CA2226917C - Rubber mixtures which contain sbr rubber gels - Google Patents
Rubber mixtures which contain sbr rubber gels Download PDFInfo
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- CA2226917C CA2226917C CA002226917A CA2226917A CA2226917C CA 2226917 C CA2226917 C CA 2226917C CA 002226917 A CA002226917 A CA 002226917A CA 2226917 A CA2226917 A CA 2226917A CA 2226917 C CA2226917 C CA 2226917C
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- rubber
- styrene
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- butadiene
- latex
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L7/00—Compositions of natural rubber
- C08L7/02—Latex
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L9/00—Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
- C08L9/06—Copolymers with styrene
- C08L9/08—Latex
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
- B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
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- 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
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L19/00—Compositions of rubbers not provided for in groups C08L7/00 - C08L17/00
- C08L19/003—Precrosslinked rubber; Scrap rubber; Used vulcanised rubber
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- 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
- C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L53/02—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/80—Technologies aiming to reduce greenhouse gasses emissions common to all road transportation technologies
- Y02T10/86—Optimisation of rolling resistance, e.g. weight reduction
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S152/00—Resilient tires and wheels
- Y10S152/905—Tread composition
Abstract
Rubber mixtures prepared from at least one styrene/butadiene rubber gel and at least one rubber which contains double bonds and optionally further fillers and rubber auxiliary substances are in particular suitable for the preparation of vulcanisates having unusually high damping at temperatures of from -20 to +20°C as well as unusually low damping at temperatures of from 40 to 80°C. The rubber mixtures may therefore be used, for example, to manufacture vehicle tyres which grip in the wet and have low rolling resistance.
Description
Le A 32 156-Foreign Countries Bg/klu/W6 Rubber miztures which contain SBR rubber gels The invention relates to mixtures of rubbers which contain C=C double bonds and styrene/butadiene rubber gels (SBR gels) and to vulcanisates prepared therefrom. The vulcanisates demonstrate unusually high damping at temperatures of from -20 to +20°C and unusually low damping at temperatures of from 40 to 80°C, and are therefore particularly suitable for manufacturing vehicle tyre treads which give good grip in the wet and low rolling resistance.
The literature describes a large number of measures designed to reduce the rolling resistance of tyres, including, inter alia, the use of polychloroprene gels (EP-A 405 216) and polybutadiene gels (DE-A 42 20 563) in tyre treads manufactured from rub-bers which contain C=C double bonds. Disadvantages of using polychloroprene gel arise from the high cost of the rubber, the high density of polychloroprene and the ecological disadvantages to which the chlorine-containing components can be ex-pected to give rise in scrap tyre recycling. While polybutadiene gels according to DE-A 42 20 563 do not have these disadvantages, the dynamic damping is in this case reduced at both low temperatures (-20 to +20°C) and also at higher temperatures (40-80°C), which in practice means that advantages in terms of rolling resistance are ac-companied by disadvantages in terms of tyre grip in the wet. Sulphur-cross-linked rubber gels according to GB-PS 1 078 400 have no reinforcing effect and are there-fore unsuitable for the present application.
It has now surprisingly been found that rubber vulcanisates which contain C=C
double bonds and are filled with special SBR gels have high dynamic damping at low tem-peratures and low dynamic damping at higher temperatures, such that advantages result in terms of both rolling resistance and grip in the wet. Particularly good proper-ties result from using SBR gels in rubber mixtures which contain polybutadiene rub-ber.
The present invention therefore provides mixtures prepared from at least one sty-rene/butadiene rubber gel (A) and at least one rubber which contains double bonds (B), wherein the styrene/butadiene rubber gel content is from 1 to 100 parts by Le A 32 156-Foreign Countries weight, preferably 5 to 75 parts by weight, related to 100 parts by weight of rubber which contains C=C double bonds, and optionally further fillers and rubber auxiliary substances.
Styrene/butadiene rubber gels (A) are understood to denote microgels which are pre-pared by cross-linking SBR - styrene/butadiene copolymers which contain from 1 to 80 wt.%, pre-ferably 5 to 50 wt.%, of styrene, and/or XSBR - styrene/butadiene copolymers and graft polymers with further polar unsaturated monomers such as acrylic acid, methacrylic acid, acryl-amide, methacrylamide, N-methoxymethyl methacrylic acid amide, N-acetoxymethyl methacrylic acid amide, acrylonitrile, dimethyl acryl-amide, hydroxyethyl acrylate, hydroxyethyl methacrylate, which con-taro from 1 to 75 wt.% of styrene and from 1 to 20 wt.% of polar monomers incorporated by polymerisation.
The styrene/butadiene rubber gels have particle diameters of from 5 to 1000, prefer-ably 20 to 400 nm (DVN value to DIN 53 206) and swelling indices (Q;) in toluene of from 1 to 1 S, preferably 1 to 10. The swelling index is calculated from the weight of the gel when it contains solvent (following centrifuging at 20,000 rpm) and its weight when dry:
Q; wet weight of gel/dry weight of gel.
As an example of determining the swelling index, 250 mg of SBR gel is swelled in 25 ml toluene for 24 hours, with shaking. The gel is centrifuged oil and weighed, and is then dried at 70°C until the weight is constant, and is reweighed.
The styrene/butadiene rubber starting products are preferably prepared by emulsion polymerisation. In this connection see, for example, I. Franta, Elastomers and Rubber Compounding Materials, Elsevier, Amsterdam 1989, pp. 88 to 92.
Le A 32 156-Foreign Countries The cross-linking of the rubber starting products to form styrene/butadiene rubber gels takes place in the latex state. This may be during polymerisation, as a result of continuing the polymerisation to high conversions or in the monomer feeding process as a result of polymerisation at high internal conversions or as a result of post-cross-linking after polymerisation, or both processes may be combined. The rubber starting products may also be prepared by polymerisation in the absence of regulators.
The styrene/butadiene rubber may also be cross-linked by copolymerisation with multifunctional compounds having a cross-linking action. Preferred multifunctional comonomers are compounds having at least two, preferably 2 to 4, copolymerisable C=C double bonds, such as diisopropenylbenzene, divinylbenzene, divinylether, divinylsulphone, diallyl phthalate, triallyl cyanurate, triallyl isocyanurate, 1,2-poly-butadiene, N,N'-m-phenylene malefic imide and/or triallyl trimellitate. The following are furthermore considered: acrylates and methacrylates of polyvalent, preferably di-valent to tetravalent, C2-C,o alcohols, such as ethylene glycol, propanediol-1,2, butanediol, hexanediol, polyethylene glycol, having 2 to 20, preferably 2 to 8 oxy ethylene units, neopentyl glycol, bisphenol A, glycerol, trimethylol propane, penta erythritol, sorbitol and unsaturated polyesters prepared from aliphatic diols and poly ols and malefic acid, fumaric acid and/or itaconic acid.
