Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/36—Sulfur-, selenium-, or tellurium-containing compounds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K13/00—Use of mixtures of ingredients not covered by one single of the preceding main groups, each of these compounds being essential
  • C08K13/02—Organic and inorganic ingredients
• • 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
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
  • B29B7/00—Mixing; Kneading
  • B29B7/002—Methods
  • B29B7/005—Methods for mixing in batches
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
  • B29B7/00—Mixing; Kneading
  • B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
  • B29B7/22—Component parts, details or accessories; Auxiliary operations
  • B29B7/28—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control
  • B29B7/286—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control measuring properties of the mixture, e.g. temperature, density
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
  • B29B7/00—Mixing; Kneading
  • B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
  • B29B7/7476—Systems, i.e. flow charts or diagrams; Plants
  • B29B7/7495—Systems, i.e. flow charts or diagrams; Plants for mixing rubber
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
  • B29B7/00—Mixing; Kneading
  • B29B7/80—Component parts, details or accessories; Auxiliary operations
  • B29B7/88—Adding charges, i.e. additives
  • B29B7/90—Fillers or reinforcements, e.g. fibres
• • 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
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/20—Compounding polymers with additives, e.g. colouring
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/34—Silicon-containing compounds
  • C08K3/36—Silica
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/36—Sulfur-, selenium-, or tellurium-containing compounds
  • C08K5/37—Thiols
  • C08K5/372—Sulfides, e.g. R-(S)x-R'
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/36—Sulfur-, selenium-, or tellurium-containing compounds
  • C08K5/37—Thiols
  • C08K5/378—Thiols containing heterocyclic rings
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/54—Silicon-containing compounds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/54—Silicon-containing compounds
  • C08K5/548—Silicon-containing compounds containing sulfur
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L21/00—Compositions of unspecified rubbers
• • 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
• • 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
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
  • B29B7/00—Mixing; Kneading
  • B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
  • B29B7/06—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
  • B29B7/10—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
  • B29B7/18—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft
  • B29B7/183—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft having a casing closely surrounding the rotors, e.g. of Banbury type

Definitions

• the present invention relates to silica-containing rubber mixtures which comprise sulphur-containing additives, and to use of these and to rubber vulcanizates produced therefrom.
• Additional materials such as fatty acid esters, fatty acid salts or mineral oils, have been proposed for improving the processability of silica-containing rubber mixtures.
• the additional materials mentioned have the disadvantage of increasing flowability but at the same time reducing the moduli at relatively high elongation (e.g. from 100% to 300%), or else the hardness, of the vulcanizates, and thus impairing the reinforcing effect of the filler. Inadequate hardness or stiffness of the vulcanizate results in unsatisfactory running performance of the tyre, particularly in curves.
• EP 1 134 253 describes polyether additives for silica-containing rubber vulcanizates which do not exhibit the abovementioned disadvantage of reducing the modulus.
• the person skilled in the art requires a usage amount of 8% by weight of the product, based on the rubber, in order to increase the Shore A hardness value by 3 units.
• the low modulus at 300% elongation is disadvantageous.
• EP 0 489 313 describes additives with good mechanical properties and with improved hysteresis performance.
• the examples reveal only slight, or no, increase of Shore A hardness in comparison with the prior art, bis[3-(triethoxysilyl)propyl]tetrasulphide according to German Offenlegungsschrift 2 255 577, and therefore no improvement of interaction between polymer and filler.
• EP 1 000 968 moreover uses bis[-3-(triethoxysilyl)propyl]tetrasulphides in combination with a specific reversion stabilizer in SBR, where the 300 modulus values are very low and therefore inadequate.
• EP 0 791 622 B1 describes a rubber composition with at least one diene-based elastomer, filler composed of silica and of carbon black, and also with silica-coupling agent selected from
• the synergetic effect is believed to result from improved interaction between polymer and filler.
