Classifications

• • 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 ; Homo- or copolymers of other iso-olefins

Definitions

• the present invention relates to polymers useful as modifiers for tire treads.
• the tire tread compound is an important compound in a tire that dictates wear, traction, and rolling resistance. It is a technical challenge to deliver excellent traction, low rolling resistance while providing good tread wear. The challenge lies in the trade-off between wet traction and rolling resistance/tread wear. Raising the compound glass transition temperature (Tg) provides better wet traction but, at the same time, increases the rolling resistance and tread wear. There is still a need to develop a tread compound additive that can provide good wet traction without increasing rolling resistance and tread wear.
• Tg compound glass transition temperature
• Functionalized SBR styrene butadiene rubber
• NANOPRENETM sub-micron to micron sized gels from Lanxess with cross-linked butadiene cores and acrylic shells
• Nanoprene can only deliver limited improvement in wet traction.
• an elastomeric composition comprising, per 100 parts by weight of rubber (phr): about 60 to about 100 phr of polybutadiene having a cis-1,4 linkage content of at least 95%; about 5 to about 40 phr of a styrene/butadiene copolymer; a curative agent; an antioxidant; about 50 to about 80 phr hydrocarbon resin; about 100 to about 140 phr silica; about 1 to about 20 phr silane coupling agent and about 5 to about 30 phr of a polymer selected from the group consisting of ethylene-propylene-diene terpolymer, butyl rubber, poly(isobutylene-co-para-methylstyrene) and poly(isobutylene-co-para-methylstyrene-co- isoprene) terpolymer.
• Fig. 1 illustrates a 1 H-NMR spectra of partially epoxidized butyl rubber obtained via a reactive mixing process.
• Fig. 2 illustrates a 1 H-NMR spectra of partially epoxidized ethylene-propylene- diene terpolymer obtained by a reactive mixing process.
• Fig. 3 illustrates a 1 H-NMR spectra of thioacetate functionalized poly(isobutylene- co-para-methylstyrene) obtained by a solution process.
• Fig. 4 illustrates a 1 H-NMR spectrum of mercaptobenzothiazole functionalized poly(isobutylene-co-para-methylstyrene) obtained by a reactive mixing process.
• Fig. 5 illustrates a 1 H-NMR spectra of poly(isobutylene-co-para-methylstyrene)- amine ionomer obtained by a reactive mixing process.
• Fig. 6 illustrates a 1 H-NMR spectra of butyl-amine ionomer obtained by a reactive mixing process.
• Fig. 7 illustrates a 1 H-NMR spectra of a poly(isobutylene-co-para-methylstyrene- co-isoprene) terpolymer 1.
• Fig. 8 illustrates a 1 H-NMR spectra of ethylene-propylene-diene terpolymer 1.
• This invention is directed to the use of polymer additives based on butyl rubber, ethylene-propylene-diene terpolymer, poly(isobutylene-co-para-methylstyrene) polymer and poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer. These polymers, which may be functionalized, are useful in tire tread compositions. [0016] It is a technical challenge to deliver excellent traction, low rolling resistance while providing good tread wear. The challenge lies in the trade-off between wet traction and rolling resistance/tread wear.
• One way to improve rolling resistance and wet braking is to incorporate a series of polyolefin additives based on butyl rubber, ethylene-propylene-diene terpolymer, poly(isobutylene-co-para-methylstyrene) polymer and poly(isobutylene-co-para- methylstyrene-co-isoprene) terpolymer in tire tread compositions.
• an elastomeric composition comprises, per 100 parts by weight of rubber (phr): about 60 to about 100 phr of polybutadiene having a cis-1,4 linkage content of at least 95%; about 5 to about 40 phr of a styrene/butadiene copolymer; a curative agent; an antioxidant; about 50 to about 80 phr hydrocarbon resin; about 100 to about 140 phr silica; about 1 to about 20 phr silane coupling agent and about 5 to about 30 phr of a polymer selected from the group consisting of ethylene-propylene-diene terpolymer, butyl rubber, poly(isobutylene-co-para-methylstyrene) and poly(isobutylene-co-para-methylstyrene-co- isoprene) terpolymer.
• the butyl copolymer rubbers are prepared by polymerizing (i) C4-C7 isoolefins with (ii) C4-C14 conjugated dienes.
• the butyl copolymer rubbers contain from 85 to 99.5 mol% C4-C7 isoolefins and from 0.5 to 15 mol% C4-C14 conjugated dienes.
• the butyl copolymer rubber is Butyl 365 (ExxonMobil Chemical).
• the butyl copolymer rubbers may be halogenated.
• the halogenated butyl copolymer rubber is ExxonTM bromobutyl rubber or ExxonTM chlorobutyl rubber.
• the ethylene-propylene-diene terpolymers are prepared by polymerizing (i) propylene with (ii) at least one of ethylene and C4-C20 a-olefins and (iii) one or more dienes such as ethylidene norbomene.
• the ethylene-propylene-diene terpolymer may be halogenated.
• the ethylene-propylene-diene terpolymer is amorphous ethylene-propylene-diene terpolymer.
• the poly(isobutylene-co-para-methylstyrene) polymers (BIMSM) are prepared as described in U.S. Pat. No.
• a catalyst solution of ethyl aluminum dichloride in methyl chloride is added to a feed blend of methyl chloride, isobutylene and para- methylstyrene in a reactor.
• the reactor is quenched by cold methanol, the methyl chloride is flashed off and the BIMSM polymer is washed in methanol.
• the poly(isobutylene- co-para-methylstyrene) polymer is ExxproTM NPX 1602 (ExxonMobil Chemical).
• the poly(isobutylene-co-para-methylstyrene) polymer may be halogenated.
• the halogenated poly(isobutylene-co-para-methylstyrene) polymer is a brominated poly(isobutylene-co-para-methylstyrene) polymer such as ExxproTM 3035, 3433, 3563 or 3745.
• the poly(isobutylene-co-para-methylstyrene) polymer may be functionalized as described in U.S. Pat. No. 5,162,445 or as described herein.
• the poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymers are prepared as described in U.S. Patent No. 6,960,632 or as described herein.
• Poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer is prepared by adding an initiator/co-initiator solution to a mixed para-methyl styrene, isoprene, and isobutylene monomer solution using standard slurry cationic polymerization techniques.
• the poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer may be halogenated.
• the tire tread composition is an important aspect in a tire that dictates wear, traction, and rolling resistance. It is a technical challenge to deliver excellent traction and low rolling resistance while providing good tread wear. The challenge lies in the trade-off between wet traction and rolling resistance/tread wear. Typically, raising the composition’ s glass transition temperature (Tg) would provide good wet traction but, at the same time, increase the rolling resistance and tread wear.
• Tg glass transition temperature
• tread compositions described herein is suitable for use in all-season tires. That is, the mechanical properties of the tread compounds indicate that corresponding tires would have enhanced handling (e.g., greater traction and grip) and improved braking capabilities.
• butyl rubber or “butyl rubber copolymer” as used in the specification means copolymers of C4 to C7 isoolefins and C4 to C14 conjugated dienes which comprise about 0.5 to about 15 mol% conjugated diene and about 85 to 99.5 mol% isoolefin.
• Illustrative examples of the isoolefins which may be used in the preparation of butyl rubber are isobutylene, 2-methyl- 1-propene, 3-methyl- 1 -butene, 4-methyl- 1-pentene and beta-pinene.
• conjugated dienes which may be used in the preparation of butyl rubber are isoprene, butadiene, 2,3-dimethyl butadiene, piperylene, 2, 5-dimethylhexa-2, 4-diene, cyclopentadiene, cyclohexadiene and methylcyclopentadiene.
• the preparation of butyl rubber is described in U.S. Patent No. 2,356,128 and is further described in an article by R. M. Thomas et al. in Ind. & Eng. Chem., vol. 32, pp. 1283 et seq., Oct., 1940.
