Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L9/00—Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
  • C08L9/06—Copolymers with styrene
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B60—VEHICLES IN GENERAL
  • B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
  • B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
  • B60C1/0016—Compositions of the tread
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/0061—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof characterized by the use of several polymeric components
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
  • C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
  • C08J9/08—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing carbon dioxide
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2201/00—Foams characterised by the foaming process
  • C08J2201/02—Foams characterised by the foaming process characterised by mechanical pre- or post-treatments
  • C08J2201/026—Crosslinking before of after foaming
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2203/00—Foams characterized by the expanding agent
  • C08J2203/02—CO2-releasing, e.g. NaHCO3 and citric acid
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2309/00—Characterised by the use of homopolymers or copolymers of conjugated diene hydrocarbons
  • C08J2309/06—Copolymers with styrene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2409/00—Characterised by the use of homopolymers or copolymers of conjugated diene hydrocarbons
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L9/00—Compositions of homopolymers or copolymers of conjugated diene hydrocarbons

Definitions

• the invention relates to motor vehicle tires as well as rubber compositions usable for the manufacture of such tires. It is more particularly related to tires whose tread comprises a vulcanized foam rubber composition, intended to reduce the noise emitted by these tires during the running of the vehicles.
• the acoustic waves emitted by the tire are directly propagated by air inside the vehicle, the latter acting as a filter; this is referred to as airborne transmission, which generally dominates in high frequencies
• noise noise refers rather to the perceived overall level in the vehicle and in a frequency range up to 2000 Hz.
• the noise called “cavity” refers to the annoyance due to the resonance of the cavity of inflation of the tire casing.
• Concerning the noise emitted outside the vehicle, are relevant the various interactions between the tire and the road surface, the tire and the air, which will cause an inconvenience to the residents of the vehicle when it rolls on a road. floor.
• the frequency range concerned here typically corresponds to a range of about 300 to 3000 Hz.
• the present invention relates to a tire whose tread comprises, in the uncured state, a heat-expandable rubber composition comprising at least: 50 to 100 phr of a copolymer based on styrene and butadiene ;
• the invention also relates to a tire in the vulcanized state obtained after baking (vulcanization) of the green tire according to the invention as described above.
• the tires of the invention are particularly intended to equip tourism-type motor vehicles, including 4x4 vehicles (four-wheel drive) and SUV vehicles ("Sport Utility Vehicles"), two-wheel vehicles (including motorcycles) as vehicles industrials chosen in particular from vans and "heavy goods vehicles” (ie, metro, buses, road transport equipment such as trucks, tractors).
• 4x4 vehicles four-wheel drive
• SUV vehicles Sport Utility Vehicles
• two-wheel vehicles including motorcycles
• industrials chosen in particular from vans
• "heavy goods vehicles” ie, metro, buses, road transport equipment such as trucks, tractors.
• iene elastomer or indistinctly rubber is meant an elastomer derived at least in part (that is to say a homopolymer or a copolymer) from monomer (s) diene (s) (ie, carrier (s) two carbon-carbon double bonds, conjugated or not).
• isoprene elastomer is meant a homopolymer or copolymer of isoprene, in other words a diene elastomer selected from the group consisting of natural rubber (NR), synthetic polyisoprenes (IR), the various copolymers of isoprene, isoprene and mixtures of these elastomers.
• the abbreviation "pce” means parts by weight per hundred parts of elastomer (of the total elastomers if several elastomers are present).
• any range of values designated by the expression “between a and b” represents the range of values greater than “a” and less than “b” (i.e., terminals a and b excluded). while any range of values designated by the term “from a to b” means the range of values from “a” to "b” (i.e. including the strict limits a and b).