The styrene/butadiene rubbers may also be cross-linked in the latex form to form SBR
rubber gels, as a result of post-cross-linking them with chemicals having a cross-link-ing action. Suitable chemicals having a cross-linking action are, for example, organic peroxides, for example, dicumyl peroxide, t-butylcumyl peroxide, bis-(t-butyl-peroxy-isopropyl) benzene, di-t-butyl peroxide, dibenzoyl peroxide, bis-(2,4-dichlorobenzoyl) peroxide, t-butyl perbenzoate, and organic azo compounds such as azo-bis-iso-butyronitrile and azo-bis-cyclohexanenitrile, and dimercapto and polymercapto com-pounds such as dimercaptoethane, 1,6-dimercaptohexane, 1,3,5-trimercaptotriazine, and mercapto-terminating polysulphide rubbers such as mercapto-terminating reaction products of bis-chloroethyl formal with sodium polysulphide. The optimal tempera-ture for the post-cross-linking operation is naturally dependent on the reactivity of the cross-linking agent and may be from room temperature up to approx.
170°C, op-Le A 32 156-Foreign Countries tionally at elevated pressure. See in this context Houben-Weyl, Methoden der or-ganischen Chemie [Methods in Organic Chemistry], 4th edition, Vol. 14/2, p.
848.
Peroxides are particularly preferred cross-linking agents.
It is also optionally possible to enlarge the particles by agglomeration before, during or after the post-cross-linking in latex form.
Styrene/butadiene rubbers which have been prepared in organic solvents may also serve as starting products for the preparation of the styrene/butadiene rubber gels. In this case it is advisable to emulsify the rubber solution in water, optionally with the aid of an emulsifying agent, and to follow this, either before or after removing the organic solvent, with cross-linking of the emulsion thus obtained using suitable cross-linking agents. The cross-linking agents previously named are suitable cross-linking agents.
Preferred rubbers (B) contain double bonds corresponding to iodine values of at least 2, preferably from 5 to 470. Iodine values are generally determined by addition of iodine chloride in ethanoic acid in accordance with Wijs, DIN 53 241, Part 1.
The iodine value defines the number of grammes of iodine chemically bound in 100 g of a substance.
The rubbers (B) generally have Mooney viscosities ML 1+4/100°C (DIN 53 523) of from 10 to 150, preferably 20 to 120.
In addition to natural rubber, synthetic rubbers are also preferred rubbers (B). Pre-ferred synthetic rubbers are described in, for example, I. Franta, Elastomers and Rub-ber Compounding Materials, Elsevier, New York 1989 or in Ullmanns' Encyclopedia of Industrial Chemistry, Vol. A23, VCH Verlagsgesellschaft, Weinheim 1993.
They include, inter alia, the following:
BR - polybutadiene ABR - butadiene/acrylic acid-C1_4 alkylester copolymers IR - polyisoprene Le A 32 156-Foreign Countries SBR - styrene/butadiene copolymers which contain from 1 to 60 wt.%, pre-ferably 2 to 50 wt.%, of styrene XSBR - styrene/butadiene copolymers and graft polymers with acrylic acid, methacrylic acid, acrylonitrile, hydroxyethyl acrylate and/or hydroxy-ethyl methacrylate, which contain from 2 to 50 wt.% of styrene and from 1 to 30 wt.% of polar monomers incorporated by polymerisation IIR - isobutylene/isoprene copolymers NBR - butadiene/acrylonitrile copolymers which contain from 5 to 60 wt.%, preferably 10 to 50 wt.%, of acrylonitrile HNBR - partially hydrogenated NBR rubber in which up to 98.5% of the double bonds are hydrogenated EPDM - ethylene/propylene/diene copolymers and mixtures of the latter rubbers.
Natural rubber, emulsion SBR rubber and solution SBR rubber having a glass transi-tion temperature above -50°C, optionally modified with silyl ethers or other functional groups, such as are described, for example, in EP-A 447 066, polybutadiene rubber having a high cis-1,4 content (> 90%) prepared using catalysts based on nickel, co-bait, titanium, or neodymium, and polybutadiene rubber which contains 0 to 75%
of vinyl, and mixtures thereof, are in particular of interest for the manufacture of, for example, vehicle tyres.
The rubber mixtures according to the invention which are prepared from the sty-rene/butadiene rubber gel (A) and the rubbers which contain double bonds (B) may additionally contain further fillers.
The following are particularly suitable fillers for the preparation of the rubber mix-tures and vulcanisates according to the invention:
- carbon blacks. The carbon blacks to be used in this case are prepared by the lamp black, furnace black or channel black processes and have BET surface Le A 32 156-Foreign Countries areas of from 20 to 200 m2/g, such as, for example, SAF, ISAF, USAF, HAF, FEF or GPF carbon blacks, - highly dispersed silicas prepared, for example, by precipitating silicate solu-tions or by flame hydrolysis of silicon halides and having specific surface areas of from 5 to 1000, preferably 20 to 400 m2/g (BET surface area), and primary particle sizes of from 5 to 400 nm. The silicas may optionally also be present as mixed oxides with other metal oxides, such as aluminium, magnesium, cal-cium, barium and zinc oxides and titanium oxides.
- synthetic silicates such as aluminium silicate, alkaline earth metal silicates such as magnesium or calcium silicate, having BET surface areas of from 20 to 400 m2/g and primary particle diameters of from 10 to 400 nm, - natural silicates such as kaolin, and other naturally occurring silicas, - metal oxides such as zinc, calcium, magnesium and aluminium oxide, - metal carbonates such as magnesium, calcium and zinc carbonate, - metal sulphates such as calcium and barium sulphate, - metal hydroxides such as aluminium and magnesium hydroxide, - glass fibres and glass fibre products (mats, extrudates) or glass microbeads - rubber gels based on polychloroprene and/or polybutadiene having particle sizes of from 5 to 1000 nm.
The named fillers may be utilised either alone or in mixture. In a particularly preferred embodiment of the process, from 10 to 100 parts by weight of styrene/butadiene rub-ber gel (A), optionally together with from 0.1 to 100 parts by weight of carbon black Le A 32 156-Foreign Countries and/or from 0.4 to 100 parts by weight of light-coloured fillers, in each case related to 100 parts by weight of rubber (B), are utilised to prepare the mixtures.
The rubber mixtures according to the invention may contain further rubber auxiliary substances such as cross-linking agents, reaction accelerators, antioxidants, heat sta-bilisers, light stabilisers, ozone stabilisers, processing auxiliary substances, plasticisers, tackifiers, blowing agents, dyes, pigments, waxes, extenders, organic acids, retar dants, metal oxides and filler activators such as triethanolamine, polyethylene glycol, hexanetriol, bis(triethoxysilylpropyl) tetrasulphide, etc., which are known in the rub ber industry.
