same - Google Patents

Rubber composition for tire and pneumatic tire obtained using same Download PDF

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Publication number
WO2020262373A1
WO2020262373A1 PCT/JP2020/024584 JP2020024584W WO2020262373A1 WO 2020262373 A1 WO2020262373 A1 WO 2020262373A1 JP 2020024584 W JP2020024584 W JP 2020024584W WO 2020262373 A1 WO2020262373 A1 WO 2020262373A1
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WIPO (PCT)
Prior art keywords
mass
rubber composition
parts
rubber
phenol resin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2020/024584
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French (fr)
Japanese (ja)
Inventor
理絵 中島
圭介 前島
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yokohama Rubber Co Ltd
Original Assignee
Yokohama Rubber Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from JP2019117108A external-priority patent/JP7095657B2/en
Priority claimed from JP2019117101A external-priority patent/JP7095656B2/en
Priority claimed from JP2020068066A external-priority patent/JP7095716B2/en
Priority claimed from JP2020068065A external-priority patent/JP7095715B2/en
Application filed by Yokohama Rubber Co Ltd filed Critical Yokohama Rubber Co Ltd
Publication of WO2020262373A1 publication Critical patent/WO2020262373A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60CVEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
    • B60C1/00Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60CVEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
    • B60C15/00Tyre beads, e.g. ply turn-up or overlap
    • B60C15/06Flipper strips, fillers, or chafing strips and reinforcing layers for the construction of the bead
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/02Elements
    • C08K3/04Carbon
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/34Silicon-containing compounds
    • C08K3/36Silica
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/17Amines; Quaternary ammonium compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/34Heterocyclic compounds having nitrogen in the ring
    • C08K5/3467Heterocyclic compounds having nitrogen in the ring having more than two nitrogen atoms in the ring
    • C08K5/3477Six-membered rings
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/34Heterocyclic compounds having nitrogen in the ring
    • C08K5/3467Heterocyclic compounds having nitrogen in the ring having more than two nitrogen atoms in the ring
    • C08K5/3477Six-membered rings
    • C08K5/3492Triazines
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L61/00Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
    • C08L61/04Condensation polymers of aldehydes or ketones with phenols only
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L61/00Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
    • C08L61/04Condensation polymers of aldehydes or ketones with phenols only
    • C08L61/06Condensation polymers of aldehydes or ketones with phenols only of aldehydes with phenols
    • C08L61/14Modified phenol-aldehyde condensates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L61/00Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
    • C08L61/34Condensation polymers of aldehydes or ketones with monomers covered by at least two of the groups C08L61/04, C08L61/18 and C08L61/20
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L9/00Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L9/00Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
    • C08L9/06Copolymers with styrene

