The composition comprises a blend of halogenated copolymer of isoolefin and para-alkylstyrene of relatively high aromatic comonomer content and relatively low halogen content with general purpose rubbers (GPR) such as butadiene rubber (BR), natural rubber (NR) and/or isoprene rubber (IR). The tire sidewall may comprise a single layer or a veneer construction wherein an outer layer comprises the blend of the halogenated copolymer with one or more general purpose rubbers, and an inner layer can comprise a blend of general purpose rubbers.

BACKGROUND OF THE INVENTION Rubber tires, such as pneumatic tires, include many components, such as, for example, sidewalls, Sidewalls are continuously subjected to distortion under normal road operating conditions. The sidewalls are subjected to extensive continuous flexing and can crack under such conditions. In addition to flex cracking, sidewalls are also subjected to atmospheric chemical action such as ozone attack. The overall effect is that the sidewalls may erode and degrade. The sidewall may even separate from the tire carcass during use, leading to tire failure.

To reduce the problems caused by ozone attack and flex cracking, tire manufacturers add chemical protectants to the general purpose rubbers used in tire sidewalls. The problem with these protectants is that they tend to be fugitive and can cause staining when in contact with white sidewalls. In some cases,

particularly in white sidewalls, polymer blends have been used to effect improvements in ozone and flex resistance.

Published International application PCT/US91/05666 filed Aug. 9, 1991 discloses a tire sidewall composition comprising a single layer prepared from a blend of a halogenated copolymer of isoolefin and para-alkylstyrene with one or more general purpose rubbers.

U.S. Patent 5,376,438 to Costemalle et al. discloses multi-layer tire sidewalls having an outer layer prepared from a blend of halogenated isomonoolefin'para-alkylstyrene copolymer and general purpose rubbers. The inner layer comprises general purpose rubber. The sidewalls are said to exhibit good ozone resistance and fatigue crack resistance as well as a reduction in staining and discoloration. This patent is hereby incorporated herein by reference in its entirety.

In the prior art, the halogen content of the halogenated isoolefin/para- alkylstyrene copolymers generally varied proportionately with the para-alkylstyrene content, e.g. higher para-methylstyrene content was used to get a higher halogen content. If the copolymer was excessively halogenated, some undesirable dihalo benzylic substitution would occur. Thus, excess para-methylstyrene was usually used. In tire sidewall compositions of the prior art, a relatively high bromine level was needed to achieve adhesion and ozone resistance, but such high bromination levels led to relatively tight cures and crack propagation. It would be desirable to be able to use a rubber blend of the halogenated isoolefin/para-alkylstyrene copolymer that has both good adhesion and ozone resistance, as well as flex crack resistance and cure properties.

SUMMARY OF THE INVENTION It has been found that the use of blends of halogenated copolymers of isoolefin and para-alkylstyrene having specific contents of aromatic monomers and halogenation, with general purpose rubbers yield tire sidewall compositions having significantly improved ozone resistance and fatigue crack propagation resistance. It has now been discovered that excellent curing and crack propagation resistance can

be achieved simultaneously with good adhesion and ozone resistance by using a relatively low halogenation content in combination with a relatively high aromatic or para-alkylstyrene content.

In one aspect, the invention is a blend of rubber and a brominated copolymer of an isoolefin and a para-alkylstyrene. The copolymer comprises at least 9.5 but less than 20 weight percent of aromatic monomers (styrenics), and at least 0.2 but less than 1 mole percent para-bromoalkylstyrene. The blend preferably comprises from 35 to 65 phr ofthe copolymer, and from 35 to 65 phr of the general purpose rubber. The styrenics can include para-alkylstyrene, brominated para-alkylstyrene, alpha-methylstyrene, brominated alpha- methylstyrene or combinations thereof The isoolefin is preferably isobutylene, whereas the para-alkylstyrene is preferably para-methylstyrene and the para-bromoalkylstyrene is preferably para-bromomethylstyrene. The general purpose rubber can be a natural rubber, styrene-butadiene rubber, polybutadiene rubber and combinations thereof. The copolymer preferably comprises from 12 to 17 weight percent unbrominated styrenics, and from 0.4 to 0.8 mole percent para- bromoalkylstyrene.

In another aspect, the invention provides a tire sidewall comprising a layer of the blend described above. The blend can also be used in a veneered tire sidewall wherein an outer layer comprises the blend described above, and an inner layer comprises a highly unsaturated rubber or blend of unsaturated rubbers.

In a further aspect, the invention provides an improvement in a tire sidewall comprising at least an outer layer comprising a blend of a copolymer of an isoolefin and a para-alkylstyrene and an unsaturated rubber, and an inner layer optionally comprising a highly saturated rubber or blend of unsaturated rubbers. The improvement is that the copolymer comprises from 9.5 to 20 weight percent aromatic monomers and from 0.2 to 1.0 mole percent para-bromoalkylstyrene.

Preferably, the blend contains quantities of bromoalkylstyrene and para- alkylstyrene which satisfy the following formula: X=[1.9l - (0.094 xY)]10.1 where "X" is mole percent bromoalkylstyrene and "Y,' is weight percent para- alkylstyrene (between the proposed limits of 9.5 to 20 weight percent). "+ 0.1" as used herein indicates that the value X may be any number within the range of 0.1 above to 0.1 below [1.91 - (0.094 x Y)]. The bromoalkylstyrene is preferably para-bromomethylstyrene and the para-alkylstyrene is preferably para- methylstyrene. More preferably, the blend of the present invention has 0.96 mole percent para-bromomethylstyrene and 10 weight percent para-methylstyrene.

Alternatively, the blend of the present invention preferably has 0.84 mole percent para-bromomethylstyrene and 12.5 weight percent para-methylstyrene.

In the preferred embodiment, the polymerized para-alkylstyrene comonomer unit is characterized by the formula: wherein R and R' are independently selected from the group consisting of hydrogen, alkyl groups having from 1 to about 5 carbon atoms, and primary and secondary alkyl halides having from 1 to about 5 carbon atoms, and s is selected from the halogen group consisting primarily of bromine, chlorine and mixtures thereof. Furthermore, the halogenated para-alkylstyrene unit is shown as being pendant from the isoolefin polymer chain, represented by the wavy lines in the formula.

The tire sidewall composition and layers of the present invention can be compounded by methods generally known in the art, such as by mixing with the

uncured polymers various fillers such as titanium dioxide; carbon black, when black sidewalls are desired, or non-black fillers and pigments; extenders such as rubber process oils; curing aids such as zinc oxide, sulfur; accelerators or retarders and other additives such as antioxidants and antiozonants.

DETAILED DESCRIPTION OF THE INVENTION The principal advantages realized by practice of the present invention primarily stem from the fact that by employing a blend of copolymer of an isoolefin and para-alkylstyrene with general purpose rubbers (GPR), wherein the copolymer has a low halogen content but high aromatics content, superior ozone resistance and flex fatigue crack resistance and adhesion can be achieved at the same time.

The invention in one embodiment involves the construction of a multi- layered tire sidewall, the outer layer of which comprises a blend of a copolymer of an isoolefin and para-alkylstyrene with one or more unsaturated rubbers (GPR).

The sidewall also comprises one or more layers constructed from conventional sidewall compositions such as those discussed in "The Vanderbilt Rubber Handbook" pp. 605 (1990).

The outer layer of the sidewall is fabricated from a blend composition comprising at least one highly unsaturated rubber selected from the group consisting of natural rubber, SBR rubber, polyisoprene and polybutadiene rubber; and a halogenated copolymer of an isoolefin and a para-alkylstyrene unit. In a particularly preferred composition useful in tire sidewalls, the halogenated copolymer comprises about 35 to 65 parts, for example, 40 parts, and the unsaturated rubber desirably comprises from 35 to 65 parts natural rubber and/or polybutadiene rubber. The outer layer blend may also optionally include from about 1 to about 90 preferably from about 5 to about 20 parts per hundred of ethylene-propylene-diene rubber (EPDM). The highly unsaturated rubber component of the outer layer may consist of a blend or mixture of two or more highly unsaturated rubbers. These optional rubbers may also contain aromatic monomers to improve their compatibility.

When white sidewalls are desired, particularly preferred outer layer compositions comprise the halogenated para-alkylstyrene copolymer and natural rubber in a weight ratio of halogenated para-alkylstyrene copolymer to natural rubber ranging from about 0.28:1 to about 3:1, preferably about 0.67:1 to about 1:1. The preferred halogenated para-alkylstyrene copolymer for white sidewall outer layers comprises preferably from about 9.5 to 20, more preferably from about 12 to about 17 weight percent para-alkylstyrene moieties and preferably from about 0.2 to about 1.0 mole percent, more preferably 0.4 to 0.8 mole percent halogenated para-alkylstyrene.