The rubber auxiliary substances are utilised in conventional quantities as dictated, inter alia, by the purpose for which they are intended. Conventional quantities are, for example, quantities of from 0.1 to 50 wt.%, related to rubber (B).
Sulphur, sulphur donors or peroxides may be utilised as conventional cross-linking agents. The rubber mixtures according to the invention may fizrthermore contain vul-canisation accelerators. Examples of suitable vulcanisation accelerators are mercapto-benzothiazoles, mercaptobenzothiazole sulphene amides, guanidines, thiurams, dithio-carbamates, thioureas and thiocarbonates. The vulcanisation accelerators and sulphur or peroxides are utilised in quantities of from 0.1 to 10 wt.%, preferably 0.1 to 5 wt.%, related to rubber (B).
The rubber mixtures according to the invention may be vulcanised at temperatures of from 100 to 200°C, preferably 130 to 180°C, optionally under 10 to 200 bar pressure.
The rubber mixtures according to the invention which have been prepared from sty-rene/butadiene rubber gel (A) and the rubbers which contain C=C double bonds (B) may be prepared by more than one method: one possibility is naturally to mix the in-dividual solid components. Rolls, internal mixers and compounding extruders are ex-amples of units suitable for this purpose. It is, however, also possible to mix them by combining the latices of the styrene/butadiene rubber gels with the lances of the un-cross-linked rubbers. The mixtures according to the invention thus prepared may be Le A 32 156-Foreign Countries -g_ isolated as normal by evaporation, precipitation or freeze coagulation (cf. US-187 146). The mixtures according to the invention may be obtained in direct manner as rubber/filler formulations as a result of mixing fillers into the latex mixtures, fol-lowed by working up.
The rubber mixtures prepared from the styrene/butadiene rubber gel (A) and the rub-bers which contain double bonds (B) may be further mixed with additional fillers and optionally rubber auxiliary substances in conventional mixing units such as rolls, inter-nal mixers and compounding extruders. Preferred mixing temperatures are around to 180°C.
The rubber vulcanisates according to the invention are suitable for making mouldings, for example for the manufacture of cable sheaths, hoses, transmission belts, conveyor belts, roll coverings, tyres, in particular tyre treads, shoe soles, sealing rings and damping elements.
Examines Examule 1 (a) Cross-linking the SBR rubber in latex form 26,976 g of a SBR Latex (BaystalTM BL 1357 from Bayer France, Port Jerome) contain-ing 24 wt.% of styrene incorporated by polymerisation and having a particle size of 60 nm (DVN) and a solids content of 37.1 wt.% were diluted with 6,708 g water.
150 g dicumyl peroxide were added in an autoclave at 60°C. The mixture was then stirred under a nitrogen atmosphere at 60°C for 2 hours, after which it was heated to 150°C
and stirred at that temperature for 45 minutes. After cooling, it was filtered through a rnonodur cloth (pore size 0.2 mm). The solids content of the rubber latex was wt.%, the swelling index of the gel particles was 5, and the particle diameter 60 nm.
(b) Mixing the cross-linked SBR rubber with uncross-linked natural robber 5 kg of the rubber latex thus treated were then stirred into a mixture prepared from 5 kg natural rubber Latex having a 30 wt.% solids content, 300 g of a 5%
aqueous rosin soap solution (Dresinate ~ 731, manufactured by Hercules) and 150 g of a 10%
aqueous dispersion of Vulkanox TM 4020 antioxidant (manufactured by Bayer AG).
The latex mixture obtained contained cross-linked rubber and natural rubber in a 1 : I
weight ratio.
(c) Coagulating the rubber mixture To precipitate 3 kg of rubber mixture, 10.45 kg of the latex mixture obtained in pro-cess step (b) were stirred at 65°C into a solution of 225 g NaCI, 40.8 g AIZ(SOa)s x 18 HZO and 4.5 g gelatine in 30 1 water, with the pH maintained at 4 by the addition of 10% HzSOa. The product was washed tHoroughly with water and dried under vaccum at 70°C for 2 days.
Le A 32 156-Foreign Countries A master batch consisting of 50 wt.% cross-linked SBR rubber particles and 50 wt.%
natural rubber was obtained.
Example 2 14,721 g of a SBR latex (SHQ 6254) containing 40 wt.% of styrene incorporated by polymerisation and having a particle size of 115 nm (DVN) and a 40.8 wt.%
solids content were diluted with 5,370 g water. 39 g dicumyl peroxide were added in an autoclave at 60°C. The autoclave was sealed, blanketed with nitrogen at 5 bar pres-sure, and the pressure relieved. The procedure was repeated 3 times. The mixture was then stirred at 60°C for 2 hours, after which it was heated to 150°C and stirred at that temperature for 45 minutes. After cooling, it was filtered through a monodur cloth (pore size 0.2 mm). The solids content of the cross-linked rubber latex was 30 wt.%, the swelling index was 7 and the particle diameter 115 nm (DVN).
5 kg of the rubber latex thus cross-linked was then mixed with 5 kg natural rubber latex (30 wt% solids content) and coagulated, in accordance with the process of Example 1 b/c. A master batch consisting of 50 wt.% cross-linked SBR rubber particles and 50 wt.% natural rubber was obtained.
Example 3 14,721 g of a SBR latex (SHQ 6254) containing 40 wt.% of styrene incorporated by polymerisation and having a particle size of 115 nm (DVN) and a 40.8 wt.%
solids content were diluted with 5,409 g water. 60 g dicumyl peroxide were added in an autoclave at 60°C. The autoclave was sealed, blanketed with nitrogen at 5 bar pres-sure, and the pressure relieved. The procedure was repeated 3 times. The mixture was then stirred at 60°C for 2 hours, after which it was heated to 150°C and stirred at that temperature for 45 minutes. After cooling, it was filtered through a monodur cloth (pore size 0.2 mm). The solids content of the cross-linked rubber latex was 30 wt.%, the swelling index was 5 and the particle diameter 115 nm (DVN).
Le A 32 lSb-Foreign Countries S kg of the rubber latex thus cross-linked was then mixed with 5 kg natural rubber latex (30 wt.% solids content) and coagulated, in accordance with the process of Example 1 b/c. A master batch consisting of 50 wt.% cross-linked SBR rubber particles and 50 wt.% natural rubber was obtained.
