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EP1920000A1 - Hochmodulige kautschukzusammensetzung - Google Patents

Hochmodulige kautschukzusammensetzung

Info

Publication number
EP1920000A1
EP1920000A1 EP06777085A EP06777085A EP1920000A1 EP 1920000 A1 EP1920000 A1 EP 1920000A1 EP 06777085 A EP06777085 A EP 06777085A EP 06777085 A EP06777085 A EP 06777085A EP 1920000 A1 EP1920000 A1 EP 1920000A1
Authority
EP
European Patent Office
Prior art keywords
composition
tpu
diol
diisocyanate
rubber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP06777085A
Other languages
English (en)
French (fr)
Inventor
Steven Kristofer Henning
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sartomer Technology Co Inc
Original Assignee
Sartomer Technology Co Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sartomer Technology Co Inc filed Critical Sartomer Technology Co Inc
Publication of EP1920000A1 publication Critical patent/EP1920000A1/de
Withdrawn legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
    • C08G18/6576—Compounds of group C08G18/69
    • C08G18/6582—Compounds of group C08G18/69 with compounds of group C08G18/32 or polyamines of C08G18/38
    • C08G18/6588—Compounds of group C08G18/69 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/83—Chemically modified polymers
    • C08G18/87—Chemically modified polymers by 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
    • C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
    • C08L75/04—Polyurethanes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00—Polymer mixtures characterised by other features
    • C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/16—Ethene-propene or ethene-propene-diene copolymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/18—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
    • C08L23/20—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
    • C08L23/22—Copolymers of isobutene; Butyl rubber; Homopolymers or copolymers of other iso-olefins
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/26—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers modified by chemical after-treatment
    • C08L23/28—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers modified by chemical after-treatment by reaction with halogens or halogen-containing compounds
    • C08L23/283—Iso-olefin halogenated homopolymers or copolymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
    • C08L75/04—Polyurethanes
    • C08L75/14—Polyurethanes having carbon-to-carbon unsaturated bonds

Definitions

  • the present invention relates to a vulcanizable composition, cured compositions and articles prepared by curing the said vulcanizable composition. More particularly the said vulcanizable composition comprises uncured rubbery polymers from natural or/and synthetic rubber, and diene-based thermoplastic polyurethanes (TPUs), as co-curable additives.
  • TPUs diene-based thermoplastic polyurethanes
  • Diene-based polymers are the most commonly used rubber in the manufacturing of tires and other engineered products. These materials are chosen for their elastomeric qualities. They can be mixed with organic and inorganic fillers and other rubber chemicals to produce a compound which processes easily on current industrial equipment. They are typically unsaturated and can therefore be vulcanized to form high modulus components using several different cure chemistries, including sulfur and peroxides. By altering the polymerization chemistry, these diene-based elastomers can exhibit a range of glass transition temperatures (Tg). The polymer Tg may thus be tuned to provide the optimum performance for a given application. Natural rubber alone blended with synthetic rubber polymers is also used for many engineered product applications.
  • Polyurethane (PU) elastomers have been commercially available for some time. These materials can exhibit high hardness in the unfilled state and, thus, produce components with good flexural properties and low hysteresis. The addition of small amounts of inorganic fillers can also provide decent tear properties. These polyurethane materials also have very good abrasion properties. Urethane chemistry also produces very polar polymers, with excellent oil and solvent resistance.
  • Conventional PUs can be formed and molded in-place into an article with a desired shape, as they are thermosets. While the production of a tire or other engineered product solely from conventional PU materials is possible, certain performance properties of the resulting product fall well below those of conventional diene-based elastomer compounds.
  • TPUs Thermoplastic polyurethanes
  • Commercially available grades are typically characterized by the chemical nature of their polymeric soft segment.
  • TPUs are formed from either polyester or polyether soft segments. They are characterized by their ability to be reprocessed by heating and subsequent reforming. However, most of these products do not contain unsaturation and cannot participate effectively in sulfur or peroxide vulcanization.