Definitions

  • the present invention relates to a rubber composition for a tire and a pneumatic tire using the same. Specifically, the present invention uses a rubber composition capable of achieving both high elastic modulus and low heat generation and increasing the vulcanization rate. It's about the pneumatic tires that were there.
  • thermosetting resin in a rubber composition for a tire for the purpose of increasing hardness and elastic modulus
  • Patent Document 1 a technique for blending a thermosetting resin in a rubber composition for a tire for the purpose of increasing hardness and elastic modulus.
  • a thermosetting resin when blended, there is a problem that heat generation is deteriorated.
  • the productivity of the tire can be improved, but there is a problem that the fracture physical properties are lowered due to the increase in modulus. Therefore, it is important to increase the vulcanization rate from the viewpoint of tire productivity, but it is necessary to balance it with other physical characteristics.
  • the productivity of the tire can be improved by further adding a vulcanization accelerator or the like to increase the vulcanization rate, but there is a problem that the fracture physical properties are lowered due to the increase in modulus. Therefore, it is important to increase the vulcanization rate from the viewpoint of tire productivity, but it is necessary to balance it with other physical characteristics.
  • an object of the present invention is to provide a rubber composition capable of increasing the vulcanization rate while achieving both high elastic modulus and low heat generation, and a pneumatic tire using the same.
  • the present inventors can solve the above-mentioned problems by blending one or more kinds selected from carbon black and silica and a specific phenol resin in a specific amount with the diene rubber.
  • the present invention is derived from 1 to 300 parts by mass of one or more selected from carbon black and silica with respect to 100 parts by mass of diene rubber, and alkyleneamine represented by the following chemical formula (1) in the molecule.
  • the present invention provides a rubber composition for a tire, which comprises 0.1 to 20 parts by mass of a phenol resin having at least one structural unit.
  • R 1 independently represents a linear or branched alkylene group having 1 to 10 carbon atoms.
  • the present invention also provides a pneumatic tire using the rubber composition for a tire of the present invention.
  • the present invention since one or more selected from carbon black and silica and a specific phenol resin are blended in a specific amount with the diene rubber, both high elastic modulus and low heat generation property are achieved, and at the same time, It is possible to provide a rubber composition for a tire capable of increasing the vulcanization rate and a pneumatic tire using the same.
  • the silanol groups on the surface of carbon black or silica interact with the structural units derived from alkylene amine in the phenol resin to promote vulcanization and increase the elastic modulus. It is presumed that low heat generation can be achieved at the same time. In addition, high fracture physical properties can be achieved at the same time.
  • the diene rubber used in the present invention is not particularly limited, and for example, natural rubber (NR), synthetic isoprene rubber (IR), styrene-butadiene copolymer rubber (SBR), butadiene rubber (BR), acrylonitrile- Examples thereof include butadiene copolymer rubber (NBR). Of these, NR, IR and SBR are preferable. These may be used alone or in combination of two or more.
  • the molecular weight and microstructure thereof are not particularly limited, and may be terminal-modified with an amine, amide, silyl, alkoxysilyl, carboxyl, hydroxyl group, or the like, or may be epoxidized.
  • the carbon black used in the present invention preferably has a nitrogen adsorption specific surface area (N 2 SA) of 33 to 500 m 2 / g from the viewpoint of improving the effect of the present invention.
  • the nitrogen adsorption specific surface area (N 2 SA) is a value obtained in accordance with JIS K6217-2.
  • the silica used in the present invention is not particularly limited, and for example, any conventionally known silica blended in a rubber composition for tire applications can be used. Specific examples of silica include wet silica, dry silica, fumed silica and the like. As the silica, one type of silica may be used alone, or two or more types of silica may be used in combination. From the viewpoint of improving the effect of the present invention, the silica used in the present invention preferably has a CTAB specific surface area of 70 to 300 m 2 / g, more preferably 80 to 250 m 2 / g. In the present specification, the CTAB specific surface area is a value obtained by measuring the amount of CTAB adsorbed on the silica surface according to JIS K6217-3: 2001 "Part 3: How to obtain the specific surface area-CTAB adsorption method".
  • the phenol resin used in the present invention has at least one structural unit derived from an alkylene amine represented by the following chemical formula (1) in its molecule.
  • R 1 independently represents a linear or branched alkylene group having 1 to 10 carbon atoms.
  • the alkylene group of R 1 has, for example, 1 to 10, preferably 2 to 6, and more preferably 2 to 4.
  • the phenol resin may contain at least one structural unit derived from ethyleneamine represented by the following chemical formula (2) in the molecule.
  • the lower limit of the content ratio of the structural unit derived from alkyleneamine or ethyleneamine in the phenol resin is, for example, 3% by mass or more, preferably 5% by mass or more, and more preferably 10% by mass or more. Thereby, the elastic modulus can be improved.
  • the upper limit of the content ratio of the structural unit derived from ethyleneamine in the phenol resin may be, for example, 50% by mass or less, preferably 45% by mass or less, and more preferably 40% by mass or less. Thereby, the softening point can be appropriately adjusted.
  • the content of the ethyleneamine-derived structure can be calculated based on the following formula.
  • the nitrogen content (mass%) in the formula can be measured by an elemental analysis method.
  • Ethyleneamine-derived structure content nitrogen content x (43/14)
  • the softening point of the phenol resin is, for example, 60 ° C. to 150 ° C., preferably 65 ° C. to 130 ° C., and more preferably 70 ° C. to 120 ° C.
  • the softening point of the phenolic resin can be appropriately controlled according to the heating temperature at the time of heating and kneading when blended with rubber. As a result, it is possible to realize a rubber having little variation in rubber physical characteristics.
  • the phenolic resin may be composed of a polymer of phenols, aldehydes, and alkyleneamines.
  • the phenolic resin may or may not contain these unreacted monomers.
  • phenols are not particularly limited, but for example, phenol; cresols such as orthocresol, metacresol, paracresol; 2,3-xylenol, 2,4-xylenol, 2,5-xylenol, 2,6- Xylenol, such as 3,5-xylenol; 2,3,5-trimethylphenol, 2-ethylphenol, 4-ethylphenol, 2-isopropylphenol, 4-isopropylphenol, n-butylphenol, isobutylphenol, tert-butylphenol Alkylphenol such as hexylphenol, octylphenol, nonylphenol, phenylphenol, benzylphenol, cumylphenol, allylphenol, cardanol, ursiol, thithiol, laccol; naphthol such as 1-naphthol and 2-naphthol; fluorophenol, chlorophenol, Halogenated phenols such as bro
  • the aldehydes are not particularly limited, but for example, formaldehyde such as formalin and paraformaldehyde; trioxane, acetaldehyde, propionaldehyde, polyoxymethylene, chloral, hexamethylenetetramine, furfural, glioxal, n-butylaldehyde, caproaldehyde, etc.
  • formaldehyde such as formalin and paraformaldehyde
  • trioxane acetaldehyde
  • propionaldehyde polyoxymethylene
  • chloral hexamethylenetetramine
  • furfural glioxal
  • n-butylaldehyde caproaldehyde
  • aldehyde examples thereof include allyl aldehyde, benz aldehyde, croton aldehyde, acrolein, tetraoxymethylene, phenylacetaldehyde, o-
  • aldehydes may be used alone or in combination of two or more.
  • aldehydes can include formaldehyde or acetaldehyde, and formalin or paraformaldehyde can be used from the viewpoint of productivity and low cost.
  • an aliphatic amine having one or more linear or branched alkylene groups having 1 to 10 carbon atoms in the molecule can be used.
  • the aliphatic amine may be a compound containing one or more primary amines and / or secondary amines.
  • Examples include polyalkylene polyamines. These may be used alone or in combination of two or more.
  • the catalyst used when synthesizing the phenol resin may be non-catalyst, or an acidic catalyst can be used from the viewpoint of producing a novolak type phenol resin.
  • the acidic catalyst is not particularly limited, and examples thereof include acids such as oxalic acid, hydrochloric acid, sulfuric acid, diethyl sulfate, and paratoluenesulfonic acid, and metal salts such as zinc acetate, which may be used alone or in combination of two or more. Can be used.
  • Water may be used as the reaction solvent used when synthesizing the phenol resin, but an organic solvent may be used.
  • organic solvent a non-polar solvent can be used and a non-aqueous system can be used.
  • organic solvents include, for example, alcohols, ketones, and aromatics
  • alcohols include methanol, ethanol, propyl alcohol, ethylene glycol, diethylene glycol, triethylene glycol, glycerin, and the like
  • ketones include. Acetone, methyl ethyl ketone and the like
  • examples of the aromatics include toluene, xylene and the like. These may be used alone or in combination of two or more.
  • the molar ratio (F / P molar ratio) of phenols (P) and aldehydes (F) may be, for example, 0.2 to 1.0 mol of aldehydes with respect to 1 mol of phenols, which is preferable. Can be 0.3-0.9 mol.
  • the reaction molar ratio (F / P) of phenols (P) and aldehydes (F) to 1.0 or less, that is, the phenol-rich condition in terms of molar ratio, an appropriate softening point is obtained.
  • a phenolic resin containing a structural unit derived from an alkyleneamine having the above can be obtained, and such a phenolic resin can be satisfactorily compatible or dispersed in rubber by mixing and kneading under heating conditions.
  • reaction temperature may be, for example, 40 ° C. to 120 ° C., preferably 60 ° C. to 110 ° C.
  • the reaction time is not particularly limited and may be appropriately determined according to the type of starting material, the compounding molar ratio, the amount and type of catalyst used, and the reaction conditions.
  • the phenolic resin used in the present invention can be obtained.
  • the phenolic resin may contain a novolak-type phenolic resin having a novolak skeleton and a structural unit derived from the ethyleneamine in the molecule.
  • the rubber composition of the present invention contains 1 to 300 parts by mass of one or more selected from carbon black and silica with respect to 100 parts by mass of diene rubber, and an alkylene amine represented by the chemical formula (1) in the molecule. It is characterized by blending 0.1 to 20 parts by mass of a phenol resin having at least one derived structural unit. If the blending amount of carbon black is less than 1 part by mass, the blending amount is too small to achieve the effect of the present invention. On the contrary, if it exceeds 300 parts by mass, the heat generation property deteriorates. If the blending amount of silica is less than 1 part by mass, the blending amount is too small to achieve the effect of the present invention.
  • the wear resistance and heat generation property are significantly deteriorated. If the blending amount of the phenol resin is less than 0.1 parts by mass, the blending amount is too small to achieve the effect of the present invention. On the contrary, if it exceeds 20 parts by mass, the wear resistance and heat generation property deteriorate.
  • the blending amount of carbon black is preferably 1 to 200 parts by mass with respect to 100 parts by mass of the diene rubber.
  • the amount of silica blended is preferably 20 to 250 parts by mass with respect to 100 parts by mass of the diene rubber.
  • the blending amount of the phenol resin is preferably 0.1 to 20 parts by mass, and more preferably 1 to 15 parts by mass with respect to 100 parts by mass of the diene rubber.
  • carbon black and silica can be used together as needed.
  • the rubber composition in the present invention includes a vulcanization or cross-linking agent; a vulcanization or cross-linking accelerator; various fillers such as zinc oxide, clay, talc, and calcium carbonate; an antiaging agent; plastic.
  • Various additives generally blended in rubber compositions such as agents can be blended, and such additives are kneaded by a general method to form a composition, which is used for vulcanization or cross-linking. Can be done.
  • the blending amount of these additives can also be a conventional general blending amount as long as it does not contradict the object of the present invention.
  • a methylene donor can be used for curing the phenol resin, and the type thereof is not particularly limited, but for example, hexamethylenetetramine and HMMM (partial condensate of hexamethoxymethylol melamine). ), Polyvalent methylol melamine derivatives such as PMMM (partial condensate of hexamethylol melamine pentamethyl ether), hexaethoxymethyl melamine, para-formaldehyde polymers, N-methylol derivatives of melamine, etc., and the effects of the present invention. From the viewpoint of improvement, hexamethylenetetramine or polyvalent methylolmelamine derivative is preferable.
  • the blending amount of the methylene donor is preferably 0.1 to 5 parts by mass, more preferably 0.1 to 2.5 parts by mass with respect to 100 parts by mass of the diene rubber.
  • the rubber composition for a tire of the present invention can produce a pneumatic tire according to a conventional method for producing a pneumatic tire, for example, a tire cap tread, an under tread, a sidewall, a belt coat, a belt cushion, a rim cushion, and the like. It can be suitably used for inner liners, bead fillers and the like.
  • Phenolic resin 2 was obtained in the same manner as in Production Example 1 except that the amount of the 37% formalin aqueous solution was 518 parts and the amount of triethylenetetraamine was 110 parts.
  • the softening point of the phenol resin 2 was 108 ° C., the nitrogen content was 4.1% by mass, and the content of the ethyleneamine-derived structure was 12.6% by mass.
  • the phenol resin 3 was obtained in the same manner as in Production Example 1 except that the amount of the 37% formalin aqueous solution was 500 parts and the amount of triethylenetetraamine was 165 parts.
  • the softening point of the phenol resin 3 was 102 ° C., the nitrogen content was 6.4% by mass, and the content of the ethyleneamine-derived structure was 19.7% by mass.
  • Examples 1 to 6 and Comparative Examples 1 to 3 Sample Preparation In the formulation (parts by mass) shown in Table 1, the vulcanization accelerator and the components excluding sulfur were kneaded with a 1.7 liter sealed Banbury mixer for 5 minutes, and the rubber was discharged to the outside of the mixer and cooled to room temperature. .. Then, the rubber was put into the same mixer again, a vulcanization accelerator and sulfur were added, and the mixture was further kneaded to obtain a rubber composition. Next, the obtained rubber composition was press-vulcanized in a predetermined mold at 160 ° C. for 20 minutes to obtain a vulcanized rubber test piece, and the unvulcanized rubber composition and the vulcanized rubber were obtained by the test method shown below. The physical properties of the test piece were measured.
  • Vulcanization rate (T95) In accordance with JIS K6300, the time (T95, min) to reach 95% vulcanization degree at an amplitude of 1 degree and 150 ° C. was measured with a vibrating disk vulcanization tester. The results are shown exponentially with the value of Comparative Example 1 as 100. The smaller this value is, the faster the vulcanization rate is and the better the productivity is.
  • Storage elastic modulus Measured at 20 ° C. with a viscoelastic spectrometer manufactured by Toyo Seiki Seisakusho under the conditions of initial strain 10%, amplitude ⁇ 2%, and frequency 20 Hz in accordance with JIS K6394. The results are shown exponentially with the value of Comparative Example 1 as 100.
  • Tan ⁇ (60 ° C.) Using a viscoelastic spectrometer manufactured by Toyo Seiki Seisakusho Co., Ltd., tan ⁇ (60 ° C.) was measured under the conditions of initial strain of 10%, amplitude of ⁇ 2%, frequency of 20 Hz, and temperature of 60 ° C. The results are shown exponentially with the value of Comparative Example 1 as 100. The smaller this value is, the lower the heat generation is. The results are also shown in Table 1.
  • the rubber compositions of Examples 1 to 6 contained carbon black and a specific phenol resin in a specific amount with respect to the diene rubber, so that the vulcanization rate was higher than that of Comparative Example 1.
  • the result was fast, high storage elastic modulus, and low calorific value.
  • Comparative Example 2 was an example in which a straight phenol resin and a methylene donor having no structural unit derived from alkyleneamine were used, and the vulcanization rate was slower than that of Comparative Example 1.
  • Comparative Example 3 is an example in which a phenol resin is not blended, and the storage elastic modulus is worse than that of Comparative Example 1.
  • Vulcanization rate (T30) The obtained rubber composition is vulcanized according to JIS K6300 until it reaches 30% of the maximum torque obtained from the vulcanization curve of the torque obtained at a temperature of 160 ° C. and the vulcanization time. The time (T30) was measured. The results are shown exponentially with the value of Standard Example 1 as 100. The smaller this value is, the faster the vulcanization rate is and the better the productivity is.
  • Storage elastic modulus Measured by the same method as above. The results are shown exponentially with the value of Standard Example 1 as 100. The larger this value is, the higher the elastic modulus is.
  • tan ⁇ (60 ° C.) Measured by the same method as above.
  • Breaking strength (TB) Tested at 20 ° C. according to JIS K 6251. The results are shown exponentially with the value of Standard Example 1 as 100. The larger this value is, the higher the breaking strength is. The results are also shown in Table 2.
  • the rubber compositions of Examples 7 to 12 contained silica and a specific phenol resin in a specific amount with respect to the diene rubber, so that the vulcanization rate was faster than that of Standard Example 1.
  • the storage elastic modulus was high, the heat generation was low, and the breaking strength was high.
  • Comparative Example 4 since the phenol resin was not blended, the vulcanization rate was slower than that in Standard Example 1, and the storage elastic modulus and the breaking strength were inferior.
  • Comparative Example 5 is an example in which a methylene donor was blended with Standard Example 1, and the result was that the vulcanization rate was slower than that of Standard Example 1. In addition, no improvement was seen in the breaking strength.
  • Examples 13 to 15 were compared with Standard Example 2
  • Examples 16 to 19 and Comparative Examples 6 to 7 were compared with Standard Example 3
  • Examples 20 to 22 were compared with Standard Example 4, and Example 23.
  • ⁇ 25 and Comparative Examples 8-9 are compared with Standard Example 5.
  • Vulcanization rate (T95): Measured by the same method as above. The results are shown exponentially with the value of Standard Example 6 as 100. The smaller this value is, the faster the vulcanization rate is and the better the productivity is.
  • Exothermic (tan ⁇ 60 ° C.): Measured by the same method as above. The results are shown exponentially with the value of Standard Example 6 as 100. The smaller this value is, the lower the heat generation is.
  • Breaking strength (TB) Measured by the same method as above. The results are shown exponentially with the value of Standard Example 6 as 100. The larger this value is, the higher the breaking strength is.
  • Abrasion resistance Using a lambourn abrasion tester manufactured by Iwamoto Seisakusho Co., Ltd., the abrasion was measured under the conditions of a load of 15 N, a slip ratio of 25%, a time of 10 minutes, and room temperature to determine the abrasion loss. The results are shown exponentially with the value of Standard Example 6 as 100. The larger the index, the better the wear resistance. The results are also shown in Table 5.

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Abstract

The present invention provides a rubber composition which attains a high modulus with low heat build-up properties and can be vulcanized at an increased rate. A hundred parts by mass of a diene-based rubber was compounded with 1-300 parts by mass of carbon black and/or silica and 0.1-20 parts by mass of a phenolic resin having, in the molecule, at least one ethyleneamine-derived structural unit represented by –(NH-C2H4)-.

Description

タイヤ用ゴム組成物およびそれを用いた空気入りタイヤRubber composition for tires and pneumatic tires using it

 本発明は、タイヤ用ゴム組成物およびそれを用いた空気入りタイヤに関するものであり、詳しくは、高弾性率および低発熱性を両立するとともに、加硫速度を速め得るゴム組成物およびそれを用いた空気入りタイヤに関するものである。 The present invention relates to a rubber composition for a tire and a pneumatic tire using the same. Specifically, the present invention uses a rubber composition capable of achieving both high elastic modulus and low heat generation and increasing the vulcanization rate. It's about the pneumatic tires that were there.

 タイヤ用ゴム組成物において、高硬度化や高弾性率化を目的として、熱硬化性樹脂を配合する技術が知られている(例えば特許文献1参照)。しかし、熱硬化性樹脂を配合すると、発熱性が悪化するという問題点がある。
 一方、タイヤ用ゴム組成物の加硫速度を速めることにより、タイヤの生産性を向上させることができるが、モジュラスの増大により破断物性が低下するという課題がある。したがって、タイヤの生産性の観点から加硫速度を速めることは重要であるが、他物性とのバランス化を図る必要がある。
There is known a technique for blending a thermosetting resin in a rubber composition for a tire for the purpose of increasing hardness and elastic modulus (see, for example, Patent Document 1). However, when a thermosetting resin is blended, there is a problem that heat generation is deteriorated.
On the other hand, by increasing the vulcanization rate of the rubber composition for a tire, the productivity of the tire can be improved, but there is a problem that the fracture physical properties are lowered due to the increase in modulus. Therefore, it is important to increase the vulcanization rate from the viewpoint of tire productivity, but it is necessary to balance it with other physical characteristics.