• the tire of the invention therefore has the essential characteristic that its tread in the uncured state, at least for its portion (radially outermost part) intended to come into direct contact with the road surface, comprises a heat-expandable rubber composition comprising at least:
• the essential heat-shrinkable rubber composition has the essential first characteristic of comprising 50 to 100 phr of a styrene-butadiene-based copolymer, that is to say a copolymer of a styrene-butadiene copolymer. at least one styrene monomer and at least one butadiene monomer; in other words, said copolymer based on styrene and butadiene has by definition at least units derived from styrene and units derived from butadiene.
• the level of said copolymer, in the thermoexpansible rubber composition is in a range of 50 to 90 phr, more preferably in a range of 60 to 85 phr.
• butadiene monomers 1,3-butadiene, 2-methyl-1,3-butadiene, 2,3-di (C 1 -C 5 alkyl) -1,3-butadienes, such as for example 2, are particularly suitable.
• styrene monomers are especially suitable styrene, methylstyrenes, para-tert-butylstyrene, methoxystyrenes, chloro styrenes.
• Said copolymer based on styrene and butadiene may have any micro structure which is a function of the polymerization conditions used, in particular the presence or absence of a modifying and / or randomizing agent and the amounts of modifying and / or randomizing agent used. . It can be for example block, statistical, sequenced, microsequenced, and be prepared in dispersion or in solution; it may be coupled and / or starred or functionalized with a coupling agent and / or starring or functionalization.
• the styrene-butadiene-based copolymer is selected from the group consisting of styrene-butadiene copolymers (abbreviated to SBR), styrene-butadiene-isoprene copolymers (abbreviated to SBIR) and mixtures of such copolymers.
• SBR styrene-butadiene copolymers
• SBIR styrene-butadiene-isoprene copolymers
• SBIR copolymers mention may in particular be made of those having a styrene content of between 5% and 50% by weight and more particularly of between 10% and 40%, an isoprene content of between 15% and 60% by weight, and especially between 20% and 50%, a butadiene content of between 5% and 50% by weight and more particularly between 20% and 40%, a content (mol%) in -1,2 units of the butadiene part of between 4% and 85%, a content (mol%) in trans-1,4 units of the butadiene part comprised between 6%> and 80%>, a content (mol%) in units -1,2 plus -3,4 of the isoprenic part between 5% and 70%> and a content (mol%) in trans -1,4 units of the isoprenic part of between 10%> and 50%>.
• an SBR copolymer is used.
• SBR copolymers there may be mentioned especially those having a styrene content of between 5% and 60% by weight and more particularly between 20% and 50%, a content (mol%) in -1,2 bonds of the butadiene part. between 4% and 75%, a content (mol%) of trans-1,4 bonds of between 10% and 80%.
• the Tg of the copolymer based on styrene and butadiene is preferably greater than -40 ° C., more preferably greater than -35 ° C., in particular between -30 ° C. and + 30 ° C. (more particularly included in one from -25 ° C to + 25 ° C).
• Tg of the elastomers described here is measured in a conventional manner, well known to those skilled in the art, on an elastomer in the dry state (ie, without extension oil) and by DSC (for example according to ASTM D3418-1999). .
• copolymer based on styrene and butadiene above may be associated with at least one other (also called second) diene elastomer, different from said copolymer (that is to say not having units derived from styrene and butadiene ), said second diene elastomer being present at a weight ratio which is therefore at most equal to 50 phr.
• second diene elastomer different from said copolymer (that is to say not having units derived from styrene and butadiene )
• said second diene elastomer being present at a weight ratio which is therefore at most equal to 50 phr.
• This second optional diene elastomer is preferably selected from the group consisting of natural rubbers (NR), synthetic polyisoprenes (IR), polybutadienes (BR), isoprene copolymers and mixtures of these elastomers.
• Such copolymers are more preferably selected from the group consisting of isoprene-butadiene copolymers (BIR) and isoprene-styrene copolymers (SIR).
• polybutadiene homopolymers and in particular those having a content (mol%) in units of 1,2,2 between 4% and 80% or those having a content (mol%) of cis-1, are particularly suitable, 4 greater than 80%>; polyisoprene homopolymers (IR); butadiene-isoprene copolymers (BIR) and in particular those having an isoprene content of between 5% and 90% by weight and a Tg of -40 ° C to -80 ° C .; isoprene-styrene copolymers (SIR) and in particular those having a styrene content of between 5% and 50% by weight and a Tg of between -25 ° C.