  • Crosslinked polyurethane (PU) elastomers based on a mixture of polydiene diols and of diisocyanates are known from prior art (US 4,104,265). They are prepared in a two steps process comprising as first step, the in-situ formation of the PU and as second step the vulcanization of the said PU at a higher temperature. Saturated thermoplastic polyurethane elastomers based on hydrogenated polybutadiene diols are also known (WO 97/00901). None of these prior art documents discloses the use of diene-based unsaturated thermoplastic polyurethanes (TPUs) which can be co-cured with natural or/and synthetic rubber.
  • TPUs diene-based unsaturated thermoplastic polyurethanes
  • TPU thermoplastic polyurethane
  • thermoplastic polyurethanes which are unsaturated thermoplastic polyurethanes, diene-based., as co-curable additives, in a vulcanizable rubber composition, comprising at least one rubbery polymer selected from natural or/and synthetic rubber.
  • Blending said TPUs into rubber compounds is possible for most TPU grades as the softening temperatures are close to the typical mixing temperatures and the shear mixing involved in the process aids incorporation and promotes dispersion of the TPU. Both softening temperature and the condition of solubility in the rubber compound must be met to form a viable rubber-TPU uncured composite.
  • the utility of TPUs in forming rubber composites is predicated by the ability to also co-cure.
  • Suitable TPUs for the present invention preferably have as molecular weight, Mn ranging from 10.000 to 100.000 and Mw ranging from 20.000 to 400.000, or/and weight content of hard segment (isocyanate + eventual chain extender) in the said TPU, ranging from 1 to 80 % and more preferably from 10 to 50 %.
  • TPE Diene-based thermoplastic elastomers
  • the said TPEs are typically linear or radial triblock polymers based on styrene-diene-styrene discrete segments. While capable of co-curing with traditional rubber compounds, they also contribute negatively to hysteresis by the nature of their triblock structure. They are effective at increasing the modulus of the resulting vulcanized compound. However, as only the internal diene-based segment can co-cure, the triblock structure also results in a large amount of hysteresis. The uncured styrene hard segments contribute to heat build-up and a loss of properties with time.
  • Performance properties such as rolling resistance and long-term durability can be negatively affected.
  • Diene-based TPUs exhibit more uniform distribution of hard and soft segments, potentially minimizing the contribution to heat build-up by providing improved curing compatibility. They are effective at increasing the modulus of the resulting vulcanized compound but without hysteresis effect.
  • Suitable diene-based TPUs comprise a (soft) segment derived from at least one linear diene diol and a (hard) segment derived from at least one organic diisocyanate and optionally a chain extender selected from at least one diol or/and diamine, preferably having 2 to 8 carbon atoms.
  • the said organic diisocyanate may be selected from the group consisting of 4,4'- diphenylmethane diisocyanate, mixtures of isomers of diphenylmethane diisocyanate, toluene diisocyanate, 4,4'-diisocyanato-dicyclohexyl methane, tetramethyl xylene diisocyanate, isophoronediisocyanate, hexamethylenediisocyanate, 3,3 '-dimethyl- 4,4'-biphenyl diisocyanate and 1,4 benzene diisocyanate.
  • the said diol chain extender may be selected from the group consisting of 1,4 butane diol,ethylene glycol, 1,6 hexane diol, 2-ethyl-l,3 hexane diol, N, N-bis(2-hydroxypropyl) aniline and hydroquinone bis (2-hydroxy ethyl) ether, while the said diamine chain extender may be selected from the group consisting of sterically hindered diamines, such as l-amino-3- aminomethyl-3,5,5-trimethyl-cyclohexane (isophorone diamine).
  • the first subject of the invention relates to a composition
  • a composition comprising at least one diene-based thermoplastic polyurethane (TPU) and at least one uncured rubbery polymer, selected from natural or/and synthetic rubber.