• Butyl rubber generally has a viscosity average molecular weight between about 100,000 to about 1,500,000, preferably about 250,000 to about 800,000 and a Wijs Iodine No. (INOPO) of about 0.5 to 50, preferably 1 to 20 (for a description of the INOPO test, see Industrial and Engineering Chemistry, Vol. 17, p. 367, 1945).
• INOPO Wijs Iodine No.
• butyl rubber also encompasses functionalized butyl rubber compounds described herein.
• the butyl rubber may have a C4 to C7 isoolefin(s) amount of from about 85 to about 99.5 mol%, or from about 90 to about 99.5 mol% or from about 95 to about 99.5 mol%, based on the weight of the butyl rubber.
• the butyl rubber may have a C4 to C14 conjugated diene(s) amount of from about 0.5 to about 15 mol%, or from about 0.5 to about 10 mol% or from about 0.5 to about 5 mol%, based on the weight of the butyl rubber.
• BUTYL 365 or 365S butyl, isobutylene-isoprene rubber (HR), available from ExxonMobil Chemical Company).
• BUTYL 365 or 365S is a copolymer of isobutylene and isoprene with about 2.3 mole% unsaturation.
• Exxon BUTYL 065 or 065 S (copolymer of isobutylene and isoprene with about 1.05 mole% unsaturation)
• Exxon BUTYL 068 (copolymer of isobutylene and isoprene with about 1.15 mole% unsaturation)
• Exxon BUTYL 268 or 268S copolymer of isobutylene and isoprene with about 1.7 mole% unsaturation.
• the butyl copolymer rubber may be halogenated.
• the halogenated butyl copolymer rubber is brominated poly (isobutylene-co-isoprene).
• examples of halogenated butyl copolymer rubbers are ExxonTM bromobutyl rubber or ExxonTM chlorobutyl rubber.
• An example of a halogenated butyl copolymer is Bromobutyl 2222 (ExxonMobil Chemical).
• Another example of a halogenated butyl rubber is Exxon SBB 6222 (Exxon Mobil), a brominated star branched butyl rubber.
• An example of a chlorinated butyl copolymer is Chlorobutyl 1066 and 1068 (ExxonMobil Chemical).
• the butyl rubber is functionalized with sulfur.
• the butyl rubber is functionalized with sulfur and an activator.
• the activator is zinc oxide or stearic acid.
• the activator is a combination of zinc oxide and stearic acid.
• the inventive compositions may include the butyl rubber in an amount of from about 5 phr to about 30 phr, from about 5 phr to about 25 phr or from about 10 phr to about 20 phr.
• the “ethylene-propylene-diene terpolymer” as used herein may be any polymer comprising propylene and other comonomers.
• the term “polymer” refers to any carbon- containing compound having repeat units from one or more different monomers.
• the term “terpolymer” as used herein refers to a polymer synthesized from three different monomers.
• ethylene-propylene-diene terpolymer also encompasses functionalized ethylene-propylene-diene terpolymer compounds described herein.
• Terpolymers in some embodiments, may be produced (1) by mixing all three monomers at the same time or (2) by sequential introduction of the different comonomers. The mixing of comonomers may be done in one, two, or possible three different reactors in series and/or in parallel.
• the ethylene-propylene-diene terpolymer comprises (i) propylene- derived units, (ii) a-olefin-derived units and (iii) diene-derived units.
• the ethylene-propylene- diene terpolymer may be prepared by polymerizing (i) propylene with (ii) at least one of ethylene and C4-C20 a-olefins and (iii) one or more dienes.
• the comonomers may be linear or branched.
• Preferred linear comonomers include ethylene or C4 to Cx a-olefins, more preferably ethylene, 1-butene, 1-hexene, and 1-octene, even more preferably ethylene or 1 -butene.
• Preferred branched comonomers include 4-methyl- 1-pentene, 3 -methyl- 1-pentene, and 3,5,5-trimethyl-l-hexene.
• the comonomers may include styrene.
• the dienes may be conjugated or non-conjugated.
• the dienes are non- conjugated.
• Illustrative dienes may include, but are not limited to, 5-ethylidene-2-norbomene (ENB); 1,4-hexadiene; 5-methylene-2-norbomene (MNB); 1,6-octadiene; 5-methyl-l,4- hexadiene; 3,7-dimethyl-l,6-octadiene; 1,3-cyclopentadiene; 1,4-cyclohexadiene; vinyl norbomene (VNB); dicyclopendadiene (DCPD); and combinations thereof.
• the diene is ENB or VNB.
• the ethylene-propylene-diene terpolymer comprises an ENB content of from 0.5 wt% to 8 wt% based on the weight of the terpolymer, or from 2 wt% to 6 wt%, or from 3 wt% to 5 wt%. More preferably, the ethylene-propylene-diene terpolymer comprises an ENB content of from 0.5 wt% to 3 wt%.
• the ethylene-propylene-diene terpolymer may have a propylene amount of from 65 wt% to 95 wt%, or from 70 wt% to 95 wt%, or from 75 wt% to 95 wt%, or from 80 wt% to 95 wt%, or from 83 wt% to 95 wt%, or from 84 wt% to 95 wt%, or from 84 wt% to 94 wt%, or from 72 wt% to 95 wt%, or from 80 wt% to 93 wt%, or from 85 wt% to 89 wt%, based on the weight of the polymer.
• the balance of the ethylene -propylene-diene terpolymer comprises at least one of ethylene and C4-C20 a-olefin and one or more dienes.
• the a-olefin may be ethylene, butene, hexane, or octene. When two or more a-olefins are present in the polymer, ethylene and at least one of butene, hexane, or octene are preferred.
• the ethylene-propylene-diene terpolymer comprises from 2 to 30 wt% of C2 and/or C4-C20 a-olefins based the weight of the ethylene-propylene-diene terpolymer.
• the combined amounts of these olefins in the polymer is preferably at least 2 wt% and falling within the ranges described herein.
• the ethylene-propylene-diene terpolymer comprises an ethylene content of from 5 wt% to 25 wt% based on the weight of the terpolymer, or from 8 wt% to 12 wt%.
• the ethylene-propylene-diene terpolymer comprises a diene content of from 1 wt% to 16 wt% based on the weight of the terpolymer, or from 1 wt% to 12 wt%, or 2 wt% to 6 wt%, or from 2 wt% to 6 wt%.
• the ethylene-propylene-diene terpolymer is halogenated.
• the ethylene-propylene-diene terpolymer may be halogenated by methods known in the art or by methods described in U.S. Patent No. 4,051,083.
• the synthesis of the ethylene-propylene-diene terpolymer utilizes a bis((4-triethylsilyl)phenyl)methylene(cyclopentadienyl)(2,7-di-tert-butyl-fluoren-9- yl) hafnium dimethyl catalyst precursor.
• a bis((4-triethylsilyl)phenyl)methylene(cyclopentadienyl)(2,7-di-tert-butyl-fluoren-9- yl) hafnium dimethyl catalyst precursor could also be used.
• the synthesis of the ethylene- propylene-diene terpolymer also utilizes a dimethylanilinium tetrakis(pentafluorophenyl)borate activator but dimethylanilinium- tetrakis(heptafluoronaphthyl)borate and other non-coordinating anion type activators or MAO could also be used.
• a copolymer material is produced in the presence of ethylene, propylene, ethylidene norbornene, and a catalyst comprising the reaction product of N,N- dimethylanilinium tetrakis(pentafluorophenyl)borate and [cyclopentadienyl(2,7-di-t- butylfluorenyl)di-p-triethylsilanephenylmethane] hafnium dimethyl.
• the copolymer solution emerging from the reactor is quenched and then devolatilized using conventionally known devolatilization methods, such as flashing or liquid phase separation, first by removing the bulk of the isohexane to provide a concentrated solution, and then by stripping the remainder of the solvent in anhydrous conditions using a devolatilizer so as to end up with a molten polymer composition containing less than 0.5 wt% of solvent and other volatiles.
• the molten polymer composition was advanced by a screw to a pelletizer from which the ethylene-propylene-diene terpolymer composition pellets are submerged in water and cooled until solid.