• IR polyisoprene homopolymers
• BIR butadiene-isoprene copolymers
• SIR isoprene-styrene copolymers
• the second diene elastomer is an isoprene elastomer, more preferably natural rubber or a synthetic polyisoprene of cis-1,4 type; of these synthetic polyisoprenes, polyisoprenes having a content (mol%) of cis-1,4 bonds greater than 90%, more preferably still greater than 98%, are preferably used.
• the second diene elastomer is a polybutadiene, preferably a polybutadiene having a cis-1,4 bond ratio greater than 90%.
• the second diene elastomer is a mixture of polybutadiene with an isoprene elastomer (natural rubber or synthetic polyisoprene).
• the level of second diene elastomer in particular polybutadiene and / or isoprene elastomer (in particular natural rubber), is in a range of 10 to 50 phr, more preferably in a range of 15 to 40 phr.
• diene elastomers previously described could also be associated, in a minor amount, with synthetic elastomers other than diene, or even polymers other than elastomers, for example thermoplastic polymers.
• Any known filler for its ability to reinforce a rubber composition is usable, for example an organic filler such as carbon black, or an inorganic filler such as silica to which is associated in a known manner a coupling agent.
• Such a charge preferably consists of nanoparticles whose average size (in mass) is less than one micrometer, generally less than 500 nm, most often between 20 and 200 nm, in particular and more preferably between 20 and 150 nm.
• the content of total reinforcing filler is between 50 and 150 phr.
• a content greater than 50 phr is favorable for good mechanical strength; above 150 phr, there is a risk of excessive rigidity of the rubber composition.
• the total reinforcing filler content is more preferably within a range of 70 to 120 phr.
• Suitable carbon blacks are, for example, all carbon blacks which are conventionally used in tires (so-called tire-grade blacks) such as blacks of the series 100, 200, 300 (ASTM grades), for example blacks NI 15, N134, N234, N326, N330, N339, N347, N375.
• the carbon blacks could for example already be incorporated into the diene elastomer, in particular isoprenic elastomer, in the form of a masterbatch (see, for example, applications WO 97/36724 or WO 99/16600).
• organic fillers other than carbon blacks mention may be made of functionalized polyvinyl organic fillers as described in applications WO-A-2006/069792 and WO-A-2006/069793, WO-A-2008/003434. and WO-A-2008/003435.
• Reinforcing inorganic filler means any inorganic or mineral filler, irrespective of its color and origin (natural or synthetic), also called “white” filler, “clear” filler or even “non-black filler” as opposed to carbon black, capable of reinforcing on its own, without any other means than an intermediate coupling agent, a rubber composition intended for the manufacture of tires, in other words able to replace, in its function of reinforcement, a conventional carbon black tire grade; such a filler is generally characterized, in known manner, by the presence of hydroxyl groups (-OH) on its surface.
• -OH hydroxyl groups
• Suitable reinforcing inorganic fillers are mineral fillers of the siliceous type, in particular silica (SiO 2 ).
• the silica used may be any reinforcing silica known to those skilled in the art, in particular any precipitated silica or pyro-interfered silica having a BET surface and a CTAB specific surface area both less than 450 m 2 / g, preferably from 30 to 400 m 2 / g, especially between 60 and 300 m 2 / g.
• HDS highly dispersible precipitated silicas
• the majority filler used is a reinforcing inorganic filler, in particular silica, at a level within a range of 70 to 120 phr, reinforcing inorganic filler to which advantageously black of carbon at a minority rate at most equal to 15 phr, in particular in a range of 1 to 10 phr.
• an at least bifunctional coupling agent (or bonding agent) is used in a well-known manner to ensure a sufficient chemical and / or physical connection between the inorganic filler (surface of its particles) and the diene elastomer.
• organosilanes or at least bifunctional polyorganosiloxanes are used.
• polysulfide silanes called “symmetrical” or “asymmetrical” silanes according to their particular structure, are used, as described for example in the applications WO03 / 002648 (or US 2005/016651) and WO03 / 002649 (or US 2005/016650).
• polysulphide silanes having the following general formula (I) are not suitable for the following definition:
• x is an integer of 2 to 8 (preferably 2 to 5);
• the symbols A which are identical or different, represent a divalent hydrocarbon radical (preferably a C 1 -C 18 alkylene group or a C 6 -C 12 arylene group, more particularly a C 1 -C 10 , especially C 1 -C 4 , alkylene, in particular propylene);