• the invention therefore provides rubber mixtures produced from at least one rubber, from a sulphur-containing alkoxysilane, from a crosslinking agent, from a filler, and optionally from further rubber auxiliaries, and also from at least one silicon-free sulphur-containing additive of the formula (I)
• silicon-free sulphur-containing additive polysulphide additive, silicon-free polysulphide additive and silicon-free polysulphide additive of the formula (I), and all formulae that derive therefrom, listed in the claims, are used as synonyms.
• At least one compound of the formula (II) is preferable to use at least one compound of the formula (II) as polysulphide additive.
• the silica-containing rubber mixture according to the invention comprises at least one SBR rubber and at least one BR rubber.
• It preferably comprises at least one SBR rubber and at least one BR rubber in an SBR:BR ratio by weight of from 60:40 to 90:10.
• It can preferably also comprise at least one NR rubber.
• it comprises at least one SBR rubber and at least one BR rubber and at least one NR rubber in a ratio of at least 60 and at most 85 percent by weight of SBR, based on rubber, and at least 10 and at most 35 percent by weight of BR, based on rubber, and at least 5 and at most 20 percent by weight of NR, based on rubber.
• Synthetic rubbers are also suitable, alongside natural rubber, for producing the rubber mixtures according to the invention and the rubber vulcanizates according to the invention.
• Preferred synthetic rubbers are described by way of example in W. Hofmann, Kautschuktechnologie [Rubber technology], Genter-Verlag, Stuttgart 1980.
• the silica-containing rubber mixtures also comprise from 0.3 to 7 parts by weight of one or more silicon-free polysulphide additives of the formula (I) or of any of the formulae derived therefrom, as listed in the claims, based on 100 parts by weight of rubber used.
• the amount of sulphur-containing alkoxysilane is greater than or equal to the amount of the silicon-free polysulphide additive.
• the sulphur-containing alkoxysilane is used in a ratio by weight of from 1.5:1 to 20:1, particularly from 5:1 to 15:1, in relation to the silicon-free polysulphide additive.
• the rubber mixture according to the invention comprises from 0.5 to 5 parts by weight, based on 100 parts by weight of rubber used, of a silicon-free polysulphide additive.
• the present invention further provides rubber vulcanizates which can be produced from the rubber mixtures according to the invention.
• the present invention further provides a process for producing filled rubber vulcanizates, characterized in that
• the silicon-free polysulphide additives according to the invention are preferably added in the first portion of the mixing process when temperatures of the composition are from 100 to 200° C. and the shear rates are those mentioned, but it can also be added later at lower temperatures (from 40 to 100° C.), for example together with sulphur and accelerator.
• the form in which the silicon-free polysulphide additives are added to the mixing process can either be pure form or else a form absorbed on inert, organic or inorganic carriers.
• Preferred carrier materials are silica, natural or synthetic silicates, aluminium oxide and/or carbon black.
• silica-containing fillers that can be used for the rubber mixture and rubber vulcanizates according to the invention comprise the following fillers:
• carbon blacks are carbon blacks.
• the carbon blacks to be used here are produced by way of example by the lamp-black process, furnace-black process or gas-black process and have BET surface areas of from 20 to 200 m 2 /g, examples being SAF, ISAF, IISAF, HAF, FEF, or GPF carbon black.
• Amounts preferably used of the sulphur-containing silicon-free polysulphide additives in the rubber mixtures according to the invention are from 0.3 to 7%, based on rubber.
• One particularly preferred variant consists in the combination of silica, carbon black and silicon-free polysulphide additives.
• the ratio of silica to carbon black in this combination can be varied within any desired limits. For the purposes of tyre technology, preference is given to silica:carbon black ratios of from 20:1 to 1.5:1.
• Sulphur-containing silanes that can be used for the rubber vulcanizates according to the invention are preferably bis(triethoxysilylpropyl)tetrasulphane and the corresponding disulphane and 3-triethoxysilyl-1-propanethiol or silanes such as Si 363 from Evonik, Germany or silane NXT or NXT Z from Momentive (previously GE, USA), where the alkoxy moiety is methoxy or ethoxy where amounts used are from 2 to 20 parts by weight, preferably from 3 to 11 parts by weight, calculated in each case as 100% strength active ingredient and based on 100 parts by weight of rubber.