• the ethylene-propylene-diene terpolymer may have a melt flow rate (MFR, 2.16 kg weight at 230°C), equal to or greater than 0.1 g/10min as measured according to the ASTM D- 1238-13.
• the MFR (2.16 kg at 230°C) is from 0.5 g/10min to 200 g/lOmin, or from 0.5 g/lOmin to 100 g/lOmin, or from 0.5 g/lOmin to 30 g/10min, or from 0.5 g/lOmin to 10 g/lOmin, or from 0.5 g/lOmin to 5 g/lOmin, or from 0.5 g/lOmin to 2 g/10min, or from 0.1 g/lOmin to 15 g/lOmin.
• the ethylene-propylene-diene terpolymer may have a heat of fusion (H f ) determined by the DSC procedure described herein, which is greater than or equal to 0 Joules per gram (J/g), and is equal to or less than 80 J/g, or equal to or less than 75 J/g, or equal to or less than 70 J/g, or equal to or less than 60 J/g, or equal to or less than 50 J/g, or equal to or less than 35 J/g.
• the H f is 0 J/g.
• the crystallinity of the ethylene-propylene-diene terpolymer may be expressed in terms of percentage of crystallinity (i.e., %crystallinity), as determined according to the DSC procedure described herein.
• the ethylene-propylene-diene terpolymer may have a %crystallinity of from 0% to 40%. Preferably, the %crystallinity is 0%.
• the ethylene- propylene-diene terpolymer preferably may have a single broad melting transition.
• the ethylene-propylene-diene terpolymer may show secondary melting peaks adjacent to the principal peak, but for purposes herein, such secondary melting peaks are considered together as a single melting point, with the highest of these peaks (relative to baseline as described herein) being considered as the melting point of the ethylene-propylene-diene terpolymer.
• the Differential Scanning Calorimetry (DSC) procedure may be used to determine heat of fusion and melting temperature of the ethylene-propylene-diene terpolymer. The method is as follows: approximately 6 mg of material placed in microliter aluminum sample pan.
• the sample is placed in a Differential Scanning Calorimeter (Perkin Elmer Pyris 1 Thermal Analysis System) and is cooled to -80°C.
• the sample is heated at 10°C/min to attain a final temperature of 120°C.
• the sample is cycled twice.
• the thermal output recorded as the area under the melting peak of the sample, is a measure of the heat of fusion and may be expressed in Joules per gram of polymer and is automatically calculated by the Perkin Elmer System.
• the melting point is recorded as the temperature of the greatest heat absorption within the range of melting of the sample relative to a baseline measurement for the increasing heat capacity of the polymer as a function of temperature.
• the ethylene-propylene-diene terpolymer may be a blend of discrete random ethylene-propylene-diene terpolymers as long as the polymer blend has the properties of the ethylene-propylene-diene terpolymer as described herein.
• the number of ethylene-propylene- diene terpolymers may be three or less, or two or less.
• the ethylene-propylene-diene terpolymer may include a blend of two ethylene-propylene-diene terpolymers differing in the olefin content, the diene content, or the both.
• the ethylene-propylene-diene terpolymer is functionalized with sulfur.
• the ethylene-propylene-diene terpolymer is functionalized with sulfur and an activator.
• the activator is zinc oxide or stearic acid.
• the activator is a combination of zinc oxide and stearic acid.
• the inventive compositions may include the ethylene -propylene-diene terpolymer in an amount of from about 5 phr to about 30 phr, or from about 5 phr to about 25 phr, or from about 10 phr to about 20 phr.
• poly(isobutylene-co-para-methylstyrene) as used in the specification means a co-polymer of isobutylene and para-methylstyrene.
• poly(isobutylene-co-para-methylstyrene) also encompasses functionalized poly(isobutylene-co-para-methylstyrene) compounds described herein.
• the poly(isobutylene-co-para-methylstyrene) polymer is ExxproTM NPX 1602 (ExxonMobil Chemical).
• the poly(isobutylene-co-para- methylstyrene) polymer is halogenated. Brominated poly(isobutylene-co-para-methylstyrene) polymer may be obtained, for example, as Exxpro 3035, 3433, 3563 or 3745, a trademark of the ExxonMobil Chemical Company.
• Exxpro 3035, 3433, 3563 and 3745 are brominated copolymers of isobutylene and paramethylstyrene containing about 0.47, 0.75, 0.85 and 1.2 mol% benzylic bromine, respectively.
• the poly(isobutylene-co-para-methylstyrene) is functionalized with sulfur.
• the poly(isobutylene-co-para-methylstyrene) is functionalized with sulfur and an activator.
• the activator is zinc oxide or stearic acid.
• the activator is a combination of zinc oxide and stearic acid.
• the inventive compositions may include the poly(isobutylene-co-para- methylstyrene) polymer in an amount of from 5 phr to 30 phr, or from 5 phr to 25 phr, or from 10 phr to 20 phr.
• poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer as used in the specification means a terpolymer comprising isobutylene, para-methylstyrene and isoprene polymers.
• poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer also encompasses functionalized poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer compounds described herein.
• the poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer contains from 4-8 mol% p-methylstyrene, 0.2-2 mol% isoprene and 90-95 mol% isobutylene based on the terpolymer.
• the poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer is functionalized with sulfur.
• the poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer is functionalized with sulfur and an activator.
• the activator is zinc oxide or stearic acid.
• the activator is a combination of zinc oxide and stearic acid.
• the inventive compositions may include the poly(isobutylene-co-para- methylstyrene-co-isoprene) terpolymer in an amount of from about 5 phr to about 30 phr, or from about 5 phr to about 25 phr, or from about 10 phr to about 20 phr.
• the term “functionalized polymer” as used in the specification means an olefin polymer which has a functional group, such as an epoxy, thioacetate, mercaptobenzothiazole, amine ionomer or phosphine ionomer functional group. Functionalization of a polymer can be implemented as described herein or as known in the art.
• the functionalized polymer has an epoxy, thioacetate, mercaptobenzothiazole, amine ionomer or phosphine ionomer functional group.
• the functionalized polymer has an epoxy functional group.
• Functionalized polymers with an epoxy functional group can be prepared by adding 3- chloroperbenzoic acid to a polyolefin polymer via a reactive mixing process or by the method described herein.
• 3-chloroperbenzoic acid other oxidizing agents may be hydrogen peroxide or hypochloride in t-butanol.
• the polyolefin polymer is a ethylene-propylene-diene terpolymer, butyl rubber, poly(isobutylene-co-para-methylstyrene) or a poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer.
• the epoxy functionalized polymer is epoxidized butyl rubber or epoxidized ethylene-propylene-diene terpolymer.
• the epoxy functionalized polymer is partially epoxidized.
• the epoxy functionalized polymer is partially epoxidized ethylene-propylene-diene terpolymer.
• the functionalized polymer has a thioacetate functional group.
• Functionalized polymers with a thioacetate functional group can be prepared by nucleophilic substitution of a polyolefin polymer with potassium thioacetate by a solution or a reactive mixing process.
• the polyolefin polymer is butyl rubber, poly(isobutylene- co-para-methylstyrene) or a poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer.
• the thioacetate functionalized polymer is thioacetate functionalized poly(isobutylene-co-para-methylstyrene) or thioacetate functionalized butyl rubber.
• the functionalized polymer has a mercaptobenzothiazole functional group.
• Functionalized polymers with a mercaptobenzothiazole functional group can be prepared by reacting tetrabutyl ammonium bromide (TBAB) and sodium mercaptobenzothiazole with a polyolefin polymer by a reactive mixing process.
• TBAB tetrabutyl ammonium bromide
• the polyolefin polymer is butyl rubber, poly(isobutylene-co-para-methylstyrene) or a poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer.
• the mercaptobenzothiazole functionalized polymer is mercaptobenzothiazole functionalized poly(isobutylene-co-para-methylstyrene) or mercaptobenzothiazole functionalized butyl rubber.