 また、地球温暖化に伴う環境規制の高まりに伴い、タイヤの低転がり抵抗化が求められており、タイヤ用ゴム組成物にてその要求を達成するため、シリカの高配合化、高配合比率化が行われてきた(例えば特許文献2参照)。シリカ配合ゴム組成物の低発熱性に起因する操縦安定性の低下を補うため、高硬度化、高弾性率化は有効な手段であるが、低転がり抵抗性と破断物性とのさらなる高次バランス化が市場から求められている。
 一方、シリカ配合ゴム組成物は、シリカ表面のシラノール基が酸化亜鉛や加硫促進剤の機能に干渉することや、熱伝導率が低下することにより、加硫速度が低下する傾向がある。そこで加硫促進剤等をさらに添加して加硫速度を速めることでタイヤの生産性を向上させることができるが、モジュラスの増大により破断物性が低下するという課題がある。したがって、タイヤの生産性の観点から加硫速度を速めることは重要であるが、他物性とのバランス化を図る必要がある。
In addition, with the rise of environmental regulations due to global warming, low rolling resistance of tires is required, and in order to meet that requirement with rubber compositions for tires, higher silica content and higher compounding ratio are required. Has been performed (see, for example, Patent Document 2). High hardness and high elastic modulus are effective means to compensate for the decrease in steering stability caused by the low heat generation of the silica-blended rubber composition, but a higher-order balance between low rolling resistance and fracture physical properties. The market is demanding the change.
On the other hand, in the silica-blended rubber composition, the silanol group on the silica surface interferes with the functions of zinc oxide and the vulcanization accelerator, and the thermal conductivity is lowered, so that the vulcanization rate tends to be lowered. Therefore, the productivity of the tire can be improved by further adding a vulcanization accelerator or the like to increase the vulcanization rate, but there is a problem that the fracture physical properties are lowered due to the increase in modulus. Therefore, it is important to increase the vulcanization rate from the viewpoint of tire productivity, but it is necessary to balance it with other physical characteristics.

特開2009-269961号公報Japanese Unexamined Patent Publication No. 2009-269961 特開2010-13551号公報Japanese Unexamined Patent Publication No. 2010-13551

 したがって本発明の目的は、高弾性率および低発熱性を両立するとともに、加硫速度を速め得るゴム組成物およびそれを用いた空気入りタイヤを提供することにある。 Therefore, an object of the present invention is to provide a rubber composition capable of increasing the vulcanization rate while achieving both high elastic modulus and low heat generation, and a pneumatic tire using the same.

 本発明者らは鋭意研究を重ねた結果、ジエン系ゴムに対し、カーボンブラックおよびシリカから選択された1種以上、および特定のフェノール樹脂を特定量でもって配合することにより、上記課題を解決できることを見出し、本発明を完成することができた。
 すなわち本発明は、ジエン系ゴム100質量部に対し、カーボンブラックおよびシリカから選択された1種以上を1~300質量部、および分子中に下記の化学式(1)で表されるアルキレンアミン由来の構造単位を少なくとも1個以上有するフェノール樹脂を0.1~20質量部配合してなることを特徴とするタイヤ用ゴム組成物を提供するものである。
As a result of intensive research, the present inventors can solve the above-mentioned problems by blending one or more kinds selected from carbon black and silica and a specific phenol resin in a specific amount with the diene rubber. We were able to complete the present invention.
That is, the present invention is derived from 1 to 300 parts by mass of one or more selected from carbon black and silica with respect to 100 parts by mass of diene rubber, and alkyleneamine represented by the following chemical formula (1) in the molecule. The present invention provides a rubber composition for a tire, which comprises 0.1 to 20 parts by mass of a phenol resin having at least one structural unit.

Figure JPOXMLDOC01-appb-C000003
Figure JPOXMLDOC01-appb-C000003

(上記一般式(1)中、Rは、それぞれ独立して、炭素数1~10の直鎖状または分岐状のアルキレン基を表す。)
 また本発明は、本発明の前記タイヤ用ゴム組成物を用いてなる空気入りタイヤを提供するものである。
(In the above general formula (1), R 1 independently represents a linear or branched alkylene group having 1 to 10 carbon atoms.)
The present invention also provides a pneumatic tire using the rubber composition for a tire of the present invention.

 本発明によれば、ジエン系ゴムに対し、カーボンブラックおよびシリカから選択された1種以上、および特定のフェノール樹脂を特定量でもって配合したので、高弾性率および低発熱性を両立するとともに、加硫速度を速め得るタイヤ用ゴム組成物およびそれを用いた空気入りタイヤを提供することができる。
 本発明において、特定のフェノール樹脂を配合することにより、カーボンブラックまたはシリカ表面のシラノール基とフェノール樹脂におけるアルキレンアミン由来の構造単位とが相互作用して加硫が促進されるとともに、高弾性率化、低発熱化を同時に達成できるものと推測される。また、高破断物性化を同時に達成できる。
According to the present invention, since one or more selected from carbon black and silica and a specific phenol resin are blended in a specific amount with the diene rubber, both high elastic modulus and low heat generation property are achieved, and at the same time, It is possible to provide a rubber composition for a tire capable of increasing the vulcanization rate and a pneumatic tire using the same.
In the present invention, by blending a specific phenol resin, the silanol groups on the surface of carbon black or silica interact with the structural units derived from alkylene amine in the phenol resin to promote vulcanization and increase the elastic modulus. It is presumed that low heat generation can be achieved at the same time. In addition, high fracture physical properties can be achieved at the same time.

 以下、本発明をさらに詳細に説明する。 Hereinafter, the present invention will be described in more detail.

(ジエン系ゴム)
 本発明で使用されるジエン系ゴムは、とくに制限されず、例えば、天然ゴム(NR)、合成イソプレンゴム(IR)、スチレン-ブタジエン共重合体ゴム(SBR)、ブタジエンゴム(BR)、アクリロニトリル-ブタジエン共重合体ゴム(NBR)等が挙げられる。中でも、NR、IR、SBRが好ましい。これらは、単独で用いてもよく、2種以上を併用してもよい。また、その分子量やミクロ構造はとくに制限されず、アミン、アミド、シリル、アルコキシシリル、カルボキシル、ヒドロキシル基等で末端変性されていても、エポキシ化されていてもよい。
(Diene rubber)
The diene rubber used in the present invention is not particularly limited, and for example, natural rubber (NR), synthetic isoprene rubber (IR), styrene-butadiene copolymer rubber (SBR), butadiene rubber (BR), acrylonitrile- Examples thereof include butadiene copolymer rubber (NBR). Of these, NR, IR and SBR are preferable. These may be used alone or in combination of two or more. The molecular weight and microstructure thereof are not particularly limited, and may be terminal-modified with an amine, amide, silyl, alkoxysilyl, carboxyl, hydroxyl group, or the like, or may be epoxidized.

(カーボンブラック)
 本発明で使用するカーボンブラックは、本発明の効果向上の観点から、窒素吸着比表面積(NSA)が33~500m/gであることが好ましい。なお、窒素吸着比表面積(NSA)はJIS K6217-2に準拠して求めた値である。
(Carbon black)
The carbon black used in the present invention preferably has a nitrogen adsorption specific surface area (N 2 SA) of 33 to 500 m 2 / g from the viewpoint of improving the effect of the present invention. The nitrogen adsorption specific surface area (N 2 SA) is a value obtained in accordance with JIS K6217-2.

(シリカ)
 本発明で使用するシリカは特に限定されず、例えばタイヤ用途でゴム組成物に配合されている従来公知の任意のシリカを用いることができる。
 シリカの具体例としては、湿式シリカ、乾式シリカ、ヒュームドシリカ等が挙げられる。シリカは、1種のシリカを単独で用いても、2種以上のシリカを併用してもよい。
 また本発明の効果向上の観点から、本発明で使用されるシリカは、CTAB比表面積が70~300m/gであるのが好ましく、80~250m/gであるのがさらに好ましい。
 なお本明細書において、CTAB比表面積は、シリカ表面へのCTAB吸着量をJIS  K6217-3:2001「第3部:比表面積の求め方-CTAB吸着法」にしたがって測定した値である。
(silica)
The silica used in the present invention is not particularly limited, and for example, any conventionally known silica blended in a rubber composition for tire applications can be used.
Specific examples of silica include wet silica, dry silica, fumed silica and the like. As the silica, one type of silica may be used alone, or two or more types of silica may be used in combination.
From the viewpoint of improving the effect of the present invention, the silica used in the present invention preferably has a CTAB specific surface area of 70 to 300 m 2 / g, more preferably 80 to 250 m 2 / g.
In the present specification, the CTAB specific surface area is a value obtained by measuring the amount of CTAB adsorbed on the silica surface according to JIS K6217-3: 2001 "Part 3: How to obtain the specific surface area-CTAB adsorption method".

(フェノール樹脂)
 本発明で使用されるフェノール樹脂は、分子中に下記の化学式(1)で表されるアルキレンアミン由来の構造単位を、少なくとも1個以上有するものである。
(Phenolic resin)
The phenol resin used in the present invention has at least one structural unit derived from an alkylene amine represented by the following chemical formula (1) in its molecule.

Figure JPOXMLDOC01-appb-C000004
Figure JPOXMLDOC01-appb-C000004

 上記一般式(1)中、Rは、それぞれ独立して、炭素数1~10の直鎖状または分岐状のアルキレン基を表す。Rのアルキレン基の炭素数は、例えば、1~10、好ましくは2~6、より好ましくは2~4である。 In the above general formula (1), R 1 independently represents a linear or branched alkylene group having 1 to 10 carbon atoms. The alkylene group of R 1 has, for example, 1 to 10, preferably 2 to 6, and more preferably 2 to 4.

 フェノール樹脂は、本発明の効果向上の観点から、分子中に下記の化学式(2)で表されるエチレンアミン由来の構造単位を少なくとも1個以上有するものを含んでもよい。 From the viewpoint of improving the effect of the present invention, the phenol resin may contain at least one structural unit derived from ethyleneamine represented by the following chemical formula (2) in the molecule.