• Liquid sulphur-containing silanes can have been absorbed on a carrier to improve ease of metering and/or ease of dispersion (dry liquid).
• Active ingredient content is from 30 to 70 parts by weight, preferably from 40 to 60 parts by weight, for every 100 parts by weight of dry liquid.
• the rubber vulcanizates according to the invention can comprise other rubber auxiliaries, for example reaction accelerators, antioxidants, heat stabilizers, light stabilizers, antiozonants, processing aids, plasticizers, tackifiers, blowing agents, dyes, pigments, waxes, extenders, organic acids, retardants, metal oxides, and also activators, such as triethanolamine, polyethylene glycol, hexanetriol, where these are known to the rubber industry.
• reaction accelerators for example reaction accelerators, antioxidants, heat stabilizers, light stabilizers, antiozonants, processing aids, plasticizers, tackifiers, blowing agents, dyes, pigments, waxes, extenders, organic acids, retardants, metal oxides, and also activators, such as triethanolamine, polyethylene glycol, hexanetriol, where these are known to the rubber industry.
• the amount used of the rubber auxiliaries is conventional and depends inter alia on the intended purpose of the vulcanizates. Conventional amounts, based on rubber, are from 0.1 to 30% by weight.
• crosslinking agents peroxides, sulphur, magnesium oxide, zinc oxide, and the known vulcanization accelerators can also be added to these, for example mercaptobenzothiazoles, -sulphenamides, thiurams, thiocarbamates, guanidines, xanthogenates and thiophosphates. Preference is given to sulphur.
• the amounts used of the crosslinking agents and vulcanization accelerators are about 0.1 to 10% by weight, preferably 0.1 to 5% by weight, based on rubber.
• Suitable phenolic antioxidants are alkylated phenols, styrenated phenol, sterically hindered phenols such as 2,6-di-tert-butylphenol, 2,6-di-tert-butyl-p-cresol (BHT), 2,6-di-tert-butyl-4-ethylphenol, sterically hindered phenols containing ester groups, sterically hindered phenols containing thioether, 2,2′-methylenebis(4-methyl-6-tert-butylphenol) (BPH), and also sterically hindered thiobisphenols.
• BHT 2,6-di-tert-butylphenol
• BHT 2,6-di-tert-butyl-p-cresol
• BPH 2,2′-methylenebis(4-methyl-6-tert-butylphenol)
• aminic antioxidants e.g. mixtures of diaryl-p-phenylenediamines (DTPD), octylated diphenylamine (ODPA), phenyl- ⁇ -naphthylamine (PAN), phenyl- ⁇ -naphthylamine (PBN), preferably those based on phenylenediamine.
• DTPD diaryl-p-phenylenediamines
• ODPA octylated diphenylamine
• PAN phenyl- ⁇ -naphthylamine
• PBN phenyl- ⁇ -naphthylamine
• phenylenediamines are N-isopropyl-N′-phenyl-p-phenylenediamine, N-1,3-dimethylbutyl-N′-phenyl-p-phenylenediamine (6PPD), N-1,4-dimethylpentyl-N′-phenyl-p-phenylenediamine (7PPD), N,N′-bis(1,4-dimethylpentyl)-p-phenylenediamine (77PD).
• phosphites such as tris(nonylphenyl)phosphite, polymerized 2,2,4-trimethyl-1,2-dihydroquinoline (TMQ), 2-mercaptobenzimidazole (MBI), methyl-2-mercaptobenzimidazole (MMBI), zinc methylmercaptobenzimidazole (ZMMBI).
• TMQ 2,2,4-trimethyl-1,2-dihydroquinoline
• MBI 2-mercaptobenzimidazole
• MMBI methyl-2-mercaptobenzimidazole
• ZMMBI zinc methylmercaptobenzimidazole
• the phosphites are generally used in combination with phenolic antioxidants.
• TMQ, MBI and MMBI are mainly used for NBR types which are vulcanized peroxidically.