• the radicals R 1 which may be substituted or unsubstituted, which are identical to or different from one another, represent a Ci-C18 alkyl, C 5 -C 8 cycloalkyl or C 6 -C 18 aryl group (preferably C 1 -C 8 alkyl groups); C 6 , cyclohexyl or phenyl, especially C 1 -C 4 alkyl groups, more particularly methyl and / or ethyl).
• the radicals R 2 substituted or unsubstituted, identical or different, represent an alkoxy group or Ci-Ci 8 cycloalkoxy, C 5 -C 8 (preferably a group chosen from C 1 -C 8 alkoxyls and C 5 -C 8 cycloalkoxyls, more preferably still selected from C 1 -C 4 alkoxyls, in particular methoxyl and ethoxyl).
• silane polysulfides are more particularly the bis (mono, trisulfide or tetrasulfide) of bis (alkoxyl (Ci-C 4) alkyl (Ci-C 4) alkyl silyl (Ci-C 4 )), such as polysulfides of bis (3-trimethoxysilylpropyl) or bis (3-triethoxysilylpropyl).
• TESPT bis (3-triethoxysilylpropyl) tetrasulfide
• TESPD bis (3-triethoxysilylpropyl) tetrasulfide
• TESPD bis-disulfide ( triethoxysilylpropyl)
• polysulfides in particular disulfides, trisulphides or tetrasulfides
• bis- (monoalkoxyl (Ci-C 4 ) -dialkyl (Ci-C 4 ) silylpropyl) more particularly bis-monoethoxydimethylsilylpropyl tetrasulfide.
• silanes carrying at least one thiol function (-SH) (called mercaptosilanes) and / or of at least one blocked thiol function, as described for example in patents or patent applications US 6,849,754, WO 99/09036, WO 2006/023815, WO 2007/098080.
• thiol function (-SH)
• mercaptosilanes) and / or of at least one blocked thiol function
• the rubber compositions When they are reinforced with an inorganic filler such as silica, the rubber compositions preferably comprise between 2 and 15 phr, more preferably between 3 and 12 phr of coupling agent.
• an inorganic filler such as silica
• the rubber compositions preferably comprise between 2 and 15 phr, more preferably between 3 and 12 phr of coupling agent.
• the essential feature of the invention is the use in combination, at particularly high levels, of a sodium or potassium carbonate or hydrogen carbonate as a blowing agent, which is associated, as activator with expansion, a carboxylic acid whose whose melting temperature is between 60 ° C and 220 ° C.
• blowing agent in English
• a blowing agent is a thermally decomposable compound, intended to release during a thermal activation, for example during the vulcanization of the tire, a significant amount of gas and thus lead to the formation of bubbles.
• the release of gas in the rubber composition therefore comes from this thermal decomposition of the blowing agent.
• the blowing agent used in accordance with the present invention is a sodium or potassium carbonate or hydrogencarbonate (sometimes also called bicarbonate).
• a sodium or potassium carbonate or hydrogencarbonate sometimes also called bicarbonate.
• it is selected from the group consisting of sodium carbonate, sodium hydrogencarbonate, potassium carbonate, potassium hydrogencarbonate and mixtures of these compounds (including, of course, their forms hydrated).
• Such an expansion agent has the advantage of only releasing carbon dioxide and water during its decomposition; it is therefore particularly favorable to the environment.
• Sodium hydrogencarbonate (NaHCO 3) is particularly used.
• the content of this blowing agent is between 5 and 25, preferably between 8 and 20 phr.
• Another essential feature of the invention is to add to the blowing agent described above a carboxylic acid whose melting temperature is between 60 ° C and 220 ° C.
• the level of this carboxylic acid is between 2 and 20 phr, preferably 2 and 15 phr.
• this carboxylic acid serves to activate chemically (ie, by chemical reaction) the blowing agent which, during its thermal decomposition, will thus release many more gas bubbles (C0 2 and H 2 0) than if it were used alone.
• Melting temperature is a well-known basic physical constant (available for example in "Handbook of Chemistry and Physics") of hot melt compounds, organic or inorganic; it can be controlled by any known method, for example by the Thiele method, the Kofler bench method or by DSC analysis.
• the pKa (Ka acid constant) of the carboxylic acid is greater than 1, more preferably between 2.5 and 12, in particular between 3 and 10.
• the carboxylic acid comprises, along its hydrocarbon chain, from 2 to 22 carbon atoms, preferably from 4 to 20 carbon atoms.
• the aliphatic monoacids preferably comprise, along their hydrocarbon chain, at least 16 carbon atoms; mention may be made, for example, of palmitic acid (Cl 6), stearic acid (Cl 8), nonadecanoic acid (Cl 9), behenic acid (C 20) and their various mixtures.