• the functionalized polymer has an amine ionomer functional group.
• Functionalized polymers with an amine ionomer functional group can be prepared by reacting dimethylsoyaalkylamine with a polyolefin polymer by a reactive mixing process or by the method described herein.
• the polyolefin polymer is, butyl rubber, poly(isobutylene-co-para-methylstyrene) or a poly(isobutylene-co-para-methylstyrene-co- isoprene) terpolymer.
• the amine ionomer functionalized polymer is partially functionalized.
• the amine ionomer functionalized polymer is modified BIMSM-amine ionomer or modified butyl-amine ionomer.
• the functionalized polymer has a phosphine ionomer functional group.
• Functionalized polymers with a phosphine ionomer functional group can be prepared by reacting diphenyldiphosphino styrene with a polyolefin polymer by a reactive mixing process.
• the polyolefin polymer is butyl rubber, poly(isobutylene-co-para- methylstyrene) or a poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer.
• the phosphine ionomer functionalized polymer is partially functionalized.
• the phosphine ionomer functionalized polymer is modified BIMSM- phosphine ionomer or modified butyl-phosphine ionomer.
• the functionalized polymer when the polymer is ethylene-propylene-diene terpolymer or butyl rubber, the functionalized polymer has an epoxy, thioacetate, mercaptobenzothiazole, amine ionomer or phosphine ionomer functional group.
• the functionalized polymer has a thioacetate, mercaptobenzothiazole, amine ionomer or phosphine ionomer functional group.
• the polymer selected from the group consisting of ethylene-propylene-diene terpolymer, butyl rubber, poly(isobutylene-co-para-methylstyrene) and poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer is functionalized with sulfur.
• the polymer selected from the group consisting of ethylene- propylene-diene terpolymer, butyl rubber, poly(isobutylene-co-para-methylstyrene) and poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer is functionalized with sulfur and an activator.
• the activator is zinc oxide or stearic acid.
• the activator is a combination of zinc oxide and stearic acid.
• the inventive tire tread compositions also comprise an elastomer.
• the range of the elastomer is from 5 to 75% by weight of the tire tread composition.
• Suitable elastomers include, for example, diene elastomers.
• diene elastomers include, for example, diene elastomers.
• “Diene elastomer” is understood to mean, in known manner, an elastomer resulting at least in part (homopolymer or copolymer) from diene monomers (monomers bearing two double carbon-carbon bonds, whether conjugated or not).
• a diene elastomer can be “highly unsaturated,” resulting from conjugated diene monomers, which have a greater than 50% molar content of units.
• each diene elastomer having a Tg from -75°C to 0°C is selected from the group consisting of natural polyisoprenes, synthetic polyisoprenes having a cis-1,4 linkage content greater than 95%, styrene/butadiene/isoprene terpolymers and a mixture of these elastomers, and each diene elastomer having a Tg from -110°C to -75°C, preferably from -100°C to -80°C, is selected from the group consisting of polybutadienes having a cis-1,4 linkage content greater than 90% and isoprene/butadiene copolymers comprising butadiene units in an amount equal to or greater than 50%.
• the elastomeric composition comprises a diene elastomer is about 60 to about 100 phr of polybutadiene having a cis-1,4 linkage content of at least 95%. In another embodiment, the elastomeric composition comprises a diene elastomer in about 70 to about 90 phr of polybutadiene having a cis-1,4 linkage content of at least 95%.
• the composition comprises a blend of at least one of the polybutadienes having a cis-1,4 linkage content greater than 90% with at least one of the natural or synthetic polyisoprenes (having a cis-1,4 linkage content greater than 95%).
• An example of a polybutadiene with a cis-1,4 linkage content is BUDENE ® 1208 available from Goodyear Chemical.
• diene elastomers can be classified into two categories: “essentially unsaturated” or “essentially saturated”.
• the term “essentially unsaturated” is understood to mean generally a diene elastomer resulting at least in part from conjugated diene monomers having a level of units of diene origin (conjugated dienes) which is greater than 15% (mol %); thus it is that diene elastomers such as butyl rubbers or copolymers of dienes and of alpha-olefins of EPDM type do not come within the preceding definition and can in particular be described as “essentially saturated” diene elastomers (low or very low level of units of diene origin, always less than 15%).
• the term “highly unsaturated” diene elastomer is understood to mean in particular a diene elastomer having a level of units of diene origin (conjugated dienes) which is greater than 50%.
• diene elastomer capable of being used herein is understood more particularly to mean: (a) any homopolymer obtained by polymerization of a conjugated diene monomer having from 4 to 12 carbon atoms; (b) any copolymer obtained by copolymerization of one or more conjugated dienes with one another or with one or more vinylaromatic compounds having from 8 to 20 carbon atoms; (c) a ternary copolymer obtained by copolymerization of ethylene and of an alpha-olefin having 3 to 6 carbon atoms with a non- conjugated diene monomer having from 6 to 12 carbon atoms, such as, for example, the elastomers obtained from ethylene and propylene with a non-conjugated diene monomer of the abovementioned type, such as, in particular, 1,4-hexadiene, ethylidenenorbornene or dicyclopentadiene; (d)
• conjugated dienes 1,3 -butadiene, 2- methyl- 1,3 -butadiene, 2,3-di(Ci-Cs alkyl)- 1,3-butadienes, such as, for example, 2,3-dimethyl- 1,3 -butadiene, 2, 3-diethyl-l, 3-butadiene, 2-methyl-3-ethyl-l, 3-butadiene or 2-methyl-3- isopropyl-1, 3-butadiene, an aryl-1, 3-butadiene, 1,3-pentadiene or 2,4-hexadiene.
• vinylaromatic compounds styrene, ortho-, meta- or para-methylstyrene, the “vinyltoluene” commercial mixture, para-(tert-butyl)styrene, methoxystyrenes, chlorostyrenes, vinylmesitylene, divinylbenzene or vinylnaphthalene.
• the copolymers can comprise from 99% to 20% by weight of diene units and from 1% to 80% by weight of vinylaromatic units.
• the elastomers can have any microstructure which depends on the polymerization conditions used, in particular on the presence or absence of a modifying and/or randomizing agent and on the amounts of modifying and/or randomizing agent employed.
• the elastomers can, for example, be block, random, sequential or microsequential elastomers and can be prepared in dispersion or in solution; they can be coupled and/or star-branched or also functionalized with a coupling and/or star-branching or functionalization agent.
• polybutadienes in particular those having a content (molar %) of 1,2-units of from 4% to 80% or those having a content (molar %) of cis- 1,4-units of greater than 80%
• polyisoprenes butadiene/styrene copolymers, a styrene content of from 5% to 60% by weight and more particularly from 20% to 50%
• butadiene/isoprene copolymers in particular those having an isoprene content of from 5% to 90% by weight
• isoprene/styrene copolymers in particular those having a styrene content of from 5% to 50% by weight.
• butadiene/styrene/isoprene copolymers those having a styrene content of from 5% to 50% by weight and more particularly of from 10% to 40%, an isoprene content of from 15% to 60% by weight and more particularly from 20% to 50%, a butadiene content of from 5% to 50% by weight and more particularly of from 20% to 40%, a content (molar %) of 1,2-units of the butadiene part of from 4% to 85%, a content (molar %) of trans- 1,4-units of the butadiene part of from 6% to 80%, a content (molar %) of 1,2- plus 3,4-units of the isoprene part of from 5% to 70% and a content (molar %) of trans- 1,4-units of the isoprene part of from 10% to 50%, and more generally any butadiene/styrene/isoprene copolymer.
• the diene elastomer chosen from the group of the highly unsaturated diene elastomers consisting of polybutadienes (abbreviated to “BR”), synthetic polyisoprenes (IR), natural rubber (NR), butadiene copolymers, isoprene copolymers and the mixtures of these elastomers.
• Such copolymers are more preferably chosen from the group consisting of butadiene/styrene copolymers (SBR), isoprene butadiene copolymers (BIR), isoprene/styrene copolymers (SIR) and isoprene butadiene/styrene copolymers (SBIR).