S
Example 4 14,721 g of a SBR latex (SHQ 6254) containing 40 wt.% of styrene incorporated by polymerisation and having a particle size of 115 nm (DVN) and a 40.8 wt.%
solids content were diluted with 5,479 g water. 90 g dicumyl peroxide were added in an autoclave at 60°C. The autoclave was sealed, blanketed with nitrogen at 5 bar pres-sure, and the pressure relieved. The procedure was repeated 3 times. The mixture was then stirred at 60°C for 2 hours, after which it was heated to 150°C and stirred at that temperature for 45 minutes. After cooling, it was filtered through a monodur cloth (pore size 0.2 mm). The solids content of the cross-linked rubber latex was 30 wt.%, the swelling index was 4 and the particle diameter 11 S nm (DVN).
5 kg of the rubber latex thus cross-linked was then mixed with 5 kg natural rubber latex (30 wt.% solids content) and coagulated, in accordance with the process of Example 1 b/c. A master batch consisting of 50 wt.% cross-linked SBR rubber particles and 50 wt.% natural rubber was obtained.
Comparative Example 1 12,368 g of a BR latex (SHQ 6022) having a particle size of 140 nm (DVI~ and a 42.5 wt.% solids content were diluted with 5,315 g water. 78.75 g dicumyl peroxide were added in an autoclave at 60°C. The autoclave was sealed, blanketed with nitro-gen at 5 bar pressure, and the pressure relieved. The procedure was repeated 3 times.
The mixture was then stirred at 60°C for 2 hours, after which it was heated to 150°C
and stirred at that temperature for 45 minutes. After cooling, it was filtered through a monodur cloth (pore size 0.2 mm). The solids content of the cross-linked rubber latex was 45 wt.%, the swelling index was 3 and the particle diameter 150 nm (DVN).
(b) Mixing the cross-linked BR rubber with uncross-linked natural rubber 3,333 kg of the rubber latex thus treated were then stirred into a mixture prepared from 5 kg natural rubber having a solids content of 30 wt.%, 300 g of a 5%
aqueous rosin soap solution (Dresinate T"" 731 manufactured by Hercules) and 150 g of a 10%
aqueous dispersion of VulkanoxTM 4020 antioxidant (manufactured by Bayer AG).
The latex mixture obtained contained cross-linked rubber and natural rubber in a 1 : 1 weight ratio.
(c) Coagulating the latex To precipitate 3 kg of rubber mixture, 8.78 kg of the latex mixture obtained in pro-cess step (b) were stirred at 65°C into a solution of 225 g NaCI, 40.8 g A12(SOa)3 x 18 H20 and 4.5 g gelatine in 30 1 water, with the pH maintained at 4 by the addition of 10% H2SO4. The product was washed thoroughly with water and dried under vaccum at 70°C for 2 days.
A master batch consisting of 50 wt.% cross-linked SBR rubber particles and 50 wt.%
natural rubber was obtained.
Comparative Example 2 Mixture of a sulphur-cross-linked SBR rubber gel (22 wt.% styrene content, swelling index 33) in natural rubber in a 1 : 1 weight ratio, prepared by the process of Example 1 of GB-PS 1 078 400.
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Le A 32 156-Forei~:n Countries The investigations show clearly that the styrene/butadiene rubber gels according to the invention afford markedly lower impact resilience values at 23°
which, experience shows, correlate with greater grip of the tyres in the wet, while impact resilience at 70°C is at the same level as that of the comparative mixture, giving a rolling resistance of the same order of size. Surprisingly, the use of polybutadiene rubber in the rubber mixture results in a marked improvement in abrasion behaviour without substantially influencing grip in the wet (derived from impact resilience at 23°C). A
sulphur-cross-linked rubber gel according to GB-PS 1 078 400 demonstrates no reinforcing proper-ties and is therefore unsuitable for the application.
The literature describes a large number of measures designed to reduce the rolling resistance of tyres, including, inter alia, the use of polychloroprene gels (EP-A 405 216) and polybutadiene gels (DE-A 42 20 563) in tyre treads manufactured from rub-bers which contain C=C double bonds. Disadvantages of using polychloroprene gel arise from the high cost of the rubber, the high density of polychloroprene and the ecological disadvantages to which the chlorine-containing components can be ex-pected to give rise in scrap tyre recycling. While polybutadiene gels according to DE-A 42 20 563 do not have these disadvantages, the dynamic damping is in this case reduced at both low temperatures (-20 to +20°C) and also at higher temperatures (40-80°C), which in practice means that advantages in terms of rolling resistance are ac-companied by disadvantages in terms of tyre grip in the wet. Sulphur-cross-linked rubber gels according to GB-PS 1 078 400 have no reinforcing effect and are there-fore unsuitable for the present application.
It has now surprisingly been found that rubber vulcanisates which contain C=C
double bonds and are filled with special SBR gels have high dynamic damping at low tem-peratures and low dynamic damping at higher temperatures, such that advantages result in terms of both rolling resistance and grip in the wet. Particularly good proper-ties result from using SBR gels in rubber mixtures which contain polybutadiene rub-ber.
The present invention therefore provides mixtures prepared from at least one sty-rene/butadiene rubber gel (A) and at least one rubber which contains double bonds (B), wherein the styrene/butadiene rubber gel content is from 1 to 100 parts by Le A 32 156-Foreign Countries weight, preferably 5 to 75 parts by weight, related to 100 parts by weight of rubber which contains C=C double bonds, and optionally further fillers and rubber auxiliary substances.
Styrene/butadiene rubber gels (A) are understood to denote microgels which are pre-pared by cross-linking SBR - styrene/butadiene copolymers which contain from 1 to 80 wt.%, pre-ferably 5 to 50 wt.%, of styrene, and/or XSBR - styrene/butadiene copolymers and graft polymers with further polar unsaturated monomers such as acrylic acid, methacrylic acid, acryl-amide, methacrylamide, N-methoxymethyl methacrylic acid amide, N-acetoxymethyl methacrylic acid amide, acrylonitrile, dimethyl acryl-amide, hydroxyethyl acrylate, hydroxyethyl methacrylate, which con-taro from 1 to 75 wt.% of styrene and from 1 to 20 wt.% of polar monomers incorporated by polymerisation.
The styrene/butadiene rubber gels have particle diameters of from 5 to 1000, prefer-ably 20 to 400 nm (DVN value to DIN 53 206) and swelling indices (Q;) in toluene of from 1 to 1 S, preferably 1 to 10. The swelling index is calculated from the weight of the gel when it contains solvent (following centrifuging at 20,000 rpm) and its weight when dry:
Q; wet weight of gel/dry weight of gel.
As an example of determining the swelling index, 250 mg of SBR gel is swelled in 25 ml toluene for 24 hours, with shaking. The gel is centrifuged oil and weighed, and is then dried at 70°C until the weight is constant, and is reweighed.