• the aliphatic diacids preferably comprise, along their hydrocarbon chain, from 2 to 10 carbon atoms; mention may be made, for example, of oxalic acid (C2), malonic acid (C3), succinic acid (C4), glutaric acid (C5), adipic acid (C6), pimellic acid (C7), suberic acid (C8), azelaic acid (C9), sebacic acid (C10) and their various mixtures.
• aromatic monoacid there may be mentioned for example benzoic acid.
• the acids having functional groups may be monoacids, diacids or triacids, of the aliphatic type as aromatic; examples that may be mentioned include tartaric acid, malic acid, maleic acid, glycolic acid, ⁇ -ketoglutaric acid, salicylic acid, phthalic acid or citric acid; .
• the carboxylic acid is chosen from the group consisting of palmitic acid, stearic acid, nonadecanoic acid, behenic acid and oxalic acid.
• malonic acid succinic acid, glutaric acid, adipic acid, pimellic acid, suberic acid, azelaic acid, sebacic acid, benzoic acid, tartaric acid, malic acid, maleic acid, glycolic acid, ⁇ -ketoglutaric acid, salicylic acid, phthalic acid, citric acid and mixtures of these acids.
• the carboxylic acid is selected from the group consisting of malic acid, ⁇ -ketoglutaric acid, citric acid, stearic acid and mixtures thereof. More preferably still, is used citric acid, stearic acid or a mixture of these two.
• the total amount of blowing agent and its associated activator is greater than 10 phr, preferably between 10 and 40 phr. This total amount is more preferably greater than 15 phr, in particular between 15 and 40 phr.
• the heat-expandable rubber composition may also comprise all or part of the usual additives usually used in tire tread rubber compositions, such as, for example, protective agents such as anti-ozone waxes, chemical anti-ozonants, oxidizing agents, plasticizing agents, a crosslinking system based on either sulfur, or sulfur and / or peroxide donors and / or bismaleimides, vulcanization accelerators, vulcanization activators.
• protective agents such as anti-ozone waxes, chemical anti-ozonants, oxidizing agents, plasticizing agents, a crosslinking system based on either sulfur, or sulfur and / or peroxide donors and / or bismaleimides, vulcanization accelerators, vulcanization activators.
• the thermo-expandable rubber composition also comprises a liquid plasticizer (at 20 ° C) whose function is to soften the matrix by diluting the diene elastomer and the reinforcing filler; its Tg (glass transition temperature) is by definition less than -20 ° C, preferably less than -40 ° C.
• this liquid plasticizer is used at a relatively reduced rate, such that the weight ratio reinforcing filler on liquid plasticizer is greater than 2.0, more preferably greater than 2.5, in particular greater than 3 , 0.
• any extender oil whether aromatic or non-aromatic, any liquid plasticizer known for its plasticizing properties vis-à-vis diene elastomers, is usable.
• these plasticizers or these oils are liquids (that is to say, as a reminder, substances having the capacity to eventually take on the shape of their container) , in contrast to, in particular, hydrocarbon plasticizing resins which are by nature solid at ambient temperature.
• liquid plasticizers selected from the group consisting of naphthenic oils (low or high viscosity, including hydrogenated or not), paraffinic oils, oils MES (Medium Extracted Solvates), oils DAE (Distillate Aromatic Extracts), Treated Distillate Aromatic Extracts (TDAE) oils, Residual Aromatic Extracts (RAE) oils, Treated Residual Aromatic Extracts (TREE) oils, Safety Residual Aromatic Extracts (SRAE) oils, mineral oils, vegetable oils, ethers plasticizers, ester plasticizers, phosphate plasticizers, sulphonate plasticizers and mixtures of these compounds.
• the liquid plasticizer is selected from the group consisting of MES oils, TDAE oils, naphthenic oils, vegetable oils and mixtures of these oils.
• phosphate plasticizers for example, mention may be made of those containing from 12 to 30 carbon atoms, for example trioctyl phosphate.
• ester plasticizers mention may be made in particular of compounds selected from the group consisting of trimellitates, pyromellitates, phthalates, 1,2-cyclohexane dicarboxylates, adipates, azelates, sebacates, glycerol and mixtures of these compounds.
• glycerol triesters preferably consisting predominantly (for more than 50%, more preferably more than 80% by weight) of an unsaturated fatty acid Ci 8 is that is to say selected from the group consisting of oleic acid, linoleic acid, linolenic acid and mixtures of these acids. More preferably, whether of synthetic or natural origin (for example vegetable oils of sunflower or rapeseed), the fatty acid used is more than 50% by weight, more preferably still more than 80% by weight. % by weight of oleic acid.