• Ozone resistance can be improved by using antioxidants known to a person skilled in the art, such as N-1,3-dimethylbutyl-M-phenyl-p-phenylenediamine (6PPD), N-1,4-dimethylpentyl-N′-phenyl-p-phenylenediamine (7PPD), N,N′-bis(1,4-dimethylpentyl)-p-phenylenediamine (77PD), enol ethers or cyclic acetals.
• antioxidants known to a person skilled in the art, such as N-1,3-dimethylbutyl-M-phenyl-p-phenylenediamine (6PPD), N-1,4-dimethylpentyl-N′-phenyl-p-phenylenediamine (7PPD), N,N′-bis(1,4-dimethylpentyl)-p-phenylenediamine (77PD), enol ethers or cyclic acetal
• Processing aids are intended to act between the rubber particles and to counteract frictional forces during the mixing, plastification and shaping process.
• Processing aids which can be present in the rubber mixture according to the invention are any of the lubricants conventionally used for the processing of plastics, for example hydrocarbons, such as oils, paraffins and PE waxes, fatty alcohols having from 6 to 20 carbon atoms, ketones, carboxylic acids, such as fatty acids and montanic acids, oxidized PE wax, metal salts of carboxylic acids, carboxamides and carboxylic esters, for example with the following alcohols: ethanol, fatty alcohols, glycerol, ethanediol, pentaerythritol, and long-chain carboxylic acids as acid component.
• the rubber mixture can be crosslinked not only with sulphur accelerator systems but also with peroxides.
• crosslinking agents examples include peroxidic crosslinking agents such as bis(2,4-dichlorobenzyl)peroxide, dibenzoyl peroxide, bis(4-chlorobenzoyl)peroxide, 1,1-bis(tert-butylperoxy)-3,3,5-trimethylcyclohexane, tert-butyl perbenzoate, 2,2-bis(tert-butylperoxy)butene, 4,4-di-tert-butyl peroxynonylvalerate, dicumyl peroxide, 2,5-di methyl-2,5-di(tert-butylperoxy)hexane, tert-butylcumyl peroxide, 1,3-bis(tert-butylperoxyisopropyl)benzene, di-tert-butyl peroxide and 2,5-di methyl-2,5-di(tert-butylperoxy)hex-3-yn
• a suitable example here being triallyl isocyanurate, triallyl cyanurate, trimethylolpropane tri(meth)acrylate, triallyl trimellitate, ethylene glycol dimethacrylate, butanediol dimethacrylate, trimethylolpropane trimethacrylate, Zn diacrylate, Zn dimethacrylate, 1,2-polybutadiene or N,N′-m-phenylenedimaleimide.
• crosslinking agent that can be used is sulphur in elemental soluble or insoluble form or sulphur donors.
• sulphur donors examples include dimorpholyl disulphide (DTDM), 2-morpholino-dithiobenzothiazole (MBSS), caprolactam disulphide, dipentamethylenethiuram tetrasulphide (DPTT), and tetramethylthiuram disulphide (TMTD).
• DTDM dimorpholyl disulphide
• MBSS 2-morpholino-dithiobenzothiazole
• caprolactam disulphide dipentamethylenethiuram tetrasulphide
• DPTT dipentamethylenethiuram tetrasulphide
• TMTD tetramethylthiuram disulphide
• Suitable additions which can be used to increase crosslinking yield are dithiocarbamates, thiurams, thiazoles, sulphenamides, xanthogenates, bi- or polycyclic amines, guanidine derivatives, dithiophosphates, caprolactams and thiourea derivatives.
• the rubber mixture composition according to the invention can also comprise flame retardants.
• flame retardant used is antimony trioxide, phosphoric esters, chloroparaffin, aluminium hydroxide, boron compounds, zinc compounds, molybdenum trioxide, ferrocene, calcium carbonate or magnesium carbonate.
• the rubber vulcanizate can also comprise further synthetic polymers, acting by way of example as polymeric processing aids or impact modifiers.
• the said synthetic polymers are selected from the group consisting of the homo- and copolymers based on ethylene, propylene, butadiene, styrene, vinyl acetate, vinyl chloride, glycidyl acrylate, glycidyl methacrylate, acrylates and methacrylates having alcohol components of branched or unbranched C1-C10-alcohols.