In a multi-layered construction, the inner layer or layers comprise one or more unsaturated rubbers selected from the group comprising natural rubber, styrene butadiene rubber, polybutadiene rubber. Typically such compositions comprise blends of natural rubber and polybutadiene rubber or blends of styrene butadiene rubber and polybutadiene rubber. The inner layer may also comprise fillers such as oils and antiozonants and other additives well known in the art.

The highly unsaturated rubbers are selected from the group consisting of natural rubbers, polyisoprene rubbers, styrene butadiene rubber (SBR) and polybutadiene rubber and mixtures thereof. The natural rubbers are selected from the group consisting of Malaysian rubber such as SMR CV, SMR 5, SMR 10, SMR 20, and SMR 50 and mixtures thereof, wherein the natural rubbers have a Mooney viscosity at 100" C (ML 1+4) of about 30 to about 120, more preferably about 40 to about 65. Comparable Indonesian rubbers, with SIR pre-fixes, may also be used. The Mooney viscosity test referred to herein is in accordance with ASTM D-1646.

The Mooney viscosity of the polybutadiene rubber as measured at 100" C (ML 1+4) may range from about 40 to about 70, more preferably about 45 to about 65, and most preferably about 50 to about 60. When both natural rubber and polybutadiene rubber are used, ranges from about 100 to 1 to 1 to 100, more preferably 5 to 1 to 1 to 5, and most preferably 2 to 1 to 1 to 2 are suggested.

EPDM is the ASTM designation for a terpolymer of ethylene, propylene and a non-conjugated diolefin. In such terpolymers the ethylene and propylene

form a fully saturate backbone of methylene linkages with the non-conjugated diolefin, e.g. dicyclopentadiene or substituted norbornene, attached so as to provide unsaturated side chains with readily available crosslinking sites for sulfur curing. The EPDM elastomers thus contain a fully saturated backbone which provides outstanding resistance to oxidation, ozone, and cracking, as well as excellent low temperature flexibility. The Mooney viscosity of the EPDM terpolymer as measured at 125° C is about 20 to 80, more preferably about 25 to 75 and most preferably about 40 to about 60. The ethylene content of the EPDM terpolymers may range from about 20 to about 90 weight percent, preferably from about 30 to about 85, more preferably from about 35 to about 80 weight percent.

The total diene monomer content in the EPDM terpolymers may suitably range from about 0.1 to about 15 weight percent, preferably from about 0.5 to about 12 weight percent.

The non-conjugated dienes may be straight chain or cyclic hydrocarbon diolefins having from 6 to 15 carbon atoms, such as dicyclopentadiene, including 5- methylene-2-norbornene, 5-vinyl-2-norbornene, 2-methylnorbornadiene, 2, 4- dimethyl-2,7-octadiene, 1,4-hexadiene and 5-ethylidene-2-norbornene. The more preferred compounds include 5-methylene-2-norbornene, dicyclopentadiene, 1,4- hexadiene and 5-ethyliene, dicyclopenta-diene, 1,4-hexadiene and 5-ethylidene-2- norbornene. A preferred EPDM terpolymer is VISTALONQ) 6505 manufactured by Exxon Chemical Company.

The term "butyl rubber" as employed herein is intended to refer to a vulcanizable rubbery copolymer containing, by weight, from about 85 to 99.5% combined isoolefin having from 4 to 8 carbon atoms. Such copolymers and their preparation are well known. The butyl rubber may be halogenated by means known in the art. The Mooney viscosity of the halobutyl rubbers useful in the instant invention are measured at 125 ° C. (ML 1+4) range from about 20 to about 80, more preferably about 25 to about 55, and most preferably about 30 to about 50.

Suitable halogen-containing copolymers of a C4 to C7 isomonoolefin and a para-alkylstyrene for use as a component of the present blends and tire sidewall

compositions comprise at least 9.5 weight percent of the para-alkylstyrene moiety.

For elastomeric copolymer products, the para-alkylstyrene moiety may range from about 9.5 weight percent to about 20 weight percent, preferably from about 12 to about 17 weight percent of the copolymer. The halogenated content of the copolymers may range from about 0.2 to about 1.0 mole percent, preferably from about 0.4 to about 0.8 mole percent. The halogen may be bromine, chlorine and mixtures thereof. Preferably, the halogen is bromine. The major portion of the halogen is chemically bound to the para-alkyl group, that is, the halogen-containing copolymer comprises para-haloalkyl groups.

The copolymers of the isomonoolefin and para-alkylstyrene useful to prepare the halogen-containing copolymers suitable as a component of the tire sidewall composition of the present invention include copolymers of isomonoolefin having from 4 to 7 carbon atoms and a para-alkylstyrene, such as those described in U.S. Pat. No. 5,162,445. The preferred isomonoolefin comprises isobutylene.

The preferred para-alkylstyrene comprises para-methylstyrene. Other aromatic monomers and styrenics, for example, alkylstyrenes such as alpha-methylstyrene and meta-methylstyrene, may be employed in lieu of some of the para-alkylstyrene, provided the total aromatic content of the copolymer is in the rage of 9.5 to 20 weight percent, preferably 12 to 17 weight percent. Sufficient amounts of the para-alkylstyrene must, of course, be used to obtain the halogenated copolymer with the halogenated para-alkyl groups.

Preferably, the blend of the present invention contains quantities of bromoalkylstyrene and para-alkylstyrene which satisfy the following formula: X={l.91 -(0.094 x Y)]t0.1 where "X" is mole percent bromoalkylstyrene and "Y" is weight percent para- alkylstyrene (between the limits of 9.5 to 20 weight percent). "+ 0.1" as used herein indicates that the value X may be any number within the range of 0. 1 above to 0.1 below [1.91 - (0.094 x Y)]. The bromoalkylstyrene is preferably para- bromomethylstyrene and the para-alkylstyrene is preferably para-methylstyrene.

More preferably, the blend of the present invention has 0.96 mole percent para-

bromomethylstyrene and 10 weight percent para-methylstyrene. Alternatively, the blend of the present invention preferably has 0.84 mole percent para- bromomethylstyrene and 12.5 weight percent para-methylstyrene.

Suitable copolymers of an isomonoolefin and a para-alkylstyrene include copolymers having a weight average molecular weight (Mw) of at least about 100,000, preferably at least about 300,000, and a number average molecular weight (Mn) of at least about 100,000. The copolymers also, preferably, have a ratio of weight to number average molecular weight, i.e., Mw/Mn of less than about 6 preferably less than about 4. The brominated copolymer of the isoolefin and para-alkylstyrene obtained by the polymerization of these particular monomers under certain specific polymerization conditions now permits one to produce copolymers which comprise the direct reaction product (that is, in their as- polymerized form), and which have unexpectedly homogeneous uniform compositional distributions. Thus, by utilizing the polymerization and bromination procedures set forth herein, the copolymers suitable for the practice of the present invention can be produced. These copolymers, as determined by gel permeation chromatography (GPC) demonstrate narrow molecular weight distributions and substantially homogeneous compositional distributions, or compositional uniformity over the entire range of compositions thereof. At least about 95 weight percent of the copolymer product has a para-alkylstyrene content within about 7 weight percent, of the average para-alkylstyrene content for the overall composition, and preferably at least about 97 weight percent of the copolymer product has a para-alkylstyrene content within about 7 weight percent, of the average para-alkylstyrene content for the overall composition. This substantially homogeneous compositional uniformity thus particularly relates to the intercompositional distribution. That is, with the specified copolymers, as between any selected molecular weight fraction the percentage of para-alkylstyrene therein, or the ratio of para-alkylstyrene to isoolefin, will be substantially the same, in the manner set forth above.

In addition, since the relative reactivity of para-alkylstyrene with isoolefin such as isobutylene is close to one, the intercompositional distribution of these copolymers will also be substantially homogeneous. That is, these copolymers are essentially random copolymers and in any particular polymer chain the para- alkylstyrene and isoolefin units will be essentially randomly distributed throughout the chain.

The halogen-containing copolymers useful in the practice of the present invention have a substantially homogenous compositional distribution and include the para-alkylstyrene moiety represented by the formula: in which R and R' are independently selected from the group consisting of hydrogen, alkyl preferably having from I to 5 carbon atoms, primary haloalkyl, secondary haloalkyl preferably having from 1 to 5 carbon atoms, and mixtures thereof and X is selected from the group consisting of bromine, chlorine and mixtures thereof, such as those disclosed in U.S. Pat. No. 5,162,445, the teachings of which are incorporated by reference.