  • this vulcanizable composition comprises from 2 to 50 parts, preferably from 5 to 30 parts of a diene-based thermoplastic polyurethane (TPU), such as defined above, per 100 parts by weight of the said rubbery polymer, selected from natural or/and synthetic rubber.
  • TPU diene-based thermoplastic polyurethane
  • diene-based TPUs to co-vulcanize with unsaturated elastomers allows for the inclusion of diene-TPU materials into traditional rubber compounds. Diene- based TPUs can be mixed into these compounds to improve various physical properties owing to their unique structure.
  • the inclusion of a high-modulus PU component in the rubber vulcanizate could provide similar performance properties when compared to a similar composition utilizing fillers alone.
  • the benefit of including a PU component would be realized only if that component can be co-cured with the diene-based rubber matrix.
  • the said vulcanizable composition according to the present invention may also comprise per 100 parts by weight of the said rubbery polymer, from about 10 to 200, preferably from 10 to 100 more preferably 30 to 100 and even more preferably, from 60 to 90 parts of a filler selected from the group of carbon black, silica, clay, and mixtures of said fillers.
  • the said vulcanizable composition can also comprise a cure effective amount of at least one curing agent preferably selected from sulfur vulcanizing agents or peroxides.
  • the said composition of the invention is a vulcanizable composition
  • a vulcanizable composition comprising by weight: a) 100 parts of a least one rubbery polymer selected from the group consisting of natural or/and synthetic rubber: b) from 2 to 50, preferably from 5 to 30 parts of at least one diene-based thermoplastic polyurethane (TPU) c) from about 10 to 200, preferably from 10 to 100 more preferably 30 to 100 and even more preferably from 60 to 90 parts of a filler selected from the group of carbon black, silica, clay, and mixtures of said fillers d) a cure effective amount of at least one curing agent, which may be selected from sulfur vulcanizating agents or peroxides
  • Diene-based TPUs have smaller hard segments dispersed throughout the structure and the co-curable soft segments are equally distributed. Such a macrostructure can provide similar benefits in the physical properties of the compound, while not as deleteriously contributing to hysteresis. Other properties of a rubber compound can be improved when containing diene-based TPU.
  • the TPU will impart a greater polarity to the compound, making the hydrocarbon-based blend more compatible with polar ingredients such as curatives and certain fillers.
  • the compound may demonstrate improved adhesion to other polar substrates or PU composites.
  • the diene-based thermoplastic polyurethanes used in the invention can be derived from polydiene diols having from 1.6 to 2, preferably 1.8 to 2, and more preferably 1.9 to 2, terminal hydroxyl groups per molecule and a number average molecular weight between 500 and 20.000, more preferably between 1000 and 10.000, an isocyanate having two isocyanate groups per molecule and optionally a low molecular weight chain extender, having two hydroxyl or amine groups per molecule, selected from at least one diol or/and diamine.
  • the polydiene diol can be made using a di-lithium initiator which is used to polymerize butadiene in a solvent.
  • the molar ratio of di-lithium initiator to monomer determines the molecular weight of the polymer.
  • the living polymer is then end-capped with two moles of ethylene oxide or propylene oxide and terminated (in termination reaction) with two moles of water to yield the desired polydiene diol.
  • the said polydiene diol can be either polybutadiene diol or polyisoprene diol or diol of a copolymer of butadiene or/and isoprene with another monomer, which may be selected from vinyl aromatic monomers like styrene.
  • diols of copolymers may be styrene- butadiene or styrene-isoprene copolymer diols (including dibloc SB or SI), such as obtainable by anionic polymerization.
  • the isocyanate used to make the TPU is a diisocyanate having a functionality of two isocyanate groups per molecule, since they produce thermoplastic polyurethane compositions when combined with a diol.
