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WO2021132822A1 - Method for preparing rubber composition, rubber composition prepared thereby, and tire manufactured using same - Google Patents

Method for preparing rubber composition, rubber composition prepared thereby, and tire manufactured using same Download PDF

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Publication number
WO2021132822A1
WO2021132822A1 PCT/KR2020/008781 KR2020008781W WO2021132822A1 WO 2021132822 A1 WO2021132822 A1 WO 2021132822A1 KR 2020008781 W KR2020008781 W KR 2020008781W WO 2021132822 A1 WO2021132822 A1 WO 2021132822A1
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WO
WIPO (PCT)
Prior art keywords
rubber
rubber composition
polymer
styrene
butadiene
Prior art date
Application number
PCT/KR2020/008781
Other languages
French (fr)
Korean (ko)
Inventor
최준걸
이도훈
정성교
유연식
Original Assignee
한화토탈 주식회사
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
Application filed by 한화토탈 주식회사 filed Critical 한화토탈 주식회사
Priority to CN202080083810.1A priority Critical patent/CN114829460A/en
Priority to JP2022534340A priority patent/JP7422878B2/en
Publication of WO2021132822A1 publication Critical patent/WO2021132822A1/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • 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
    • B60C1/00Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
    • B60C1/0016Compositions of the tread
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F6/00Post-polymerisation treatments
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F6/00Post-polymerisation treatments
    • C08F6/001Removal of residual monomers by physical means
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L21/00Compositions of unspecified rubbers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/18Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
    • C08L23/20Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
    • C08L23/22Copolymers of isobutene; Butyl rubber; Homopolymers or copolymers of other iso-olefins

Definitions

  • the present invention relates to a method for producing a rubber composition capable of improving the physical properties of a final product.
  • processing aids such as reinforcing materials and additives together with raw material rubber into a compounding machine and mix them in a bulk state, or to produce a final rubber composite product by mixing them together after manufacturing a master batch.
  • a master batch elastic body comprising 50 to 150 parts by weight of a reinforcing material and 50 to 150 parts by weight of polybutene (PIB) with respect to 100 parts by weight of raw rubber, a rubber composition for tire tread comprising the same, and
  • the present invention relates to a tire manufactured using the same.
  • the master batch elastic body is prepared by including polybutene (PIB), which has been used as free oil in the existing rubber composition for tire tread, in the master batch elastic body, and by using the polybutene in the tread rubber composition. It is introduced that it can increase the overall content of (PIB), solve the problem of processability caused by excessive use in the rubber composition for tire tread, and improve the grip performance of the tire and maintain the grip performance.
  • PIB polybutene
  • the above method uses raw rubber, a filler, and polybutene (PIB) to prepare an elastic body in the form of a master batch, for that reason, to increase the dispersibility of the filler, but this method also uses polybutene (PIB) as free oil It is difficult to handle liquid polybutene (PIB) with adhesive properties as in the case of using it as an adhesive, and it takes a lot of time and energy to produce a master batch type elastomer containing 50 phr or more of polybutene (PIB). do.
  • An object of the present invention is to provide a method for manufacturing a rubber composition capable of greatly improving the physical properties of a final product obtained while minimizing changes in existing equipment due to a simple process.
  • Another object of the present invention is to provide a rubber composition having improved physical properties required depending on the product.
  • Another object of the present invention is to provide a tire with improved physical properties.
  • the present invention is a method for preparing a polymer dispersed rubber composition in which a polymer is dispersed in a solution phase in rubber, and in the rubber manufacturing process step, a monomer, a solvent and a catalyst comprising a recovering residual monomers after polymerizing the rubber composition; and adding a polymer to the rubber solution remaining after recovering the residual monomer and uniformly dispersing in the solution phase; It provides a method for producing a rubber composition comprising a.
  • the polymer is a C 4-9- based polymer and has a weight average molecular weight of 300 to 20,000 g/mol, and 0.1 to 100 phr (parts per hundred rubber) is possible with respect to the rubber content. If it is, it is preferable that it is added at 1 to 50 phr.
  • the polymer is preferably a C4, C5, C9-based polymer.
  • the monomer is preferably at least one selected from the group consisting of styrene, butadiene, isobutylene, isoprene, ethylene and propylene.
  • the rubber is emulsion styrene-butadiene rubber (ESBR), solution styrene-butadiene rubber (SSBR), styrene-butadiene-styrene rubber (SBS), styrene-ethylene-butadiene-styrene rubber (SEBS), It is preferably a polyolefin elastomer (POE) such as butadiene rubber (BR), butyl rubber (IR), isoprene-isobutylene rubber (IIR) or ethylene propylene rubber (EPM), ethylene propylene diene rubber (EPDM).
  • ESBR emulsion styrene-butadiene rubber
  • SSBR solution styrene-butadiene rubber
  • SBS styrene-butadiene-styrene rubber
  • SEBS styrene-ethylene-butadiene-styrene rubber
  • POE polyo
  • the rubber composition is preferably used as a rubber composition for a tire tread, a rubber composition for a sealant, and a rubber composition for a hot-melt adhesive.
  • the present invention provides a rubber composition for a tire tread comprising the rubber composition prepared according to the present invention.
  • Another object of the present invention is to provide a tire manufactured by using the rubber composition for a tire tread according to the present invention.
  • the rubber composition prepared according to the present invention can increase the physical properties of the final rubber product.
  • the tire manufactured with the rubber composition for a tire tread manufactured according to the present invention has improved processability, grip property (wet road traction), low fuel efficiency, and abrasion performance.
  • the manufacturing method of the rubber composition according to the present invention can significantly improve the physical properties of rubber products while using existing equipment, so that the unit cost can be very low and the environment is excellent.
  • the present invention includes the step of preparing a polymer liquid dispersion rubber composition in which a polymer is dispersed in a solution phase in rubber, wherein the production step of the polymer liquid dispersion rubber composition comprises a monomer, a solvent and a catalyst in the rubber manufacturing process step Recovering the residual monomer after polymerizing the rubber composition, adding a polymer to the rubber solution remaining after recovering the residual monomer and uniformly dispersing it in the solution phase, solidification by removing the solvent from the rubber/polymer mixed solution, and drying , It provides a method for producing a rubber composition comprising a molding process step.
  • the difference between the present invention and the prior art lies in the step of adding the polymer and the properties of the polymer to be added.
  • the polymer is not directly mixed with the rubber when the rubber composition is manufactured, but the polymer is added in the rubber solvent remaining after removing the residual monomer remaining after the reaction in the rubber manufacturing process step, and the polymer is dispersed in the rubber solution. It has to go through the steps that exist in the form.
  • a hydrocarbon-based organic solvent such as normal hexane, cyclohexane, or mixed heptane may be mainly used.
  • the final desired physical properties may vary depending on the type of the final rubber product. For example, when a tire tread is a final rubber product, excellent braking properties and low fuel efficiency are required, so durability, grip properties, and low rolling resistance are important.
  • a rubber composition for manufacturing a tire tread when manufacturing a tire tread, a rubber composition for manufacturing a tire tread must be prepared.
  • a polymer for example, polybutene (PIB) is liquid-dispersed in the rubber used.
  • PIB polybutene
  • PIB polybutene
  • synthetic rubber or a mixture of natural rubber and synthetic rubber may be used.
  • the natural rubber may be a general natural rubber or a modified natural rubber.
  • the natural rubber mainly includes cis-1,4-polyisoprene, but may also include trans-1,4-polyisoprene according to required properties. Therefore, the natural rubber includes a cloth containing cis-1,4-polyisoprene as a main component.
  • the modified natural rubber means that the general natural rubber is modified or refined.
  • examples of the modified natural rubber include epoxidized natural rubber (ENR), deproteinized natural rubber (DPNR), and hydrogenated natural rubber.
  • the synthetic rubber is styrene butadiene rubber (SBR), modified styrene butadiene rubber, butadiene rubber (BR), modified butadiene rubber, chlorosulfonated polyethylene rubber, epichlorohydrin rubber, silicone rubber, nitrile rubber, hydrogenated nitrile rubber, Nitrile Butadiene Rubber (NBR), Modified Nitrile Butadiene Rubber, Styrene Butadiene Styrene Rubber (SBS), Styrene Ethylene Butylene Styrene (SEBS) Rubber, Ethylene Propylene Rubber (EPM), Ethylene Propylenediene (EPDM) Rubber, Hypalon Rubber, Chloroprene Rubber, ethylene vinyl acetate rubber, acrylic rubber, hydrin rubber, vinyl benzyl chloride styrene butadiene rubber, bromomethyl styrene butadiene rubber, maleate styrene butadiene rubber, carboxylate
  • the polymer may be polybutene (PIB), preferably polybutene having a number average molecular weight of 150 to 5,000 g/mol as highly reactive polybutene (PIB).
  • PIB polybutene
  • High-reactivity polybutene (PIB) is advantageous in terms of durability compared to conventional polybutene (PIB) because the carbon-carbon double bond is mainly located at the end of polybutene (PIB), so the bondability with the raw rubber increases during the reaction. because it works As such, polymers can be used differently depending on the desired physical properties of the final rubber product.
  • the polymer is a C 4-9 polymer and has a weight average molecular weight of 300 to 20,000 g/mol, and 0.1 to 100 phr (parts per hundred rubber), preferably 1 to 100 phr (parts per hundred rubber) based on the rubber content. It is preferable to input at 50 phr.
  • the physical properties of the final rubber product are not significantly improved, and when the polymer is included in more than 50 phr, the original physical properties of rubber may not appear.
  • the polymer is preferably a C4, C5, or C9-based polymer, more preferably a C4-based polybutene (PIB).