The styrene/butadiene rubber starting products are preferably prepared by emulsion polymerisation. In this connection see, for example, I. Franta, Elastomers and Rubber Compounding Materials, Elsevier, Amsterdam 1989, pp. 88 to 92.
Le A 32 156-Foreign Countries The cross-linking of the rubber starting products to form styrene/butadiene rubber gels takes place in the latex state. This may be during polymerisation, as a result of continuing the polymerisation to high conversions or in the monomer feeding process as a result of polymerisation at high internal conversions or as a result of post-cross-linking after polymerisation, or both processes may be combined. The rubber starting products may also be prepared by polymerisation in the absence of regulators.
The styrene/butadiene rubber may also be cross-linked by copolymerisation with multifunctional compounds having a cross-linking action. Preferred multifunctional comonomers are compounds having at least two, preferably 2 to 4, copolymerisable C=C double bonds, such as diisopropenylbenzene, divinylbenzene, divinylether, divinylsulphone, diallyl phthalate, triallyl cyanurate, triallyl isocyanurate, 1,2-poly-butadiene, N,N'-m-phenylene malefic imide and/or triallyl trimellitate. The following are furthermore considered: acrylates and methacrylates of polyvalent, preferably di-valent to tetravalent, C2-C,o alcohols, such as ethylene glycol, propanediol-1,2, butanediol, hexanediol, polyethylene glycol, having 2 to 20, preferably 2 to 8 oxy ethylene units, neopentyl glycol, bisphenol A, glycerol, trimethylol propane, penta erythritol, sorbitol and unsaturated polyesters prepared from aliphatic diols and poly ols and malefic acid, fumaric acid and/or itaconic acid.
The styrene/butadiene rubbers may also be cross-linked in the latex form to form SBR
rubber gels, as a result of post-cross-linking them with chemicals having a cross-link-ing action. Suitable chemicals having a cross-linking action are, for example, organic peroxides, for example, dicumyl peroxide, t-butylcumyl peroxide, bis-(t-butyl-peroxy-isopropyl) benzene, di-t-butyl peroxide, dibenzoyl peroxide, bis-(2,4-dichlorobenzoyl) peroxide, t-butyl perbenzoate, and organic azo compounds such as azo-bis-iso-butyronitrile and azo-bis-cyclohexanenitrile, and dimercapto and polymercapto com-pounds such as dimercaptoethane, 1,6-dimercaptohexane, 1,3,5-trimercaptotriazine, and mercapto-terminating polysulphide rubbers such as mercapto-terminating reaction products of bis-chloroethyl formal with sodium polysulphide. The optimal tempera-ture for the post-cross-linking operation is naturally dependent on the reactivity of the cross-linking agent and may be from room temperature up to approx.
170°C, op-Le A 32 156-Foreign Countries tionally at elevated pressure. See in this context Houben-Weyl, Methoden der or-ganischen Chemie [Methods in Organic Chemistry], 4th edition, Vol. 14/2, p.
848.
Peroxides are particularly preferred cross-linking agents.
It is also optionally possible to enlarge the particles by agglomeration before, during or after the post-cross-linking in latex form.
Styrene/butadiene rubbers which have been prepared in organic solvents may also serve as starting products for the preparation of the styrene/butadiene rubber gels. In this case it is advisable to emulsify the rubber solution in water, optionally with the aid of an emulsifying agent, and to follow this, either before or after removing the organic solvent, with cross-linking of the emulsion thus obtained using suitable cross-linking agents. The cross-linking agents previously named are suitable cross-linking agents.
Preferred rubbers (B) contain double bonds corresponding to iodine values of at least 2, preferably from 5 to 470. Iodine values are generally determined by addition of iodine chloride in ethanoic acid in accordance with Wijs, DIN 53 241, Part 1.
The iodine value defines the number of grammes of iodine chemically bound in 100 g of a substance.
The rubbers (B) generally have Mooney viscosities ML 1+4/100°C (DIN 53 523) of from 10 to 150, preferably 20 to 120.
In addition to natural rubber, synthetic rubbers are also preferred rubbers (B). Pre-ferred synthetic rubbers are described in, for example, I. Franta, Elastomers and Rub-ber Compounding Materials, Elsevier, New York 1989 or in Ullmanns' Encyclopedia of Industrial Chemistry, Vol. A23, VCH Verlagsgesellschaft, Weinheim 1993.
They include, inter alia, the following:
BR - polybutadiene ABR - butadiene/acrylic acid-C1_4 alkylester copolymers IR - polyisoprene Le A 32 156-Foreign Countries SBR - styrene/butadiene copolymers which contain from 1 to 60 wt.%, pre-ferably 2 to 50 wt.%, of styrene XSBR - styrene/butadiene copolymers and graft polymers with acrylic acid, methacrylic acid, acrylonitrile, hydroxyethyl acrylate and/or hydroxy-ethyl methacrylate, which contain from 2 to 50 wt.% of styrene and from 1 to 30 wt.% of polar monomers incorporated by polymerisation IIR - isobutylene/isoprene copolymers NBR - butadiene/acrylonitrile copolymers which contain from 5 to 60 wt.%, preferably 10 to 50 wt.%, of acrylonitrile HNBR - partially hydrogenated NBR rubber in which up to 98.5% of the double bonds are hydrogenated EPDM - ethylene/propylene/diene copolymers and mixtures of the latter rubbers.
Natural rubber, emulsion SBR rubber and solution SBR rubber having a glass transi-tion temperature above -50°C, optionally modified with silyl ethers or other functional groups, such as are described, for example, in EP-A 447 066, polybutadiene rubber having a high cis-1,4 content (> 90%) prepared using catalysts based on nickel, co-bait, titanium, or neodymium, and polybutadiene rubber which contains 0 to 75%
of vinyl, and mixtures thereof, are in particular of interest for the manufacture of, for example, vehicle tyres.
The rubber mixtures according to the invention which are prepared from the sty-rene/butadiene rubber gel (A) and the rubbers which contain double bonds (B) may additionally contain further fillers.
The following are particularly suitable fillers for the preparation of the rubber mix-tures and vulcanisates according to the invention:
- carbon blacks. The carbon blacks to be used in this case are prepared by the lamp black, furnace black or channel black processes and have BET surface Le A 32 156-Foreign Countries areas of from 20 to 200 m2/g, such as, for example, SAF, ISAF, USAF, HAF, FEF or GPF carbon blacks, - highly dispersed silicas prepared, for example, by precipitating silicate solu-tions or by flame hydrolysis of silicon halides and having specific surface areas of from 5 to 1000, preferably 20 to 400 m2/g (BET surface area), and primary particle sizes of from 5 to 400 nm. The silicas may optionally also be present as mixed oxides with other metal oxides, such as aluminium, magnesium, cal-cium, barium and zinc oxides and titanium oxides.