• Such high oleic acid triesters (trioleates) are well known and have been described, for example, in application WO 02/088238, as plasticizers in tire treads.
• the rubber composition of the invention may also comprise, as solid plasticizer (at 23 ° C.), a hydrocarbon resin having a Tg greater than + 20 ° C., preferably greater than + 30 ° C, as described for example in the applications WO 2005/087859, WO 2006/061064 or WO 2007/017060.
• Hydrocarbon resins are polymers that are well known to those skilled in the art, essentially based on carbon and hydrogen, and therefore inherently miscible in diene (s) elastomer compositions when they are further qualified as “plasticisers". ". They may be aliphatic, aromatic or aliphatic / aromatic type that is to say based on aliphatic and / or aromatic monomers. They may be natural or synthetic, whether or not based on petroleum (if so, also known as petroleum resins). They are preferably exclusively hydrocarbon-based, that is to say they contain only carbon and hydrogen atoms. Preferably, the plasticizing hydrocarbon resin has at least one, more preferably all, of the following characteristics: a Tg greater than 20 ° C (more preferably between 40 and 100 ° C);
• Mn a number-average molecular weight (Mn) of between 400 and 2000 g / mol (more preferentially between 500 and 1500 g / mol);
• the Tg of this resin is measured in a known manner by DSC (Differential Scanning Calorimetry), according to the ASTM D3418 standard.
• the macro structure (Mw, Mn and Ip) of the hydrocarbon resin is determined by steric exclusion chromatography (SEC): tetrahydroiuran solvent; temperature 35 ° C; concentration 1 g / 1; flow rate 1 ml / min; filtered solution on 0.45 ⁇ porosity filter before injection; Moore calibration with polystyrene standards; set of 3 "WATERS” columns in series (“STYRAGEL” HR4E, HR1 and HR0.5); differential refractometer detection ("WATERS 2410") and its associated operating software (“WATERS EMPOWER”).
• the plasticizing hydrocarbon resin is chosen from the group consisting of cyclopentadiene homopolymer or copolymer resins (abbreviated to CPD), dicyclopentadiene homopolymer or copolymer resins (abbreviated to DCPD), terpene homopolymer or copolymer resins, homopolymer or C5 cut copolymer resins, homopolymer or C9 cut copolymer resins, alpha-methyl-styrene homopolymer or copolymer resins and mixtures thereof. resins.
• CPD cyclopentadiene homopolymer or copolymer resins
• DCPD dicyclopentadiene homopolymer or copolymer resins
• terpene homopolymer or copolymer resins homopolymer or C5 cut copolymer resins
• homopolymer or C9 cut copolymer resins homopolymer or C9 cut copolymer resins
• copolymer resins are more preferably used those selected from the group consisting of (D) CPD / vinylaromatic copolymer resins, (D) CPD / terpene copolymer resins, copolymer resins (D) CPD / C5 cut, (D) CPD / C9 cut copolymer resins, terpene / vinylaromatic copolymer resins, terpene / phenol copolymer resins, C5 / vinylaromatic cut copolymer resins, C9 / vinylaromatic cut copolymer resins, and mixtures of these resins.
• pene here combines in a known manner the alpha-pinene, beta-pinene and limonene monomers; preferably, a limonene monomer is used which is present in a known manner in the form of three possible isomers: L-limonene (laevorotatory enantiomer), D-limonene (dextrorotatory enantiomer), or the dipentene, racemic of the dextrorotatory and levorotatory enantiomers. .
• Suitable vinylaromatic monomers are, for example, styrene, alpha-methylstyrene, ortho-, meta-, para-methylstyrene, vinyltoluene, para-tert-butylstyrene, methoxystyrenes, chlorostyrenes, hydroxy styrenes, vinylmesitylene, divinylbenzene, vinylnaphthalene, any vinylaromatic monomer from a C 9 cut (or more generally from a C 8 to C 10 cut).
• the vinyl-aromatic compound is styrene or a vinylaromatic monomer derived from a C 9 cut (or more generally from a C 8 to C 10 cut).
• the vinylaromatic compound is the minor monomer, expressed as a mole fraction, in the copolymer under consideration.
• the content of hydrocarbon resin is preferably between 3 and 60 phr, more preferably between 3 and 40 phr, especially between 5 and 30 phr.
• reinforcing resins eg acceptors and donors of methylene
• the heat-expandable rubber composition may also contain coupling enhancers when a coupling agent is used, inorganic filler recovery agents when an inorganic filler is used, or more generally, filler agents.
• implementability likely in known manner, through an improvement in the dispersion of the load in the rubber matrix and a lowering of the viscosity of the compositions, to improve their processability in the green state; these agents are for example hydroxysilanes or hydrolysable silanes such as alkyl-alkoxysilanes, polyols, polyethers, amines, hydroxylated or hydrolysable polyorganosiloxanes.