• the SBR may be prepared in emulsion (“ESBR”) or an SBR prepared in solution (“SSBR”), or an SBR/BR, SBR/NR (or SBR IR), BR/NR (or BR/IR) or also SBR/BR/NR (or SBR BR IR) blend (mixture).
• ESBR emulsion
• SSBR SBR prepared in solution
• an SBR (ESBR or SSBR) elastomer use is made in particular of an SBR having a moderate styrene content, for example of from 20% to 35% by weight, or a high styrene content, for example from 35 to 45%, a content of vinyl bonds of the butadiene part of from 15% to 70%, a content (molar %) of trans- 1,4-bonds of from 15% to 75% and a Tg of from -10 °C to -55 °C; such an SBR can advantageously be used as a mixture with a BR preferably having more than 90% (molar %) of cis- 1,4-bonds.
• An example of a SBR is SPRINT AN ® SLR-4602, a partially coupled functionalized SBR.
• isoprene elastomer is understood to mean, in a known way, an isoprene homopolymer or copolymer, in other words a diene elastomer chosen from the group consisting of natural rubber (NR), synthetic polyisoprenes (IR), the various copolymers of isoprene and the mixtures of these elastomers.
• NR natural rubber
• IR synthetic polyisoprenes
• isoprene copolymers of isobutene/isoprene copolymers (butyl rubber IM), isoprene/styrene copolymers (SIR), isoprene/butadiene copolymers (BIR) or isoprene/butadiene/styrene copolymers (SBIR).
• isoprene copolymers of isobutene/isoprene copolymers (butyl rubber IM), isoprene/styrene copolymers (SIR), isoprene/butadiene copolymers (BIR) or isoprene/butadiene/styrene copolymers (SBIR).
• This isoprene elastomer is preferably natural rubber or a synthetic cis- 1,4- polyisoprene; use is preferably made, among these synthetic polyisoprenes, of the polyisoprenes having a level (molar %) of cis-1, 4-bonds of greater than 90%, more preferably still of greater than 98%.
• a natural rubber is SVR 3 CV60 available from Standard Vietnamese Rubber CV 60.
• SIR 10 Standard Indonesian Rubber
• compositions described herein can comprise a single diene elastomer or a mixture of several diene elastomers, it being possible for the diene elastomer or elastomers to be used in combination with any type of synthetic elastomer other than a diene elastomer, indeed even with polymers other than elastomers, for example thermoplastic polymers.
• Useful tire tread compositions can comprise, per 100 parts by weight of rubber (phr), about 60 to about 100 phr of polybutadiene having a cis-1,4 linkage content of at least 95%; about 5 to 40 phr of a styrene/butadiene copolymer; a curative agent; an antioxidant; about 50 to about 80 phr hydrocarbon resin; about 100 to about 140 phr silica; about 1 to about 20 phr silane coupling agent and about 5 to about 30 phr of a polymer selected from the group consisting of ethylene-propylene-diene terpolymer, butyl rubber, poly(isobutylene-co-para- methylstyrene) and poly(isobutylene-co-para-methylstyrene-co-isoprene) terpolymer.
• filler refers to any material that is used to reinforce or modify physical properties, impart certain processing properties, or reduce cost of an elastomeric composition.
• Examples of preferred filler include, but are not limited to, calcium carbonate, clay, mica, silica, silicates, talc, titanium dioxide, alumina, zinc oxide, starch, wood flour, carbon black, or mixtures thereof.
• the fillers may be any size and range, for example in the tire industry, from 0.0001 pm to 100 pm.
• silica is meant to refer to any type or particle size silica or another silicic acid derivative, or silicic acid, processed by solution, pyrogenic, or the like methods, including untreated, precipitated silica, crystalline silica, colloidal silica, aluminum or calcium silicates, fumed silica, and the like.
• Precipitated silica can be conventional silica, semi-highly dispersible silica, or highly dispersible silica.
• a preferred filler is commercially available by Rhodia Company under the trade name ZEOSILTM Z1165 or ZEOSILTM 1165 MP.
• the elastomeric composition comprises, per 100 parts by weight of rubber (phr), about 5 to 20 phr carbon black filler.
• an elastomeric composition comprises, per 100 parts by weight of rubber (phr), about 100 to about 140 phr silica. In another embodiment, the elastomeric composition comprises, per 100 parts by weight of rubber (phr), about 110 to about 130 phr of silica. In a further embodiment, the elastomeric composition comprises, per 100 parts by weight of rubber (phr), about 115 to about 120 phr silica.
• Use may be made of any type of reinforcing filler known for its capabilities of reinforcing a rubber composition which can be used for the manufacture of tires, for example an organic filler, such as carbon black, a reinforcing inorganic filler, such as silica, or a blend of these two types of filler, in particular a blend of carbon black and silica.
• the elastomeric composition of the present invention comprises a filler blend of carbon black and silica.
• All carbon blacks in particular blacks of the HAF, ISAF or SAF type, conventionally used in tires (“tire-grade” blacks) are suitable as carbon blacks. Mention will more particularly be made, among the latter, of the reinforcing carbon blacks of the 100, 200 or 300 series (ASTM grades), such as, for example, the N115, N134, N234, N326, N330, N339, N347 or N375 blacks, or also, depending on the applications targeted, the blacks of higher series (for example, N660, N683 or N772).
• the carbon blacks might, for example, be already incorporated in the isoprene elastomer in the form of a masterbatch (see, for example, International Applications WO 97/36724 or WO 99/16600).
• the carbon black is Vulcan ® 3 N330 from Cabot Corp. or Vulcan 7H N234 from Cabot Corp.
• the term “reinforcing inorganic filler” should be understood, in the present patent application, by definition, as meaning any inorganic or mineral filler, whatever its color and its origin (natural or synthetic), also known as “white filler”, “clear filler” or even “non-black filler”, in contrast to carbon black, capable of reinforcing by itself alone, without means other than an intermediate coupling agent, a rubber composition intended for the manufacture of tires, in other words capable of replacing, in its reinforcing role, a conventional tire-grade carbon black; such a filler is generally characterized, in a known way, by the presence of hydroxyl (—OH) groups at its surface.
• —OH hydroxyl
• reinforcing inorganic filler is not important, whether it is in the form of a powder, of microbeads, of granules, of beads or any other appropriate densified form.
• reinforcing inorganic filler is also understood to mean mixtures of different reinforcing inorganic fillers, in particular of highly dispersible siliceous and/or aluminous fillers as described below.
• Mineral fillers of the siliceous type in particular silica (S1O2), or of the aluminous type, in particular alumina (AI2O3), are suitable in particular as reinforcing inorganic fillers.
• the silica used can be any reinforcing silica known to a person skilled in the art, in particular any precipitated or pyrogenic silica exhibiting a BET surface and a CTAB specific surface both of less than 450 m 2 /g, preferably from 30 to 400 m 2 /g.
• HDS highly dispersible precipitated silicas
• ULTRASILTM 7000 and ULTRASILTM 7005 silicas from Degussa the ZEOSILTM 1165 MP, C5 MP and 1115 MP silicas from Rhodia
• HI-SILTM EZ150G silica from PPG
• Zeopol 8715, 8745 and 8755 silicas from Huber or silicas with a high specific surface.
• the silica is alone or a combination of silica compounds. In another embodiment, the silica is not a combination of silica compounds. In another embodiment, when the silica is a combination of silica compounds, one of the silica compounds has a BET surface of from 110 to 175 m 2 /g.
• inorganic filler being capable of being used, of reinforcing aluminum (oxide), hydroxides, titanium oxides or silicon carbides (see, for example, International Application No. WO 02/053634 or U.S. Publication No. 2004/0030017).
• the composition of the present invention does not contain the inorganic filler magnesium sulphate.
• the reinforcing inorganic filler is silica, preferably with a BET surface of from 45 to 400 m 2 /g, more preferably of from 60 to 300 m 2 /g. In one embodiment, the silica has a BET surface of from 110 to 175 m 2 /g.