  • suitable diisocyanates are selected from the group consisting of 4,4'-diphenylmethane diisocyanate, mixtures of isomers of diphenylmethane diisocyanate, toluene diisocyanate, 4,4'-diisocyanato-dicyclohexylmethane, tetramethylxylene diisocyanate, isophorone diisocyanate, hexamethylene diisocyanate, 3, 3 '-dimethyl -4,4'- biphenyl diisocyanate, and 1,4-benzene diisocyanate and the like.
  • the optional chain extenders used to make the polyurethane composition may be low molecular weight diols having two hydroxyl groups per molecule or/and diamines.
  • the said diol chain extender may be selected from the group consisting of: 1,4 butane diol, ethylene glycol, 1,6 hexane diol, 2-ethyl-l,3 hexane diol, 2-ethyl-2-butyl-l,3-propane diol, 2,2,4- trimethyl-l,3-pentane diol, N, N-bis(2-hydroxypropyl) aniline and hydroquinone bis (2- hydroxy ethyl) ether, while the said diamine chain extender may be selected from the group consisting of sterically hindered diamines, such as l-amino-3-aminomethyl-3,5,5-trimethyl- cyclohexane (isophorone diamine).
  • the preferred chain extenders have methyl, ethyl or higher carbon side chains which make these diols or diamines less polar and therefore more compatible with the non-polar polydienes.
  • chain extenders are 2-ethyl-l,3- hexanediol, 2-ethyl-2-butyl-l,3-propane diol and 2,2,4-trimethyl-l,3-pentane diol.
  • Linear chain extenders without carbon side chains such as 1,4-butane diol, ethylene diamine, 1,6- hexane diol and the like, also result in polyurethane compositions if a prepolymer method is used to avoid incompatibility.
  • the weight content in the said TPU, of the resulting hard segment (isocyanate + eventual chain extender) ranges from 1 to 80% and more preferably from 10 to 50%.
  • Thermoplastic polyurethanes can be prepared by either one-shot or two-step prepolymer method.
  • a preferred way to make TPUs is by the prepolymer method where the isocyanate component is reacted first with the polydiene diol to form an isocyanate- terminated prepolymer, which can then be reacted further with the chain extender of choice (the suitable diol or/and diamine).
  • the polydiene diol is heated to at least 7O 0 C and not more than 100 0 C and then mixed with the desired amount of isocyanate for at least 2 hours under nitrogen flow.
  • the desired amount of chain extender is added and thoroughly mixed.
  • the mixture is then poured into a heated mold treated with a mold release compound.
  • the polyurethane composition is formed by curing into the mold for several hours and then post curing the TPU above 110 0 C for at least 2 hours.
  • Vulcanizable rubber compounds having improved properties are provided by this invention. Either sulfur or peroxide vulcanizing systems can be employed.
  • the uncrosslinked rubbers which are incorporated into the vulcanizable compounds are natural rubber, synthetic cis-l,4-polyisoprene, polybutadiene, copolymers of isoprene and butadiene, copolymers of acrylonitrile and butadiene, copolymers of isoprene and isobutylene, halogenated copolymers of isoprene and isobutylene, terpolymers of styrene, butadiene and isoprene, copolymers of styrene and butadiene and blends thereof.
  • the synthetic rubbers among such scrubbers can be emulsion polymerized or solution polymerized.
  • sulfur vulcanizing agents examples include elemental sulfur (free sulfur also named “sulfur” in the present invention) or a sulfur-donating vulcanizing agent, for example, an amine disulfide, polymeric polysulfide or sulfur olefin adducts or mixtures thereof.
  • the sulfur vulcanizing agent is elemental sulfur (sulfur).
  • the amount of sulfur vulcanizing agent will vary depending on the components of the rubber stock and the particular type of sulfur vulcanizing agent that is used.
  • the sulfur vulcanizing agent is generally present in an amount ranging from about 0.5 to about 6 phr.
  • the sulfur vulcanizing agent is present in an amount ranging from about 0.75 phr to about 4.0 phr.