  • PIB polybutene
  • the monomer is preferably at least one selected from the group consisting of styrene, butadiene, isobutylene, isoprene, ethylene and propylene.
  • the rubber is emulsion styrene-butadiene rubber (ESBR), solution styrene-butadiene rubber (SSBR), styrene-butadiene-styrene rubber (SBS), styrene-ethylene-butadiene-styrene rubber (SEBS), It is preferably a polyolefin elastomer (POE) such as butadiene rubber (BR), butyl rubber (IR), isoprene-isobutylene rubber (IIR) or ethylene propylene rubber (EPM), ethylene propylene diene rubber (EPDM).
  • ESBR emulsion styrene-butadiene rubber
  • SSBR solution styrene-butadiene rubber
  • SBS styrene-butadiene-styrene rubber
  • SEBS styrene-ethylene-butadiene-styrene rubber
  • POE polyo
  • the rubber composition is preferably used as a rubber composition for a tire tread, a rubber composition for a sealant, and a rubber composition for a hot-melt adhesive.
  • the rubber is isoprene-isobutylene rubber (IIR), it can be used as a butyl rubber for a sealant.
  • IIR isoprene-isobutylene rubber
  • the rubber is a styrene-butadiene-styrene block copolymer (SBS) and a styrene-ethylene-butadiene-styrene resin (SEBS), it can be used for manufacturing a hot-melt adhesive.
  • SBS styrene-butadiene-styrene block copolymer
  • SEBS styrene-ethylene-butadiene-styrene resin
  • the present invention provides a rubber composition for a tire tread comprising the rubber composition prepared according to the present invention.
  • the rubber composition for a tire tread includes, in addition to the raw material rubber and highly reactive polybutene (PIB), silica and/or carbon black as reinforcing fillers, process oil as a softener, sulfur as a vulcanizing agent, CBS as a vulcanization accelerator, and 1,3-diphenylguanidine (DPG), zinc oxide as a vulcanizing activator, stearic acid, a coupling agent for improving dispersibility, and an anti-aging agent may include a rubber compounding agent generally used in a rubber composition for a tire tread.
  • PIB highly reactive polybutene
  • silica and/or carbon black as reinforcing fillers
  • process oil as a softener
  • sulfur as a vulcanizing agent
  • CBS as a vulcanization accelerator
  • DPG 1,3-diphenylguanidine
  • zinc oxide as a vulcanizing activator
  • stearic acid stearic acid
  • the type of silica that can be used as a reinforcing filler in the present invention is not particularly limited, but preferably has a surface area of 175 ⁇ 5 m 2 /g, a moisture content of 6.0 ⁇ 0.5 wt%, and a silicon dioxide (SiO2) content of 90 wt% or more. Do.
  • the carbon black used in the present invention is not particularly limited in its type, but has a BET (Brunauer, Emmett, Teller) specific surface area of 80 to 90 m 2 /g, and a DBP (Di-n-bibutyl) Phthalate) adsorption value is 100-110 g/100g, and iodine adsorption value is preferably in the range of 90-120 mg/g.
  • the carbon black is preferably used in an amount of 40 to 100 parts by weight based on 100 parts by weight of the raw rubber. If the amount is less than 40 parts by weight, it is not preferable because a sufficient reinforcing effect is not exhibited. It is not preferable because it does not show
  • the process oil acts as a softener, and the aromatic content in the oil is 5 to 25 wt%, the naphthalene content is 25 to 45 wt%, and the paraffinic content is preferably 35 to 65 wt%.
  • Other various additives used in the present invention are general components used in the rubber composition for tire tread, and details thereof will be omitted.
  • the rubber composition for a tire tread according to the present invention improves grip performance on the tread of an automobile tire, particularly a tire for a high-speed race car, while continuously maintaining the same without affecting the basic physical properties of the tire. make it possible
  • Another object of the present invention is to provide a tire manufactured by using the rubber composition for a tire tread according to the present invention.
  • the polymerized product was cooled to 50 o C and depressurized to prepare a butadiene rubber/hexane solution from which residual 1,3-butadiene was removed.
  • the prepared butadiene rubber/hexane solution is measured and transferred to a 5L blend tank equipped with a stirrer after measuring total solid content (TSC).
  • TSC total solid content
  • PIB polybutene
  • the prepared butadiene rubber/polybutene/hexane mixture is removed using a steam stripper to remove hexane as a solvent to obtain a butadiene rubber solid in which polybutene is evenly dispersed, and the moisture of the solid is dried using a processing roll at 100 o C.
  • a sample of butadiene rubber with 37.5 phr of PIB extension was prepared.
  • Polybutadiene rubber (BR) was polymerized in the same manner as in Preparation Example 1, and residual 1,3-butadiene and solvent were removed to obtain polybutadiene rubber (BR).
  • Comparative Example 1 only the polybutadiene rubber prepared in Comparative Preparation Example 1 was used, and in Comparative Example 2, the polybutadiene prepared in Comparative Preparation Example 1 and HRPIB470 manufactured by Hanwha Total Co., Ltd. were mixed.
  • Examples 1 to 5 each prepared polybutadiene rubber (BR) according to Preparation Example 1, and after removing the monomer, different polybutenes (PIB) according to Table 1 were added, and polybutene (PIB) according to Table 1 ) was prepared in a liquid dispersion (extension) butadiene rubber (BR).
  • PIB polybutadiene rubber
  • CPIB650 conventional PIB (Mn 1,300g/mol), PB1300 (Daelim Industrial Co., Ltd.)
  • HRPIB190 high reactive PIB (Mn 1,000g/mol), HRPB1000 (Daelim Industrial Co., Ltd.)
  • HRPIB470 high reactive PIB (Mn 1,300g/mol), HRPB1300 (Daelim Industrial Co., Ltd.)
  • a composite material before crosslinking was prepared using MIX-LABO (Mixing capacity: 0.5liter, Main motor: 15HP) manufactured by Moriyama.
  • BR in which PIB is dispersed was a rubber in which polybutene (PIB) prepared in Preparation Example 1 was dispersed in a liquid (PIB extended rubber), and Comparative Example 1 was used in Comparative Preparation Example 1. Only the prepared polybutadiene rubber was used, and Comparative Example 2 was a mixture of the polybutadiene rubber prepared in Comparative Preparation Example 1 and polybutene (PIB, HRPIB470).
  • the compounding was carried out in two steps. For the first kneading, fill 75% based on the volume of the 0.5 liter compounder and set the rotor speed to 70 rpm. Rubber composition, filler (silica), oil, zinc oxide (ZnO), stearic acid, silane coupling agent (Si-) 69) to control the temperature to obtain a primary rubber composition at 140 ⁇ 150°C.
  • the mixture is cooled to room temperature and sulfur, DPG (Diphenyl Guanidine), CBS (N-cyclohexyl-2-benzothiazole sulfonamide), and antioxidant (6-PPD) are added at 90° C. or less at 50 rpm. and kneaded for 2 minutes.
  • DPG Diphenyl Guanidine
  • CBS N-cyclohexyl-2-benzothiazole sulfonamide
  • antioxidant (6-PPD) are added at 90° C. or less at 50 rpm. and kneaded for 2 minutes.
  • each rubber composite was heated at 160°C for the time obtained by measuring the vulcanization characteristics at 160°C, 40 minutes, and 1% strain with a Rubber Process Analyzer (RPA), plus 2 minutes to the time of T90.
  • RPA Rubber Process Analyzer
  • silica A primary compound (SMB, silica master batch) is prepared by adding 5.6 parts by weight of a coupling agent (SI-69) and 10 parts by weight of TDAE (treated distillate aromatic extracted) oil,
  • Example 5 Compared to the first formulation, 1.5 parts by weight of sulfur, 1.8 parts by weight of diphenylguanidine (DPG) as a vulcanization accelerator, 1.8 parts by weight of cyclohexylbenzocyazolesulfenamide (CBS), and 0.2 parts by weight of antioxidant (6PPD) are further added to the secondary formulation (FMB, final master batch) was prepared. However, in Example 5, there is a difference only in that the content of sulfur is 1.8 parts by weight.
  • DPG diphenylguanidine
  • CBS cyclohexylbenzocyazolesulfenamide
  • 6PPD antioxidant
  • a rubber composite specimen was prepared in the same manner as in Example 1, except that BR not containing polybutene (PIB) was used.
  • a rubber composite specimen was prepared in the same manner as in Example 4, except that the polybutene (PIB) of HRPIB470 was added directly to a blender and blended with rubber without a separate liquid dispersion step.
  • PIB polybutene
  • Mooney viscosity was measured using a Mooney viscometer (MV2000, Alpha Technologies) by using a Mooney viscometer (MV2000, Alpha Technologies) to preheat a large rotor at 100°C for 1 minute and read the value 4 minutes after starting the rotor. .
  • Modulus measurement was performed with a tensile tester manufactured by Instron after cutting a specimen into a dumbbell shape.
  • the 100% and 200% modulus refer to the stress applied to the specimen when the specimen is elongated by 100% and 200%, respectively.
  • Tensile strength For the tensile strength, a No. 3 dumbbell test piece described in JIS K6251 (2001) was prepared by punching a vulcanized rubber sheet. Using this test piece, according to the method specified in JIS K6251, a tensile test was conducted under the conditions of a measurement temperature of 25°C and a tensile rate of 500 mm/min, and 100% modulus (M100), 200% modulus (M200), 300% modulus ( M300) Tensile break stress TB and tensile break elongation EB were measured.