• the term “coupling agent” is meant to refer to any agent capable of facilitating stable chemical and/or physical interaction between two otherwise non-interacting species, e.g., between a filler and a diene elastomer.
• Coupling agents cause silica to have a reinforcing effect on the rubber.
• Such coupling agents may be pre-mixed, or pre-reacted, with the silica particles or added to the rubber mix during the rubber/silica processing, or mixing, stage. If the coupling agent and silica are added separately to the rubber mix during the rubber/silica mixing, or processing stage, it is considered that the coupling agent then combines in situ with the silica.
• the coupling agent may be a sulfur-based coupling agent, an organic peroxide- based coupling agent, an inorganic coupling agent, a polyamine coupling agent, a resin coupling agent, a sulfur compound-based coupling agent, oxime-nitrosamine -based coupling agent and sulfur.
• preferred for a rubber composition for tires is the sulfur-based coupling agent.
• the coupling agent is at least bifunctional.
• bifunctional coupling agents include organosilanes or polyorganosiloxanes.
• suitable coupling agents include silane polysulfides, referred to as “symmetrical” or “unsymmetrical” depending on their specific structure.
• Silane polysulphides can be described by the formula (V):
• the Z symbols, which are identical or different correspond to one of the three formulae (VI): in which the R 1 radicals, which are substituted or unsubstituted and identical to or different from one another, represent a Ci-Cis alkyl, C 5 -C 18 cycloalkyl or C 6 -C 18 aryl group (preferably C 1 -C 6 alkyl, cyclohexyl or phenyl groups, in particular C 1 -C 4 alkyl groups, more particularly methyl and/or ethyl); the R 2 radicals, which are substituted or unsubstit
• Non-limiting examples of silane polysulphides include bis((Ci-C4)alkoxy(Ci- C4)alkylsilyl(Ci-C4)alkyl)polysulphides (in particular disulphides, trisulphides or tetrasulphides), such as, for example, bis(3-trimethoxysilylpropyl) or bis(3- triethoxysilylpropyl)polysulphides.
• Further examples include bis(3- triethoxysilylpropyl)tetrasulphide (TESPT) of formula [(C 2 H 5 0) 3 Si(CH 2 ) 3 S 2 ] 2 , or bis(triethoxysilylpropyl)disulphide (TESPD) of formula [(C 2 H 5 0) 3 Si(CH 2 ) 3 S] 2 .
• Other examples include bis (mono(Ci-C4)alkoxyldi(Ci-C4)alkylsilylpropyl)polysulphides (in particular disulphides, trisulphides or tetrasulphides), more particularly bis(monoethoxydimethylsilylpropyl)tetrasulphide.
• the elastomeric composition of the present invention comprises, per 100 parts be weights of rubber, about 1 to about 20 phr silane coupling agent. In a further embodiment, the elastomeric composition comprises, per 100 parts be weights of rubber, about 1 to about 15 phr silane coupling agent. In a futher embodiment, the silane coupling agent is bis(3-triethoxysilylpropyl)tetrasulphide (TESPT).
• TESPT bis(3-triethoxysilylpropyl)tetrasulphide
• the coupling agent can also be bifunctional POSs (polyorganosiloxanes), or hydroxysilane polysulphides, or silanes or POSs bearing azodicarbonyl functional groups.
• the coupling agent can also include other silane sulphides, for example, silanes having at least one thiol ( — SH) functional group (referred to as mercaptosilanes) and/or at least one masked thiol functional group.
• the coupling agent can also include combinations of one or more coupling agents such as those described herein, or otherwise known in the art.
• a preferred coupling agent comprises alkoxysilane or polysulphurized alkoxysilane.
• a particularly preferred polysulphurized alkoxysilane is bis(triethoxysilylpropyl) tetrasulphide, which is commercially available by Degussa under the trade name X50STM.
• the silane coupling agent is also available as a 50:50 blend of bis(3-triethoxysilylpropyl)tetrasulphide (TESPT) and N330 carbon black (available as X50-S ® from Evonik Industries).
• plasticizer or “plasticizing agent” includes a petroleum derived processing oil and synthetic plasticizer. Such oils are primarily used to improve the processability of the composition. Suitable plasticizers include, but are not limited to, aliphatic acid esters or hydrocarbon plasticizer oils such as paraffinic oils, aromatic oils, naphthenic petroleum oils, and polybutene oils. A particularly preferred plasticizer is naphthenic oil, which is commercially available from Nynas under the trade name NU ⁇ CTM 4700.
• MES and TDAE oils are well known to a person skilled in the art; for example, reference is made to publication KGK (Kautschuk Gummi Kunstoffe), 52nd year, No. 12/99, pp. 799-805, entitled “Safe Process Oils for Tires with Low Environmental Impact”.
• MES oils whether they are of the “extracted” or “hydrotreated” type
• TDAE oils for example, of the products sold under the names FLEXONTM 683 by ExxonMobil, VIVATECTM 200 or VIVATECTM 500 by H&R European, PLAXOLENETM MS by Total, or CATENEXTM SNR by Shell.
• the resins (it should be remembered that the term “resin” is reserved by definition for a solid compound) formed of Cs fraction/vinylaromatic copolymer, in particular of Cs fraction/styrene or Cs fraction C9 fraction copolymer, are well known; they have been essentially used to date for application as tackifying agents for adhesives and paints but also as processing aids in tire rubber compositions.
• An example of a hydrocarbon resin is OpperaTM PR373 from ExxonMobil Chemical Co.
• Another example of a hydrocarbon resin is EscorezTM E5320 from ExxonMobil Chemical Co.
• the plasticizing agent is a hydrocarbon resin.
• the elastomeric composition of the present invention comprises at least 40 phr hydrocarbon resin.
• the elastomeric composition of the present invention comprises at least 45 phr hydrocarbon resin.
• the elastomeric composition of the present invention comprises about 50 to about 80 phr hydrocarbon resin.
• the elastomeric composition comprises about 50 to about 70 phr hydrocarbon resin.
• Triester and fatty acid generally refer to a mixture of triesters or a mixture of fatty acids, respectively.
• the fatty acid preferably consists of more than 50%, more preferably to more than 80% by weight of an unsaturated C18 fatty acid, that is to say one selected from among the group consisting of oleic acid, linoleic acid, linolenic acid and mixtures thereof. More preferably, be it synthetic or natural in origin, the fatty acid used is constituted to more than 50% by weight, more preferably still to more than 80% by weight, of oleic acid.
• Antidegradants encompass antioxidants, antiozonants and waxes. Antiozonanats are used to protect rubber products from ozone. Waxes are also used to provided rubber ozone protection. An example of an antiozone wax is AKROWAXTM 5084 from AkroChem. [00122] As used herein, the term “antioxidant” refers to a chemical that combats oxidative degradation. Suitable antioxidants include diphenyl-p-phenylenediamine and those disclosed in The Vanderbilt Rubber Handbook (1978), Pages 344 to 346.
• a particularly preferred antioxidant is para-phenylenediamines, which is commercially available from Flexsys under the trade name SANTOFLEXTM 6PPD (N-( 1 ,3-Dimethylhutyl)-N '-phenyl- 1 ,4- phenylenediamine).
• Another preferred antioxidant is a high-molecular-weight, hindered amine light stabilizer, which is commercially available as CHIMASSORB ® 2020 from BASF Corp. Crosslinking Agents. Curatives.
• the elastomeric compositions and the articles made from those elastomeric compositions described herein are generally manufactured with the aid of at least one cure package, at least one curative, at least one vulcanizing or crosslinking agent, and/or undergo a process to cure the elastomeric composition.
• at least one curative package refers to any material or method capable of imparting cured properties to a rubber as is commonly understood in the industry.
• Preferred crosslinking agents are sulfur, sulfur halides, organic peroxides, quinone dioximes, organic polyvalent amine compounds, methylol group- containing alkylphenol resins and the like are mentioned.
• a preferred crosslinking agent is sulfur.