  • Peroxides can also be used in the present invention as curing agents. These include alkoxy-based organic peroxides, like di-teit-butyl peroxide, dicumyl peroxide, 2,5-bis (tert- butyl peroxy)-2,5-dimethyl-hexane, ⁇ , ⁇ '-bis-(tert-butylperoxy) diisopropyl benzene, tert- butyl cumyl peroxide, and 2,5-dimethyl-2,5 (di-tert-butylperoxy) hexyne-3. Typically, reactive coagents are also used in addition to peroxides to more effectively cure the composition.
  • Such coagents include multifunctional acrylate or methacrylate esters., allylic- containing compounds, or bismaleimides. Active peroxides are generally used at 1 to 20 phr. Coagents are used at 1 to 50 phr.
  • Such rubber additives may be incorporated in the rubber stock of the present invention.
  • Such additives can include fillers, plasticizers, waxes, processing oils, peptizers, retarders, antiozonants, antioxidants and the like.
  • the total amount of filler that may be used may range from about 10 to 200 phr, with a range of from about 10 to 100 phr being preferred and more preferably 30 to 100 phr and even more preferably from 60 to 90 phr.
  • Fillers include clays, calcium carbonate, calcium silicate, titanium dioxide and carbon black. Representative carbon blacks that are commonly used in rubber stocks include NI lO, N121, N220, N231, N234, N242, N293, N299, N330, N326, N330, N332, N339, N343, N347, N351, N358, N375, N472, N660, N754, N762, N765 and N990.
  • Plasticizers are conventionally used in amounts ranging from about 2 to about 50 phr with a range of about 5 to about 30 phr (with respect to the said rubbery polymer) being preferred.
  • the amount of plasticizer used will depend upon the softening effect desired.
  • suitable plasticizers include aromatic extract oils, petroleum softeners including asphaltenes, pentachlorophenol, saturated and unsaturated hydrocarbons and nitrogen bases, coal tar products, cumarone-indene resins and esters such as dibutylphthalate and tricresol phosphate.
  • Common waxes may be used, which include paraffinic waxes and microcrystalline blends. Such waxes are used in amounts ranging from about 0.5 to 5 phr.
  • Processing oils may also be used, at typical amounts from about 1 to 70 phr.
  • Such processing oils can include, for example, aromatic, naphthenic and/or paraffinic processing oils.
  • Peptizers can also be used, at typical amounts of about 0.1 to about 1 phr.
  • Typical peptizers may be, for example, pentachlorothiophenol and dibenzamido-diphenyl disulfide.
  • Materials used in compounding which function as an accelerator-activator includes metal oxides such as zinc oxide and magnesium oxide, which are used in conjunction with acidic materials such as fatty acid, for example, stearic acid, oleic acid, murastic acid and the like.
  • the amount of the metal oxide may range from about 1 to about 14 phr with a range of from about 2 to about 8 phr being preferred.
  • the amount of fatty acid which may be used may range from about 0 phr to about 5.0 phr with a range of from about 0 phr to about 2 phr being preferred.
  • Accelerators are used to control the time and/or temperature required for vulcanization and to improve the properties of the vulcanizate.
  • One embodiment provides, a single primary accelerator system.
  • the primary accelerator(s) may be used in total amounts ranging from about 0.5 to about 4, preferably about 0.8 to about 2.0 phr. In another embodiment, combinations of primary and secondary accelerators can be used, with the secondary accelerator being used in a smaller, equal or greater amount to the primary accelerator. Combinations of these accelerators might be expected to produce a synergistic effect on the final properties and are somewhat better than those produced by use of either accelerator alone. In addition, delayed action accelerators may be used which are not affected by normal processing temperatures but produce a satisfactory cure at ordinary vulcanization temperatures.
  • Suitable types of accelerators that may be used in the present invention are amines, disulfides, guanidines, thioureas, thiazoles, thiurams, sulfenamides, dithiocarbamates and xanthates.