Figure JPOXMLDOC01-appb-C000005
Figure JPOXMLDOC01-appb-C000005

 フェノール樹脂中におけるアルキレンアミンまたはエチレンアミン由来の構造単位の含有比率の下限は、例えば、3質量%以上、好ましくは5質量%以上、より好ましくは10質量%以上である。これにより、弾性率を向上できる。一方、フェノール樹脂中におけるエチレンアミン由来の構造単位の含有比率の上限は、例えば、50質量%以下、好ましくは45質量%以下、より好ましくは40質量%以下でもよい。これにより、軟化点を適当に調整することができる。
 エチレンアミン由来構造の含有率は、以下の式に基づいて算出できる。式中の含窒素量(質量%)は、元素分析法により測定できる。
 エチレンアミン由来構造の含有率=含窒素量×(43/14)
The lower limit of the content ratio of the structural unit derived from alkyleneamine or ethyleneamine in the phenol resin is, for example, 3% by mass or more, preferably 5% by mass or more, and more preferably 10% by mass or more. Thereby, the elastic modulus can be improved. On the other hand, the upper limit of the content ratio of the structural unit derived from ethyleneamine in the phenol resin may be, for example, 50% by mass or less, preferably 45% by mass or less, and more preferably 40% by mass or less. Thereby, the softening point can be appropriately adjusted.
The content of the ethyleneamine-derived structure can be calculated based on the following formula. The nitrogen content (mass%) in the formula can be measured by an elemental analysis method.
Ethyleneamine-derived structure content = nitrogen content x (43/14)

 フェノール樹脂の軟化点は、例えば、60℃~150℃、好ましくは65℃~130℃、より好ましくは70℃~120℃である。フェノール樹脂の軟化点は、ゴムに配合したときの加熱混練時における加熱温度に応じて、適切に制御され得る。これにより、ゴム物性バラツキの少ないゴムを実現できる。 The softening point of the phenol resin is, for example, 60 ° C. to 150 ° C., preferably 65 ° C. to 130 ° C., and more preferably 70 ° C. to 120 ° C. The softening point of the phenolic resin can be appropriately controlled according to the heating temperature at the time of heating and kneading when blended with rubber. As a result, it is possible to realize a rubber having little variation in rubber physical characteristics.

 フェノール樹脂は、フェノール類、アルデヒド類、およびアルキレンアミンの重合物で構成されてもよい。フェノール樹脂は、これらの未反応モノマーを含んでもよいし、含まなくてもよい。 The phenolic resin may be composed of a polymer of phenols, aldehydes, and alkyleneamines. The phenolic resin may or may not contain these unreacted monomers.

 フェノール類の一例としては、特に限定されないが、例えば、フェノール;オルソクレゾール、メタクレゾール、パラクレゾール等のクレゾール;2、3-キシレノール、2、4-キシレノール、2、5-キシレノール、2、6-キシレノール、3、5-キシレノール等のキシレノール;2,3,5-トリメチルフェノール、2-エチルフェノール、4-エチルフェノール、2-イソプロピルフェノール、4-イソプロピルフェノール、n-ブチルフェノール、イソブチルフェノール、tert-ブチルフェノール、ヘキシルフェノール、オクチルフェノール、ノニルフェノール、フェニルフェノール、ベンジルフェノール、クミルフェノール、アリルフェノール、カルダノール、ウルシオール、チチオール、ラッコール等のアルキルフェノール;1-ナフトール、2-ナフトール等のナフトール;フルオロフェノール、クロロフェノール、ブロモフェノール、ヨードフェノール等のハロゲン化フェノール、p-フェニルフェノール、アミノフェノール、ニトロフェノール、ジニトロフェノール、トリニトロフェノール等の1価フェノール置換体;レゾルシン、アルキルレゾルシン、ピロガロール、カテコール、アルキルカテコール、ハイドロキノン、アルキルハイドロキノン、フロログルシン、ビスフェノールA、ビスフェノールF、ビスフェノールS、ジヒドロキシナフタリン、ナフタレン等の多価フェノール;などが挙げられる。これらを単独で用いても2種以上を組み合わせて用いてもよい。これらの中でも、フェノール類は、フェノール、クレゾール、キシレノールおよびアルキルフェノールからなる群より選ばれた1種以上を含ことができ、安価な観点から、フェノールを用いることができる。 Examples of phenols are not particularly limited, but for example, phenol; cresols such as orthocresol, metacresol, paracresol; 2,3-xylenol, 2,4-xylenol, 2,5-xylenol, 2,6- Xylenol, such as 3,5-xylenol; 2,3,5-trimethylphenol, 2-ethylphenol, 4-ethylphenol, 2-isopropylphenol, 4-isopropylphenol, n-butylphenol, isobutylphenol, tert-butylphenol Alkylphenol such as hexylphenol, octylphenol, nonylphenol, phenylphenol, benzylphenol, cumylphenol, allylphenol, cardanol, ursiol, thithiol, laccol; naphthol such as 1-naphthol and 2-naphthol; fluorophenol, chlorophenol, Halogenated phenols such as bromophenol and iodophenol, monovalent phenol substitutions such as p-phenylphenol, aminophenol, nitrophenol, dinitrophenol and trinitrophenol; resorcin, alkylresorcin, pyrogallol, catechol, alkylcatechol, hydroquinone, Polyhydric phenols such as alkylhydroquinone, fluoroglucin, bisphenol A, bisphenol F, bisphenol S, dihydroxynaphthalin, and naphthalene; and the like can be mentioned. These may be used alone or in combination of two or more. Among these, phenols can include one or more selected from the group consisting of phenol, cresol, xylenol and alkylphenol, and phenol can be used from an inexpensive viewpoint.

 アルデヒド類としては、特に限定されないが、例えば、ホルマリンやパラホルムアルデヒド等のホルムアルデヒド;トリオキサン、アセトアルデヒド、プロピオンアルデヒド、ポリオキシメチレン、クロラール、ヘキサメチレンテトラミン、フルフラール、グリオキザール、n-ブチルアルデヒド、カプロアルデヒド、アリルアルデヒド、ベンズアルデヒド、クロトンアルデヒド、アクロレイン、テトラオキシメチレン、フェニルアセトアルデヒド、o-トルアルデヒド、サリチルアルデヒド等が挙げられる。これらのアルデヒド類は単独または2種以上を組み合わせて使用してもよい。この中でも、アルデヒド類は、ホルムアルデヒドまたはアセトアルデヒドを含むことができ、生産性および安価な観点から、ホルマリンまたはパラホルムアルデヒドを用いることができる。 The aldehydes are not particularly limited, but for example, formaldehyde such as formalin and paraformaldehyde; trioxane, acetaldehyde, propionaldehyde, polyoxymethylene, chloral, hexamethylenetetramine, furfural, glioxal, n-butylaldehyde, caproaldehyde, etc. Examples thereof include allyl aldehyde, benz aldehyde, croton aldehyde, acrolein, tetraoxymethylene, phenylacetaldehyde, o-tolu aldehyde and salicyl aldehyde. These aldehydes may be used alone or in combination of two or more. Among these, aldehydes can include formaldehyde or acetaldehyde, and formalin or paraformaldehyde can be used from the viewpoint of productivity and low cost.

 アルキレンアミンは、分子内に、炭素数1~10の直鎖状または分岐状のアルキレン基を1個以上備える脂肪族アミンを用いることができる。脂肪族アミンは、1個以上の一級アミン及び/又は二級アミンを含む化合物であってもよい。例えば、脂肪族アミンとして、ジエチレントリアミン、トリエチレンテトラアミン、テトラエチレンペンタアミン、ペンタエチレンヘキサアミン、ポリエチレンイミン、ジプロピレントリアミン、トリプロピレンテトラアミン、テトラプロピレンペンタアミン、ペンタプロピレンヘキサアミン、ポリプロピレンイミン等のポリアルキレンポリアミンが挙げられる。これらを単独で用いても2種以上を組み合わせて用いてもよい。 As the alkylene amine, an aliphatic amine having one or more linear or branched alkylene groups having 1 to 10 carbon atoms in the molecule can be used. The aliphatic amine may be a compound containing one or more primary amines and / or secondary amines. For example, as aliphatic amines, diethylene triamine, triethylene tetraamine, tetraethylene pentaamine, pentaethylene hexaamine, polyethyleneimine, dipropylene triamine, tripropylene tetraamine, tetrapropylene pentaamine, pentapropylene hexaamine, polypropyleneimine and the like Examples include polyalkylene polyamines. These may be used alone or in combination of two or more.

 詳細なメカニズムは定かではないが、アルデヒド類が、フェノール類およびアルキレンアミンの両方に反応すると考えられる。 Although the detailed mechanism is not clear, it is thought that aldehydes react with both phenols and alkyleneamines.

 フェノール樹脂を合成する際に用いる触媒は、無触媒でも構わないし、ノボラック型フェノール樹脂を製造する観点から、酸性触媒を用いることができる。酸性触媒としては、特に限定するものではないが、例えば、蓚酸、塩酸、硫酸、ジエチル硫酸、パラトルエンスルホン酸等の酸類、酢酸亜鉛等の金属塩類が挙げられ、これらを単独または2種類以上併用して使用できる。 The catalyst used when synthesizing the phenol resin may be non-catalyst, or an acidic catalyst can be used from the viewpoint of producing a novolak type phenol resin. The acidic catalyst is not particularly limited, and examples thereof include acids such as oxalic acid, hydrochloric acid, sulfuric acid, diethyl sulfate, and paratoluenesulfonic acid, and metal salts such as zinc acetate, which may be used alone or in combination of two or more. Can be used.

 フェノール樹脂を合成する際に用いる反応溶媒としては、水を用いてもよいが、有機溶剤を用いてもよい。有機溶剤としては、非極性溶媒を用いて非水系を用いることができる。有機溶剤の一例としては、例えば、アルコール類、ケトン類、芳香族類で、アルコール類としては、メタノール、エタノール、プロピルアルコール、エチレングリコール、ジエチレングリコール、トリエチレングリコール、グリセリン等で、ケトン類としては、アセトン、メチルエチルケトン等で、芳香族類としては、トルエン、キシレン等が挙げられる。これらを単独で用いても2種以上を組み合わせて用いてもよい。 Water may be used as the reaction solvent used when synthesizing the phenol resin, but an organic solvent may be used. As the organic solvent, a non-polar solvent can be used and a non-aqueous system can be used. Examples of organic solvents include, for example, alcohols, ketones, and aromatics, alcohols include methanol, ethanol, propyl alcohol, ethylene glycol, diethylene glycol, triethylene glycol, glycerin, and the like, and ketones include. Acetone, methyl ethyl ketone and the like, and examples of the aromatics include toluene, xylene and the like. These may be used alone or in combination of two or more.

 また、フェノール類(P)とアルデヒド類(F)のモル比(F/Pモル比)は、フェノール類1モルに対し、例えば、アルデヒド類を0.2~1.0モルとしてもよく、好ましくは0.3~0.9モルとすることができる。アルデヒド類を上記範囲とすることで、未反応フェノール量を少なくすることができ、歩留まりを上げることができる。また、フェノール類(P)とアルデヒド類(F)の反応モル比(F/P)を1.0以下の条件、すなわち、モル比換算でフェノールリッチの条件を制御することで、適度な軟化点を有するアルキレンアミン由来の構造単位を含むフェノール樹脂が得られ、このようなフェノール樹脂は、加熱条件下での混合・混練によってゴム中に良好に相溶または分散させることが可能である。 The molar ratio (F / P molar ratio) of phenols (P) and aldehydes (F) may be, for example, 0.2 to 1.0 mol of aldehydes with respect to 1 mol of phenols, which is preferable. Can be 0.3-0.9 mol. By setting the aldehydes in the above range, the amount of unreacted phenol can be reduced and the yield can be increased. Further, by controlling the reaction molar ratio (F / P) of phenols (P) and aldehydes (F) to 1.0 or less, that is, the phenol-rich condition in terms of molar ratio, an appropriate softening point is obtained. A phenolic resin containing a structural unit derived from an alkyleneamine having the above can be obtained, and such a phenolic resin can be satisfactorily compatible or dispersed in rubber by mixing and kneading under heating conditions.