• the rubber compositions are manufactured in suitable mixers, for example using two successive preparation phases according to a general procedure known to those skilled in the art: a first phase of work or thermomechanical mixing (sometimes referred to as a "non-productive" phase ) at a high temperature, up to a maximum temperature of between 130 ° C and 200 ° C, preferably between 145 ° C and 185 ° C, during which is incorporated in particular the expansion activator (carboxylic acid), followed by a second phase of mechanical work (sometimes called “productive" phase) at low temperature, typically below 120 ° C, for example between 60 ° C and 100 ° C, finishing phase during which are incorporated the expansion agent and the crosslinking or vulcanization system.
• a first phase of work or thermomechanical mixing (sometimes referred to as a "non-productive" phase ) at a high temperature, up to a maximum temperature of between 130 ° C and 200 ° C, preferably between 145 ° C and 185 ° C, during which is incorporated in particular
• a process that can be used for the manufacture of such rubber compositions comprises, for example, and preferably the following steps: incorporating in a mixer, at least the filler and the carboxylic acid, by thermomechanically kneading the whole, in one or more times, until a maximum temperature of between 130 ° C. and 130 ° C. is reached in a mixer, at the elastomer or in the mixture of elastomers; 200 ° C;
• blowing agent Na or K carbonate or hydrogen carbonate
• a suitable mixer such as a conventional internal mixer.
• the blowing agent and the crosslinking system After thermomechanical work, falling and cooling of the mixture thus obtained, it is then preferably incorporated in this order, the blowing agent, then the vulcanization retarder (if such a compound is used), finally the rest of the vulcanization system. (sulfur and accelerator) at low temperature, usually in an external mixer such as a roll mill; the whole is then mixed (productive phase) for a few minutes, for example between 5 and 15 min.
• the actual crosslinking system is preferably based on sulfur and a primary vulcanization accelerator, in particular a sulfenamide type accelerator.
• a primary vulcanization accelerator in particular a sulfenamide type accelerator.
• various known secondary accelerators or vulcanization activators such as zinc oxide, stearic acid, guanidine derivatives (especially diphenylguanidine), etc.
• the sulfur content is preferably between 0.5 and 5 phr, that of the primary accelerator is preferably between 0.5 and 8 phr.
• accelerator any compound capable of acting as accelerator for vulcanization of diene elastomers in the presence of sulfur, in particular thiazole-type accelerators and their derivatives, accelerators of the thiuram type, zinc dithiocarbamates.
• accelerators are for example selected from the group consisting of 2-mercaptobenzothiazyl disulfide (abbreviated "MBTS”), tetrabenzylthiuram disulfide (“TBZTD”), N-cyclohexyl-2-benzothiazyl sulfenamide (“CBS”), N, N dicyclohexyl-2-benzothiazylsulfenamide (“DCBS”), N-tert-butyl-2-benzothiazylsulfenamide (“TBBS”), N-tert-butyl-2-benzothiazylsulfenamide (“TBSI”), zinc dibenzyldithiocarbamate (“ ZBEC ”) and mixtures of these compounds.
• MBTS 2-mercaptobenzothiazyl disulfide
• TBZTD tetrabenzylthiuram disulfide
• CBS N-cyclohexyl-2-benzothiazyl sulfenamide
• the carboxylic acid has the possible effect of reducing the induction time (that is to say the time required for the beginning of the vulcanization reaction) during the baking of the composition, it is advantageous to use a retarder of vulcanization to counteract this phenomenon, and thus to provide the rubber composition the time necessary for full expansion before vulcanization.
• the level of this vulcanization retarder is preferably between 0.5 and 10 phr, more preferably between 1 and 5 phr, in particular between 1 and 3 phr.
• Vulcanization retarders are well known to those skilled in the art. Mention may be made, for example, of N-cyclohexylthiophthalimide sold under the name "Vulkalent G” by the company Lanxess, N- (trichloromethylthio) benzenesulfonamide sold under the name "Vulkalent E / C” by Lanxess, or else marketed phthalic anhydride. under the name “Vulkalent B / C" by Lanxess.
• CTP N-cyclohexylthiophthalimide
• the final composition thus obtained is then calendered, for example in the form of a sheet or a plate, in particular for a characterization in the laboratory, or else calendered or extruded in the form of a heat-expandable tread.
• the density or density denoted Di of the heat-expandable rubber composition is preferably between 1, 100 and 1, 400 g / cm 3 , more preferably in a range from 1.50 to 1. 350 g / cm 3 .