  • Viscoelasticity is measured using dynamic mechanical analysis (DMA), and 0°C Tan ⁇ is used as a substitute for the braking performance of the tire on a wet road surface, and the higher the value, the better the performance. 60°C Tan ⁇ is used as a substitute for the tire rolling resistance value, and the lower the value, the better the rolling resistance is, indicating that fuel efficiency increases.
  • DMA dynamic mechanical analysis
  • Abrasion is measured according to ASTM D5963 method while applying a 5N load using a DIN abrasion tester, and expressed as a relative index, the larger the value, the better the wear performance.
  • the specimen prepared by dispersing PIB in a solution phase in rubber has improved durability, grip properties, and low rotational resistance compared to that containing no PIB or adding the same amount of PIB directly to the compounding machine. Braking characteristics, low fuel consumption characteristics and wear performance were improved.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
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  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

The present invention relates to a method for preparing a rubber composition which can improve physical properties of a final product. In order to achieve the purpose of the present invention, the present invention comprises a step of preparing a polymer-dispersed rubber composition in which a polymer is dispersed in a solution phase in rubber and provides a method for preparing a rubber composition, wherein the step of preparing a polymer-dispersed rubber composition comprises, after polymerization of a rubber composition containing a monomer, a solvent, and a catalyst in a rubber preparation processing step, collecting a residual monomer, and introducing a polymer to a remaining rubber solution from which the residual monomer has been collected. Application of the rubber composition thus prepared, to a tire tread composite can improve durability, grip properties, low balanced rotation resistance, thus achieving effects of excellent braking and fuel-efficient characteristics, and improving abrasive wear performance.

Description

고무 조성물의 제조방법, 이의 방법으로 제조된 고무 조성물 및 이를 이용하여 제조된 타이어Manufacturing method of rubber composition, rubber composition manufactured by same method, and tire manufactured using same
본 발명은 최종 제품의 물성을 개선할 수 있는 고무 조성물의 제조방법에 관한 것이다. The present invention relates to a method for producing a rubber composition capable of improving the physical properties of a final product.
일반적으로 고무를 이용한 제품으로는 내구성이 우수해야 하는 타이어, 신발밑창, 벨트(belt), 호스(hose), 시트(sheet), 밀폐제(sealant)와 더불어 접착력이 우수해야 하는 접착제 등 다양한 제품들이 있다.In general, there are various products using rubber, such as tires, shoe soles, belts, hoses, sheets, sealants, which must have excellent durability, and adhesives, which must have excellent adhesion. .
이러한 제품을 최종적으로 완성하기 위해서는 원료가 되는 고무와 함께 보강재, 첨가제를 비롯한 가공조제를 배합기에 직접 투입하여 벌크 상태로 혼합하거나, 마스터배치 제조 후 함께 혼합시켜 최종 고무 복합재 제품을 제조하는 것이 일반적이다. In order to finally complete these products, it is common to directly inject processing aids such as reinforcing materials and additives together with raw material rubber into a compounding machine and mix them in a bulk state, or to produce a final rubber composite product by mixing them together after manufacturing a master batch. .
예를 들어, 타이어 트래드용 고무 조성물의 개선과 관련해서는, 종래에는 국내특허 등록번호 10-1276654호에서는 원료고무 100중량부에 대하여 보강재 50~150중량부, 및 폴리부텐(PIB) 50~150중량부를 포함하는 마스터 배치 탄성체, 이를 포함하는 타이어 트레드용 고무 조성물, 및 이를 이용하여 제조된 타이어에 관한 것으로 기존 타이어 트레드용 고무 조성물의 Free oil로 사용하던 폴리부텐(PIB)을 마스터 배치 탄성체에 포함시켜 마스터 배치 탄성체를 제조하고, 이를 사용함으로써 트레드 고무 조성물 내에서 폴리부텐(PIB)의 전체적인 함량을 증가시키고, 타이어 트레드용 고무 조성물에서 과량 사용에 따라 발생되는 가공성의 문제를 해결하고 타이어의 그립성능 향상 및 그립성능의 지속을 유지시킬 수 있는 것으로 소개하고 있다.For example, with respect to the improvement of the rubber composition for a tire tread, conventionally In Korean Patent Registration No. 10-1276654, a master batch elastic body comprising 50 to 150 parts by weight of a reinforcing material and 50 to 150 parts by weight of polybutene (PIB) with respect to 100 parts by weight of raw rubber, a rubber composition for tire tread comprising the same, and The present invention relates to a tire manufactured using the same. The master batch elastic body is prepared by including polybutene (PIB), which has been used as free oil in the existing rubber composition for tire tread, in the master batch elastic body, and by using the polybutene in the tread rubber composition. It is introduced that it can increase the overall content of (PIB), solve the problem of processability caused by excessive use in the rubber composition for tire tread, and improve the grip performance of the tire and maintain the grip performance.
하지만, 상기 방법은 원료고무, 충진제, 폴리부텐(PIB)을 이용하여 마스터 배치 형태의 탄성체를 제조하는데, 그 이유로 충진재의 분산성을 높이기 위해서 이다, 하지만 이 방법도 폴리부텐(PIB)을 free oil로 사용하는 경우와 마찬가지로 접착성을 가진 액상의 폴리부텐(PIB)을 취급하는데 어려움이 있으며, 폴리부텐(PIB)이 50 phr이상 포함된 마스터 배치 형태의 탄성체를 제조하기 위해서는 많은 시간과 에너지가 소모된다. However, the above method uses raw rubber, a filler, and polybutene (PIB) to prepare an elastic body in the form of a master batch, for that reason, to increase the dispersibility of the filler, but this method also uses polybutene (PIB) as free oil It is difficult to handle liquid polybutene (PIB) with adhesive properties as in the case of using it as an adhesive, and it takes a lot of time and energy to produce a master batch type elastomer containing 50 phr or more of polybutene (PIB). do.
따라서 최종 고무 제품의 물성을 개선하면서도 공정을 단순화하여 제조단가를 높이지 않고 성능은 개선시키는 새로운 제조방법이 필요하게 되었다.Therefore, there is a need for a new manufacturing method that improves the physical properties of the final rubber product while simplifying the process to improve the performance without increasing the manufacturing cost.
본 발명의 목적은 공정은 단순하여 기존 설비의 변경을 최소화하면서도, 얻어지는 최종 제품의 물성을 크게 개선시킬 수 있는 고무 조성물의 제조방법을 제공하는 것이다.An object of the present invention is to provide a method for manufacturing a rubber composition capable of greatly improving the physical properties of a final product obtained while minimizing changes in existing equipment due to a simple process.
또한, 본 발명의 또 다른 목적은 제품에 따라 필요한 물성이 개선된 고무 조성물을 제공하는 것이다.In addition, another object of the present invention is to provide a rubber composition having improved physical properties required depending on the product.
또한, 본 발명의 또 다른 목적은 물성이 개선된 타이어를 제공하는 것이다.Another object of the present invention is to provide a tire with improved physical properties.
본 발명의 목적을 달성하기 위하여 본 발명은 고무에 폴리머가 용액상으로 분산된(polymer extended rubber), 폴리머 분산 고무 조성물을 제조하는 방법으로서, 고무 제조 공정단계에서, 단량체, 용제 및 촉매를 포함하는 고무 조성물을 중합 반응시킨 후 잔류 단량체를 회수하는 단계; 및 상기 잔류 단량체를 회수한 후 남은 고무 용액에 폴리머를 투입하고 용액상에서 균일하게 분산시키는 단계; 를 포함하는 고무 조성물의 제조방법을 제공한다. 본 발명의 일 실시예에 의하면, 상기 폴리머는 C4~9 계 폴리머로서 중량평균분자량이 300 ~ 20,000 g/mol이고, 상기 고무 함량에 대하여 0.1~100phr(parts per hundred rubber)이 가능하며, 되도록이면 1~50phr로 투입되는 것이 바람직하다.In order to achieve the object of the present invention, the present invention is a method for preparing a polymer dispersed rubber composition in which a polymer is dispersed in a solution phase in rubber, and in the rubber manufacturing process step, a monomer, a solvent and a catalyst comprising a recovering residual monomers after polymerizing the rubber composition; and adding a polymer to the rubber solution remaining after recovering the residual monomer and uniformly dispersing in the solution phase; It provides a method for producing a rubber composition comprising a. According to an embodiment of the present invention, the polymer is a C 4-9- based polymer and has a weight average molecular weight of 300 to 20,000 g/mol, and 0.1 to 100 phr (parts per hundred rubber) is possible with respect to the rubber content. If it is, it is preferable that it is added at 1 to 50 phr.
본 발명의 일 실시예에 의하면, 상기 폴리머는 C4, C5, C9계 폴리머인 것이 바람직하다.According to an embodiment of the present invention, the polymer is preferably a C4, C5, C9-based polymer.
본 발명의 일 실시예에 의하면, 상기 단량체는 스티렌, 부타디엔, 이소부틸렌, 이소프렌, 에틸렌 및 프로필렌등으로 이루어진 군으로부터 선택된 1종 이상인 것이 바람직하다.According to an embodiment of the present invention, the monomer is preferably at least one selected from the group consisting of styrene, butadiene, isobutylene, isoprene, ethylene and propylene.