 また、反応温度は、例えば、40℃~120℃としてもよく、好ましくは60℃~110℃としてもよい。なお、反応時間は、特に制限はなく、出発原料の種類、配合モル比、触媒の使用量及び種類、反応条件に応じて適宜決定すればよい。 Further, the reaction temperature may be, for example, 40 ° C. to 120 ° C., preferably 60 ° C. to 110 ° C. The reaction time is not particularly limited and may be appropriately determined according to the type of starting material, the compounding molar ratio, the amount and type of catalyst used, and the reaction conditions.

 以上により、本発明で使用されるフェノール樹脂を得ることができる。フェノール樹脂は、分子中に、ノボラック骨格及び前記エチレンアミン由来の構造単位を有するノボラック型フェノール樹脂を含んでもよい。 From the above, the phenolic resin used in the present invention can be obtained. The phenolic resin may contain a novolak-type phenolic resin having a novolak skeleton and a structural unit derived from the ethyleneamine in the molecule.

(タイヤ用ゴム組成物の配合割合)
 本発明のゴム組成物は、ジエン系ゴム100質量部に対し、カーボンブラックおよびシリカから選択された1種以上を1~300質量部、および前記分子中に化学式(1)で表されるアルキレンアミン由来の構造単位を少なくとも1個以上有するフェノール樹脂を0.1~20質量部配合してなることを特徴とする。
 カーボンブラックの配合量が1質量部未満であると配合量が少な過ぎて本発明の効果を奏することができない。逆に300質量部を超えると発熱性が悪化する。
 シリカの配合量が1質量部未満であると配合量が少な過ぎて本発明の効果を奏することができない。逆に300質量部を超えると耐摩耗性や発熱性の悪化が著しい。
 前記フェノール樹脂の配合量が0.1質量部未満であると、配合量が少な過ぎて本発明の効果を奏することができない。逆に20質量部を超えると耐摩耗性および発熱性が悪化する。
(Mixing ratio of rubber composition for tires)
The rubber composition of the present invention contains 1 to 300 parts by mass of one or more selected from carbon black and silica with respect to 100 parts by mass of diene rubber, and an alkylene amine represented by the chemical formula (1) in the molecule. It is characterized by blending 0.1 to 20 parts by mass of a phenol resin having at least one derived structural unit.
If the blending amount of carbon black is less than 1 part by mass, the blending amount is too small to achieve the effect of the present invention. On the contrary, if it exceeds 300 parts by mass, the heat generation property deteriorates.
If the blending amount of silica is less than 1 part by mass, the blending amount is too small to achieve the effect of the present invention. On the contrary, if it exceeds 300 parts by mass, the wear resistance and heat generation property are significantly deteriorated.
If the blending amount of the phenol resin is less than 0.1 parts by mass, the blending amount is too small to achieve the effect of the present invention. On the contrary, if it exceeds 20 parts by mass, the wear resistance and heat generation property deteriorate.

 また、本発明のゴム組成物において、カーボンブラックの配合量は、ジエン系ゴム100質量部に対し、1~200質量部であることが好ましい。
 シリカの配合量は、ジエン系ゴム100質量部に対し、20~250質量部であることが好ましい。
 前記フェノール樹脂の配合量は、ジエン系ゴム100質量部に対し、0.1~20質量部であることが好ましく、1~15質量部であることがさらに好ましい。
Further, in the rubber composition of the present invention, the blending amount of carbon black is preferably 1 to 200 parts by mass with respect to 100 parts by mass of the diene rubber.
The amount of silica blended is preferably 20 to 250 parts by mass with respect to 100 parts by mass of the diene rubber.
The blending amount of the phenol resin is preferably 0.1 to 20 parts by mass, and more preferably 1 to 15 parts by mass with respect to 100 parts by mass of the diene rubber.

 なお、カーボンブラックとシリカとは必要に応じて併用することもできる。 In addition, carbon black and silica can be used together as needed.

(その他成分)
 本発明におけるゴム組成物には、前記した成分に加えて、加硫又は架橋剤;加硫又は架橋促進剤;酸化亜鉛、クレー、タルク、炭酸カルシウムのような各種充填剤;老化防止剤;可塑剤などのゴム組成物に一般的に配合されている各種添加剤を配合することができ、かかる添加剤は一般的な方法で混練して組成物とし、加硫又は架橋するのに使用することができる。これらの添加剤の配合量も、本発明の目的に反しない限り、従来の一般的な配合量とすることができる。
(Other ingredients)
In addition to the above-mentioned components, the rubber composition in the present invention includes a vulcanization or cross-linking agent; a vulcanization or cross-linking accelerator; various fillers such as zinc oxide, clay, talc, and calcium carbonate; an antiaging agent; plastic. Various additives generally blended in rubber compositions such as agents can be blended, and such additives are kneaded by a general method to form a composition, which is used for vulcanization or cross-linking. Can be done. The blending amount of these additives can also be a conventional general blending amount as long as it does not contradict the object of the present invention.

 なお本発明におけるゴム組成物は、前記フェノール樹脂の硬化のためにメチレンドナーを使用することもでき、その種類としてはとくに制限されないが、例えばヘキサメチレンテトラミン、HMMM(ヘキサメトキシメチロールメラミンの部分縮合物)、PMMM(ヘキサメチロールメラミンペンタメチルエーテルの部分縮合物)のような多価メチロールメラミン誘導体、ヘキサエトキシメチルメラミン、パラ-ホルムアルデヒドのポリマー、メラミンのN-メチロール誘導体等が挙げられ、本発明の効果向上の観点から、ヘキサメチレンテトラミンまたは多価メチロールメラミン誘導体が好ましい。 In the rubber composition of the present invention, a methylene donor can be used for curing the phenol resin, and the type thereof is not particularly limited, but for example, hexamethylenetetramine and HMMM (partial condensate of hexamethoxymethylol melamine). ), Polyvalent methylol melamine derivatives such as PMMM (partial condensate of hexamethylol melamine pentamethyl ether), hexaethoxymethyl melamine, para-formaldehyde polymers, N-methylol derivatives of melamine, etc., and the effects of the present invention. From the viewpoint of improvement, hexamethylenetetramine or polyvalent methylolmelamine derivative is preferable.

 メチレンドナーの配合量は、前記ジエン系ゴム100質量部に対し、0.1~5質量部が好ましく、0.1~2.5質量部がさらに好ましい。 The blending amount of the methylene donor is preferably 0.1 to 5 parts by mass, more preferably 0.1 to 2.5 parts by mass with respect to 100 parts by mass of the diene rubber.

 また本発明のタイヤ用ゴム組成物は従来の空気入りタイヤの製造方法に従って空気入りタイヤを製造することができ、例えばタイヤ用キャップトレッド、アンダートレッド、サイドウォール、ベルトコート、ベルトクッション、リムクッション、インナーライナー、ビードフィラー等に好適に用いることができる。 Further, the rubber composition for a tire of the present invention can produce a pneumatic tire according to a conventional method for producing a pneumatic tire, for example, a tire cap tread, an under tread, a sidewall, a belt coat, a belt cushion, a rim cushion, and the like. It can be suitably used for inner liners, bead fillers and the like.

 以下、本発明を実施例および比較例によりさらに説明するが、本発明は下記例に制限されるものではない。なお、例中、部となるのは特記しない限り質量基準である。 Hereinafter, the present invention will be further described with reference to Examples and Comparative Examples, but the present invention is not limited to the following examples. In the example, the part is based on mass unless otherwise specified.

<フェノール樹脂の合成>
(製造例1)
 攪拌装置、還流冷却器及び温度計を備えた反応器に、フェノール1000部、37%ホルマリン水溶液561部、トリエチレンテトラアミン55部を仕込み、還流条件下で2時間反応させた。ついで水を蒸留除去しながら200℃で3時間反応させた。さらに所定の水分、遊離モノマー量になるまで減圧下で水、未反応モノマーの蒸留除去を行った後、反応器から取り出し、フェノール樹脂1を得た。
 フェノール樹脂1の、軟化点は110℃であり、含窒素量は2.2質量%であり、エチレンアミン由来構造の含有率は6.8質量%であった。
<Synthesis of phenolic resin>
(Manufacturing Example 1)
A reactor equipped with a stirrer, a reflux condenser and a thermometer was charged with 1000 parts of phenol, 561 parts of a 37% formalin aqueous solution, and 55 parts of triethylenetetraamine, and reacted under reflux conditions for 2 hours. Then, the reaction was carried out at 200 ° C. for 3 hours while removing water by distillation. Further, water and unreacted monomers were distilled and removed under reduced pressure until a predetermined amount of water and free monomers were reached, and then the mixture was taken out from the reactor to obtain phenol resin 1.
The softening point of the phenol resin 1 was 110 ° C., the nitrogen content was 2.2% by mass, and the content of the ethyleneamine-derived structure was 6.8% by mass.

(製造例2)
 37%ホルマリン水溶液の配合量を518部、トリエチレンテトラアミンの配合量を110部としたこと以外は、製造例1と同様にしてフェノール樹脂2を得た。
 フェノール樹脂2の、軟化点は108℃であり、含窒素量は4.1質量%であり、エチレンアミン由来構造の含有率は12.6質量%であった。
(Manufacturing Example 2)
Phenolic resin 2 was obtained in the same manner as in Production Example 1 except that the amount of the 37% formalin aqueous solution was 518 parts and the amount of triethylenetetraamine was 110 parts.
The softening point of the phenol resin 2 was 108 ° C., the nitrogen content was 4.1% by mass, and the content of the ethyleneamine-derived structure was 12.6% by mass.

(製造例3)
 37%ホルマリン水溶液の配合量を500部、トリエチレンテトラアミンの配合量を165部としたこと以外は、製造例1と同様にしてフェノール樹脂3を得た。
 フェノール樹脂3の、軟化点は102℃であり、含窒素量は6.4質量%であり、エチレンアミン由来構造の含有率は19.7質量%であった。
(Manufacturing Example 3)
The phenol resin 3 was obtained in the same manner as in Production Example 1 except that the amount of the 37% formalin aqueous solution was 500 parts and the amount of triethylenetetraamine was 165 parts.
The softening point of the phenol resin 3 was 102 ° C., the nitrogen content was 6.4% by mass, and the content of the ethyleneamine-derived structure was 19.7% by mass.

実施例1~6および比較例1~3
サンプルの調製
 表1に示す配合(質量部)において、加硫促進剤と硫黄を除く成分を1.7リットルの密閉式バンバリーミキサーで5分間混練し、ゴムをミキサー外に放出して室温冷却した。次いで、該ゴムを同ミキサーに再度入れ、加硫促進剤および硫黄を加えてさらに混練し、ゴム組成物を得た。次に得られたゴム組成物を所定の金型中で160℃、20分間プレス加硫して加硫ゴム試験片を得、以下に示す試験法で未加硫のゴム組成物および加硫ゴム試験片の物性を測定した。
Examples 1 to 6 and Comparative Examples 1 to 3
Sample Preparation In the formulation (parts by mass) shown in Table 1, the vulcanization accelerator and the components excluding sulfur were kneaded with a 1.7 liter sealed Banbury mixer for 5 minutes, and the rubber was discharged to the outside of the mixer and cooled to room temperature. .. Then, the rubber was put into the same mixer again, a vulcanization accelerator and sulfur were added, and the mixture was further kneaded to obtain a rubber composition. Next, the obtained rubber composition was press-vulcanized in a predetermined mold at 160 ° C. for 20 minutes to obtain a vulcanized rubber test piece, and the unvulcanized rubber composition and the vulcanized rubber were obtained by the test method shown below. The physical properties of the test piece were measured.