- synthetic silicates such as aluminium silicate, alkaline earth metal silicates such as magnesium or calcium silicate, having BET surface areas of from 20 to 400 m2/g and primary particle diameters of from 10 to 400 nm, - natural silicates such as kaolin, and other naturally occurring silicas, - metal oxides such as zinc, calcium, magnesium and aluminium oxide, - metal carbonates such as magnesium, calcium and zinc carbonate, - metal sulphates such as calcium and barium sulphate, - metal hydroxides such as aluminium and magnesium hydroxide, - glass fibres and glass fibre products (mats, extrudates) or glass microbeads - rubber gels based on polychloroprene and/or polybutadiene having particle sizes of from 5 to 1000 nm.
The named fillers may be utilised either alone or in mixture. In a particularly preferred embodiment of the process, from 10 to 100 parts by weight of styrene/butadiene rub-ber gel (A), optionally together with from 0.1 to 100 parts by weight of carbon black Le A 32 156-Foreign Countries and/or from 0.4 to 100 parts by weight of light-coloured fillers, in each case related to 100 parts by weight of rubber (B), are utilised to prepare the mixtures.
The rubber mixtures according to the invention may contain further rubber auxiliary substances such as cross-linking agents, reaction accelerators, antioxidants, heat sta-bilisers, light stabilisers, ozone stabilisers, processing auxiliary substances, plasticisers, tackifiers, blowing agents, dyes, pigments, waxes, extenders, organic acids, retar dants, metal oxides and filler activators such as triethanolamine, polyethylene glycol, hexanetriol, bis(triethoxysilylpropyl) tetrasulphide, etc., which are known in the rub ber industry.
The rubber auxiliary substances are utilised in conventional quantities as dictated, inter alia, by the purpose for which they are intended. Conventional quantities are, for example, quantities of from 0.1 to 50 wt.%, related to rubber (B).
Sulphur, sulphur donors or peroxides may be utilised as conventional cross-linking agents. The rubber mixtures according to the invention may fizrthermore contain vul-canisation accelerators. Examples of suitable vulcanisation accelerators are mercapto-benzothiazoles, mercaptobenzothiazole sulphene amides, guanidines, thiurams, dithio-carbamates, thioureas and thiocarbonates. The vulcanisation accelerators and sulphur or peroxides are utilised in quantities of from 0.1 to 10 wt.%, preferably 0.1 to 5 wt.%, related to rubber (B).
The rubber mixtures according to the invention may be vulcanised at temperatures of from 100 to 200°C, preferably 130 to 180°C, optionally under 10 to 200 bar pressure.
The rubber mixtures according to the invention which have been prepared from sty-rene/butadiene rubber gel (A) and the rubbers which contain C=C double bonds (B) may be prepared by more than one method: one possibility is naturally to mix the in-dividual solid components. Rolls, internal mixers and compounding extruders are ex-amples of units suitable for this purpose. It is, however, also possible to mix them by combining the latices of the styrene/butadiene rubber gels with the lances of the un-cross-linked rubbers. The mixtures according to the invention thus prepared may be Le A 32 156-Foreign Countries -g_ isolated as normal by evaporation, precipitation or freeze coagulation (cf. US-187 146). The mixtures according to the invention may be obtained in direct manner as rubber/filler formulations as a result of mixing fillers into the latex mixtures, fol-lowed by working up.
The rubber mixtures prepared from the styrene/butadiene rubber gel (A) and the rub-bers which contain double bonds (B) may be further mixed with additional fillers and optionally rubber auxiliary substances in conventional mixing units such as rolls, inter-nal mixers and compounding extruders. Preferred mixing temperatures are around to 180°C.
The rubber vulcanisates according to the invention are suitable for making mouldings, for example for the manufacture of cable sheaths, hoses, transmission belts, conveyor belts, roll coverings, tyres, in particular tyre treads, shoe soles, sealing rings and damping elements.
Examines Examule 1 (a) Cross-linking the SBR rubber in latex form 26,976 g of a SBR Latex (BaystalTM BL 1357 from Bayer France, Port Jerome) contain-ing 24 wt.% of styrene incorporated by polymerisation and having a particle size of 60 nm (DVN) and a solids content of 37.1 wt.% were diluted with 6,708 g water.
150 g dicumyl peroxide were added in an autoclave at 60°C. The mixture was then stirred under a nitrogen atmosphere at 60°C for 2 hours, after which it was heated to 150°C
and stirred at that temperature for 45 minutes. After cooling, it was filtered through a rnonodur cloth (pore size 0.2 mm). The solids content of the rubber latex was wt.%, the swelling index of the gel particles was 5, and the particle diameter 60 nm.
(b) Mixing the cross-linked SBR rubber with uncross-linked natural robber 5 kg of the rubber latex thus treated were then stirred into a mixture prepared from 5 kg natural rubber Latex having a 30 wt.% solids content, 300 g of a 5%
aqueous rosin soap solution (Dresinate ~ 731, manufactured by Hercules) and 150 g of a 10%
aqueous dispersion of Vulkanox TM 4020 antioxidant (manufactured by Bayer AG).
The latex mixture obtained contained cross-linked rubber and natural rubber in a 1 : I
weight ratio.
(c) Coagulating the rubber mixture To precipitate 3 kg of rubber mixture, 10.45 kg of the latex mixture obtained in pro-cess step (b) were stirred at 65°C into a solution of 225 g NaCI, 40.8 g AIZ(SOa)s x 18 HZO and 4.5 g gelatine in 30 1 water, with the pH maintained at 4 by the addition of 10% HzSOa. The product was washed tHoroughly with water and dried under vaccum at 70°C for 2 days.
Le A 32 156-Foreign Countries A master batch consisting of 50 wt.% cross-linked SBR rubber particles and 50 wt.%
natural rubber was obtained.
Example 2 14,721 g of a SBR latex (SHQ 6254) containing 40 wt.% of styrene incorporated by polymerisation and having a particle size of 115 nm (DVN) and a 40.8 wt.%
solids content were diluted with 5,370 g water. 39 g dicumyl peroxide were added in an autoclave at 60°C. The autoclave was sealed, blanketed with nitrogen at 5 bar pres-sure, and the pressure relieved. The procedure was repeated 3 times. The mixture was then stirred at 60°C for 2 hours, after which it was heated to 150°C and stirred at that temperature for 45 minutes. After cooling, it was filtered through a monodur cloth (pore size 0.2 mm). The solids content of the cross-linked rubber latex was 30 wt.%, the swelling index was 7 and the particle diameter 115 nm (DVN).
5 kg of the rubber latex thus cross-linked was then mixed with 5 kg natural rubber latex (30 wt% solids content) and coagulated, in accordance with the process of Example 1 b/c. A master batch consisting of 50 wt.% cross-linked SBR rubber particles and 50 wt.% natural rubber was obtained.