본 발명의 일 실시예에 있어서, 상기 고무는 에멀젼 스티렌부타디엔 고무(ESBR), 솔루션 스티렌부타디엔 고무(SSBR), 스티렌-부타디엔-스티렌 고무(SBS), 스티렌-에틸렌-부타디엔-스티렌 고무(SEBS), 부타디엔 고무(BR), 부틸고무(IR), 이소프렌-이소부틸렌 고무(IIR) 또는 에틸렌프로필렌 고무(EPM), 에틸렌프로필렌디엔 고무(EPDM)과 같은 폴리올레핀 엘라스토머(POE)인 것이 바람직하다.In one embodiment of the present invention, the rubber is emulsion styrene-butadiene rubber (ESBR), solution styrene-butadiene rubber (SSBR), styrene-butadiene-styrene rubber (SBS), styrene-ethylene-butadiene-styrene rubber (SEBS), It is preferably a polyolefin elastomer (POE) such as butadiene rubber (BR), butyl rubber (IR), isoprene-isobutylene rubber (IIR) or ethylene propylene rubber (EPM), ethylene propylene diene rubber (EPDM).
본 발명의 일 실시예에 의하면, 상기 고무 조성물이 타이어 트래드용 고무 조성물, 실란트용 고무 조성물, Hot-melt 접착제용 고무 조성물로 사용되는 것이 바람직하다.According to an embodiment of the present invention, the rubber composition is preferably used as a rubber composition for a tire tread, a rubber composition for a sealant, and a rubber composition for a hot-melt adhesive.
본 발명의 또 다른 목적을 달성하기 위하여 본 발명은 본 발명에 따라 제조된 고무 조성물을 포함하는 타이어 트래드용 고무 조성물을 제공한다.In order to achieve another object of the present invention, the present invention provides a rubber composition for a tire tread comprising the rubber composition prepared according to the present invention.
본 발명의 또 다른 목적을 달성하기 위하여 본 발명에 따른 타이어 트래드용 고무 조성물을 이용하여 제조된 타이어를 제공한다. Another object of the present invention is to provide a tire manufactured by using the rubber composition for a tire tread according to the present invention.
본 발명에 따라 제조된 고무 조성물은 최종 고무 제품의 물성을 증가시킬 수 있다.The rubber composition prepared according to the present invention can increase the physical properties of the final rubber product.
또한, 본 발명에 따라 제조된 타이어 트래드용 고무 조성물로 제조된 타이어는 가공성, 그립성(젖은 노면 접지력), 저연비 특성, 마모성능이 개선된다.In addition, the tire manufactured with the rubber composition for a tire tread manufactured according to the present invention has improved processability, grip property (wet road traction), low fuel efficiency, and abrasion performance.
또한 본 발명에 따른 고무 조성물의 제조방법은 기존 설비를 이용할 수 있으면서도 고무 제품의 물성을 획기적으로 개선할 수 있어, 단가를 매우 낮출 수 있으며 환경적으로도 우수하다.In addition, the manufacturing method of the rubber composition according to the present invention can significantly improve the physical properties of rubber products while using existing equipment, so that the unit cost can be very low and the environment is excellent.
본 발명을 이하 보다 상세히 설명하나, 이는 본 발명의 설명을 위한 것으로, 본 발명의 범위를 제한하는 방법으로 해석되어서는 안 된다.The present invention will be described in more detail below, but this is for the purpose of explanation of the present invention and should not be construed as limiting the scope of the present invention.
본 발명은 고무에 폴리머가 용액상으로 분산된, 폴리머 액상 분산 고무 조성물을 제조하는 단계를 포함하고, 상기 폴리머 액상 분산 고무 조성물의 제조단계는 고무 제조 공정단계에서, 단량체, 용제 및 촉매를 포함하는 고무 조성물을 중합 반응시킨 후 잔류 단량체를 회수하는 단계, 상기 잔류 단량체를 회수한 후 남은 고무 용액에 폴리머를 투입하여 용액상에서 균일하게 분산 시키는 단계, 고무/폴리머 혼합용액에서 용매제거를 통한 고형화, 건조, 성형 공정 단계를 포함하는 고무 조성물의 제조방법을 제공한다.The present invention includes the step of preparing a polymer liquid dispersion rubber composition in which a polymer is dispersed in a solution phase in rubber, wherein the production step of the polymer liquid dispersion rubber composition comprises a monomer, a solvent and a catalyst in the rubber manufacturing process step Recovering the residual monomer after polymerizing the rubber composition, adding a polymer to the rubber solution remaining after recovering the residual monomer and uniformly dispersing it in the solution phase, solidification by removing the solvent from the rubber/polymer mixed solution, and drying , It provides a method for producing a rubber composition comprising a molding process step.
<폴리머 액상 분산 고무 조성물><Polymer liquid dispersion rubber composition>
본 발명과 종래 기술의 차이점은 폴리머의 투입 단계 및 투입되는 폴리머의 성상에 있다. The difference between the present invention and the prior art lies in the step of adding the polymer and the properties of the polymer to be added.
즉, 본 발명에서는 고무 조성물의 제조 시 고무에 폴리머를 바로 혼합하는 것이 아니라, 고무 제조공정 단계에서 반응 후 남은 잔류 단량체를 제거한 후 남은 고무 용제 상태에서 폴리머를 첨가하는 것으로서 폴리머가 고무 용액에 분산된 형태로 존재하는 단계를 반드시 거쳐야 하는 것이다.That is, in the present invention, the polymer is not directly mixed with the rubber when the rubber composition is manufactured, but the polymer is added in the rubber solvent remaining after removing the residual monomer remaining after the reaction in the rubber manufacturing process step, and the polymer is dispersed in the rubber solution. It has to go through the steps that exist in the form.
이와 같이 폴리머가 액상으로 분산된 고무 조성물을 이용하여 고무를 제조한 경우에만 최종 고무 제품을 제조하였을 때 원하는 물성을 얻을 수 있다.As described above, desired physical properties can be obtained when the final rubber product is manufactured only when the rubber is manufactured using the rubber composition in which the polymer is dispersed in the liquid phase.
상기 용제는 노말헥산, 시클로헥산, 혼합헵탄 등의 하이드로카본계 유기용매를 주로 사용 할 수 있다.As the solvent, a hydrocarbon-based organic solvent such as normal hexane, cyclohexane, or mixed heptane may be mainly used.
여기서 최종 원하는 물성이란 최종 고무 제품의 종류에 따라 달라질 수 있다. 예를 들어 타이어 트래드가 최종 고무 제품인 경우 우수한 제동 특성 및 저연비 특성이 요구되므로, 내구성, 그립(grip)성, 낮은 회전저항성이 중요하다. Here, the final desired physical properties may vary depending on the type of the final rubber product. For example, when a tire tread is a final rubber product, excellent braking properties and low fuel efficiency are required, so durability, grip properties, and low rolling resistance are important.
따라서 본 발명에서는 타이어 트래드를 제조하고자 할 때, 타이어 트래드 제조용 고무 조성물을 제조하여야 하며, 상기 타이어 트래드용 고무 조성물을 제조할 때, 사용되는 고무에 폴리머, 예를 들어 폴리부텐(PIB)을 액상 분산시켜 폴리부텐(PIB) 액상 분산 고무 조성물을 제조하는 단계를 포함하여야 한다. 타이어 트래드를 제조하고자 할 때 사용될 수 있는 고무는 합성고무 또는 천연 고무와 합성 고무의 혼합물을 사용할 수 있다. Therefore, in the present invention, when manufacturing a tire tread, a rubber composition for manufacturing a tire tread must be prepared. When manufacturing the rubber composition for a tire tread, a polymer, for example, polybutene (PIB) is liquid-dispersed in the rubber used. to prepare a polybutene (PIB) liquid dispersion rubber composition. As the rubber that can be used to manufacture the tire tread, synthetic rubber or a mixture of natural rubber and synthetic rubber may be used.
상기 천연고무는 일반적인 천연고무 또는 변성 천연고무일 수 있다. The natural rubber may be a general natural rubber or a modified natural rubber.
일반적인 천연고무는 천연고무로서 알려진 것이면 어느 것이라도 사용될 수 있고, 원산지 등이 한정되지 않는다. 상기 천연고무는 시스-1,4-폴리이소프렌을 주체로서 포함하지만, 요구 특성에 따라서 트랜스-1,4-폴리이소프렌을 포함할 수도 있다. 따라서, 상기 천연고무에는 시스-1,4-폴리이소프렌을 주체로서 포함하는 천Any general natural rubber may be used as long as it is known as natural rubber, and the country of origin is not limited. The natural rubber mainly includes cis-1,4-polyisoprene, but may also include trans-1,4-polyisoprene according to required properties. Therefore, the natural rubber includes a cloth containing cis-1,4-polyisoprene as a main component.
연고무 외에, 예컨대 남미산 사포타과의 고무의 일종인 발라타 등, 트랜스-1,4-이소프렌을 주체로서 포함하는 천연고무도 포함할 수 있다.In addition to the ointment rubber, natural rubber containing trans-1,4-isoprene as a main component, such as Valata, which is a type of rubber of the Sapotaceae family from South America, may also be included.
상기 변성 천연고무는, 상기 일반적인 천연고무를 변성 또는 정제한 것을 의미한다. 예컨대, 상기 변성 천연 고무로는 에폭시화 천연고무(ENR), 탈단백 천연고무(DPNR), 수소화 천연고무 등을 들 수 있다.The modified natural rubber means that the general natural rubber is modified or refined. For example, examples of the modified natural rubber include epoxidized natural rubber (ENR), deproteinized natural rubber (DPNR), and hydrogenated natural rubber.