 加硫速度(T95):JIS K6300に準拠して、振動式ディスク加硫試験機にて、振幅1度、150℃で95%の加硫度に達する時間(T95、分)を測定した。結果は、比較例1の値を100として指数で示した。この値が小さいほど、加硫速度が速く、生産性に優れることを示す。
 貯蔵弾性率:JIS  K6394に準拠し、初期歪10%、振幅±2%、周波数20Hzの条件下で、東洋精機製作所製粘弾性スペクトロメータにより20℃で測定した。結果は、比較例1の値を100として指数で示した。この値が大きいほど、高弾性率であることを示す。
 tanδ(60℃):(株)東洋精機製作所製、粘弾性スペクトロメーターを用い、初期歪10%、振幅±2%、周波数20Hz、温度60℃の条件で、tanδ(60℃)を測定した。結果は、比較例1の値を100として指数で示した。この値が小さいほど、低発熱性であることを示す。
 結果を表1に併せて示す。
Vulcanization rate (T95): In accordance with JIS K6300, the time (T95, min) to reach 95% vulcanization degree at an amplitude of 1 degree and 150 ° C. was measured with a vibrating disk vulcanization tester. The results are shown exponentially with the value of Comparative Example 1 as 100. The smaller this value is, the faster the vulcanization rate is and the better the productivity is.
Storage elastic modulus: Measured at 20 ° C. with a viscoelastic spectrometer manufactured by Toyo Seiki Seisakusho under the conditions of initial strain 10%, amplitude ± 2%, and frequency 20 Hz in accordance with JIS K6394. The results are shown exponentially with the value of Comparative Example 1 as 100. The larger this value is, the higher the elastic modulus is.
Tanδ (60 ° C.): Using a viscoelastic spectrometer manufactured by Toyo Seiki Seisakusho Co., Ltd., tanδ (60 ° C.) was measured under the conditions of initial strain of 10%, amplitude of ± 2%, frequency of 20 Hz, and temperature of 60 ° C. The results are shown exponentially with the value of Comparative Example 1 as 100. The smaller this value is, the lower the heat generation is.
The results are also shown in Table 1.

Figure JPOXMLDOC01-appb-T000006
Figure JPOXMLDOC01-appb-T000006

表1中における番号の詳細は以下の通りである。
*1:NR(STR20)
*2:カーボンブラック(キャボットジャパン社製N339、窒素吸着比表面積(NSA)=90m/g)
*3:ストレートフェノール樹脂(住友ベークライト株式会社製PR50731。アルキレンアミン由来の構造単位を持たない。)
*4:フェノール樹脂1(前記製造例1で製造したフェノール樹脂1)
*5:フェノール樹脂2(前記製造例2で製造したフェノール樹脂2)
*6:フェノール樹脂3(前記製造例3で製造したフェノール樹脂3)
*7:ヘキサメチレンテトラミン(大内新興化学工業株式会社製ヘキサメチレンテトラミン)
*8:酸化亜鉛(正同化学工業株式会社製酸化亜鉛3種)
*9:ステアリン酸(日油株式会社製ビーズステアリン酸YR)
*10:オイル(昭和シェル石油株式会社製エキストラクト4号S)
*11:硫黄(細井化学工業株式会社製油処理イオウ)
*12:加硫促進剤(三新化学工業株式会社製サンセラーNS-P)
The details of the numbers in Table 1 are as follows.
* 1: NR (STR20)
* 2: Carbon black (N339 manufactured by Cabot Japan, nitrogen adsorption specific surface area (N 2 SA) = 90 m 2 / g)
* 3: Straight phenolic resin (PR50731 manufactured by Sumitomo Bakelite Co., Ltd., which does not have a structural unit derived from alkyleneamine)
* 4: Phenolic resin 1 (phenol resin 1 produced in Production Example 1)
* 5: Phenolic resin 2 (phenol resin 2 produced in Production Example 2)
* 6: Phenolic resin 3 (phenolic resin 3 produced in Production Example 3)
* 7: Hexamethylenetetramine (hexamethylenetetramine manufactured by Ouchi Shinko Kagaku Kogyo Co., Ltd.)
* 8: Zinc oxide (3 types of zinc oxide manufactured by Shodo Chemical Industry Co., Ltd.)
* 9: Stearic acid (bead stearic acid YR manufactured by NOF CORPORATION)
* 10: Oil (Extract No. 4 S manufactured by Showa Shell Sekiyu Co., Ltd.)
* 11: Sulfur (oil-treated sulfur from Hosoi Chemical Industry Co., Ltd.)
* 12: Vulcanization accelerator (Suncellor NS-P manufactured by Sanshin Chemical Industry Co., Ltd.)

 表1の結果から、実施例1~6のゴム組成物は、ジエン系ゴムに対し、カーボンブラックおよび特定のフェノール樹脂を特定量でもって配合したので、比較例1に比べて、加硫速度が速く、貯蔵弾性率が高く、発熱性が低い結果となった。
 これに対し、比較例2は、アルキレンアミン由来の構造単位を持たないストレートフェノール樹脂およびメチレンドナーを使用した例であり、比較例1に比べて、加硫速度が遅い結果となった。
 比較例3は、フェノール樹脂を配合していない例であり、比較例1に比べて、貯蔵弾性率が悪化した。
From the results in Table 1, the rubber compositions of Examples 1 to 6 contained carbon black and a specific phenol resin in a specific amount with respect to the diene rubber, so that the vulcanization rate was higher than that of Comparative Example 1. The result was fast, high storage elastic modulus, and low calorific value.
On the other hand, Comparative Example 2 was an example in which a straight phenol resin and a methylene donor having no structural unit derived from alkyleneamine were used, and the vulcanization rate was slower than that of Comparative Example 1.
Comparative Example 3 is an example in which a phenol resin is not blended, and the storage elastic modulus is worse than that of Comparative Example 1.

標準例1、実施例7~12および比較例4~5
サンプルの調製
 表2に示す配合(質量部)において、加硫促進剤と硫黄を除く成分を1.7リットルの密閉式バンバリーミキサーで5分間混練し、ゴムをミキサー外に放出して室温冷却した。次いで、該ゴムを同ミキサーに再度入れ、加硫促進剤および硫黄を加えてさらに混練し、ゴム組成物を得た。次に得られたゴム組成物を所定の金型中で160℃、20分間プレス加硫して加硫ゴム試験片を得、以下に示す試験法で未加硫のゴム組成物および加硫ゴム試験片の物性を測定した。
Standard Example 1, Examples 7 to 12 and Comparative Examples 4 to 5
Sample Preparation In the formulation (parts by mass) shown in Table 2, the vulcanization accelerator and the components excluding sulfur were kneaded with a 1.7 liter sealed Banbury mixer for 5 minutes, and the rubber was discharged to the outside of the mixer and cooled to room temperature. .. Then, the rubber was put into the same mixer again, a vulcanization accelerator and sulfur were added, and the mixture was further kneaded to obtain a rubber composition. Next, the obtained rubber composition was press-vulcanized in a predetermined mold at 160 ° C. for 20 minutes to obtain a vulcanized rubber test piece, and the unvulcanized rubber composition and the vulcanized rubber were obtained by the test method shown below. The physical properties of the test piece were measured.

  加硫速度(T30):得られたゴム組成物をJIS K6300に準拠し、温度160℃において得られるトルクと加硫時間との加硫曲線から求めた最大トルクの30%に達する迄の加硫時間(T30)を測定した。結果は、標準例1の値を100として指数で示した。この値が小さいほど、加硫速度が速く、生産性に優れることを示す。
 貯蔵弾性率:上記と同様の方法で測定した。結果は、標準例1の値を100として指数で示した。この値が大きいほど、高弾性率であることを示す。
 tanδ(60℃):上記と同様の方法で測定した。結果は、標準例1の値を100として指数で示した。この値が小さいほど、低発熱性であることを示す。
 破断強度(TB):JIS K 6251に従い、20℃で試験した。結果は、標準例1の値を100として指数で示した。この値が大きいほど、高破断強度であることを示す。
 結果を表2に併せて示す。
Vulcanization rate (T30): The obtained rubber composition is vulcanized according to JIS K6300 until it reaches 30% of the maximum torque obtained from the vulcanization curve of the torque obtained at a temperature of 160 ° C. and the vulcanization time. The time (T30) was measured. The results are shown exponentially with the value of Standard Example 1 as 100. The smaller this value is, the faster the vulcanization rate is and the better the productivity is.
Storage elastic modulus: Measured by the same method as above. The results are shown exponentially with the value of Standard Example 1 as 100. The larger this value is, the higher the elastic modulus is.
tan δ (60 ° C.): Measured by the same method as above. The results are shown exponentially with the value of Standard Example 1 as 100. The smaller this value is, the lower the heat generation is.
Breaking strength (TB): Tested at 20 ° C. according to JIS K 6251. The results are shown exponentially with the value of Standard Example 1 as 100. The larger this value is, the higher the breaking strength is.
The results are also shown in Table 2.

Figure JPOXMLDOC01-appb-T000007
Figure JPOXMLDOC01-appb-T000007

表2中における番号の詳細は以下の通りである。
*1:SBR(旭化成株式会社製E581、油展量=SBR100質量部に対し37.5質量部)
*2:BR(日本ゼオン株式会社製Nipol BR1220)
*3:シリカ(Solvay社製ZEOZIL 1165MP、CTAB比表面積=155m/g)
*4:カーボンブラック(キャボットジャパン社製N339)
*5:カシュー変性フェノール樹脂(住友ベークライト株式会社製PSM-9450。アルキレンアミン由来の構造単位を持たない。)
*6:フェノール樹脂1(前記製造例1で製造したフェノール樹脂1)
*7:フェノール樹脂2(前記製造例2で製造したフェノール樹脂2)
*8:フェノール樹脂3(前記製造例3で製造したフェノール樹脂3)
*9:ヘキサメチレンテトラミン(三新化学工業株式会社製サンセラーHT-PO)
*10:シランカップリング剤(エボニック社製Si69)
*11:酸化亜鉛(正同化学工業株式会社製酸化亜鉛3種)
*12:ステアリン酸(日油株式会社製ビーズステアリン酸YR)
*13:老化防止剤(EASTMAN社製6PPD)
*14:ワックス(大内新興化学工業株式会社製パラフィンワックス)
*15:オイル(昭和シェル石油株式会社製エキストラクト4号S)
*16:硫黄(細井化学工業株式会社製油処理イオウ)
*17:加硫促進剤1(三新化学工業株式会社製サンセラーCM-G)
*18:加硫促進剤2(住友化学株式会社製ソクシールD-G)
The details of the numbers in Table 2 are as follows.
* 1: SBR (E581 manufactured by Asahi Kasei Corporation, oil spread = 37.5 parts by mass with respect to 100 parts by mass of SBR)
* 2: BR (Nipol BR1220 manufactured by Zeon Corporation)
* 3: Silica (ZEOZIL 1165MP manufactured by Solvay, CTAB specific surface area = 155m 2 / g)
* 4: Carbon black (N339 manufactured by Cabot Japan)
* 5: Cashew-modified phenolic resin (PSM-9450 manufactured by Sumitomo Bakelite Co., Ltd., which does not have a structural unit derived from alkyleneamine)
* 6: Phenolic resin 1 (Phenolic resin 1 produced in Production Example 1)
* 7: Phenolic resin 2 (phenol resin 2 produced in Production Example 2)
* 8: Phenolic resin 3 (phenolic resin 3 produced in Production Example 3)
* 9: Hexamethylenetetramine (Suncellor HT-PO manufactured by Sanshin Chemical Industry Co., Ltd.)
* 10: Silane coupling agent (Si69 manufactured by Evonik Industries)
* 11: Zinc oxide (3 types of zinc oxide manufactured by Shodo Chemical Industry Co., Ltd.)
* 12: Stearic acid (bead stearic acid YR manufactured by NOF CORPORATION)
* 13: Anti-aging agent (6PPD manufactured by EASTMAN)
* 14: Wax (paraffin wax manufactured by Ouchi Shinko Kagaku Kogyo Co., Ltd.)
* 15: Oil (Extract No. 4 S manufactured by Showa Shell Sekiyu Co., Ltd.)
* 16: Sulfur (oil-treated sulfur from Hosoi Chemical Industry Co., Ltd.)
* 17: Vulcanization accelerator 1 (Suncellor CM-G manufactured by Sanshin Chemical Industry Co., Ltd.)
* 18: Vulcanization accelerator 2 (Sulfur DG manufactured by Sumitomo Chemical Co., Ltd.)