Various methods may be used to produce the copolymers of isomonoolefin and para-alkylstyrene, as known in the art. Preferably, the polymerization is carried out continuously in a typical continuous polymerization process using a baffled tank-type reactor fitted with an efficient agitation means such as a turbo mixer or propeller, and draft tube, external cooling jacket and internal cooling coils or other means of removing the heat of polymerization, inlet pipes for monomers, catalyst and diluents, temperature sensing means and an effluent overflow to a holding drum or quench tank. The reactor is purged of air and moisture and

charged with dry, purified solvent or a mixture of solvent prior to introducing monomers and catalysts.

Reactors which are typically used in butyl rubber polymerization are generally suitable for use in polymerization reaction to produce the desired para- alkylstyrene copolymers suitable for use in the present invention. The polymerization temperature may range from about minus 35° C to about minus 100" C, preferably from about minus 40° to about minus 80" C.

The processes for producing the copolymers can be carried out in the form of a slurry of polymer formed in the diluents employed, or as a homogeneous solution process. The use of a slurry process is, however, preferred, since in that case, lower viscosity mixtures are produced in the reactor and slurry concentrations of up to 40 weight percent of polymer are possible. However, a solution process is preferred for the higher levels of PMS.

The copolymers of isomonoolefins and para-alkylstyrene may be produced by admixing the isomonoolefin and the para-alkylstyrene in a copolymerization reactor under copolymerization conditions in the presence of a diluent and a Lewis acid catalyst.

Typical examples of the diluents which may be used alone or in a mixture include propane, butane, pentane, cyclopentane, hexane, toluene, heptane, isooctane, etc., and various halohydrocarbon solvents which are particularly advantageous herein, including methylene chloride, chloroform, carbon tetrachloride, and methyl chloride, with methyl chloride being particularly preferred.

An important element in producing the copolymer is the exclusion of the impurities from the polymerization reactor, namely, impurities which if present, will result in complexing with the catalyst or copolymerization with the isomonoolefins or the para-alkylstyrene, which in turn will prevent one from producing the para- alkylstyrene copolymer product useful in the practice of the present invention.

Most particularly, these impurities include the catalyst poisons, moisture and the like. These impurities should be kept out of the system.

In producing the suitable copolymers, it is preferred that the para- alkylstyrene be at least 95.0 weight percent pure, preferably 97.5 weight percent pure, most preferably 99.5 weight percent pure, that the isomonoolefin be at least 99.5 weight percent pure, preferably at least 99.8 weight percent pure, and that the diluents employed be at least 99 weight percent pure, and preferably at least 99.8 weight percent pure.

The most preferred Lewis acid catalysts are ethyl aluminum dichloride and preferably mixtures of ethyl aluminum dichloride with diethyl aluminum chloride.

The amount of such catalysts employed will depend on the desired molecular weight and the desired molecular weight distribution of the copolymer being produced, but will generally range from about 20 ppm to 1 weight percent and preferably from about 0.001 to 0.2 weight percent based upon the total amount of monomer to be polymerized.

Halogenation of the polymer can be carried out in the bulk phase (e.g. melt phase) or either in solution or in a finely dispersed slurry. Bulk halogenation can be effected in an extruder, or other internal mixer, suitably modified to provide adequate mixing and for handling the halogen and corrosive by-products of the reaction. The details of such bulk halogenation processes are set forth in U.S. Pat.

No. 4,548,995, which is hereby incorporated by reference.

Suitable solvents for solution halogenation include the low boiling hydrocarbons (C4 to C7) and halogenated hydrocarbons. Since the high boiling point para-methylstyrene makes its removal by conventional distillation impractical, and since it is difficult to completely avoid solvent halogenation, it is very important where solution or slurry halogenation is to be used that the diluent and halogenation conditions be chosen to avoid diluent halogenation, and that residual para-methylstyrene has been reduced to an acceptable level.

With halogenation of para-methylstyrene/isobutylene copolymers, it is possible to halogenate the ring carbons, but the products are rather inert and of little interest. However, it is possible to introduce halogen desired functionality into the para-methylstyrene/isobutylene copolymers hereof in high yields and under

practical conditions without obtaining excessive polymer breakdown, cross-linking or other undesirable side reactions.

It should be noted that radical bromination of the enchained para- methylstyryl moiety in the useful copolymers for the practice of this invention can be made highly specific with almost exclusive substitution occurring on the para- methyl group, to yield the desired benzylic bromine functionality. The specificity of the bromination reaction can thus be maintained over a broad range of reaction conditions, provided, however, the factors which would promote the ionic reaction route are avoided (i.e., polar diluents, Friedel-Crafts catalysts, etc.).

Thus, solutions of the suitable para-methylstyrene/isobutylene copolymers in hydrocarbon solvents such as pentane, hexane or heptane can be selectively brominated using light, heat, or selected radical initiators (according to conditions, i.e., a particular radical initiator must be selected which has an appropriate half-life for the particular temperature condition being utilized, with generally longer half- lives preferred at warmer halogenation temperatures) as promoters of radical halogenation, to yield almost exclusively the desired benzylic bromine functionality, via substitution on the para-methyl group, and without appreciable chain scission and/or crosslinking.

This reaction can be initiated by formation of a bromine atom, either photochemically or thermally (with or without the use of sensitizers), or the radical initiator used can be one which preferentially reacts with a bromine molecule rather than one which reacts indiscriminately with bromine atoms, or the solvents or polymer (i.e., via hydrogen abstraction). The sensitizers referred to are those photochemical sensitizers which will themselves absorb lower energy photons and disassociate, thus causing in turn, disassociation of the bromine, including materials such as iodine. It is, thus, preferred to utilize an initiator which has a half life of between about 0.5 and 2500 minutes under the desired reaction conditions, more preferably about 10 to 300 minutes. The amount of initiator employed will usually vary between 0.02 and 1 percent by weight on the copolymer, preferably between about 0.02 and 0.3 percent. The preferred initiators are bis azo compounds such as azo bis isobutyronitrile (AIBN), azo bis(2,4-dimethylvalero)nitrile, azo bis(2-

methylbutyro)nitrile, and the like. Other radical initiators can also be used, but it is preferred to use a radical initiator which is relatively poor at hydrogen abstraction, so that it reacts preferentially with the bromine molecules to form bromine atoms rather than with the copolymer or solvent to form alkyl radicals. In those cases, there would then tend to be resultant copolymer molecular weight loss, and promotion of undesirable side reactions, such as crosslinking. The radical bromination reaction of the copolymers of para-methylstyrene and isobutylene is highly selective, and almost exclusively produces the desired benzylic bromine functionality. Indeed, the only major side reaction which appears to occur in disubstitution at the para-methyl group to yield the dibromo derivative, but even this does not occur until more than about 60 percent of the enchained para-methylstyryl moieties have been monosubstituted. Hence, any desired amount of benzylic bromine functionality in the monobromo form can be introduced into the above stated copolymers, up to about 60 mole percent of the para- methylstyrene content. Stated differently the para-methylstyrene content should preferably be at least twice the desired para-bromomethylstyrene content to avoid dibromination.

It is desirable that the termination reactions be minimized during bromination, so that long, rapid radical chain reactions occur, and so that many benzylic bromines are introduced for each initiation, with a minimum of the side reactions resulting from termination. Hence, system purity is important, and steady-state radical concentrations must be kept low enough to avoid extensive recombinations and possible crosslinking. The reactions must also be quenched once the bromine is consumed, so that continued radical production with resultant secondary reactions (in the absence of bromine) do not then occur. Quenching may be accomplished by cooling, turning off the light source, adding dilute caustic, the addition of a radical trap, or combinations thereof.

Since one mole of HBr is produced for each mole of bromine reacted with or substituted on the enchained para-methylstyryl moiety, it is also desirable to neutralize or otherwise remove this HBr during the reaction, or at least during polymer recovery in order to prevent it from becoming involved in or catalyzing

undesirable side reactions. Such neutralizations and removal can be accomplished with a post-reaction caustic wash, generally using a molar excess of caustic on the HBr. Alternatively, neutralization can be accomplished by having a particulate base (which is relatively nonreactive with bromine) such as calcium carbonate powder present in dispersed form during the bromination reaction to absorb the HBr as it is produced. Removal of the HBr can also be accomplished by stripping with an inert gas (e.g., N2) preferably at elevated temperatures.

The brominated, quenched, and neutralized para-methylstyrene/isobutylene copolymers can be recovered and finished using conventional means with appropriate stabilizers being added to yield highly desirable and versatile functional saturated copolymers.