  • the primary accelerator is a sulfenamide.
  • the secondary accelerator is preferably a disulfide, guanidine, dithiocarbamate or thiuram compound.
  • Siliceous pigments may also be used in the rubber compound applications of the present invention, including precipitated siliceous pigments (silica).
  • the siliceous pigments employed in this invention are precipitated silicas such as, for example, those obtained by the acidification of a soluble silicate, e.g., sodium silicate.
  • silicas might be characterized, for example, by having a BET surface area, as measured using nitrogen gas, preferably in the range of about 40 to about 600, and more usually in a range of about 50 to about 300 square meters per gram. The BET method of measuring surface area is described in the Journal of the American Chemical Society, Volume 60, page 304 (1930).
  • the silica may also be typically characterized by having a dibutylphthalate (DBP) absorption value in a range of about 100 to about 400, and more usually about 150 to about 300.
  • DBP dibutylphthalate
  • the silica might be expected to have an average ultimate particle size, for example, in the range of 0.01 to 0.05 micron as determined by the electron microscope, although the silica particles may be even smaller, or possibly larger, in size.
  • Various commercially available silicas may be used, for example, silicas commercially available from PPG Industries under the Hi-SiI trademark with designations 210, 243, silicas available from Rhodia, with, for example, designations of Zl 165MP and Z165GR and silicas available from Degussa AG with, for example, designations VN2 and VN3.
  • the PPG Hi-SiI silicas are currently preferred.
  • scorch retarders A class of compounding materials known as scorch retarders are commonly used with sulfur cured systems. Phthalic anhydride, salicylic acid, sodium acetate and N-cyclohexyl thiophthalimide are known retarders for sulfur cure. Weakly to moderately acidic (hydrogen- donating) compounds are effective scorch retarders for peroxide cure. Retarders are generally used in an amount ranging from about 0.1 to 0.5 phr.
  • antioxidants and sometimes antiozonants are added to rubber stocks.
  • Representative antidegradants include monophenols, bisphenols, thiobisphenols, polyphenols, hydroquinone derivatives, phosphites, thioesters, naphthyl amines, diphenyl-p-phenylenediamines, diphenylamines and other diaryl amine derivatives, para-phenylenediamines, quinolines and mixtures thereof.
  • Specific examples of such antidegradants are disclosed in The Vanderbilt Rubber Handbook (1990), pages 282-286.
  • Antidegradants are generally used in amounts from about 0.25 to about 5.0 phr with a range of from about 1.0 to about 3.0 phr being preferred.
  • the vulcanizable rubber compound is cured at a rubber temperature ranging from about 125°C to 180°C.
  • the rubber compound is heated for a time sufficient to vulcanize the rubber which may vary depending on the level of curatives and temperature selected. Generally speaking, the time may range from 3 to 60 minutes.
  • the mixing of the rubber compound can be accomplished by well known methods.
  • the ingredients are typically mixed in at least two stages, namely at least one non-productive stage followed by a productive mix stage.
  • the final curatives are typically mixed in the final stage which is conventionally called the "productive" mix stage in which the mixing typically occurs at a temperature, or ultimate temperature, lower than the mix temperature(s) than the preceding non-productive mix stage(s).
  • the terms "non-productive” and “productive” mix stages are well known terms to those having skill in the rubber mixing art.
  • the above-described TPU materials according to the present invention may be added in a non-productive stage or productive stage.
  • the TPU is added in a nonproductive stage.
  • the method of mixing the various components of the rubber containing the TPU material may be in a conventional manner. Examples of such methods include the use of internal mixers (Banbury), mills, extruders and the like. An important aspect is to intimately disperse the TPU material throughout the rubber and improve its effectiveness.
  • the vulcanized rubber composition of this invention can be used for various purposes.