상기에서 합성고무는 스티렌 부타디엔 고무(SBR), 변성 스티렌 부타디엔 고무, 부타디엔 고무(BR), 변성 부타디엔 고무, 클로로 술폰화 폴리에틸렌 고무, 에피클로로 하이드린 고무, 실리콘 고무, 니트릴 고무, 수소화된 니트릴 고무, 니트릴 부타디엔 고무(NBR), 변성 니트릴 부타디엔 고무, 스티렌 부타디엔 스티렌 고무(SBS), 스티렌 에틸렌 부틸렌 스티렌(SEBS) 고무, 에틸렌 프로필렌 고무(EPM), 에틸렌 프로필렌디엔(EPDM) 고무, 하이팔론 고무, 클로로프렌 고무, 에틸렌 비닐아세테이트 고무, 아크릴 고무, 히드린 고무, 비닐 벤질 클로라이드 스티렌 부타디엔 고무, 브로모 메틸 스티렌 부틸 고무, 말레인산 스티렌 부타디엔 고무, 카르복실산스티렌 부타디엔 고무, 에폭시 이소프렌 고무, 말레인산 에틸렌 프로필렌 고무, 카르복실산 니트릴 부타디엔고무, 브로미네이티드 폴리이소부틸 이소프렌-코-파라메틸 스티렌(brominated polyisobutyl isoprene-coparamethylstyrene, BIMS) 및 이들의 조합으로 이루어진 군에서 선택되는 어느 하나일 수 있다.In the above, the synthetic rubber is styrene butadiene rubber (SBR), modified styrene butadiene rubber, butadiene rubber (BR), modified butadiene rubber, chlorosulfonated polyethylene rubber, epichlorohydrin rubber, silicone rubber, nitrile rubber, hydrogenated nitrile rubber, Nitrile Butadiene Rubber (NBR), Modified Nitrile Butadiene Rubber, Styrene Butadiene Styrene Rubber (SBS), Styrene Ethylene Butylene Styrene (SEBS) Rubber, Ethylene Propylene Rubber (EPM), Ethylene Propylenediene (EPDM) Rubber, Hypalon Rubber, Chloroprene Rubber, ethylene vinyl acetate rubber, acrylic rubber, hydrin rubber, vinyl benzyl chloride styrene butadiene rubber, bromomethyl styrene butyl rubber, maleate styrene butadiene rubber, carboxylate styrene butadiene rubber, epoxy isoprene rubber, ethylene propylene maleate rubber, carboxylate It may be any one selected from the group consisting of acid nitrile butadiene rubber, brominated polyisobutyl isoprene-coparamethylstyrene (BIMS), and combinations thereof.
상기 폴리머는 폴리부텐(PIB), 바람직하게는 고반응성 폴리부텐(PIB)으로서 수평균 분자량이 150 내지 5,000 g/mol인 폴리부텐이 사용될 수 있다. 고반응성 폴리부텐(PIB)은 탄소-탄소 이중결합의 위치가 주로 폴리부텐(PIB)의 말단에 위치하기 때문에 반응시 원료 고무와 결합성이 증가하여 기존 폴리부텐(PIB)에 비하여 내구력 측면에서 유리하게 작용하기 때문이다. 이처럼 폴리머도 최종 고무 제품의 원하는 물성에 따라 다르게 사용할 수 있다.The polymer may be polybutene (PIB), preferably polybutene having a number average molecular weight of 150 to 5,000 g/mol as highly reactive polybutene (PIB). High-reactivity polybutene (PIB) is advantageous in terms of durability compared to conventional polybutene (PIB) because the carbon-carbon double bond is mainly located at the end of polybutene (PIB), so the bondability with the raw rubber increases during the reaction. because it works As such, polymers can be used differently depending on the desired physical properties of the final rubber product.
본 발명의 일 실시예에 의하면, 상기 폴리머는 C4~9 폴리머로서 중량평균분자량이 300 ~ 20,000 g/mol 이고, 상기 고무 함량에 대하여 0.1~100phr(parts per hundred rubber), 바람직하게는 1~50phr로 투입되는 것이 바람직하다.According to an embodiment of the present invention, the polymer is a C 4-9 polymer and has a weight average molecular weight of 300 to 20,000 g/mol, and 0.1 to 100 phr (parts per hundred rubber), preferably 1 to 100 phr (parts per hundred rubber) based on the rubber content. It is preferable to input at 50 phr.
폴리머가 고무 함량에 대해 1phr보다 적게 포함되면, 최종 고무 제품의 물성이 크게 개선되지 않으며, 50phr보다 많이 포함되면, 고무 본래의 물성이 나타나지 않을 수 있다.When the polymer is included in less than 1 phr with respect to the rubber content, the physical properties of the final rubber product are not significantly improved, and when the polymer is included in more than 50 phr, the original physical properties of rubber may not appear.
본 발명의 일 실시예에 의하면, 상기 폴리머는 C4, C5, C9계 폴리머인 것이 바람직하며, 보다 바람직하게는 C4계인 폴리부텐(PIB)이 바람직하다.According to an embodiment of the present invention, the polymer is preferably a C4, C5, or C9-based polymer, more preferably a C4-based polybutene (PIB).
합성고무를 사용한 경우에는, 유기용매를 사용하기 때문에 앞선 방법과 같이 잔류 단량체 제거 후 저장탱크나 블랜드 탱크에 폴리부텐(PIB)을 직접 투입하여 혼합 후 제품화 공정을 거치면 폴리머가 액상으로 분산된 고무를 얻을 수 있다.In the case of using synthetic rubber, since an organic solvent is used, as in the previous method, after removing residual monomer, polybutene (PIB) is directly put into a storage tank or blend tank, mixed, and then goes through a commercialization process to obtain a rubber in which the polymer is dispersed in a liquid phase. can be obtained
본 발명의 일 실시예에 의하면, 상기 단량체는 스티렌, 부타디엔, 이소부틸렌, 이소프렌, 에틸렌 및 프로필렌등으로 이루어진 군으로부터 선택된 1종 이상인 것이 바람직하다.According to an embodiment of the present invention, the monomer is preferably at least one selected from the group consisting of styrene, butadiene, isobutylene, isoprene, ethylene and propylene.
본 발명의 일 실시예에 있어서, 상기 고무는 에멀젼 스티렌부타디엔 고무(ESBR), 솔루션 스티렌부타디엔 고무(SSBR), 스티렌-부타디엔-스티렌 고무(SBS), 스티렌-에틸렌-부타디엔-스티렌 고무(SEBS), 부타디엔 고무(BR), 부틸고무(IR), 이소프렌-이소부틸렌 고무(IIR) 또는 에틸렌프로필렌 고무(EPM), 에틸렌프로필렌디엔 고무(EPDM)과 같은 폴리올레핀 엘라스토머(POE)인 것이 바람직하다.In one embodiment of the present invention, the rubber is emulsion styrene-butadiene rubber (ESBR), solution styrene-butadiene rubber (SSBR), styrene-butadiene-styrene rubber (SBS), styrene-ethylene-butadiene-styrene rubber (SEBS), It is preferably a polyolefin elastomer (POE) such as butadiene rubber (BR), butyl rubber (IR), isoprene-isobutylene rubber (IIR) or ethylene propylene rubber (EPM), ethylene propylene diene rubber (EPDM).
본 발명의 일 실시예에 의하면, 상기 고무 조성물이 타이어 트래드용 고무 조성물, 실란트용 고무 조성물, Hot-melt 접착제용 고무 조성물로 사용되는 것이 바람직하다.According to an embodiment of the present invention, the rubber composition is preferably used as a rubber composition for a tire tread, a rubber composition for a sealant, and a rubber composition for a hot-melt adhesive.
특히 바람직하게는 상기 고무가 이소프렌-이소부틸렌 고무(IIR)인 경우 실란트용 부틸고무로 사용할 수 있다.Particularly preferably, when the rubber is isoprene-isobutylene rubber (IIR), it can be used as a butyl rubber for a sealant.
또한, 특히 바람직하게는 상기 고무가 스티렌-부타디엔-스티렌 블록공중합체(SBS) 및 스티렌-에틸렌-부타디엔-스티렌 수지(SEBS)인 경우에는 Hot-melt 접착제 제조에 사용할 수 있다. In addition, particularly preferably, when the rubber is a styrene-butadiene-styrene block copolymer (SBS) and a styrene-ethylene-butadiene-styrene resin (SEBS), it can be used for manufacturing a hot-melt adhesive.
본 발명의 또 다른 목적을 달성하기 위하여 본 발명은 본 발명에 따라 제조된 고무 조성물을 포함하는 타이어 트래드용 고무 조성물을 제공한다.In order to achieve another object of the present invention, the present invention provides a rubber composition for a tire tread comprising the rubber composition prepared according to the present invention.
본 발명의 일예에 따른 타이어 트레드용 고무 조성물은, 상기한 원료고무 및 고반응성 폴리부텐(PIB) 이외에도 보강충전제인 실리카 및/또는 카본 블랙, 연화제인 프로세스 오일, 가황제인 유황, 가황 촉진제인 CBS와 1,3-디페닐구아니딘(DPG), 가류활성제인 산화아연, 스테아린산, 분산성 향상을 위한 커플링제 및 노화방지제 등 타이어 트레드용 고무 조성물에 일반적으로 사용되는 고무배합제를 포함할 수 있다. The rubber composition for a tire tread according to an embodiment of the present invention includes, in addition to the raw material rubber and highly reactive polybutene (PIB), silica and/or carbon black as reinforcing fillers, process oil as a softener, sulfur as a vulcanizing agent, CBS as a vulcanization accelerator, and 1,3-diphenylguanidine (DPG), zinc oxide as a vulcanizing activator, stearic acid, a coupling agent for improving dispersibility, and an anti-aging agent may include a rubber compounding agent generally used in a rubber composition for a tire tread.