• polyacrylates having identical or different alcohol moieties from the group of the C4-C8-alcohols particularly of butanol, hexanol, octanol and 2-ethylhexanol, polymethyl methacrylate, methyl methacrylate-butyl acrylate copolymers, methyl methacrylate-butyl methacrylate copolymers, ethylene-vinyl acetate copolymers, chlorinated polyethylene, ethylene-propylene copolymers, ethylene-propylene-diene copolymers.
• the rubber vulcanizate according to the invention can be used for producing foams.
• chemical or physical blowing agents are added.
• Chemical blowing agents that can be used are any of the substances known for this purpose, for example azodicarbonamide, p-toluolsulphonyl hydrazide, 4,4′-oxybis(benzenesulphonyl hydrazide), p-toluenesulphonylsemicarbazide, 5-phenyltetrazole, N,N′-dinitrosopentamethylenetetramine, zinc carbonate or sodium hydrogencarbonate, and also mixtures comprising these substances.
• An example of a suitable physical blowing agent is carbon dioxide or halogenated hydrocarbons.
• the vulcanization process can take place at temperatures of from 100 to 200° C., preferably from 130 to 180° C., optionally under a pressure of from 10 to 200 bar.
• the blending of the rubber with the filler and with the sulphur-containing additives of the formula (I) can be carried out in/on conventional mixing assemblies, for example rolls, internal mixers and mixing extruders.
• the rubber vulcanizates according to the invention are suitable for producing mouldings with improved properties, e.g. for producing cable sheathing, hoses, drive belts, conveyor belts, roll coverings, tyres, shoe soles, sealing rings and damping elements.
• the rubber mixture initially prepared with the additives has low flow viscosity (Mooney viscosity ML 1+4/100° C.), so that it is easy to process.
• the intention is that the vulcanization process which follows (for example at 170° C., t95) for the rubber mixture is to proceed as rapidly as possible with exposure to heat, in order to restrict the cost of time and of energy.
• the scorch time (for example t5) is intended to be relatively long, depending on the shaping process.
• the loss factor tan delta of a vulcanizate produced from the silica-containing rubber mixture according to the invention by heating at 170° C./t95 is ⁇ 0.2 at 60° C. and that the Shore A hardness thereof is simultaneously >67 at 23° C.
• the loss factor tan delta is ⁇ 0.17 at 60° C. and that the shore A hardness is simultaneously >70 at 23° C.
• the 300 modulus value of the vulcanizate is >12 MPa, preferably >15 MPa.
• the loss factor tan delta of a vulcanizate produced from the silica-containing rubber mixture by heating at 170° C./t95 is less than 0.17 at 60° C. and that its scorch time is simultaneously greater than 1000 seconds.
• the loss factor tan delta of a vulcanizate produced from the silica-containing rubber mixture by heating at 170° C./t95 is less than 0.17 at 60° C. and that its full vulcanization time is simultaneously less than 2000 seconds.
• the scorch time of a vulcanizate produced from the silica-containing rubber mixture by heating at 170° C./t95 is greater than 1000 seconds and that its full vulcanization time is simultaneously less than 2000 seconds.
• the ML 1+4 viscosity of the silica-containing rubber mixture at 100° C. is preferably less than 150, preferably less than 100, particularly preferably less than 95.
• a further invention is the use of the silica-containing rubber mixture according to the invention for producing vulcanizates and rubber mouldings of any type, in particular for producing tyres and tyre components.
• a first indication of wet grip and rolling resistance is given by the loss factor tan delta. This should be as high as possible at 0° C. (good wet grip) and as low as possible at from 60 to 70° C. (low rolling resistance).
• the hardness of a rubber vulcanizate gives a first indication of its stiffness.