Example 3 14,721 g of a SBR latex (SHQ 6254) containing 40 wt.% of styrene incorporated by polymerisation and having a particle size of 115 nm (DVN) and a 40.8 wt.%
solids content were diluted with 5,409 g water. 60 g dicumyl peroxide were added in an autoclave at 60°C. The autoclave was sealed, blanketed with nitrogen at 5 bar pres-sure, and the pressure relieved. The procedure was repeated 3 times. The mixture was then stirred at 60°C for 2 hours, after which it was heated to 150°C and stirred at that temperature for 45 minutes. After cooling, it was filtered through a monodur cloth (pore size 0.2 mm). The solids content of the cross-linked rubber latex was 30 wt.%, the swelling index was 5 and the particle diameter 115 nm (DVN).
Le A 32 lSb-Foreign Countries S kg of the rubber latex thus cross-linked was then mixed with 5 kg natural rubber latex (30 wt.% solids content) and coagulated, in accordance with the process of Example 1 b/c. A master batch consisting of 50 wt.% cross-linked SBR rubber particles and 50 wt.% natural rubber was obtained.
S
Example 4 14,721 g of a SBR latex (SHQ 6254) containing 40 wt.% of styrene incorporated by polymerisation and having a particle size of 115 nm (DVN) and a 40.8 wt.%
solids content were diluted with 5,479 g water. 90 g dicumyl peroxide were added in an autoclave at 60°C. The autoclave was sealed, blanketed with nitrogen at 5 bar pres-sure, and the pressure relieved. The procedure was repeated 3 times. The mixture was then stirred at 60°C for 2 hours, after which it was heated to 150°C and stirred at that temperature for 45 minutes. After cooling, it was filtered through a monodur cloth (pore size 0.2 mm). The solids content of the cross-linked rubber latex was 30 wt.%, the swelling index was 4 and the particle diameter 11 S nm (DVN).
5 kg of the rubber latex thus cross-linked was then mixed with 5 kg natural rubber latex (30 wt.% solids content) and coagulated, in accordance with the process of Example 1 b/c. A master batch consisting of 50 wt.% cross-linked SBR rubber particles and 50 wt.% natural rubber was obtained.
Comparative Example 1 12,368 g of a BR latex (SHQ 6022) having a particle size of 140 nm (DVI~ and a 42.5 wt.% solids content were diluted with 5,315 g water. 78.75 g dicumyl peroxide were added in an autoclave at 60°C. The autoclave was sealed, blanketed with nitro-gen at 5 bar pressure, and the pressure relieved. The procedure was repeated 3 times.
The mixture was then stirred at 60°C for 2 hours, after which it was heated to 150°C
and stirred at that temperature for 45 minutes. After cooling, it was filtered through a monodur cloth (pore size 0.2 mm). The solids content of the cross-linked rubber latex was 45 wt.%, the swelling index was 3 and the particle diameter 150 nm (DVN).
(b) Mixing the cross-linked BR rubber with uncross-linked natural rubber 3,333 kg of the rubber latex thus treated were then stirred into a mixture prepared from 5 kg natural rubber having a solids content of 30 wt.%, 300 g of a 5%
aqueous rosin soap solution (Dresinate T"" 731 manufactured by Hercules) and 150 g of a 10%
aqueous dispersion of VulkanoxTM 4020 antioxidant (manufactured by Bayer AG).
The latex mixture obtained contained cross-linked rubber and natural rubber in a 1 : 1 weight ratio.
(c) Coagulating the latex To precipitate 3 kg of rubber mixture, 8.78 kg of the latex mixture obtained in pro-cess step (b) were stirred at 65°C into a solution of 225 g NaCI, 40.8 g A12(SOa)3 x 18 H20 and 4.5 g gelatine in 30 1 water, with the pH maintained at 4 by the addition of 10% H2SO4. The product was washed thoroughly with water and dried under vaccum at 70°C for 2 days.
A master batch consisting of 50 wt.% cross-linked SBR rubber particles and 50 wt.%
natural rubber was obtained.
Comparative Example 2 Mixture of a sulphur-cross-linked SBR rubber gel (22 wt.% styrene content, swelling index 33) in natural rubber in a 1 : 1 weight ratio, prepared by the process of Example 1 of GB-PS 1 078 400.
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Le A 32 156-Forei~:n Countries The investigations show clearly that the styrene/butadiene rubber gels according to the invention afford markedly lower impact resilience values at 23°
which, experience shows, correlate with greater grip of the tyres in the wet, while impact resilience at 70°C is at the same level as that of the comparative mixture, giving a rolling resistance of the same order of size. Surprisingly, the use of polybutadiene rubber in the rubber mixture results in a marked improvement in abrasion behaviour without substantially influencing grip in the wet (derived from impact resilience at 23°C). A
sulphur-cross-linked rubber gel according to GB-PS 1 078 400 demonstrates no reinforcing proper-ties and is therefore unsuitable for the application.
Claims (8)
1. A rubber mixture prepared from at least one styrene/butadiene rubber gel (A) and at least one rubber which contains double bonds (B), wherein the styrene/butadiene rubber gel content is from 1 to 100 parts by weight, related to 100 parts by weight of rubber which contains C=C double bonds, wherein the styrene/butadiene rubber gel (A) has a swelling index in toluene of from 1 to 15 and a particle size of from 5 to 1000 nm.
2. The mixture according to claim 1, wherein the swelling index is from 1 to 10 and the particle size is from 20 to 400 nm.
3. The mixture according to claim 1 or 2, wherein rubber (B) contains double bonds corresponding to an iodine value of from 5 to 470.
4. The mixture according to claim 1, 2 or 3, wherein the styrene/butadiene rubber gel content is from 5 to 75 parts by weight, related to 100 parts by weight of rubber which contains C=C double bonds.