본 발명에서 보강충전제로 사용될 수 있는 실리카는 그 종류에는 특별한 제한이 없으나, 표면적이 175 ± 5 ㎡/g, 수분 함량은 6.0 ± 0.5 중량%, 이산화규소(SiO2) 함량은 90 중량% 이상인 것이 바람직하다.The type of silica that can be used as a reinforcing filler in the present invention is not particularly limited, but preferably has a surface area of 175 ± 5 m 2 /g, a moisture content of 6.0 ± 0.5 wt%, and a silicon dioxide (SiO2) content of 90 wt% or more. Do.
본 발명에 사용되는 카본 블랙은, 그 종류에 특별한 제한은 없으나, BET(Brunauer, Emmett, Teller) 비표면적이 80~90 ㎡/g 이고, DBP(Di-n-bibutyl Phthalate)흡착가가 100~110 g/100g이며, 요오드 흡착가가 90~120 mg/g 범위인 것이 바람직하다. 상기 카본 블랙은 원료 고무 100 중량부에 대하여 40~100 중량부를 사용하는 것이 바람직한데, 그 사용량이 40 중량부 미만이면 충분한 보강 효과를 나타내지 못하여 바람직하지 않고, 100 중량부를 초과하면 발열 및 내마모 효과를 나타내지 못하여 바람직하지 않다.The carbon black used in the present invention is not particularly limited in its type, but has a BET (Brunauer, Emmett, Teller) specific surface area of 80 to 90 m 2 /g, and a DBP (Di-n-bibutyl) Phthalate) adsorption value is 100-110 g/100g, and iodine adsorption value is preferably in the range of 90-120 mg/g. The carbon black is preferably used in an amount of 40 to 100 parts by weight based on 100 parts by weight of the raw rubber. If the amount is less than 40 parts by weight, it is not preferable because a sufficient reinforcing effect is not exhibited. It is not preferable because it does not show
상기 프로세스 오일은 연화제 역할을 하며, 오일내 방향족계 함량이 5~25 중량%이고, 나프탈렌 함량이 25~45 중량%이며, 파라핀계 함량이 35~65 중량%인 것이 바람직하다. 기타 본 발명에서 사용되는 다양한 첨가제에 대하여는 타이어 트레드용 고무 조성물에 사용되는 일반적인 성분으로서 그 자세한 내용은 생략한다.The process oil acts as a softener, and the aromatic content in the oil is 5 to 25 wt%, the naphthalene content is 25 to 45 wt%, and the paraffinic content is preferably 35 to 65 wt%. Other various additives used in the present invention are general components used in the rubber composition for tire tread, and details thereof will be omitted.
이상과 같이 하여 본 발명에 따른 상기 타이어 트레드용 고무 조성물은, 타이어의 제반 기본 물성에 영향을 주지 않으면서 자동차 타이어 특히 고속 경주용자동차용 타이어의 트레드부에 그립 성능을 향상시키는 반면 이를 지속적으로 유지 가능하게 한다.As described above, the rubber composition for a tire tread according to the present invention improves grip performance on the tread of an automobile tire, particularly a tire for a high-speed race car, while continuously maintaining the same without affecting the basic physical properties of the tire. make it possible
본 발명의 또 다른 목적을 달성하기 위하여 본 발명에 따른 타이어 트래드용 고무 조성물을 이용하여 제조된 타이어를 제공한다. Another object of the present invention is to provide a tire manufactured by using the rubber composition for a tire tread according to the present invention.
이하에서는 구체적인 실시예와 비교예를 들어 본 발명을 더욱 구체적으로 설명한다. 다만 이는 본 발명을 보다 이해하기 쉽게 설명하기 위한 것에 불과하며, 본 발명의 범위를 제한하는 방법으로 해석되어서는 안 된다. Hereinafter, the present invention will be described in more detail with reference to specific examples and comparative examples. However, this is merely to explain the present invention more easily, and should not be construed as limiting the scope of the present invention.
제조예 1: 폴리부텐(PIB)이 액상으로 분산된(extension) 부타디엔 고무(BR)의 제조Preparation Example 1: Preparation of butadiene rubber (BR) in which polybutene (PIB) is dispersed in a liquid phase (extension)
질소로 치환된 10L 오토크레이브 반응기에, 수분이 제거된 1,3-부타디엔 1500g, 헥산 5250g을 넣은 후에 반응기 온도를 교반기로 돌리면서 95oC로 승온하였다. 온도가 95oC로 안정화 된 후 트리이소부틸알루미늄/니켈옥사노에이트/불산을 조합한 촉매를 투입하고, 온도가 급격히 올라가지 않도록 조절하면서 2시간 동안 폴리부타디엔고무(BR)의 중합을 진행하였다. 이후 반응 정지제로 알킬 포스페이트계 화합물 2.5g과 폐놀계 산화 방지제를 5g 투입하여 반응을 종료시켰다. 이렇게 중합한 중합물을 50oC로 냉각 후 해압하여 잔류 1,3-부타디엔을 제거한 부타디엔고무/헥산 용액을 제조하였다. 제조한 부타디엔고무/헥산 용액은 고형분 함량(TSC, total solid content) 측정 후 계량하여 교반기가 달린 5L 블랜드 탱크로 이송한다. 이 부타디엔고무/헥산 용액에 고형분 대비 37.5 phr의 표 1에 따른 폴리부텐(PIB)을 추가한 후 PIB가 완전히 용해될 때까지 교반해 준다. 제조된 부타디엔고무/폴리부텐/헥산 혼합물을 스팀스트리퍼를 활용하여 용매인 헥산을 제거하여 폴리부텐이 고르게 분산된 부타디엔고무 고형물을 얻고, 고형물의 수분은 100oC의 가공롤을 이용 수분을 건조하여 PIB가 37.5phr extension된 부타디엔고무 샘플을 제조하였다.In a 10L autoclave reactor substituted with nitrogen, 1500 g of 1,3-butadiene from which moisture was removed, and 5250 g of hexane were put, and then the temperature of the reactor was raised to 95 o C while turning the reactor with a stirrer. After the temperature was stabilized to 95 o C, a catalyst in a combination of triisobutylaluminum/nickeloxanoate/hydrofluoric acid was added, and polymerization of polybutadiene rubber (BR) was carried out for 2 hours while controlling the temperature not to rise rapidly. Afterwards, 2.5 g of an alkyl phosphate-based compound and 5 g of a phenol-based antioxidant were added as a reaction terminator to terminate the reaction. The polymerized product was cooled to 50 o C and depressurized to prepare a butadiene rubber/hexane solution from which residual 1,3-butadiene was removed. The prepared butadiene rubber/hexane solution is measured and transferred to a 5L blend tank equipped with a stirrer after measuring total solid content (TSC). After adding polybutene (PIB) according to Table 1 at 37.5 phr of solid content to this butadiene rubber/hexane solution, the solution is stirred until the PIB is completely dissolved. The prepared butadiene rubber/polybutene/hexane mixture is removed using a steam stripper to remove hexane as a solvent to obtain a butadiene rubber solid in which polybutene is evenly dispersed, and the moisture of the solid is dried using a processing roll at 100 o C. A sample of butadiene rubber with 37.5 phr of PIB extension was prepared.
비교제조예 1: 폴리부타디엔(BR)의 제조Comparative Preparation Example 1: Preparation of polybutadiene (BR)
제조예 1과 동일한 방법으로 폴리부타디엔고무(BR)를 중합하고, 잔류 1, 3-부타디엔과 용매를 제거하여, 폴리부타디엔고무(BR)을 얻었다.Polybutadiene rubber (BR) was polymerized in the same manner as in Preparation Example 1, and residual 1,3-butadiene and solvent were removed to obtain polybutadiene rubber (BR).
비교예 1 및 2Comparative Examples 1 and 2
비교예 1은 비교제조예 1에서 제조된 폴리부타디엔 고무만을 사용하였고, 비교예 2는 비교제조예 1에서 제조된 폴리부타디엔과 ㈜한화토탈에서 제조한 HRPIB470을 혼합하였다. In Comparative Example 1, only the polybutadiene rubber prepared in Comparative Preparation Example 1 was used, and in Comparative Example 2, the polybutadiene prepared in Comparative Preparation Example 1 and HRPIB470 manufactured by Hanwha Total Co., Ltd. were mixed.
실시예 1 내지 5Examples 1 to 5
실시예 1 내지 5는 각각 제조예 1에 따라 폴리부타디엔 고무(BR)을 제조하고 단량체를 제거한 후 표 1에 기재된 바에 따른 각기 다른 폴리부텐(PIB)을 첨가하여, 표 1에 따른 폴리부텐(PIB)이 액상으로 분산된(extension) 부타디엔 고무(BR)의 제조하였다.Examples 1 to 5 each prepared polybutadiene rubber (BR) according to Preparation Example 1, and after removing the monomer, different polybutenes (PIB) according to Table 1 were added, and polybutene (PIB) according to Table 1 ) was prepared in a liquid dispersion (extension) butadiene rubber (BR).
사용한 Raw material의 정보Information on the raw material used
비교예comparative example 실시예Example
1One 22 1One 22 33 44 55
폴리부텐(PIB)Polybutene (PIB) 미사용unused HRPIB470HRPIB470 CPIB230CPIB230 HRPIB190HRPIB190 CPIB650CPIB650 HRPIB470HRPIB470 HRPIB470HRPIB470
고무Rubber BRBR BRBR BRBR BRBR BRBR BRBR BRBR
- PIB: ㈜한화토탈 CPIB230, CPIB650, HRPIB190, HRPIB470 1) CPIB230: conventional PIB (Mn 950g/mol), PB950(㈜대림산업)- PIB: Hanwha Total Co., Ltd. CPIB230, CPIB650, HRPIB190, HRPIB470 1) CPIB230: conventional PIB (Mn 950g/mol), PB950 (Daelim Industrial Co., Ltd.)