• the amount of sulfur to be blended is preferably from 0.1 to 5 parts by mass and more preferably from 0.5 to 3 parts by mass based on 100 parts by mass of the total of the polymer components contained in the polymer composition.
• the sulfur may be provided either as free sulfur, through a sulfur donor or combinations thereof.
• Suitable free sulfur includes, for example, pulverized sulfur, rubber maker's sulfur, commercial sulfur, and insoluble sulfur.
• a source of free sulfur is super fine sulfur available from Rubbermakers (Harwick Standard Distribution Corp.).
• the elastomeric compositions of the present invention comprise sulfur functionalized polymers, wherein the polymers are further functionalized with sulfur and an activator.
• the activator is zinc oxide or stearic acid.
• the activator is a combination of zinc oxide and stearic acid.
• the cure package may also contain various chemicals, additives, and the like which are commonly used in the rubber industry, as desired.
• chemicals or additives include vulcanizing aids, processing aids, vulcanizing accelerators, process oils, anti-aging agents, anti- scorching agents, zinc oxide, stearic acid, and the like.
• zinc oxide is in naphthenic oil such as AKRO-ZINC ® BAR 85 available from Akrochem Corp.
• Examples of vulcanizing accelerators are sulfenamide-based, guanidine-based, thiuram-based, thiourea-based, benzothiazole-based, dithiocarbamic acid-based, and xanthogenic acid-based compounds, and preferably include 2-mercaptobenzothiazole, dibenzothiazyl disulfide, N-cyclohexyl-2-benzothiazylsulfenamide, N-t-butyl-2- benzothiazolesulfenamide, N-oxyethylene-2-benzothiazolesulfenamide, N-oxyethylene-2- benzothiazolesulfenamide, N,N'-diisopropyl-2-benzothiazolesulfenamide, diphenylguanidine, diorthotolylguanidine, orthotolylbisguanidine, and the like.
• Examples of guanidine -based vulcanizing accelerators are diphenylguanidine (DPG),
• Examples of dithiocarbamic acid-based vulcanizing accelerators are tetramethylthiuram monosulfide (TMTM), tetramethylthiuram disulfide (TMTD) and zinc diethylthiocarbamate (ZDEC).
• TMTM tetramethylthiuram monosulfide
• TMTD tetramethylthiuram disulfide
• ZDEC zinc diethylthiocarbamate
• sulfenamide-based vulcanizing accelerators are N-cyclohexyl-2-benzothiazylsulfenamide (CBS), N-t-butyl-2-benzothiazolesulfenamide (TBBS), N-oxyethylene-2-benzothiazolesulfenamide, N-oxyethylene-2- benzothiazolesulfenamide, N,N'-diisopropyl-2-benzothiazolesulfenamide, 2- morpholinothiobenzothiazole (MBS) and N-dicyclohexylbenzothiazole-2-sulfenamide (DCBS).
• benzothiazole-based vulcanizing accelerators are 2- mercaptobenzothiazole (MBT), dibenzothiazyl disulfide and 2,2’-dithiobisbenzothiazole (MBTS).
• the vulcanizing accelerator is N-cyclohexyl-2-benzothiazylsulfenamide (CBS) available from Kemai Chemical Co.
• CBS N-cyclohexyl-2-benzothiazylsulfenamide
• Another preferred vulcanizing accelerator is diphenyl guanidine available as Ekaland DPG from MLPC International (Arkema).
• the vulcanizing accelerator may be a single vulcanizing accelerator or a mixture of accelerators.
• the mixture of accelerators is a mixture of different types of accelerators, such as a benzothiazole-based vulcanizing accelerator with a dithiocarbamic acid- based vulcanizing accelerator or a guanidine-based vulcanizing accelerator.
• the amount of the vulcanizing accelerator (or mixture thereof) to be blended is usually from 0.1 to 5 parts by mass and preferably from 0.4 to 4 parts by mass based on 100 parts by mass of the total of the polymer components contained in the polymer composition.
• a tire tread composition comprises the elastomeric composition described herein.
• an article comprises the tire tread composition described herein.
• a tread for all-season tire comprises the tire tread composition described herein.
• the tire tread composition has many desirable properties when the functionalized or unfunctionalized polymer selected from the group consisting of ethylene-propylene-diene terpolymer, butyl rubber, poly(isobutylene-co-para-methylstyrene) and poly(isobutylene-co- para-methylstyrene-co-isoprene) terpolymer is present in the elastomeric compositions.
• One way of measuring a desirable property of a tread composition is by utilizing the Dynamic Mechanical Thermal Analysis (DMT A) test method. All tire tread compositions were compression molded and cured into pads.
• DMT A Dynamic Mechanical Thermal Analysis
• the temperature at which the maximum tan delta occurred is recorded is the glass transition temperature, Tg.
• the maximum Energy Loss (Tangent Delta, wherein the slope is zero) of the immiscible polyolefin domain of the cured composition is at a temperature within the range from about -60 to 20°C.
• Example 1 Preparation of partially (ca. 20%) epoxidized Butyl rubber via reactive mixing process.
• SW: 19.99 ppm or 10,000 Hz Zg30 is a 30° pulse; 5mm probe, 16 scans, Is delay, 500MHz.
• Example 2 Preparation of partially (ca. 20%) epoxidized ethylene-propylene-diene terpolymer via reactive mixing process.
• All mixing experiments were performed in a Brabender Intelli-torque internal mixer using roller type 6 blades. The mixer temperature was set to 70°C. 60 g of ethylene-propylene- diene terpolymer (90.6 wt% C3, 6.9 wt% C2, 2.5 wt% ENB) was fluxed for 30 seconds at 25 rpms, 0.56 g of 3-chloroperbenzoic acid (Aldrich, ⁇ 77% purity) was added slowly to the mixer. Once addition is complete, the compound was mixed for 10-12 minutes at 60 rpms. The epoxidized ethylene -propylene-diene terpolymer product was removed from the mixer and cooled to room temperature by pressing between two Teflon sheets in a Carver press.
• the partially epoxidized (ca. 20%) ethylene-propylene-diene terpolymer product was characterized using proton NMR spectroscopy showing the oxirane proton at 3.09 ppm, and the ENB olefinic protons at 5.21 and 5.01 ppm.
• the 1 H-NMR spectra of partially epoxidized ethylene-propylene-diene terpolymer obtained by a reactive mixing process (Example 2) is disclosed at Figure 2.
• Example 3 Preparation of thioacetate functionalized poly(isobutylene-co-para-methylstyrene) by a solution process.
• Nucleophilic substitution reaction of potassium thioacetate with ExxproTM NPX
• THF Tetrahydrofuran
• the slurry was added to the polymer solution slowly, with constant stirring.
• the reaction mixture was held at 25 °C for 24 h.
• the reaction mixture is introduced into the quench pot containing 100L of isopropanol to precipitate the functionalized polymer.
• the precipitated polymer was re-dissolved in a reactor containing 20L of isohexane and 2wt% of Butylated hydroxytoluene (BHT; Sigma Aldrich).
• BHT Butylated hydroxytoluene
• the re dissolved polymer was introduced into the 50L steam stripping pot, connected with a condenser and a chiller.
• the steam stripping is done using 20Kg/h of steam under nitrogen blanket.
• the steam stripped functionalized polymer was finally dried using heated roll mill to obtain 4200 g of functionalized ExxproTM.
• the dried polymer was characterized using proton NMR spectroscopy & FUR. Complete conversion was achieved in 24h.
• the thioacetate functionalized poly(isobutylene-co-para-methylstyrene) product was characterized using proton NMR spectroscopy showing complete disappearance of methylene proton ( ⁇ CthBr), with new resonance appearing at 4.09 ppm for ⁇ CH2S-COCH3 [00148]
• the 1 H-NMR spectra of the thioacetate functionalized poly(isobutylene-co-para- methylstyrene) obtained by a solution process (Example 3) is disclosed at Figure 3.