• Toluene and 3-mercaptopropionic acid are used as initial charge in the nitrogen-flushed apparatus. Once the 3-mercaptopropionic acid has been completely dissolved, the disulphur dichloride is added dropwise within about 1 h with nitrogen blanketing at a temperature of from 0 to 5° C. The feed rate is to be adjusted so as to avoid exceeding a temperature of 5′C. Once the reaction has ended, stirring is continued overnight at room temperature under nitrogen blanketing.
• reaction suspension is then subjected to suction filtration by means of a D4 frit, and the product isolated by filtration is transferred to a 2 L glass beaker, in which 800 ml of deionized water are mixed with the product and the suspension is stirred for 5 min.
• the product is again subjected to suction filtration, and the product in the suction funnel is washed twice, each time with 200 ml of deionized water.
• the product is now again transferred to a glass beaker (1 L), where it is slurried for 5 min with 500 ml of toluene.
• the product Once the product has been isolated by suction filtration, it is dried in a vacuum drying oven at room temperature (about 25° C.).
• Dried cyclohexane and methyl 3-mercaptopropionate are used as initial charge in the nitrogen-flushed apparatus. Once the methyl 3-mercaptopropionate has been completely dissolved, the disulphur dichloride is added dropwise within about 1 h with nitrogen blanketing at a temperature of from 5 to 10° C. The feed rate is to be adjusted so as to avoid exceeding a temperature of 10° C.
• reaction solution is then concentrated by rotating on a Rotavapor at 50° C., and is then dried to constant weight at 60° C. in a vacuum drying oven.
• Example 3 Mooney viscosity [MU] 53523 95 94 82 97 (ML 1 + 4) Mooney scorch time sec acc. to ASTM 1253 1418 1244 1072 at 130° C. (t5) D 5289-95 Full vulcanization sec 53529 1417 1692 1617 1234 at 170° C./t95 Shore A hardness [Shore A] 53505 66 73 72 68 at 23° C.
• Viscosity can be determined directly from the resisting force exerted by the rubbers (and rubber mixtures) while they are processed.
• Mooney shearing-disc viscometer a grooved disc is surrounded above and below by sample substance and is rotated at about two revolutions per minute in a heatable chamber. The force required for this purpose is measured in the form of torque and corresponds to the respective viscosity.
• the specimen is generally preheated to 100° C. for 1 minute; the measurement takes a further 4 minutes, while the temperature is held constant.
• the viscosity is given together with the respective test conditions, an example being ML (1+4) 100° C. (Mooney viscosity, large rotor, preheat time and test time in minutes, test temperature).
• the viscosities of the rubber mixtures specified in table 1 are measured by means of a Mooney shearing-disk viscometer.
• the same test can also be used as described above to measure the “scorch” performance of a mixture.
• the temperature selected in this patent is 130° C.
• the rotor runs until, after the torque value has passed through a minimum, it has risen to 5 Mooney units relative to the minimum value (t5). The greater the value (the unit here being seconds), the slower the scorch (high scorch values here).
• the time at which 95% of the rubber has crosslinked is measured as the full vulcanization time.
• the temperature selected was 170° C.
• milled sheets of thickness 6 mm made of the rubber mixture were produced according to formulations from table 1. Test specimens of diameter 35 mm were cut from the milled sheets, and the Shore A hardness values were determined for these by means of a digital Shore hardness tester (Zwick GmbH & Co. KG, Ulm).
• the tensile test serves directly to determine the loading limits of an elastomer.
• the longitudinal elongation at break is divided by the initial length to give the elongation at break.
• the force required to reach certain stages of elongation mostly 50, 100, 200 and 300%, is also determined and expressed as modulus (tensile strength at the given elongation of 300%, or 300 modulus).
• Table 2 lists the test results.
• Dynamic test methods are used to characterize the deformation performance of elastomers under loadings which change periodically. An external stress changes the conformation of the polymer chain.
• This measurement determines the loss factor tan delta indirectly by way of the ratio between loss modulus G′′ and storage modulus G′.

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• Mechanical Engineering (AREA)
• Compositions Of Macromolecular Compounds (AREA)
• Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

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• 2011
  • 2011-04-29 EP EP11164319A patent/EP2517898A1/de not_active Withdrawn
• 2012
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