• the vulcanization (or cooking) is conducted in a known manner at a temperature generally between 130 ° C and 200 ° C, for a sufficient time which may vary for example between 5 and 90 min depending in particular on the cooking temperature, the system of vulcanization adopted and the kinetics of vulcanization of the composition under consideration.
• the density denoted D 2 of the rubber composition once expanded is preferably between 0.500 and 1 000 g / cm 3 , more preferably in a range from 0.600 to 0.850 g / cm 3 .
• its Shore A hardness (measured according to ASTM D 2240-86) is in a range from 45 to 60.
• the heat-expandable rubber composition described above is advantageously usable in the treads, at least for their portion which is intended to come into direct contact with the road surface, of tires for any type of vehicle, in particular in the tires for passenger vehicles, as demonstrated in the tests that follow.
• compositions (denoted C-0 and C-1) were prepared whose formulation is given in Table 1 (rate of the various products expressed in phr).
• the composition C-0 is the control composition.
• the composition C-1 is that according to the invention, it additionally comprises the blowing agent (sodium hydrogen carbonate) and the carboxylic acid (citric acid) associated with it, as well as a vulcanization retarder (CTP).
• the reinforcing filler, the diene elastomer (SBR cutting and blending) were successively introduced into an internal mixer, the initial batch temperature of which was approximately 60 ° C. BR), the carboxylic acid for the composition Cl, as well as the various other ingredients with the exception of the vulcanization system and the blowing agent; the mixer was thus filled to about 70% (% by volume).
• Thermomechanical work (non-productive phase) was then carried out in a step of about 2 to 4 minutes, until a maximum "falling" temperature of about 150 ° C. was reached.
• the mixture thus obtained was recovered, cooled to about 50 ° C., then the blowing agent (Na-hydrogen carbonate), the vulcanization retarder (CTP), then the sulfenamide accelerator and the sulfur on an external mixer (homo-finisher) at 30 ° C, mixing the whole (productive phase) for a few minutes.
• compositions C-0 and Cl thus prepared were then vulcanized in press, and their properties measured before and after curing (see Table 2 attached).
• the rubber composition according to the invention has after baking, once in the state of foam rubber (ie, expanded), a significantly reduced density corresponding to a particularly high volume expansion rate of about 70%.
• expansion capacity gives it improved sound barrier properties, which can help reduce the noise emitted both inside and outside the vehicles when rolling their tires.
• a tire rolling test was conducted in which the sound level emitted by the tires was evaluated by measuring the sound pressure level during a rolling of the vehicle. at a speed of 60 km / h, thanks to several microphones arranged inside the vehicle ("road noise”).
• the vehicle used was a "Subaru” brand vehicle ("RI” model); the road surface used for this test corresponds to a semi-rough asphalt; when passing through the measuring area, the sound pressure recording is triggered.
• Table 5 express the differences in sound level recorded between the tires P-3 according to the invention and the control tires rated P-2, in a frequency range of 300 to 1900 Hz. These differences are expressed in acoustic energy. (dB (A)) which corresponds to the integration of sound pressure as a function of frequency over the frequency ranges considered, a negative value indicating a reduction of noise with respect to the reference (P-2 tires).

Landscapes

• 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)
• Materials Engineering (AREA)
• General Chemical & Material Sciences (AREA)
• Mechanical Engineering (AREA)
• Compositions Of Macromolecular Compounds (AREA)

Priority Applications (4)

Applications Claiming Priority (2)

Publications (1)

Family

ID=46331252

Family Applications (1)

Country Status (6)

Cited By (4)

Families Citing this family (20)

Citations (28)

Family Cites Families (17)

• 2011
  • 2011-06-01 FR FR1154799A patent/FR2975998B1/fr not_active Expired - Fee Related
• 2012
  • 2012-05-31 EP EP12729050.0A patent/EP2714788B1/fr not_active Not-in-force
  • 2012-05-31 WO PCT/EP2012/060216 patent/WO2012164001A1/fr not_active Ceased
  • 2012-05-31 JP JP2014513186A patent/JP5968432B2/ja not_active Expired - Fee Related
  • 2012-05-31 CN CN201280026095.3A patent/CN103597020B/zh not_active Expired - Fee Related
  • 2012-05-31 US US14/122,394 patent/US20140228480A1/en not_active Abandoned

Patent Citations (34)

Also Published As

Similar Documents

Legal Events