In summary, halogenation to produce a copolymer useful in the present invention is preferably accomplished by halogenating an isobutylene-para- methylstyrene copolymer using bromine in a normal alkane (e.g., pentane, hexane or heptane) solution utilizing a bis azo initiator, e.g., MBN or VAZOX 52: 2,2'- azobis(2,4-dimethyl-pentane nitrile), at about 55" to 800 C, for a time period ranging from about 4.5 to about 30 minutes, followed by a caustic quench. The halogen content is generally controlled by limiting the quantity of halogen reactant.

The recovered polymer is washed in basic water and water/isopropanol washes, recovered, stabilized and dried.

The aromatic halomethyl groups permit facile crosslinking to be accomplished in a variety of ways, for example, either directly through the halomethyl group or by conversion to other functional groups, as indicated above, to permit the desired crosslinking reactions to be employed. Direct crosslinking can be effected with a variety of polyfunctional groups, as indicated above, to permit the desired crosslinking reactions to be employed. Direct crosslinking can be effected with a variety of polyfunctional nucleophilic reagents such as ammonia, amines, or polyamines; metal dicarboxylates; metal dithiolates; promoted metal oxides (e.g., ZnO+zinc stearates and/or dithiocarbamates), etc. Crosslinking can also be effected via polyalkylation reactions. The aromatic halomethyl groups thus provide a wide choice of crosslinking reactions which can be used.

Various fillers can also be used in single layer or the outer and/or inner layer blend compositions of the present invention, and these include a variety of carbon blacks, clays, silicas, carbonates, oils, resins, and waxes. Carbon blacks preferred for use in black tire sidewall compositions of this invention include those types designated N339, N774, N660, N35 1 and N375. Alternatively, non-black filers and pigments may be used for white tire sidewalls. The blends are cured with conventional curatives for highly unsaturated or chlorobutyl rubbers, including sulfur, alkylphenol disulfide, zinc oxide, sulfenamide derivatives, guanidines, berizothiazyldisulfide (MBTS) and mercaptobenzothiazole (MBT).

When constructing tires employing the sidewalls of the invention, the sidewalls can be made of the blend composition, or the present blend composition can be used as an outer layer or veneer over an inner layer. The thickness of the inner and outer layers will vary depending upon the type and size of the tires being built. Typically for a passenger car tire, the outer layer thickness may vary from about 0.8 mm to about 2.0 mm. The inner layer may vary from about 1.0 mm to about 2.0 mm. For example, a tire size 185/60-HR-14 would have a sidewall width of about 95 mm and an overall length of about 1210 mm.

The single-layer or multi-layered tire sidewall compositions of the present invention may be vulcanized by subjecting them to heat and/or light or radiation according to any vulcanization process.

The single-layer or multi-layered tire sidewall of the present invention may be used as the sidewall for motor vehicle tires such as truck tires, bus tires, passenger automobile, motorcycle tires and the like.

Suitable tire sidewall layer compositions may be prepared by using conventional mixing techniques including, e.g., kneading, roller milling, extruder mixing, internal mixing (such as with a Banbury(g) mixer), etc. The sequence of mixing and temperatures employed are well known to the skilled rubber compounder, the objective being the dispersion of fillers, activators and curatives in the polymer matrix without excessive heat buildup. A useful mixing procedure utilizes a Banbury mixer in which the rubber components, fillers, and plasticizer are added and the composition mixed for the desired time to a particular temperature

to achieve adequate dispersion of the ingredients. Alternatively, the rubbers and a portion of the fillers (e.g., one-third to two-thirds) is mixed for a short time (e.g. about 1 to 3 minutes) followed by the remainder of the fillers and oil. Mixing is continued for about 5 to 10 minutes at high rotor speed during which time the mixed components reach a temperature of about 1500 C. Following cooling, the components are mixed in a second step on a rubber mill or in a Banbury mixer during which the curing agent and optional accelerator, are thoroughly and uniformly dispersed at a relatively low temperature, e.g., about 80" to about 105° C. Variations in mixing will be readily apparent to those skilled in the art and the present invention is not limited to any specific mixing procedure. The mixing is performed to disperse all components of the composition thoroughly and uniformly.

Tires are generally built on a drum from at least three layers, namely, an outer layer comprising a tread portion and sidewalls comprising the inner and outer layers of this invention, an intermediate layer, and an innerliner. After the uncured tire has been built on a building drum, the uncured tire may be placed in a heated mold to shape it and heat it to vulcanization temperatures and, thereby, to produce a cured unitary tire from the multi-layers.

Vulcanization of the molded tire, typically, is carried out in heated presses under conditions well known to those skilled in the art.

Curing time will be affected by the thickness of the tire to be molded and the concentration and type of curing agent as well as the halogen content of the halogenated copolymer. However, the vulcanization parameters can readily be established with a few experiments utilizing, e.g., a laboratory characterization device well known in the art, the Monsanto Oscillating Disc Cure Rheometer (ODR, described in detail in American Society for Testing and Materials, Standard ASTM D 2084).

Tires produced according to the present invention offer black or white sidewall tire with the features of improved adhesion and ozone resistance as well as good curing and flex crack resistance. In the present tire, by using the halogenated copolymer in the tire sidewall, or in only the outer layer, good ozone resistance is

achieved. In addition, the outer layer acts as a barrier preventing migration of additives in protectants from the inner layer to the outside, thus eliminating the staining and discoloring problem discussed above.

The following examples are presented to illustrate the invention. All parts and percentages herein are by weight unless otherwise specified.

EXAMPLE 1 Master batches of brominated isobutylene/para-methylstyrene copolymers of varying bromination level, comonomer content and molecular weight were prepared. The copolymers had the properties listed in Table 1.

TABLE 1 COPOLYMER PROPERTY EXXPRO EXXPRO EXXPRO A A C 89-1 934 96-3 Para-Methvlstyrene 3.0 7.3 7.3 9.3 13.6 13.6 (wot%) Bromomethylstyrene 0.75 1.2 0.75 1.0 1.0 0.8 (moo%) Mooney Viscosity (ML(1+8)1250C) 33+3 38*3 40+3 33+3 38+3 44+3 Test compositions were compounded using 3-pass mixing conditions to blend the master batch components and the cure additives listed in Table 2. The compositions were cured at 1500 C (18 minutes for tensile and fatigue testing; 21 minutes for Demattia and outdoor flex testing and 175° C (11 minutes for tensile and fatigue testing; 14 minutes for Demattia and outdoor flex testing).