 表2の結果から、実施例7~12のゴム組成物は、ジエン系ゴムに対し、シリカおよび特定のフェノール樹脂を特定量でもって配合したので、標準例1に比べて、加硫速度が速く、貯蔵弾性率が高く、発熱性が低く、破断強度が高い結果となった。
 これに対し、比較例4は、フェノール樹脂を配合していないので、標準例1に比べて、加硫速度が遅くなり、また貯蔵弾性率、破断強度に劣る結果となった。
 比較例5は、標準例1に対しメチレンドナーを配合した例であり、標準例1に比べて、加硫速度が遅くなる結果となった。また破断強度にも改善が見られなかった。
From the results in Table 2, the rubber compositions of Examples 7 to 12 contained silica and a specific phenol resin in a specific amount with respect to the diene rubber, so that the vulcanization rate was faster than that of Standard Example 1. As a result, the storage elastic modulus was high, the heat generation was low, and the breaking strength was high.
On the other hand, in Comparative Example 4, since the phenol resin was not blended, the vulcanization rate was slower than that in Standard Example 1, and the storage elastic modulus and the breaking strength were inferior.
Comparative Example 5 is an example in which a methylene donor was blended with Standard Example 1, and the result was that the vulcanization rate was slower than that of Standard Example 1. In addition, no improvement was seen in the breaking strength.

標準例2~5、実施例13~25および比較例6~9
サンプルの調製
 表3、4に示す配合(質量部)において、加硫促進剤と硫黄を除く成分を1.7リットルの密閉式バンバリーミキサーで5分間混練し、ゴムをミキサー外に放出して室温冷却した。次いで、該ゴムを同ミキサーに再度入れ、加硫促進剤および硫黄を加えてさらに混練し、ゴム組成物を得た。次に得られたゴム組成物を所定の金型中で160℃、20分間プレス加硫して加硫ゴム試験片を得、以下に示す試験法で未加硫のゴム組成物および加硫ゴム試験片の物性を測定した。
Standard Examples 2-5, Examples 13-25 and Comparative Examples 6-9
Sample preparation In the formulation (parts by mass) shown in Tables 3 and 4, the vulcanization accelerator and the components excluding sulfur were kneaded in a 1.7 liter sealed Banbury mixer for 5 minutes, and the rubber was released to the outside of the mixer to room temperature. Cooled. Then, the rubber was put into the same mixer again, a vulcanization accelerator and sulfur were added, and the mixture was further kneaded to obtain a rubber composition. Next, the obtained rubber composition was press-vulcanized in a predetermined mold at 160 ° C. for 20 minutes to obtain a vulcanized rubber test piece, and the unvulcanized rubber composition and the vulcanized rubber were obtained by the test method shown below. The physical properties of the test piece were measured.

 貯蔵弾性率:上記と同様の方法で測定した。結果は、各標準例の値を100として指数で示した。この値が大きいほど、高硬度であることを示す。
 破断強度(TB):上記と同様の方法で測定した。結果は、各標準例の値を100として指数で示した。この値が大きいほど、高破断強度であることを示す。
 発熱性(tanδ60℃):上記と同様の方法で測定した。結果は、各標準例の値を100として指数で示した。この値が小さいほど、低発熱性であることを示す。
 結果を表3、4に併せて示す。
Storage elastic modulus: Measured by the same method as above. The results are shown exponentially with the value of each standard example as 100. The larger this value is, the higher the hardness is.
Breaking strength (TB): Measured by the same method as above. The results are shown exponentially with the value of each standard example as 100. The larger this value is, the higher the breaking strength is.
Exothermic (tan δ60 ° C.): Measured by the same method as above. The results are shown exponentially with the value of each standard example as 100. The smaller this value is, the lower the heat generation is.
The results are also shown in Tables 3 and 4.

 なお、実施例13~15は標準例2と対比され、実施例16~19および比較例6~7は標準例3と対比され、実施例20~22は標準例4と対比され、実施例23~25および比較例8~9は標準例5と対比される。 In addition, Examples 13 to 15 were compared with Standard Example 2, Examples 16 to 19 and Comparative Examples 6 to 7 were compared with Standard Example 3, and Examples 20 to 22 were compared with Standard Example 4, and Example 23. ~ 25 and Comparative Examples 8-9 are compared with Standard Example 5.

Figure JPOXMLDOC01-appb-T000008
Figure JPOXMLDOC01-appb-T000008

Figure JPOXMLDOC01-appb-T000009
Figure JPOXMLDOC01-appb-T000009

表3、4中における番号の詳細は以下の通りである。
*1:NR(STR20)
*2:SBR(日本ゼオン株式会社製Nipol 1502)
*3:カーボンブラックHAF(キャボットジャパン社製N330T、窒素吸着比表面積(NSA)=70m/g)
*4:カーボンブラックGPF(キャボットジャパン社製N660、窒素吸着比表面積(NSA)=36m/g)
*5:ストレートフェノール樹脂(住友ベークライト株式会社製PR50731。アルキレンアミン由来の構造単位を持たない。)
*6:フェノール樹脂1(前記製造例1で製造したフェノール樹脂1)
*7:フェノール樹脂2(前記製造例2で製造したフェノール樹脂2)
*8:フェノール樹脂3(前記製造例3で製造したフェノール樹脂3)
*9:メチレンドナー(大内新興化学工業株式会社製ヘキサメチレンテトラミン)
*10:酸化亜鉛(正同化学工業株式会社製酸化亜鉛3種)
*11:ステアリン酸(日油株式会社製ビーズステアリン酸YR)
*12:オイル(昭和シェル石油株式会社製エキストラクト4号S)
*13:硫黄(細井化学工業株式会社製油処理イオウ)
*14:加硫促進剤(大内新興化学工業株式会社製ノクセラーCZ-G)
The details of the numbers in Tables 3 and 4 are as follows.
* 1: NR (STR20)
* 2: SBR (Nipol 1502 manufactured by Zeon Corporation)
* 3: Carbon black HAF (Cabot Japan N330T, nitrogen adsorption specific surface area (N 2 SA) = 70 m 2 / g)
* 4: Carbon black GPF (Cabot Japan N660, nitrogen adsorption specific surface area (N 2 SA) = 36 m 2 / g)
* 5: Straight phenolic resin (PR50731 manufactured by Sumitomo Bakelite Co., Ltd., which does not have a structural unit derived from alkyleneamine)
* 6: Phenolic resin 1 (Phenolic resin 1 produced in Production Example 1)
* 7: Phenolic resin 2 (phenol resin 2 produced in Production Example 2)
* 8: Phenolic resin 3 (phenolic resin 3 produced in Production Example 3)
* 9: Methylene donor (hexamethylenetetramine manufactured by Ouchi Shinko Kagaku Kogyo Co., Ltd.)
* 10: Zinc oxide (3 types of zinc oxide manufactured by Shodo Chemical Industry Co., Ltd.)
* 11: Stearic acid (bead stearic acid YR manufactured by NOF CORPORATION)
* 12: Oil (Extract No. 4 S manufactured by Showa Shell Sekiyu Co., Ltd.)
* 13: Sulfur (oil-treated sulfur from Hosoi Chemical Industry Co., Ltd.)
* 14: Vulcanization accelerator (Noxeller CZ-G manufactured by Ouchi Shinko Kagaku Kogyo Co., Ltd.)

 表3、4の結果から、実施例13~25のゴム組成物は、各標準例に比べて、高硬度、高破断強度および低発熱性を同時に達成し得ることが分かった。
 これに対し、比較例6、8は特定のフェノール樹脂を配合していないので、硬度が低下した。
 比較例7、9は、特定のフェノール樹脂の配合量が本発明で規定する上限を超えているので、破断強度が改善されず、発熱性が悪化した。
From the results in Tables 3 and 4, it was found that the rubber compositions of Examples 13 to 25 can simultaneously achieve high hardness, high breaking strength and low heat generation as compared with each standard example.
On the other hand, in Comparative Examples 6 and 8, since the specific phenol resin was not blended, the hardness was lowered.
In Comparative Examples 7 and 9, since the blending amount of the specific phenol resin exceeded the upper limit specified in the present invention, the breaking strength was not improved and the heat generating property was deteriorated.

標準例6、実施例26~31および比較例10~11
サンプルの調製
 表5に示す配合(質量部)において、加硫促進剤と硫黄を除く成分を1.7リットルの密閉式バンバリーミキサーで5分間混練し、ゴムをミキサー外に放出して室温冷却した。次いで、該ゴムを同ミキサーに再度入れ、加硫促進剤および硫黄を加えてさらに混練し、ゴム組成物を得た。次に得られたゴム組成物を所定の金型中で160℃、20分間プレス加硫して加硫ゴム試験片を得、以下に示す試験法で未加硫のゴム組成物および加硫ゴム試験片の物性を測定した。
Standard Example 6, Examples 26-31 and Comparative Examples 10-11
Sample Preparation In the formulation (parts by mass) shown in Table 5, the vulcanization accelerator and the components excluding sulfur were kneaded with a 1.7 liter sealed Banbury mixer for 5 minutes, and the rubber was discharged to the outside of the mixer and cooled to room temperature. .. Then, the rubber was put into the same mixer again, a vulcanization accelerator and sulfur were added, and the mixture was further kneaded to obtain a rubber composition. Next, the obtained rubber composition was press-vulcanized in a predetermined mold at 160 ° C. for 20 minutes to obtain a vulcanized rubber test piece, and the unvulcanized rubber composition and the vulcanized rubber were obtained by the test method shown below. The physical properties of the test piece were measured.