  • the rubber compounds may be in the form of a tire, hose, belt (particularly movement transmission belt or transportation belt), roller or shoe sole or rubber-fabric composite.
  • Another object of the present invention relates to a cured composition, as obtained by vulcanizing the said vulcanizable composition of the invention. More particularly the said cured composition is adhering on polar substrates selected from metal, polar fabrics, or other polar elastomers.
  • a last object of the invention is an article which comprises the said cured composition as defined above.
  • Such articles include tire, hose, belt, roller, or shoe sole or a rubber-fabric composite.
  • a TPU was prepared by a one-shot procedure in which a reaction vessel is charged with lOOg polybudiene diol resin, 2000 g/mol, 65% vinyl (Krasol LBH 2000 brand from Sartomer Company), 15. Ig 2-ethyl-l,3-hexanediol (EHD) chain extender, and 1.6g stabilizer (Tinuvin B75 brand). The mixture was heated to 80-90° C. An amount of diphenylmethane 4,4'- diisocyanate (MDI) preheated to about 45° C sufficient to maintain the NCO index at 1.0 was added, resulting in a TPU with 35 weight percent hard segment designated as Poly bd 2035 TPU having properties reported in Table 1.
  • MDI diphenylmethane 4,4'- diisocyanate
  • Example 2 Comparative Thermoplastic Polymers Properties of the following three polymers used in comparative experiments reported in the following examples are also reported in Table I: polyether TPU (Estane 58630, Noveon, Inc.), styrene-butadiene-styrene triblock TPE (D-1133, Kraton Polymers, LLC) and styrene- ethylene/butylene-styrene triblock TPE (G-1650, Kraton Polymers, LLC).
  • polyether TPU Estane 58630, Noveon, Inc.
  • styrene-butadiene-styrene triblock TPE D-1133, Kraton Polymers, LLC
  • G-1650 styrene- ethylene/butylene-styrene triblock TPE
  • Compounded stocks of each thermoplastic described in Table 1 with rubber were mixed in a preparatory mixer of 450 cc volume in two stages.
  • the non-productive stage was mixed for 3 minutes, at 100 rpm and 100°C initial temperature.
  • the non-productive compound was milled between stages.
  • the productive stage was mixed for 2 minutes at 60 rpm and 60°C initial temperature.
  • the determination of vulcanization behavior of the productive compounds was performed on a moving die rheometer (MDR) according to ASTM D 5289. Cure temperature for sample preparation is 160 0 C.
  • the individual calculated t 9 o times were used for subsequent test sample preparation. Stress-strain and tear data were acquired on a tensile tester following ASTM D 412 and D 624 (Die C).
  • Rebound testing was performed according to ASTM D 1054. Peel adhesion testing was performed based on ASTM D1876-01. The test was modified by restricting adhesion area to a 7.62 cm (3") by 0.635 cm (0.25") window by masking with a nylon insert between the substrates.
  • the formulations of the invention, Compound B, the control, Compound A, and the comparatives, Compounds C, D, and E, are set forth in Table II. Table II
  • Compound A is a control with no thermoplastic additive.
  • Compound B contains Poly bd 2035 TPU.
  • Compounds C-E are comparative samples.
  • Compound C contains a polyether TPU (Estane 58630)
  • Compound D contains a styrene-butadiene-styrene triblock TPE (Kraton D-1133)
  • Compound E contains a styrene-ethylene/butylene-styrene triblock TPE (Kraton D-1650.)
  • Table HI provides the data from vulcanizate testing. Table HI
  • Compounds A-E have similar 100% modulus values. All compounds incorporating thermoplastic additives exhibit elevated high strain modulus (300%) and improved tensile and tear strength compared to the control. However, only Compound B maintained hysteresis (as demonstrated in 100 0 C pendulum rebound data, higher value better).