TABLE 2 RECIPES 1A 1B 1C 1D 1E 1F 1G 1H Master Batch (phr) EXXPRO 89-1 40 EXXPRO 934 40 EXXPRO 96-3 40 Copolymer 1A 40 40 Copolymer 1B 40 40 Copolymer 1C 40 BUDENE 1207 50 50 50 50 50 50 50 50 SMR20 10 10 10 10 10 10 10 10 Black N660 40 40 40 40 40 40 40 40 FLEXON 641 12 12 12 12 12 12 12 12 ESCOREZ 1102 5 5 5 5 5 5 5 5 STRUCKOL 40MS 4 4 4 4 4 4 4 4 SP 1068 2 2 2 2 2 2 2 2 Cure Package (phr) Sulfur 0.40 0.40 0.40 0.40 0.40 0.40 0.80 0.80 Zinc Oxide 0.75 0.75 0.75 '0.75 0.75 0.75 2.00 2.00 RYLEX 3011 0.60 0.60 0.60 0.60 0.60 0.60 Stearic Acid 0.50 0.50 0.50 0.50 0.50 0.50 MBTS 0.80 0.80 0.80 0.80 0.80 0.80 TBBS 1.60 1.60 DURALINK HTS 2.00 2.00 SANTOVAR TAHQ 1.50 1.50 TOTAL PER 166.05 166.05 166.05 166.05 | 166.05 166.05 170.9 170.9 The test compositions (1A through 1H) were tested for cure characteristics, tensile strength, flex fatigue, adhesion and ozone resistance. The results are presented in Table 3 below. The following descriptors are used herein to refer to cracking types and ratings: Descriptor Meaning Excel No cracking Good Edge cracking only Fair Minor or Major cracking Poor Deep cracking, tear or separation 0 No cracking 1 Minor cracking 2 Major cracking 3 Deep Cracking 4 Tearing 5 Separated 6 Edge crack TABLE 3 RECIPES 1A 1B 1C 1D 1E 1F 1G 1H Mooney Scorch @ 135°C 1 MU, min 7.5 6.3 8.0 8.6 8.4 8.3 1.8 5.9 2 MU, min 8.8 7.2 9.3 ~ 10.0 9.0 9.5 4.2 7.1 5 MU, min 11. 8.7 11.4 12.1 12.0 11.5 9.1 9.1 10 MU min 13.5 10.4 13.8 14.1 14.0 13.6 11.7 10.3 20 MU, min 16.7 12.8 16.0 16.6 17.0 16.6 14.2 | 11.2 ODR @ 150°C, 1° Arc, 30 Min My, dim 3.6 4.1 3.9 4.6 3.7 3.8 4.8 4.0 MH, dNm 14.3 18.1 15.1 19.6 16.0 14.1 18.3 19.2 ts2, min 7.6 5.8 7.7 6.8 7.7 8.1 7.4 5.7 t25, min 8.8 7.4 9.2 8.8 9.3 9.1 8.7 6.6 t50, min 13.5 10.7 14.1 13.1 13.5 13.6 12.3 9.1 t90, min 22.7 17.7 23.4 21.8 21.7 22.5 23.6 17.7 Peak Rate, dNm,/min 1.5 1.4 0.8 1.1 1.0 0.9 1.2 2.1 Curve Type SLM P SLM SLM SLM P M P ODR @ 175°C, 1° Arc, 30 min ML, dNm 4.0 4.1 4.2 4.0 3.8 4.1 4.0 4.1 MH, dNm 21.0 23.7 21.5 22.1 20.9 | 19.6 20.2 24.7 ts2, min 2.5 2.2 2.5 2.5 2.5 2.8 2.5 2.1 t25, min 3.1 2.8 3.2 3.2 3.1 3.4 2.9 2.5 t50, min 4.2 3.6 4.3 4.1 4.0 4.4 3.9 3.1 t90, min 7.8 8.7 7.8 7.2 6.8 8.1 9.0 6.3 Peak Rate, dNm/min 4.5 7.0 4.5 5.2 5.3 4.0 5.0 9.4 Curve T P P P P P P P SLR Stress-Strain, Unaged, Tested @ RT, Cured @ 150°C Stress @ break (MPa) 12.3 10.1 12.2 11.5 13.4 11.0 10.5 13.3 Stress @ 100% (MPa) 0.9 1.2 0.9 1.0 0.9 0.9 0.8 1.2 Stress @ 200% (MPa) 1.8 2.6 1.7 2.0 1.9 1.6 1.7 2.3 Stress @ 300% (MPa) 1.7 1.8 2.0 1.9 1.6 2.7 2.3 2.6 % Elongation @ break 776 603 831 752 789 808 799 752 Shore A @ 4 sec 38.1 41.5 38.9 40.5 39.3 37.7 36.3 43.1 Stress-Strain, Unaged, Tested @ RT, Cured @ 175°C Stress @ break (MPa) 13.1 11.9 13.1 14.0 12.8 12.8 12.9 10.2 Stress @ 100% (MPa) 1.1 1.4 1.1 1.2 1.0 1.0 0.9 1.3 Stress @ 200% (MPa) 2.1 3.0 2.1 2.6 2.1 2.0 1.8 6.2 Stress @ 300% (MPa) 3.6 5.0 3.6 4.2 3.6 3.3 3.0 4.2 % Elongation @ break 765 616 817 711 780 790 834 643 Shore A @ 4 sec 40.9 43.5 41.5 42.7 41.5 40.5 39.1 43.3 (Table 3 continued) RECIPES 1A 1B 1C 1D 1E 1F 1G 1H Pierced Demattia Flex, 300 Cycles/min, 60° bend, Unaged, Cured @ 175°C for 14 min Cycles mm mm mm mm mm mm mm mm 0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 4,500 3.1 3.5 3.3 3.4 3.3 3.3 3.2 5.3 9,000 3.6 4.4 3.4 3.6 3.5 3.8 3.6 8.0 13,500 3.9 4.7 4.0 4.2 5.1 3.9 4.1 9.6 18,000 4.2 5.0 4.1 4.4 5.6 4.5 4.2 10.5 36,000 5.1 6.4 4.8 5.0 7.5 5.6 4.8 14.0 54,000 6.2 8.3 5.2 5.5 8.4 6.5 5.4 16.0 72,000 6.4 7.8 6.0 5.7 8.7 7.1 5.9 18.1 90,000 7.4 8.2 6.4 6.1 10.0 7.4 6.2 19.8 378,000 11.0 8.4 7.8 7.0 13.0 11.8 7.6 25.0 810,000 11.1 8.5 8.0 8.8 14.0 12.4 9.0 25.0 1,242,000 11.1 8.5 8.2 9.0 14.6 12.9 100.0 25.0 1,674,000 12.7 8.5 8.2 10.7 15.1 13.0 9.8 25.0 2,200,000 12.8 8.7 8.2 10.7 15.1 13.0 10.4 25.0 Pierced Demattia Flex, 300 Cycles/min, 60° bend, Aged 70 Days, Cured @ 175°C for 14 min Cycles mm mm mm mm mm mm mm mm 0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 4,500 6.7 10.2 8.3 6.6 5.5 5.1 8.6 25.0 9.000 S.9 13.2 10.0 7.2 6.5 6.4 10.9 25.0 13,500 10.1 15.6 12.0 8.9 7.3 7.1 13.7 25.0 18,000 11.4 18.1 12.6 9.6 7.4 7.5 14.5 25.0 36,000 14.0 23.4 15.4 11.0 7.6 9.4 18.7 25.0 54,000 14.0 25.0 17.9 12.0 7.9 9.6 23.1 25.0 72,000 16.1 25.0 19.3 12.3 8.1 10.0 23.8 25.0 90,000 16.2 25.0 20.5 12.7 8.2 10.1 24.4 25.0 378,000 20.1 25.0 22.9 15.1 13.2 10.3 25.0 25.0 810.000 20.7 25.0 23.S 16.3 13.5 10.S 25.0 25.0 1,242,000 20.9 25.0 24.4 17.2 13.6 11.7 25.0 25.0 1,674,000 21.0 25.0 24.4 18.1 14.5 11.8 25.0 25.0 2,200,000 21.0 25.0 24.4 21.5 17.9 11.8 25.0 25.0 Fatigue-to-Failure, 101% Elong., 100 Cycles/min, Unaged, Tested @ RT, Cured @ 175°C for 14 min 1 299469 474437 423700 568681 851035 249825 250295 503018 2 55249 323169 295957 489560 646772 206753 395717 495203 3 229232 272149 235538 524730 455105 262721 543253 608057 4 246140 378201 271244 662392 555320 213633 500604 671023 5 385646 351162 371391 576613 808128 253651 436442 591463 6 401886 434100 361917 727105 843489 255568 430599 596135 7 285398 471884 290089 834011 896678 368895 451971 605052 1 292774 417911 394121 84S445 1E+06 273305 529245 814932 Mean, cycles 274474 391339 331457 654030 757741 260544 443141 610610 Rounded Off(x 1000) 275 391 332 654 75S 261 443 611 Fatigue to Failure, 101% Elong., 100 Cycles/min, Aged 70 Days (i 70°C, Tested @ RT, Cured @ 175°C for 14 min 1 514957 119872 77077 21566 12457 304584 193522 48003 2 632240 272194 619631 516511 187557 338433 251824 13264 3 459893 134145 295085 459893 404585 368364 296195 32935 4 556415 308092 677578 790353 623963 341525 293385 64726 5 663633 371743 496268 624169 791603 545887 398263 39982 6 590643 359202 375256 433444 721574 564278 527785 74095 7 402796 367100 681192 686172 915044 367767 503897 6491 8 570675 311924 510982 774470 1E+06 688728 605345 9490 Mean. cycles 548907 280534 466634 538322 584184 439946 383777 36123 Rounded Off (x 1000) 549 281 467 538 584 440 384 36 (Table 3 continued) RECIPE 1A 1B 1C 1D 1E 1F 1G 1H Fatigue to Failure, 101% Elong., 100 Cycles/min. Unaged, Tested @ RT. Cured @ 150°C for 21 min 1 253958 183000 >1M >1M >1M 148815 204163 209386 2 227774 224530 >1M >1M >1M 237701 241507 258459 3 293006 173431 >1M >1M >1M 417194 186062 252981 4 401986 196761 >1M >1M >1M 355230 223373 184522 5 372749 173965 >1M >1M >1M 373614 231736 329088 6 362091 172382 >1M >1M >1M 390818 331287 336883 7 651507 282682 >1M >1M >1M 376861 335870 223471 8 494900 876872 >1M >1M >1M 350848 362558 203840 Mean, cycles 382246 219578 >1M >1M >1M 331385 367070 249829 Rounded Off (x 1000) 382 220 >1M >1M >1M 331 267 250 1" Strip Adhesion to "Carcass" Tested @ 100°C, Cured @ 150°C for 21 min Avg. Peak (lb) 146 114 170 148 146 84 128 55 Avg. Peel (lb) 117 93 149 124 118 66 108 46 Surface Appearance P/P P/P P/P P/P P/P SP/SP P/P P/P 1" Strip Adhesion to "Self" Tested @ 100°C, Cured @ 150°C for 21 min Avg. Peak (lb) 162 136 177 164 164 149 145 68 Avg. Peel (lb) 149 115 168 151 150 142 125 57 Surface Appearance P-T/P-T P/P P-T/P-T P/T-P/T P-T/P-T P-T/P-T P/P P/P 1" Strip Adhesion to "Carcass". Tested @ 100°C, Cured @ 175°C for 14 min Avg. Peak (lb) 120 93 138 121 139 113 95 50 Avg. Peel (lb) 110 76 115 100 110 80 81 44 Surface Appearance P/P P/P P/P P/P P/P SP/SP P/P SP/SP 1" Strip Adhesion to "Self" Tested @ 100°C. Cured @ 175°C for 14 min Avg. Peak (lb) 136 108 153 153 163 141 129 67 Avg. Peak (lb) 122 86 129 123 135 116 107 56 Surface Appearance P-T/P-T P/P P/P P/P P/P P/P P/P P/P Ozone Static - Bent Loop @ 40°C & 25 pphm of O3, Unaged, Cured @ 150°C for 21 min Crack 1, days/Type of Crack 0 0 0 0 0 0 0 0 Crack 2, days/Type of Crack Crack 3, days/Type of Crack Crack 4, days/Type of Crack Test Duration, Days 22 22 22 22 22 22 22 22 Rating Excel Excel Excel Excel Excel Excel Excel Excel Ozone Static - Bent Loop @ 40°C & 25 pphm of O3, Aged 70 Days @ 70°C, Cured @ 150°C for 21 min Crack 1, days/Type of Crack 0 0 0 0 0 0 24/1 24/1 Crack 2, days/Type of Crack Crack 3, days/Type of Crack Crack 4, days/Type of Crack Test Duration, Days 28 28 28 28 28 28 28 28 Ratings Excel Excel Excel Excel Excel Excel Fair Fair (Table 3 continued) RECIPE 1A 1B 1C 1D 1E 1F 1G 1H Ozone Static - Bent Loop @ 40°C & 25 pphm of O3, Unaged, Cured @ 175°C for 14 min Crack 1, days/Type of Crack 0 0 0 0 0 0 7/1 6/2 Crack 2, days/Type of Crack 0 12/4 12/3 Crack 3, days/Type of Crack 13/4 Crack 4, days/Type of Crack Test Duration, Days 22 22 22 22 22 22 22 22 Ratings Excel Excel Excel Excel Excel Excel Poor Poor Ozone Static - Bent Loop till 40°C & 25 pphm of 03, Aged 70 Days till 70°C, Cured @ 175°C for 14 min Crack 1. days/Type of Crack 0 0 0 0 0 0 0 0 Crack 2. days/Type of Crack Crack 3. day/Type of Crack Crack 4. days/Type of Crack Test Duration/Days 28 28 28 28 28 28 28 28 Ratings Excel Excel Excel Excel Excel Excel Excel Excel Ozone Dynamic - Tensile @ 40°C & 25 pphm of O3, Unaged, Cured @ 150°C for 21 min Crack 1, days/Type of Crack 0 0 0 0 0 0 14/1 6/5 Crack 2, days/Type of Crack 17/4 Crack 3, days/Type of Crack 21/5 Crack 4, days/Type of Crack Test Duration/Davs 22 22 22 22 22 22 22 22 Ratings Excel Excel Excel Excel Excel Excel Poor Poor Ozone Dynamic - Tensile @ 40°C & 25 pphm of O3, Aged for 70 Days @ 70°C, Cured @ 150°C for 21 min Crack 1. days/Type Crack 0 15/5 0 0 15/5 0 @ 18/2 # 15/4 Crack 2, days/Type of Crack 21/4 18/5 Crack 3, days/Type of Crack 28/5 Crack 4. days/Type of Crack Test Duration/Days 28 28 28 28 28 28 28 28 Ratings Excel Poor Excel Excel Excel Excel Poor Poor Ozone Dynamic - Tensile @ 40°C & 25 pphm of O3, Unaged, Cured @ 175°C for 14 min Crack 1, days/Type of Crack 0 0 12/4 0 0 0 6/1 6/2 Crack 2, days/Type of Crack 14/5 12/5 7/3 Crack 3. da's1,T e of Crack 8/5 Crack 4. days/Type of Crack Test Duration/Days 22 22 22 22 22 22 22 22 Ratin Excel Excel Poor Excel Excel Excel Poor Poor Ozone Dynamic - Tensile @ 40°C& 25 pphm of O3, Aged for 70 Days @ 70°C, Cured @ 175°C for 14 min Crack 1, days/Type of Crack 0 0 0 0 0 0 0 21/5 Crack 2. davs1Tv e of Crack Crack 3. days/Type of Crack Crack 4. days/Type of Crack Test Duration/Days 28 28 28 28 28 28 28 28 Ratings Excel Excel Excel Excel Excel Excel Excel Excel Outdoor Flex. Unaged, Cured till 150"C for 21 will. Crack 1, days/Type of Crack 18/6 0 18/6 0 0 0 8/1 5/1 Crack 2, days/Type of Crack 21/2 14/2 Crack 3. davs1T ofCrack 21/3 Crack 4. days/Type of Crack Test Duration/Days 26 26 26 26 26 26 26 26 Ratings Good Excel Good Excel Excel Excel Fair Poor Outdoor Flex, Aged 70 Days @ 70°C, Cured @150°C for 21 min Crack 1, days/Type of Crack 14/6 14/6 21/6 15/6 1/4 0 6/6 24/6 Crack 2, days/Type of Crack 27/1/6 24/1/6 9/4/6 30/1/6 Crack 3, days/Type of Crack Crack 4, days/Type of Crack Test Duration/Days 37 37 37 37 37 37 37 37 Rating Fair Good Fair Good Poor Excel Poor Fair GPR - Minor Cracking @ 29 Days