 加硫速度(T95):上記と同様の方法で測定した。結果は、標準例6の値を100として指数で示した。この値が小さいほど、加硫速度が速く、生産性に優れることを示す。
 発熱性(tanδ60℃):上記と同様の方法で測定した。結果は、標準例6の値を100として指数で示した。この値が小さいほど、低発熱性であることを示す。
 破断強度(TB):上記と同様の方法で測定した。結果は、標準例6の値を100として指数で示した。この値が大きいほど、高破断強度であることを示す。
 耐摩耗性:岩本製作所(株)製のランボーン摩耗試験機を用い、荷重15N、スリップ率25%、時間10分、室温の条件にて測定し摩耗減量を求めた。結果は、標準例6の値を100として指数で示した。指数が大きいほど耐摩耗性に優れることを示す。
 結果を表5に併せて示す。
Vulcanization rate (T95): Measured by the same method as above. The results are shown exponentially with the value of Standard Example 6 as 100. The smaller this value is, the faster the vulcanization rate is and the better the productivity is.
Exothermic (tan δ60 ° C.): Measured by the same method as above. The results are shown exponentially with the value of Standard Example 6 as 100. The smaller this value is, the lower the heat generation is.
Breaking strength (TB): Measured by the same method as above. The results are shown exponentially with the value of Standard Example 6 as 100. The larger this value is, the higher the breaking strength is.
Abrasion resistance: Using a lambourn abrasion tester manufactured by Iwamoto Seisakusho Co., Ltd., the abrasion was measured under the conditions of a load of 15 N, a slip ratio of 25%, a time of 10 minutes, and room temperature to determine the abrasion loss. The results are shown exponentially with the value of Standard Example 6 as 100. The larger the index, the better the wear resistance.
The results are also shown in Table 5.

Figure JPOXMLDOC01-appb-T000010
Figure JPOXMLDOC01-appb-T000010

表5中における番号の詳細は以下の通りである。
*1:SBR(旭化成株式会社製SBR E581、油展量=SBR100質量部に対し37.5質量部)
*2:BR(日本ゼオン株式会社製Nipol BR1220)
*3:シリカ(Evonik社製ULTRASIL 9100GR、CTAB比表面積=210m/g)
*4:カーボンブラック(キャボットジャパン社製N339)
*5:カシュー変性フェノール樹脂(住友ベークライト株式会社製PSM-9450。アルキレンアミン由来の構造単位を持たない。)
*6:フェノール樹脂1(前記製造例1で製造したフェノール樹脂1)
*7:フェノール樹脂2(前記製造例2で製造したフェノール樹脂2)
*8:フェノール樹脂3(前記製造例3で製造したフェノール樹脂3)
*9:シランカップリング剤(Evonik社製Si69)
*10:酸化亜鉛(正同化学工業株式会社製酸化亜鉛3種)
*11:ステアリン酸(日油株式会社製ビーズステアリン酸YR)
*12:老化防止剤(EASTMAN社製6PPD)
*13:ワックス(大内新興化学工業株式会社製パラフィンワックス)
*14:オイル(昭和シェル石油株式会社製エキストラクト4号S)
*15:硫黄(細井化学工業株式会社製油処理イオウ)
*16:加硫促進剤CBS(三新化学工業株式会社製サンセラーCM-G)
*17:加硫促進剤DPG(住友化学株式会社製ソクシールD-G)
*18:末端変性SBR(旭化成株式会社製タフデンF3420。グリシジルアミン基で末端が変性されている。)
The details of the numbers in Table 5 are as follows.
* 1: SBR (SBR E581 manufactured by Asahi Kasei Corporation, oil spread = 37.5 parts by mass with respect to 100 parts by mass of SBR)
* 2: BR (Nipol BR1220 manufactured by Zeon Corporation)
* 3: Silica (ULTRASIL 9100GR manufactured by Evonik, CTAB specific surface area = 210 m 2 / g)
* 4: Carbon black (N339 manufactured by Cabot Japan)
* 5: Cashew-modified phenolic resin (PSM-9450 manufactured by Sumitomo Bakelite Co., Ltd., which does not have a structural unit derived from alkyleneamine)
* 6: Phenolic resin 1 (Phenolic resin 1 produced in Production Example 1)
* 7: Phenolic resin 2 (phenol resin 2 produced in Production Example 2)
* 8: Phenolic resin 3 (phenolic resin 3 produced in Production Example 3)
* 9: Silane coupling agent (Si69 manufactured by Evonik)
* 10: Zinc oxide (3 types of zinc oxide manufactured by Shodo Chemical Industry Co., Ltd.)
* 11: Stearic acid (bead stearic acid YR manufactured by NOF CORPORATION)
* 12: Anti-aging agent (6PPD manufactured by EASTMAN)
* 13: Wax (paraffin wax manufactured by Ouchi Shinko Kagaku Kogyo Co., Ltd.)
* 14: Oil (Extract No. 4 S manufactured by Showa Shell Sekiyu Co., Ltd.)
* 15: Sulfur (oil-treated sulfur from Hosoi Chemical Industry Co., Ltd.)
* 16: Vulcanization accelerator CBS (Suncellor CM-G manufactured by Sanshin Chemical Industry Co., Ltd.)
* 17: Vulcanization accelerator DPG (Sulfur DG manufactured by Sumitomo Chemical Co., Ltd.)
* 18: Terminal-modified SBR (Toughden F3420 manufactured by Asahi Kasei Corporation. The terminal is modified with a glycidylamine group.)

 表5の結果から、実施例26~31のゴム組成物は、標準例6に比べて、発熱性、破断強度および耐摩耗性が同時に改善されている。
 これに対し、比較例10は特定のフェノール樹脂を配合していないので、破断強度が悪化した。
 比較例11は、特定のフェノール樹脂の配合量が本発明で規定する上限を超えているので、発熱性および破断強度が悪化した。
From the results in Table 5, the rubber compositions of Examples 26 to 31 are simultaneously improved in heat generation, breaking strength and wear resistance as compared with Standard Example 6.
On the other hand, in Comparative Example 10, since the specific phenol resin was not blended, the breaking strength was deteriorated.
In Comparative Example 11, since the blending amount of the specific phenol resin exceeded the upper limit specified in the present invention, the heat generating property and the breaking strength deteriorated.

Claims (7)

 ジエン系ゴム100質量部に対し、カーボンブラックおよびシリカから選択された1種以上を1~300質量部、および分子中に下記の化学式(1)で表されるアルキレンアミン由来の構造単位を少なくとも1個以上有するフェノール樹脂を0.1~20質量部配合してなることを特徴とするタイヤ用ゴム組成物。
Figure JPOXMLDOC01-appb-C000001
(上記一般式(1)中、Rは、それぞれ独立して、炭素数1~10の直鎖状または分岐状のアルキレン基を表す。)
1 to 300 parts by mass of one or more selected from carbon black and silica with respect to 100 parts by mass of diene rubber, and at least 1 structural unit derived from alkylene amine represented by the following chemical formula (1) in the molecule. A rubber composition for a tire, which comprises 0.1 to 20 parts by mass of a phenol resin having one or more of them.
Figure JPOXMLDOC01-appb-C000001
(In the above general formula (1), R 1 independently represents a linear or branched alkylene group having 1 to 10 carbon atoms.)
 前記フェノール樹脂が、分子中に下記の化学式(2)で表されるエチレンアミン由来の構造単位を少なくとも1個以上有することを特徴とする請求項1に記載のタイヤ用ゴム組成物。
Figure JPOXMLDOC01-appb-C000002
The rubber composition for a tire according to claim 1, wherein the phenol resin has at least one structural unit derived from ethyleneamine represented by the following chemical formula (2) in the molecule.
Figure JPOXMLDOC01-appb-C000002
 前記フェノール樹脂中における前記エチレンアミン由来の構造単位の含有比率が、3質量%以上50質量%以下であることを特徴とする請求項2に記載のタイヤ用ゴム組成物。 The rubber composition for a tire according to claim 2, wherein the content ratio of the structural unit derived from ethyleneamine in the phenol resin is 3% by mass or more and 50% by mass or less.  前記フェノール樹脂の軟化点が、60℃以上150℃以下であることを特徴とする請求項1に記載のタイヤ用ゴム組成物。 The rubber composition for a tire according to claim 1, wherein the softening point of the phenol resin is 60 ° C. or higher and 150 ° C. or lower.  前記ジエン系ゴム100質量部に対し、さらに、メチレンドナーを0.1~5質量部配合してなることを特徴とする請求項1に記載のタイヤ用ゴム組成物。 The rubber composition for a tire according to claim 1, wherein 0.1 to 5 parts by mass of methylene donor is further blended with respect to 100 parts by mass of the diene rubber.  前記メチレンドナーが、ヘキサメチレンテトラミンまたは多価メチロールメラミン誘導体であることを特徴とする請求項5に記載のタイヤ用ゴム組成物。 The rubber composition for a tire according to claim 5, wherein the methylene donor is hexamethylenetetramine or a polyvalent methylolmelamine derivative.  請求項1に記載のタイヤ用ゴム組成物を用いてなる空気入りタイヤ。 A pneumatic tire using the rubber composition for a tire according to claim 1.
PCT/JP2020/024584 2019-06-25 2020-06-23 Rubber composition for tire and pneumatic tire obtained using same Ceased WO2020262373A1 (en)

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JP2019117108A JP7095657B2 (en) 2019-06-25 2019-06-25 Rubber composition for tires and pneumatic tires using them
JP2019-117101 2019-06-25
JP2019-117108 2019-06-25
JP2019117101A JP7095656B2 (en) 2019-06-25 2019-06-25 Rubber composition for tires and pneumatic tires using them
JP2020-068066 2020-04-06
JP2020068066A JP7095716B2 (en) 2020-04-06 2020-04-06 Rubber composition for tires and tires using them
JP2020-068065 2020-04-06
JP2020068065A JP7095715B2 (en) 2020-04-06 2020-04-06 Rubber composition for tires and tires using them

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Publication number Priority date Publication date Assignee Title
JP2021004270A (en) * 2019-06-25 2021-01-14 住友ベークライト株式会社 Phenol resin

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JPH07508786A (en) * 1992-07-08 1995-09-28 コムパニー ゼネラール デ エタブリッスマン ミシュラン − ミシュラン エ コムパニー Method and composition using melamine substitute as curing agent for novolak resin
JP2007509226A (en) * 2003-10-20 2007-04-12 ユニロイヤル ケミカル カンパニー インコーポレイテッド Rubber composition and method for reducing tangent delta value and wear index
JP2010502816A (en) * 2006-09-05 2010-01-28 エスアイ・グループ・インコーポレイテッド Modified hydrocarbylphenol-aldehyde resin for use as a tackifier and rubber composition containing the same
JP2015205971A (en) * 2014-04-18 2015-11-19 横浜ゴム株式会社 Rubber composition for tire cap tread and pneumatic tire using the same

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JPH07508786A (en) * 1992-07-08 1995-09-28 コムパニー ゼネラール デ エタブリッスマン ミシュラン − ミシュラン エ コムパニー Method and composition using melamine substitute as curing agent for novolak resin
JP2007509226A (en) * 2003-10-20 2007-04-12 ユニロイヤル ケミカル カンパニー インコーポレイテッド Rubber composition and method for reducing tangent delta value and wear index
JP2010502816A (en) * 2006-09-05 2010-01-28 エスアイ・グループ・インコーポレイテッド Modified hydrocarbylphenol-aldehyde resin for use as a tackifier and rubber composition containing the same
JP2015205971A (en) * 2014-04-18 2015-11-19 横浜ゴム株式会社 Rubber composition for tire cap tread and pneumatic tire using the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021004270A (en) * 2019-06-25 2021-01-14 住友ベークライト株式会社 Phenol resin

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