2) CPIB650: conventional PIB (Mn 1,300g/mol), PB1300(㈜대림산업) 2) CPIB650: conventional PIB (Mn 1,300g/mol), PB1300 (Daelim Industrial Co., Ltd.)
3) HRPIB190: high reactive PIB (Mn 1,000g/mol), HRPB1000(㈜대림산업) 3) HRPIB190: high reactive PIB (Mn 1,000g/mol), HRPB1000 (Daelim Industrial Co., Ltd.)
4) HRPIB470: high reactive PIB (Mn 1,300g/mol), HRPB1300(㈜대림산업) 4) HRPIB470: high reactive PIB (Mn 1,300g/mol), HRPB1300 (Daelim Industrial Co., Ltd.)
- Hx: ㈜한화토탈 n-Hexane- Hx: Hanwha Total Co., Ltd. n-Hexane
- CHx: ㈜덕산케미칼 Cyclohexane- CHx: Duksan Chemical Co., Ltd. Cyclohexane
<실시예 1 내지 6><Examples 1 to 6>
표 2의 조성으로 Moriyama사의 MIX-LABO(Mixing capacity: 0.5liter, Main motor: 15HP)를 이용하여 가교전 복합재를 제조하였다. With the composition shown in Table 2, a composite material before crosslinking was prepared using MIX-LABO (Mixing capacity: 0.5liter, Main motor: 15HP) manufactured by Moriyama.
표 2에서 실시예 1 내지 5는 PIB가 분산된 BR 은 제조예 1에서 제조된 폴리부텐(PIB)이 액상에서 분산된 고무(PIB extended rubber)를 사용하였고, 비교예 1은 비교제조예 1에서 제조된 폴리부타디엔 고무만을 사용한 것이고, 비교예 2는 비교제조예 1에서 제조된 폴리부타디엔 고무와 폴리부텐(PIB, HRPIB470)를 혼합한 것이다. In Examples 1 to 5 in Table 2, BR in which PIB is dispersed was a rubber in which polybutene (PIB) prepared in Preparation Example 1 was dispersed in a liquid (PIB extended rubber), and Comparative Example 1 was used in Comparative Preparation Example 1. Only the prepared polybutadiene rubber was used, and Comparative Example 2 was a mixture of the polybutadiene rubber prepared in Comparative Preparation Example 1 and polybutene (PIB, HRPIB470).
배합은 2단계로 진행하였다. 제1혼련으로는 0.5리터 배합기의 부피기준 75% 충전하고 로터 회전수를 70rpm조건으로 고무조성물, 충진제(실리카), 오일, 산화아연(ZnO), 스테아린산(stearic acid), 실란커플링제(Si-69)를 넣어 온도를 제어하여 140~150℃에서 1차 고무조성물을 얻는다. The compounding was carried out in two steps. For the first kneading, fill 75% based on the volume of the 0.5 liter compounder and set the rotor speed to 70 rpm. Rubber composition, filler (silica), oil, zinc oxide (ZnO), stearic acid, silane coupling agent (Si-) 69) to control the temperature to obtain a primary rubber composition at 140~150℃.
제2혼련으로는 배합물을 실온까지 냉각하고 90℃ 이하에서 황(sulfur)과 DPG(Diphenyl Guanidine), CBS(N-cyclohexyl-2-benzothiazole sulfonamide), 산화방지제(6-PPD)를 첨가하여 50rpm조건으로 2분간 혼련하였다.For the second kneading, the mixture is cooled to room temperature and sulfur, DPG (Diphenyl Guanidine), CBS (N-cyclohexyl-2-benzothiazole sulfonamide), and antioxidant (6-PPD) are added at 90° C. or less at 50 rpm. and kneaded for 2 minutes.
배합된 고무복합재의 가교를 위해 Rubber Process Analyzer(RPA)로 160℃, 40분, 변형율 1%의 조건으로 가류특성을 측정하여 얻어진 T90의 시간에 2분을 더한 시간 동안 각각의 고무 복합재를 160℃ 고온프레스에서 가교하여 타이어 트래드용 고무복합재 시편을 제조하였다.For crosslinking of the blended rubber composite, each rubber composite was heated at 160℃ for the time obtained by measuring the vulcanization characteristics at 160℃, 40 minutes, and 1% strain with a Rubber Process Analyzer (RPA), plus 2 minutes to the time of T90. A rubber composite specimen for tire tread was prepared by crosslinking in a high-temperature press.
기타 첨가제로서, SBR, BR 및 PIB를 포함하는 고무 조성물 100 중량부에 대하여, 징크옥사이드(ZnO) 3중량부, 스테아릭산(St-A) 2 중량부, 실리카(ULTRASIL 7000Gr) 70중량부, 실리카 커플링제(SI-69) 5.6중량부, TDAE(treated distillate aromatic extracted) Oil 10중량부를 첨가하여 1차 배합물(SMB, silica master batch)을 제조하고,As other additives, with respect to 100 parts by weight of the rubber composition comprising SBR, BR and PIB, zinc oxide (ZnO) 3 parts by weight, stearic acid (St-A) 2 parts by weight, silica (ULTRASIL 7000Gr) 70 parts by weight, silica A primary compound (SMB, silica master batch) is prepared by adding 5.6 parts by weight of a coupling agent (SI-69) and 10 parts by weight of TDAE (treated distillate aromatic extracted) oil,
1차 배합물 대비 황 1.5중량부, 가황촉진제인 디페닐구아니딘(DPG) 1.8 중량부, 시클로헥실벤조사이아졸설펜아미드(CBS) 1.8중량부, 산화방지제(6PPD) 0.2 중량부를 더 첨가하여 2차 배합물(FMB, final master batch)을 제조하였다. 다만, 실시예 5에서 황의 함량은 1.8 중량부인 것에만 차이가 있다.Compared to the first formulation, 1.5 parts by weight of sulfur, 1.8 parts by weight of diphenylguanidine (DPG) as a vulcanization accelerator, 1.8 parts by weight of cyclohexylbenzocyazolesulfenamide (CBS), and 0.2 parts by weight of antioxidant (6PPD) are further added to the secondary formulation (FMB, final master batch) was prepared. However, in Example 5, there is a difference only in that the content of sulfur is 1.8 parts by weight.
<비교예 1><Comparative Example 1>
폴리부텐(PIB)을 포함하지 않는 BR를 사용한 것을 제외하고는 실시예 1과 동일하게 하여 고무 복합재 시편을 제조하였다. A rubber composite specimen was prepared in the same manner as in Example 1, except that BR not containing polybutene (PIB) was used.
<비교예 2><Comparative Example 2>
표 1의 조성으로, HRPIB470의 폴리부텐(PIB)을 별도로 액상 분산화시키는 단계를 거치지 않고 배합기에 바로 투입하여 고무와 배합하는 것을 제외하고는 실시예 4와 동일하게 하여 고무 복합재 시편을 제조하였다.With the composition shown in Table 1, a rubber composite specimen was prepared in the same manner as in Example 4, except that the polybutene (PIB) of HRPIB470 was added directly to a blender and blended with rubber without a separate liquid dispersion step.
(단위: 중량%)(Unit: % by weight)
비교예comparative example 실시예Example
1One 22 1One 22 33 44 55
SBR(KKPC 5260H)SBR(KKPC 5260H) 8080 8080 8080 8080 8080 8080 8080
비교제조예 1의 BRBR of Comparative Preparation Example 1 2020 14.514.5
고반응성 폴리부텐(HRPIB)470 배합기 직접투입Direct injection of highly reactive polybutene (HRPIB) 470 compounding machine 5.55.5
제조예 1(각 PIB가 37.5 phr포함된 BR)Preparation Example 1 (BR containing 37.5 phr of each PIB) 2020 2020 2020 2020 2020
실험예:Experimental example:
상기 비교예와 실시예에 따라 제조된 각 고무 복합재 시편을 ASTM 관련규정에 의하여 다음과 같이 물성을 측정하였으며, 그 결과를 다음 표 3에 나타내었다.The physical properties of each rubber composite specimen prepared according to the Comparative Examples and Examples were measured as follows according to ASTM related regulations, and the results are shown in Table 3 below.
(1) 배합점도(Mooney viscosity, MV): 무니점도계(MV2000, 알파테크놀로지사)를 사용하여 100℃에서 큰 로우터로 예열 1분에서 로우터 시동 후 4분 후의 값을 측정 판독하여 무니점도를 측정하였다. (1) Mooney viscosity (MV): Mooney viscosity was measured using a Mooney viscometer (MV2000, Alpha Technologies) by using a Mooney viscometer (MV2000, Alpha Technologies) to preheat a large rotor at 100°C for 1 minute and read the value 4 minutes after starting the rotor. .
(2) 경도: 경도 시험은 JIS K6253(2001년)에 준거해 실시하여 스프링 경도 HA(쇼어-A경도)를 측정하였다. (2) Hardness: The hardness test was performed based on JIS K6253 (2001), and the spring hardness HA (Shore-A hardness) was measured.
(3) 모듈러스: 모듈러스 측정은 시편을 아령형으로 잘라서 인스트론사에서 제작한 인장시험기로 실시하였다. 100% 및 200% 모듈러스는 시편을 100% 및 200% 각각 신장시켰을 경우 시편에 작용하는 스트레스를 일컫는다. (3) Modulus : Modulus measurement was performed with a tensile tester manufactured by Instron after cutting a specimen into a dumbbell shape. The 100% and 200% modulus refer to the stress applied to the specimen when the specimen is elongated by 100% and 200%, respectively.