(Table 3 continued) RECIPE 1A 1B 1C 1D 1E 1F 1G 1H Outdoor Flex, Unaged, Cured @ 175°C for 14 min Crack 1, days/Type of Crack 8/1 19/6 8/1 0 0 19/6 8/1 3/1 Crack 2, days/Type of Crack 12/1/6 18/2/6 20/1/6 18/1/6 19/1/6 Crack 3. days/Type of Crack 18/2/6 | 23/3/6 21/2/6 23/1/6 Crack 4, days/Type of Crack 23/3/6 Test Duration/Days 26 26 26 26 26 26 26 26 Rating Poor Good Poor Excel Excel Good Fair Good Outdoor Flex, Aged 70 Days @ 70°C, Cured @ 175°C for 14 min Crack 1, days/Type of Crack 24/1/6 27/6 21/6 27/1/6 0 27/6 27/1 15/6/2 Crack 1, days/Type of Crack 24/1/6 30/2 21/4/6 Crack 1, dsvs/,T of Crack 37/2/6 33/5 Crack 1, days/Type of Crack Test Duration/Days 37 37 37 37 37 37 37 37 Rating Fair Good Fair Fair Excel Good Fair Poor Blends 1D through 1H exhibited similar cure characteristics to blends 1A, 1B and 1C and similar tensile properties. Blends 1D and 1F had better fatigue-to-failure and flex crack propagation resistance, and comparable ozone resistance.

EXAMPLE 2 Blends of rubber with a high-bromine, low para-methylstyrene copolymer and a low-bromine, high para-methylstyrene copolymer were prepared at varying ratios. The high-bromine, low para-methylstyrene copolymer was EXXPRO 93-4 copolymer comprised of 7.5 weight percent para-methylstyrene and 1.2 mole percent benzylic bromine. It had a Mooney viscosity ML (1+8) at 125° C of 38 + 5. The low-bromine, high para-methylstyrene copolymer (Copolymer 2) was comprised of 13.6 weight percent para-methylstyrene and 0.56 mole percent benzylic bromine (0.78 weight percent bromine). It has a Mooney viscosity ML (1 + 8) at 1250 C of 37 i 5. The blends were compounded as described in Example 1 and cured at 1800 C for 15 minutes. The blends had the compositions of Table 4.