  • Peel adhesion tests were performed against a polyurethane substrate in order to demonstrate the adhesive properties of a polyisoprene-based compound that contains polybutadiene TPU as an additive. Peel adhesion testing between these thermoplastic grades and poly(urethanes) shows that in the class of thermoplastic materials containing diene soft segments, only the TPU demonstrated adhesion to a polar polyurethane substrate, Adiprene® L 100, Uniroyal cured with 4,4' - methylene-bis (2-chloroaniline). Pure substrates were used. The SBS grade delaminated at the interface with the mode of failure being adhesive. The polybutadiene TPU produced an adhesive strength of 28.6 kg/cm.
  • polybutadiene-based TPU in elastomeric compounds can also increase the adhesion of the vulcanizate to polar substrates.
  • the polybutadiene TPU was added to a polyisoprene (IR) compound.
  • IR polyisoprene
  • Table IV The formulation is provided in Table IV in which Compound G represents the invention, Compound F is the control, and Compounds H and I are additional compounds representing the invention, for comparison. Mix procedures were identical to that outlined above.
  • thermoplastic polyurethane (Estane 58630,
  • Table V provides the results from the peel adhesion testing.
  • the natural rubber compound containing the polybutadiene TPU exhibits improvements in adhesion at loadings greater than 10 phr.
  • Compound G (5 phr) in the illustrated formulation showed no improvement compared to the control (no TPU).
  • adhesion to the polyurethane substrate improves with loading. Improvements in adhesion correspond to the solubility limit of the TPU in cis-polyisoprene.
  • By dynamic mechanical testing in tension (- 100 0 C to 100 0 C at 11 Hz and 0.1% strain amplitude) the TPU forms a distinct phase from the polyisoprene matrix at 10 phr. This point of incompatibility is manifested as the evolution of a second peak in the tangent delta profile. The two peaks are readily identified as they correspond to the separate glass transition temperatures of the components.

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DE602007002450D1 (de) 2006-07-26 2009-10-29 Sumitomo Rubber Ind Gummimischung und Reifen damit
US9944763B2 (en) 2009-12-01 2018-04-17 Gates Corporation Polyurea-urethane cord treatment for power transmission belt and belt
FR2969631B1 (fr) 2010-12-23 2012-12-28 Michelin Soc Tech Pneumatique dont la bande de roulement comporte un copolymere bloc polyurethane thermoplastique
US9879131B2 (en) 2012-08-31 2018-01-30 Soucy Techno Inc. Rubber compositions and uses thereof
DE102013217661B4 (de) * 2013-09-04 2023-01-12 Leibniz-Institut Für Polymerforschung Dresden E.V. Verfahren zur Herstellung von Blends aus thermoplastischen Polyurethanen und Kautschuken und damit hergestellte Blends
WO2015054779A1 (en) 2013-10-18 2015-04-23 Soucy Techno Inc. Rubber compositions and uses thereof
CA2925929C (en) 2013-12-19 2018-12-04 Soucy Techno Inc. Rubber compositions and uses thereof
WO2017162529A1 (de) 2016-03-21 2017-09-28 Basf Se Vernetztes polyurethan
CN107417879B (zh) * 2016-05-24 2020-06-09 北京化工大学 一种高性能轮胎用溶聚丁苯橡胶-聚氨酯弹性体材料及制备方法
JP2019522573A (ja) 2016-06-29 2019-08-15 ナイキ イノヴェイト シーヴィーＮｉｋｅ Ｉｎｎｏｖａｔｅ Ｃ．Ｖ． 多層構造体及びその使用
DE102016218978A1 (de) * 2016-09-30 2018-04-05 Tesa Se Thermisch vulkanisierbarer Klebstoff und daraus hergestelltes Klebeband
TWI791392B (zh) 2017-06-01 2023-02-01 荷蘭商耐克創新有限合夥公司 具有多個結合區域之物件
JP6961825B2 (ja) 2017-12-15 2021-11-05 株式会社ブリヂストン ポリウレタン含有トレッドゴム組成物及びその関連方法
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