(4)인장강도: 인장강도는 가황 고무 시트를 뚫어 JIS K6251(2001년)에 기재되어 있는 3호형 덤벨 시험편을 제조하였다. 이 시험편을 이용해 동 JIS K6251에 규정되는 방법에 따라, 측정 온도 25℃, 인장 속도 500mm/분의 조건으로 인장 시험을 실시하여 100% 모듈러스 (M100), 200% 모듈러스(M200), 300% 모듈러스(M300) 인장 파단점 응력 TB 및 인장 파단점 신도(伸度) EB를 측정하였다. (4) Tensile strength : For the tensile strength, a No. 3 dumbbell test piece described in JIS K6251 (2001) was prepared by punching a vulcanized rubber sheet. Using this test piece, according to the method specified in JIS K6251, a tensile test was conducted under the conditions of a measurement temperature of 25°C and a tensile rate of 500 mm/min, and 100% modulus (M100), 200% modulus (M200), 300% modulus ( M300) Tensile break stress TB and tensile break elongation EB were measured.
(5) 신율: 인장강도 측정시 파단점까지의 변형율(%)로 측정하였다. (5) Elongation: When measuring the tensile strength, it was measured as the strain (%) up to the breaking point.
(6)점탄성: 점탄성은 Dynamic mechanical analysis(DMA)를 이용하여 측정하며 0℃ Tanδ는 젖은 노면에서의 타이어의 제동 성능의 대용 수치로 이용되며, 그 수치가 높을수록 우수한 성능을 나타낸다. 60℃ Tanδ는 타이어 회전저항값의 대용 수치로 사용되며, 그 수치가 낮을수록 회전저항이 우수하여 연비효율이 상승하는 것을 나타낸다. (6) Viscoelasticity: Viscoelasticity is measured using dynamic mechanical analysis (DMA), and 0℃ Tanδ is used as a substitute for the braking performance of the tire on a wet road surface, and the higher the value, the better the performance. 60℃ Tanδ is used as a substitute for the tire rolling resistance value, and the lower the value, the better the rolling resistance is, indicating that fuel efficiency increases.
(7)마모: 마모는 DIN마모 시험기를 이용하여 5N하중을 주면서 ASTM D5963법에 따라 마모되어 줄어든 중량을 측정하며, 상대지수로 표시하여 그 수치가 클수록 마모성능이 우수함을 나타낸다. (7) Abrasion: Abrasion is measured according to ASTM D5963 method while applying a 5N load using a DIN abrasion tester, and expressed as a relative index, the larger the value, the better the wear performance.
물성Properties 비교예comparative example 실시예Example
1One 22 1One 22 33 44 55
가공성machinability 배합점도(MV)Mixed viscosity (MV) 110110 105105 100100 100100 100100 100100 100100
가교특성Crosslinking properties 가교밀도(dNm)Crosslinking density (dNm) 2727 2525 2525 2525 2525 2525 2727
인장물성tensile properties 경도(SHORE-A)Hardness (SHORE-A) 6767 6868 6868 6969 6969 6969 6969
100%모듈러스(kgf/cm2)100% modulus (kgf/cm2) 6464 6060 5858 6262 5757 5656 5959
200%모듈러스(kgf/cm2)200% modulus (kgf/cm2) 142142 132132 136136 146146 133133 131131 147147
인장강도(kgf/cm2)Tensile strength (kgf/cm2) 215215 187187 200200 209209 195195 199199 188188
신율(%)Elongation (%) 274274 258258 267267 263263 268268 273273 240240
점탄성viscoelastic 0℃Tanδ0℃Tanδ 0.22570.2257 0.23250.2325 0.27050.2705 0.26730.2673 0.25610.2561 0.28090.2809 0.31600.3160
60℃Tanδ60℃Tanδ 0.07620.0762 0.07920.0792 0.08090.0809 0.07810.0781 0.08230.0823 0.07650.0765 0.06760.0676
마모Wear 지수Indices 100100 9696 103103 101101 101101 110110 111111
표3과 같이 PIB를 고무에 용액상으로 분산하여 제조 한 시편이 PIB를 포함하지 않거나 동일한 양의 PIB를 배합기에 직접 투입한 것 대비하여 내구성, 그립(grip)성, 낮은 회전저항성이 개선되어 우수한 제동 특성, 저연비 특성 및 마모성능이 향상 되는 결과를 얻었다.As shown in Table 3, the specimen prepared by dispersing PIB in a solution phase in rubber has improved durability, grip properties, and low rotational resistance compared to that containing no PIB or adding the same amount of PIB directly to the compounding machine. Braking characteristics, low fuel consumption characteristics and wear performance were improved.

Claims (8)

  1. 고무에 폴리머가 용액상으로 분산된(polymer extended rubber), 폴리머 분산 고무 조성물을 제조하는 방법으로서, A method for preparing a polymer dispersed rubber composition in which a polymer is dispersed in a solution phase in rubber (polymer extended rubber),
    고무 제조 공정단계에서, 단량체, 용제 및 촉매를 포함하는 고무 조성물을 중합 반응시키는 단계; Polymerizing a rubber composition comprising a monomer, a solvent and a catalyst in the rubber manufacturing process step;
    잔류 단량체를 회수하는 단계; 및recovering residual monomer; and
    상기 잔류 단량체를 회수한 후 남은 고무 용액에 폴리머를 투입하는 단계;를 포함하는 것을 특징으로 하는 고무 조성물의 제조방법.A method for producing a rubber composition comprising: adding a polymer to the rubber solution remaining after recovering the residual monomer.
  2. 제1항에 있어서,According to claim 1,
    상기 폴리머는 C4계 폴리머로서 중량평균분자량이 300 ~ 20,000 g/mol이고,The polymer is C4 As a polymer, the weight average molecular weight is 300 ~ 20,000 g / mol,
    상기 고무 함량에 대하여 1~50phr(parts per hundred rubber)로 투입되는 것을 특징으로 하는 고무 조성물의 제조방법.A method for producing a rubber composition, characterized in that it is added in an amount of 1 to 50 phr (parts per hundred rubber) with respect to the rubber content.
  3. 제1항에 있어서,According to claim 1,
    상기 폴리머는 C4계 폴리머인 폴리부텐(PIB)인 것을 특징으로 하는 고무 조성물의 제조방법.The polymer is a method for producing a rubber composition, characterized in that the C4 polymer polybutene (PIB).
  4. 제1항에 있어서,According to claim 1,
    상기 단량체는 스티렌, 부타디엔, 이소부틸렌, 이소프렌, 에틸렌 및 프로필렌 등으로 이루어진 군으로부터 선택된 1종 이상인 것을 특징으로 하는 고무 조성물의 제조방법.The method for producing a rubber composition, characterized in that the monomer is at least one selected from the group consisting of styrene, butadiene, isobutylene, isoprene, ethylene and propylene.
  5. 제1항에 있어서,According to claim 1,
    상기 고무는 에멀젼 스티렌부타디엔 고무(ESBR), 솔루션 스티렌부타디엔 고무(SSBR), 스티렌-부타디엔-스티렌 고무(SBS), 스티렌-에틸렌-부타디엔-스티렌 고무(SEBS), 부타디엔 고무(BR), 부틸고무(IR), 이소프렌-이소부틸렌 고무(IIR) 또는 에틸렌프로필렌 고무(EPM), 에틸렌프로필렌디엔 고무(EPDM)과 같은 폴리올레핀 엘라스토머(POE)인 것을 특징으로 하는 고무 조성물의 제조방법.The rubber is emulsion styrene-butadiene rubber (ESBR), solution styrene-butadiene rubber (SSBR), styrene-butadiene-styrene rubber (SBS), styrene-ethylene-butadiene-styrene rubber (SEBS), butadiene rubber (BR), butyl rubber ( IR), isoprene-isobutylene rubber (IIR) or ethylene propylene rubber (EPM), ethylene propylene diene rubber (EPDM), such as a polyolefin elastomer (POE), characterized in that the manufacturing method of the rubber composition.
  6. 제1항 내지 제5항 중 어느 한 항에 있어서,6. The method according to any one of claims 1 to 5,
    상기 고무 조성물이 타이어 트래드용 고무 조성물, 실란트용 고무 조성물, Hot-melt 접착제용 고무 조성물, 신발밑창용 고무 조성물, 벨트(belt)용 고무 조성물, 호스(hose)용 고무 조성물, 또는 시트(sheet)용 고무조성물로 사용되는 것을 특징으로 하는 고무 조성물의 제조방법.The rubber composition is a rubber composition for a tire tread, a rubber composition for a sealant, a rubber composition for a hot-melt adhesive, a rubber composition for a shoe sole, a rubber composition for a belt, a rubber composition for a hose, or a sheet. A method for producing a rubber composition, characterized in that it is used as a rubber composition for use.
  7. 제1항 내지 제5항 중 어느 한 항의 제조방법에 따라 제조된 고무 조성물을 포함하는 것을 특징으로 하는 타이어 트래드용 고무 조성물.[Claim 6] A rubber composition for a tire tread comprising the rubber composition prepared according to any one of claims 1 to 5.
  8. 제7항에 따른 타이어 트래드용 고무 조성물을 이용하여 제조된 것을 특징으로 하는 타이어.A tire, characterized in that it is manufactured using the rubber composition for a tire tread according to claim 7.
PCT/KR2020/008781 2019-12-24 2020-07-06 Method for preparing rubber composition, rubber composition prepared thereby, and tire manufactured using same WO2021132822A1 (en)

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