TABLE 4 RECIPES 1 2 3 4 5 6 7 8 9 10 11 12 13 14 Master Batch EXXPRO 93-4 35 40 45 50 55 60 65 Copolymer 2 35 40 45 50 55 60 65 BUDENE 54.17 50 45.83 41.67 37.5 33.33 29.17 54.17 50 45.83 41.67 37.5 33.33 29.17 1207 SMR 20 10.83 10 9.17 8.33 7.5 6.67 5.83 10.83 10 9.17 8.33 7.5 6.67 5.83 N351 40 40 40 40 40 40 40 40 40 40 40 40 40 40 FLEXON 641 12 12 12 12 12 12 12 12 12 12 12 12 12 12 STRUCKTOL 4 4 4 4 4 4 4 4 4 4 4 4 4 4 40MS ESCOREZ 5 5 5 5 5 5 5 5 5 5 5 5 5 5 1102 SP 1068 2 2 2 2 2 2 2 2 2 2 2 2 2 2 Curc Package Stearic Acid 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 Sulfur 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 Zinc Oxide 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 RYLEX 3011 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 MBTS 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 TOTAL PHR 166.05 166.05 166.05 166.05 166.05 166.05 166.05 166.05 166.05 166.05 166.05 166.05 166.05 166.05 The blends were evaluated for cure characteristics, tensile and hardness properties, flex crack propagation resistance, tensile fatigue-to-failure, static and dynamic ozone resistance, and outdoor flex resistance. The results are presented in Table 5 using the same descriptor meanings as in Table 3.

TABLE 5 RECIPES 2A 2B 2C 2D 2E 2F 2G 2H 2I 2J 2K 2L 2M 2N Moon@y Viscosity @ 100°C ML1+4min (MU) 45.3 42.9 44.7 43.5 43.7 44.6 45.0 44.9 43.7 44.2 43.5 44.4 44.4 ML1+8min(MU) 42.4 43.6 41.2 43.4 42.2 42.1 43.2 43.4 43.5 42.3 42.6 42.0 42.9 43.2 Mooney Scorch @ 135°C 5 MU, MIN 12.8 12.2 12.2 12 12.4 12.8 12.3 16 15.5 15.1 15.1 15.4 14.5 14.2 10 MU, min 14.7 13.8 13.8 13.5 13.8 14.2 13.7 18.9 18.3 17.7 17.6 17.8 16.6 16.3 MDR @ 160°C, 5°Arc, 60 min ML, dNm 1.35 1.37 1.32 1.37 1.32 1.27 1.27 1.46 1.44 1.39 1.38 1.34 1.37 1.38 MH, dNm 8.67 9.03 9.27 10.08 10.21 10.33 10.74 7.89 7.73 7.7 7.44 7.22 7.33 7.29 Max-Min, dNm 7.32 7.66 7.94 8.71 8.88 9.06 9.46 6.36 6.29 6.28 6.06 5.87 5.95 5.90 @s2, min 4.92 4.55 4.51 4.34 4.29 4.31 4.22 5.34 5.20 5.16 5.19 5.06 4.99 4.92 125, min 4.72 4.46 4.49 4.50 4.47 4.52 4.50 4.80 4.67 4.63 4.59 4.38 4.33 4.26 t50, min 6.72 6.36 6.35 6.28 6.26 6.26 6.28 6.82 6.61 6.54 6.46 6.25 6.24 6.14 t90, min 21.99 20.45 19.67 17.49 17.15 15.52 14.70 14.55 14.14 14.06 13.69 13.61 15.18 14.83 Peak Rate, dNm/min 1.00 1.20 1.20 1.40 1.40 1.50 1.50 0.90 1.00 1.00 0.90 0.90 0.90 0.90 Curve Type SLM SLM SLM P P P P P P P P P P P MDR @ 180°C, 5° Arc. 30 min ML, dNm 1.16 1.19 1.17 1.21 1.17 1.12 1.08 1.22 1.20 1.16 1.21 1.16 1.13 1.10 MH, dNm 8.11 8.91 9.33 10.06 10.38 10.66 10.90 7.12 7.18 7.26 7.52 7.36 7.29 7.05 Max-Min, dNm 6.95 7.73 8.16 8.86 9.21 9.54 9.83 5.90 5.98 6.10 6.32 6.21 6.16 5.95 ts2,min 1.72 1.69 1.57 1.55 1.57 1.59 1.65 1.87 1.83 1.81 1.69 1.69 1.74 1.76 t25, min 1.64 1.68 1.59 1.59 1.63 1.68 1.76 1.65 1.63 1.63 1.55 1.55 1.58 1.59 t50, min 2.14 2.16 2.05 2.05 2.09 2.17 2.32 2.25 2.22 2.19 2.07 2.05 2.1 2.11 t90, min 4.18 4.20 3.94 3.97 4.09 4.18 4.63 4.23 4.14 4.05 3.83 3.76 4.02 3.98 Peak Rate, dNm/min 3.60 4.10 4.60 5.00 5.20 5.20 4.70 2.60 2.70 2.90 3.20 3.20 3.00 2.90 Curve Type P P SLR P P P P SLR SLR SLR SLR SLR SLR P Stress-Strain Unaged, Tested @ RT, Cured @ 150°C Stress @ break (MPa) 12.23 13.09 11.66 12.19 11.48 11.93 11.15 14.35 14.35 15.62 15.35 13.97 14.40 13.85 Stress @ 100% (MPa) 1.42 1.63 1.68 1.89 2.19 2.30 2.79 1.00 1.00 1.09 1.15 1.16 1.29 1.35 Stress @ 135% (MPa) 1.99 2.32 2.36 2.73 3.21 3.52 4.13 1.29 1.29 1.44 1.51 1.53 1.74 1.81 Stress @ 200% (MPa) 3.36 3.95 3.89 4.72 5.42 5.94 6.83 2.09 2.09 2.35 2.49 2.46 2.87 2.92 Stress @ 300% (MPa) 6.00 6.92 6.89 8.12 8.86 9.61 10.71 3.83 3.83 4.29 4.48 4.39 5.05 5.00 % Elongation @ break 533 509 462 421 377 376 211 764 808 807 761 727 717 700 Shore A @ 4 sec. 48.3 49.9 49.9 49.9 51.3 52.3 52.9 42.7 43.3 44.1 43.9 45.5 45.3 45.5 (Table 5 continued) RECIPE 2A 2B 2C 2D 2E 2F 2G 2H 2I 2J 2K 2L 2M 2N Pierced Demattia Flex, 300 Cycles/min, 60° bend, CYCLES 0 2.00 2.0 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 1,500 4.10 4.10 5.10 6.60 7.95 10.70 11.80 3.50 3.10 3.10 3.20 3.20 3.20 3.40 3,000 4.70 4.70 6.30 8.60 10.00 13.50 16.40 3.70 3.50 3.50 3.50 3.50 3.50 3.50 4,500 4.80 5.40 6.50 9.50 10.35 15.85 20.70 3.90 3.80 3.80 3.80 3.80 3.80 3.80 6,000 5.50 6.20 7.60 9.85 11.15 17.45 23.90 3.90 3.90 3.90 3.90 3.90 3.90 3.90 7,500 5.70 6.45 8.10 11.00 12.30 19.15 25.00 4.00 4.00 4.00 4.00 4.00 4.00 4.00 9,000 6.00 6.75 8.20 11.15 13.25 20.75 25.00 4.10 4.10 4.10 4.10 4.10 4.10 4.10 13,500 6.55 7.55 10.10 12.50 14.60 23.90 25.00 4.20 4.20 4.20 4.20 4.20 4.20 5.00 18,000 6.90 8.05 11.10 13.40 15.95 24.55 25.00 5.60 4.70 5.00 5.25 6.80 6.75 6.75 36,000 7.70 9.75 13.20 15.55 19.65 25.00 25.00 5.60 4.70 5.00 5.25 6.80 6.75 6.75 54,000 8.10 10.85 14.30 16.50 22.95 25.00 25.00 5.75 4.80 5.90 5.85 8.05 7.40 7.95 72,000 8.95 11.60 15.70 18.10 24.20 25.00 25.00 6.00 5.00 6.50 6.55 8.45 7.90 8.15 90,000 9.35 11.80 17.00 19.85 24.35 25.00 25.00 6.05 5.15 6.85 6.60 9.05 8.20 8.85 378,000 10.05 11.90 22.80 20.85 24.90 25.00 25.00 6.05 5.15 7.05 6.60 11.65 10.50 12.15 847,165 15.60 12.40 25.00 22.00 25.0 25.00 25.00 8.25 5.20 7.05 7.15 16.90 11.05 14.55 1,242,000 15.70 12.50 25.00 22.25 25.00 25.00 25.00 8.25 5.20 7.30 7.35 17.10 12.05 15.05 2,200,000 16.10 12.50 25.00 22.25 25.00 25.00 25.00 8.35 5.20 7.35 7.45 17.50 14.90 15.80 Fatigue-to-Failure, 101% Elong., 100 Cycles/min, Unaged, Tested @ RT, Cured @ 180°C for 15 min 1 382.098 155446 106195 142066 89762 194773 109250 692186 131425 366569 415308 744755>1M >1M 2 348919 107814 105536 71838 117265 63778 111594 692914 290035 338539 293552 62931 >1M >1M 3 393855 110177 53523 342040 53111 70859 17893 536780 168475 326686 543833 268469 >1M >1M 4 357880 101538 62925 131567 58382 39272 82772 809775 411101 319488 557428 1032000 >1M >1M 5 448392 81502 902147 236514 142532 96451 27533 737100 551878 263500 716738 1679504 >1M >1M 6 554181 286427 166066 469875 282887 142961 25545 1358755 763175 349740 562505 1143315 >1M >1M 7 569631 307435 161290 57740 276731 152161 76609 1797677 603086 435001 880249 1865972 >1M >1M 8 562373 320560 130784 570482 567069 327414 110034 1504745 244402 504176 689401 673777 >1M >1M Mean 452166 183862 211058 252765 198467 123459 70154 1016242 395447 362962 582377 937590 >1M >1M Rounded Off 452 184 211 253 199 124 70 >1M 395 363 582 938 >1M >1M (x 1000) Ozone Satic - Bent Loop @ 40°C & 25 pphm of O3 Crack 1, Days/Type 0 0 0 0 0 0 0 0 0 0 0 0 0 0 of Crack Test Duration/Days 31 31 31 31 31 31 31 31 31 31 31 31 31 31 Rating Excel Excel Excel Excel Excel Excel Excel Excel Excel Excel Excel Excel Excel Excel (Table 5 continued) RECIPE 2A 2B 2C 2D 2E 2F 2G 2H 2I 2J 2K 2L 2M 2N Ozone Dynamic - Tensile @ 40°C & 25 pphm of O3 Crack 1, Days/Type of 17.4 0 0 0 0 0 0 7.4 0 0 0 0 0 0 Crack Crack 2, Days/Type of 26.5 0 0 0 0 0 0 13.5 0 0 0 0 0 0 Crack Test Duration/Days 31 31 31 31 31 31 31 31 31 31 31 31 31 31 Rating Poor Excel Excel Excel Excel Excel Excel Poor Excel Excel Excel Excel Excel Excel Outdoor Flex Crack 1, Days/Type of 10.1 24.6 0 0 0 0 0 4.2 10.1 24.1 24.1 24.1 24.1 24.1 Crack Crack 2, Days/Type of 28.1/6 31.1/6 0 0 0 0 0 7.2/6 21.2 0 0 0 0 0 Crack Crack 3, Days/Type of 0 0 0 0 0 0 0 10.3/6 38.3 0 0 0 0 0 Crack Crack 4, Days/Type of 0 0 0 0 0 0 0 0 31.3/6 0 0 0 0 0 Crack Test Duration/Days 41 41 41 41 41 41 41 41 41 41 41 41 41 41 Rating Fair Fair Excel Excel Excel Excel Excel Poor Poor Poor Fair Fair Fair Fair These results show that blends with Copolymer 2 had cure characteristics comparable or slightly better than blends with the EXXPRO 93-4, better tensile properties, comparable hardness, substantially better flex crack propagation resistance, better fatigue-to-failure, and better static and dynamic ozone resistance.