• Example 4 Preparation of mercaptobenzothiazole functionalized poly(isobutylene-co-para- methylstyrene) by a reactive mixing process.
• Example 5 Preparation of modified poly(isobutylene-co-para-methylstyrene) (BIMSM)- amine ionomer via a reactive mixing process.
• BIMSM modified poly(isobutylene-co-para-methylstyrene)
• Example 6 Preparation of modified butyl-amine ionomer via a reactive mixing process.
• All mixing experiments were performed in a Brabender Intelli-torque internal mixer using roller type 6 blades. The mixer temperature was set to 120-150°C. 60 g of Bromobutyl 2222 (ExxonMobil Chemical) was fluxed for 30 seconds at 60 rpms, 1.41 g (0.54 mol equiv.) of Armeen DMSVD from AkzoNobel was added slowly to the mixer. Once addition is complete, the compound was mixed for 10-15 minutes at 60 rpms. The modified butyl product mixture was removed from the mixer and cooled to room temperature by pressing between two Teflon sheets in a Carver press.
• Bromobutyl 2222 ExxonMobil Chemical
• Example 7 Preparation of (isobutylene-co-isoprene-co-para-methylstyrene) terpolymer.
• the IB-IP-PMS terpolymer samples were prepared using standard slurry cationic polymerization technique in a dry box. A premixed para-methyl styrene, isoprene, and isobutylene monomer solution in MeCl was prepared at -95 °C. An initiator/co-initiator solution of HCl/EtAlCh in MeCl was also prepared at -95 °C. [00158] The initiator/co-initiator solution was added slowly into mixed monomer solution with stirring.
• Catalyst precursor was bis((4- triethylsilyl)phenyl)methylene(cyclopentadienyl)(2,7-di-tert-butyl-fluoren-9-yl) hafnium dimethyl.
• the activator was dimethylanilinium tetrakis(pentafluorophenyl)borate, but dimethylanilinium-tetrakis(heptafluoronaphthyl)borate and other non-coordinating anion type activators or MAO could also be used.
• copolymer compositions were synthesized in a single continuous stirred tank reactor. A mixture containing unreacted monomers and solvent was fed to the reactor as fuel for a polymerization reaction. The polymerization was performed in solution using isohexane as solvent. During the polymerization process, hydrogen addition and temperature control were used to achieve the desired melt flow rate. The catalyst, activated externally to the reactor, was added as needed in amounts effective to maintain the target polymerization temperature.
• the copolymer material was produced in the presence of ethylene, propylene, ethylidene norbornene, and a catalyst comprising the reaction product of N,N- dimethylanilinium tetrakis(pentafluorophenyl)borate and [cyclopentadienyl(2,7-di-t- butylfluorenyl)di-p-triethylsilanephenylmethane] hafnium dimethyl.
• the copolymer solution emerging from the reactor was quenched and then devolatilized using conventionally known devolatilization methods, such as flashing or liquid phase separation, first by removing the bulk of the isohexane to provide a concentrated solution, and then by stripping the remainder of the solvent in anhydrous conditions using a devolatilizer so as to end up with a molten polymer composition containing less than 0.5 wt% of solvent and other volatiles.
• the molten polymer composition was advanced by a screw to a pelletizer from which the polymer composition pellets are submerged in water and cooled until solid.
• EPDM ethylene-propylene-diene terpolymer
• Ethylene-propylene-diene terpolymer, EPDM 1 contained 90.6wt% propylene, 6.9 wt% ethylene and 2.5 wt% 2-ethylidene-5-norbomene (ENB).
• Ethylene-propylene-diene terpolymer, EPDM 2 contained 82.0wt% propylene, 15.3 wt% ethylene and 2.8 wt% ENB.
• the two ethylene-propylene-diene terpolymers differed in their ratio of propylene to ethylene.
• EPDM 1 contained more propylene while EPDM 2 contained more ethylene and more ENB.
• the 1 H-NMR spectra of EPDM 1 is disclosed at Figure 8.
• sample preparation (polymer dissolution) was performed at 140°C where 20 miligrams of polymer was dissolved in an appropriate amount of solvent to give a final polymer solution volume of 1 ml.
• the 1 H solution NMR was performed on a 5mm probe at a field of at least 500 MHz in an ODCB (ortho-dichlorobenzene) and benzene-d6 (CeDe) mixture (9:1) at 120°C with a flip angle of 30°, 15s delay, and 512 transients. Chemical shifts were referenced to the ODCB peak at 7.22 ppm. Signals were integrated and the 2-ethylidene-5-norbornene (ENB) weight percent was reported.
• ODCB ortho-dichlorobenzene
• CeDe benzene-d6
• Imajor Integral of major ENB species from 5.2-5.4 ppm
• Iminor Integral of minor ENB species from 4.6-5.12 ppm
• the 13 C solution NMR was performed on a 10mm cryoprobe of at least 600MHz in an ODCB (ortho-dichlorobenzene) and benzene-d6 (CeDe) mixture (9:1) at 120°C with a flip angle of 90° and inverse gated decoupling.
• Sample preparation (polymer dissolution) was performed at 140°C where 0.20 grams of polymer was dissolved in an appropriate amount of solvent to give a final polymer solution volume of 3 ml. Chemical shifts were referenced to the ODCB solvent central peak at 130ppm. 13 C NMR determines the ethylene and propylene composition, not accounting for the ENB present.
• Table 1 lists the functionalized polymers and their respective additive formulation.
• Tire tread compound formulations are listed in the tables below. All components are listed in phr, or part per hundred, of polymer unit. These compounds were mixed in suitable mixers, using at least two successive passes well known to the person skilled in the art.
• the non-productive passes (mixing without crosslinking system) have mixing at high temperatures between 110°C and 190°C.
• the non-productive passes are followed by a productive pass where the crosslinking system is added.
• the temperature for this mixing is typically below 110°C.
• the duration of the mixing for each of the individual mixing steps is between 1 and 20 minutes.
• tread formulations TT1 to TT10 examples of tire tread formulations are listed in the table below as tread formulations TT1 to TT10.
• tread formulations TT1 and TT10 examples of tire tread formulations are listed in the table below as tread formulations TT1 to TT10.
• Tread compound controls with no Table 1 polymer additive are tread formulations TT1 and TT10.
• SPRINTAN ® SLR-4602 is a partially coupled functionalized SBR
• Carbon black (Vulcan ® 3 N330 from Cabot Corp.)
• tread compound formulations TT11 to TT17 A second set of tread compound formulations are listed below as tire tread formulations TT11 to TT17. Tread compound controls with no Table 1 polymer additive are tread formulations TT11 and TT17.
• SPRINTAN ® SLR-4602 is a partially coupled functionalized SBR for improved polymer/filler interaction
• Carbon black Vulcan ® 3 N330 from Cabot Corp.
• Zinc oxide in naphthenic oil AKRO-ZINC ® BAR 85 from Akrochem Corp.
• tread formulations were compression molded and cured into pads. Afterward, a rectangular test specimen (12 mm wide & 30 mm long) was died out of the cured pads and mounted in an ARES G2 (Advanced Rheometric Expansion System, TA instruments) for dynamic mechanical testing in torsion rectangular geometry. Though the thickness of the test specimen was around 1.8 mm, the thickness of the specimens varied and was measured manually for each test. A strain sweep at room temperature up to 5.5% strains and at 10 Hz was conducted first followed by a temperature sweep at 4% strain and 10 Hz from -26°C to 100°C at 2°C/min ramp rates. Storage and loss moduli were measured along with the loss tangent values.
• the tables below provide the loss tangent measurements and the normalized loss tangent measurements for the all-season tire tread formulations TT1 to TT10 and TT11 to TT17, respectively, using the polymers of Table 1.
• the tables with the normalized loss tangent measurements provide the same measurements but as a percentage of the corresponding control tire tread formulation, TT1 and TT10 for TT2 to TT9 and TT11 and TT17 for TT12 to TT16.
• Control tire tread formulations TT1, TT10, TT11 and TT17 do not contain a polymer from Table 1.

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