5. The mixture according to any one of claims 1 to 4 further comprising a filler.
6. Use of the rubber mixture according to any one of claims 1 to 5 for the preparation of a rubber vulcanisate.
7. Use of the rubber mixture according to any one of claims 1 to 5 for the manufacture of a moulding.
8. Use of the rubber mixture according to any one of claims 1 to 5 for the manufacture of a tyre tread.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19701488.7 | 1997-01-17 | ||
| DE19701488A DE19701488A1 (en) | 1997-01-17 | 1997-01-17 | Rubber mixtures containing SBR rubber gels |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2226917A1 CA2226917A1 (en) | 1998-07-17 |
| CA2226917C true CA2226917C (en) | 2006-12-05 |
Family
ID=7817630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002226917A Expired - Fee Related CA2226917C (en) | 1997-01-17 | 1998-01-14 | Rubber mixtures which contain sbr rubber gels |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US6127488A (en) |
| EP (1) | EP0854170B1 (en) |
| JP (1) | JP3794810B2 (en) |
| KR (1) | KR100535281B1 (en) |
| CN (1) | CN1111564C (en) |
| CA (1) | CA2226917C (en) |
| DE (2) | DE19701488A1 (en) |
| TW (1) | TW523534B (en) |
Families Citing this family (246)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19834802A1 (en) * | 1998-08-01 | 2000-02-03 | Continental Ag | Rubber compound |
| DE19834804A1 (en) | 1998-08-01 | 2000-02-03 | Continental Ag | Rubber compound |
| DE19834803A1 (en) * | 1998-08-01 | 2000-02-03 | Continental Ag | Rubber compound |
| US6447905B1 (en) * | 1999-01-19 | 2002-09-10 | Pirelli Tire Llc | Green tire bead and composition |
| US6852785B1 (en) * | 1999-04-22 | 2005-02-08 | Dunlop Tire Corporation | Vulcanizable elastomeric compositions for use as tire treads |
| EP1063259A1 (en) | 1999-06-26 | 2000-12-27 | Bayer Ag | Rubber compositions containing rubber microgels and sulfur-bearing organosilicon compounds |
| DE19939865A1 (en) * | 1999-08-23 | 2001-03-01 | Bayer Ag | Rubber mixtures and vulcanizates containing agglomerated rubber gels |
| JP2001139729A (en) | 1999-08-31 | 2001-05-22 | Yokohama Rubber Co Ltd:The | Rubber composition and method for producing the same |
| JP4628511B2 (en) * | 1999-12-27 | 2011-02-09 | 住友ゴム工業株式会社 | Tread rubber composition and pneumatic tire using the same |
| US6747095B2 (en) | 2000-04-27 | 2004-06-08 | Jsr Corporation | Crosslinked rubber particles and rubber compositions |
| EP1149866A3 (en) | 2000-04-27 | 2003-04-23 | JSR Corporation | Rubber mixtures based on crosslinked rubber particles and non-crosslinked rubbers |
| EP1152030B1 (en) | 2000-05-01 | 2012-12-12 | JSR Corporation | Rubber mixtures based on crosslinked rubber particles and non-crosslinked rubbers |
| EP1291369B1 (en) * | 2000-06-07 | 2006-03-29 | Zeon Corporation | Conjugated diene rubber gel, rubber compositions containing the same and process for production of conjugated diene rubber |
| JP4852736B2 (en) * | 2000-06-29 | 2012-01-11 | Ｊｓｒ株式会社 | Rubber composition |
| DE10035493A1 (en) | 2000-07-21 | 2002-01-31 | Bayer Ag | Process for the production of crosslinked rubber particles |
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| GB1078400A (en) * | 1963-08-13 | 1967-08-09 | Rubber Res Inst Of Malaya Boar | Processing improvements to synthetic rubbers |
| GB1087400A (en) * | 1964-01-03 | 1967-10-18 | Super Temp Corp | Method and apparatus for consolidation of powdered materials and articles of manufacture produced therefrom |
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| US4042647A (en) * | 1975-03-21 | 1977-08-16 | Uniroyal, Inc. | Latex suspension process and graft polyblend composition using small particle size spine |
| US4104210A (en) * | 1975-12-17 | 1978-08-01 | Monsanto Company | Thermoplastic compositions of high unsaturation diene rubber and polyolefin resin |
| JPS58129032A (en) * | 1982-01-28 | 1983-08-01 | Toyo Tire & Rubber Co Ltd | Composition for pneumatic tire |
| JPS5936144A (en) * | 1982-08-23 | 1984-02-28 | Sumitomo Rubber Ind Ltd | Diene rubber composition and tire with the same used in tread |
| JPS62156145A (en) * | 1985-12-28 | 1987-07-11 | Toyo Tire & Rubber Co Ltd | Rubber composition for use in tread |
| JPH0798880B2 (en) * | 1987-09-11 | 1995-10-25 | 株式会社ブリヂストン | Pneumatic tire |
| US5354487A (en) * | 1990-04-06 | 1994-10-11 | Nippon Oil Co., Ltd. | Solid lubricant and composition |
| DE4220563A1 (en) * | 1992-06-24 | 1994-01-13 | Bayer Ag | Rubber mixtures containing polybutadiene gel |
| US5262213A (en) * | 1992-09-14 | 1993-11-16 | The Goodyear Tire & Rubber Company | Styrene-butadiene rubber for truck tires |
| US6024146A (en) * | 1994-05-02 | 2000-02-15 | The Goodyear Tire & Rubber Company | Pneumatic tire having an innerliner of a cured rubber compound containing trans 1,4-polybutadiene rubber |
| US5510419A (en) * | 1994-09-16 | 1996-04-23 | National Rubber Technology Inc. | Polymer-modified rubber composition |
| US5859133A (en) * | 1996-03-18 | 1999-01-12 | The Goodyear Tire & Rubber Company | Tire tread compound |
-
1997
- 1997-01-17 DE DE19701488A patent/DE19701488A1/en not_active Withdrawn
-
1998
- 1998-01-03 DE DE59810369T patent/DE59810369D1/en not_active Expired - Lifetime
- 1998-01-03 EP EP98100049A patent/EP0854170B1/en not_active Expired - Lifetime
- 1998-01-06 TW TW087100100A patent/TW523534B/en not_active IP Right Cessation
- 1998-01-12 JP JP01640298A patent/JP3794810B2/en not_active Expired - Fee Related
- 1998-01-12 US US09/005,966 patent/US6127488A/en not_active Expired - Lifetime
- 1998-01-14 CA CA002226917A patent/CA2226917C/en not_active Expired - Fee Related
- 1998-01-16 CN CN98103655A patent/CN1111564C/en not_active Expired - Fee Related
- 1998-01-16 KR KR1019980001211A patent/KR100535281B1/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| DE19701488A1 (en) | 1998-07-23 |
| KR100535281B1 (en) | 2006-02-28 |
| JPH10204217A (en) | 1998-08-04 |
| KR19980070564A (en) | 1998-10-26 |
| CN1188117A (en) | 1998-07-22 |
| EP0854170A1 (en) | 1998-07-22 |
| CN1111564C (en) | 2003-06-18 |
| JP3794810B2 (en) | 2006-07-12 |
| TW523534B (en) | 2003-03-11 |
| DE59810369D1 (en) | 2004-01-22 |
| EP0854170B1 (en) | 2003-12-10 |
| US6127488A (en) | 2000-10-03 |
| CA2226917A1 (en) | 1998-07-17 |
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| EEER | Examination request | ||
| MKLA | Lapsed |