EXAMPLE 3 Master batches of brominated isobutylene/para-methylstyrene copolymers of varying bromination level, comonomer content and molecular weight were prepared. The copolymers had the properties listed in Table 6.

TABLE 6 COPOLYMER PROPERTY EXXPRO Test 1 Test 2 90-10 Para-Methylstyrene 7.5 10.0 12.5 (wt%) Bromomethylstyrene 1.2 0.96 0.84 (mol%) Mooney Viscosity (ML(1+8)125"C) 45 i 5 39+5 46 # 5 Test compositions were compounded to blend the master batch components and the cure additives listed in Table 7. Three-pass mixing conditions were used for samples 1W, 1X and 1Y. Two-pass mixing conditions were used for sample 1Z.

BUDENETM 1207 is a trademarked butadiene rubber available from Goodyear.

FLEXON 641 is a naphthenic petroleum oil. FLEXON 815 is a paraffinic petroleum oil.

TABLE 7 RECIPES 1W 1X 1Y 1Z Master Batch (phr) EXXPRO 90-10 ~ 40.00 Test I 50.00 Test 2 50.00 BUDENE 1207 # 50.00 ~ 41.67 41.67 50.00 SMR 10.00 8.33 8.33 50.00 Black N330 55.00 40.00 40.00 Black N660 50.00 FLEXON 641 12.00 12.00 10.00 FLEXON 815 12.00 STRUKTOL 40MS 5.00 4.00 4.00 ESCOREZ 1102 3.00 5.00 5.00 5.00 SP 1068 3.00 2.00 2.00 6PPD 3.00 TMQ 1.00 Sunolite 240 3.00 Cure Package (phr) Stearic Acid 1.00 0.50 0.50 2.00 Zinc Oxide 1.00 0.75 0.75 3.00 Sulfur 0.32 0.40 0.40 1.00 RYLEX 3011 0.50 0.60 0.60 MBTS 1.50 0.80 0.80 DHT4A2 0.50 TBBS 2.00 TOTAL PHR 182.82 166.05 166.05 180.00 The test compositions (1W through IZ) were tested for cure characteristics, tensile strength, flex fatigue, adhesion and ozone resistance. The results are presented in Table 8.

TABLE 8 PROPERTIES 1W 1X 1Y 1Z Mooney Viscosity 1+4 @ 74 55 58 51 100°C Mooney Scorch (iii), 121"C 5 MU, min 23.4 30.7 30.2 30.7 10 MU, min 28.4 35.7 35.2 35.7 MDR @ 1800C, 0.5" Arc ML, dNm 1.88 1.00 1.18 1.48 MH, dNm 11.31 8.17 7.63 11.12 ts2, min 1.45 1.89 1.88 1.31 t25, min 1.57 1.83 1.75 1.39 t50, min 2.14 2.35 2.30 1.68 t90, min 3.50 4.49 4.38 2.26 Peak Rate, dNm,/min Curve Type Stress-Strain, Unaged, Tested til RT, Cured @ 180°C Time of Cure (min) 7.0 7.0 7.0 5.0 Stress @ break (MPa) 15.9 11.6 12.7 16.4 Stress @ 100% (MPa) 1.9 1.5 1.4 1.3 Stress @ 300% (MPa) 7.8 6.0 5.1 6.6 % Elongation @ break 580 509 639 556 Shore A 54.0 45.0 43.0 46.0 Outdoor Flex @ 672 hours, 4 9 10 7 0=Broken; 10=No cracks Pierced Demattia Flex @ 12.75 16.10 8.15 7.40 1,307,890 cycles Fatigue-to-Failure, 101% 73,706 72,137 215,166 378,980 Elong., 100 Cycles/min, Unwaged, Tested (2 RT Die B Tear @ 100°C 238 72 101 147 Die C Tear @ 100°C 188 93 101 143 1" Strip Adhesion to "Carcass" Tested @ 100°C Avg. Peak (lb) 91 93 115 118 Surface Appearance T P P P 1" Strip Adhesion to "Self" Tested @ 100°C Avg. Peak (lb) 69 100 127 112 Surface Appearance T P P P Dynamic Ozone, 50 pphm, <24 <24 <48 <48 NC@336; <48 <48 60% Extension, Hrs. to First 336 Crack Blends 1X and 1Y exhibited superior outdoor flex and ozone resistance over blends 1W and 1Z. The test compositions (1W through 1Z) were used to re-side tires. Tests were conducted on the tires to measure wear and ozone resistance.

The results are presented in Table 9.

TABLE 9 PROPERTIES 1W 1X 1Y 1Z 5% Deflection, 18,550 miles Crackin none none none slight Color good good good brown bloom 10% Deflection, 18,500 miles Cracking none none none slight Color moderate stain good good brown bloom Flexays Ozone Wheel Test, 6 8 10 6 500 hours, 10=no cracks, 0=failure Blends 1X and 1Y exhibited superior wear characteristics to blends 1W and 1Z. Blends 1X and 1Y also exhibited superior ozone resistance over blends 1W and 1Z.