ETHYLEN E/ALKYL ACRYLATE COPOLYMERS AND COMPOUNDS AND VULCANIZATES THEREOF

[0001] The invention relates to ethylene copolymers derived from ethylene, an alkyl acrylate, and optionally an acid cure site comonomer. The invention also relates to compositions using the copolymers and to articles derived from these compositions.

BACKGROUND

[0002] The automotive and transportation industries use elastomeric (rubber-like) materials for a number of underhood or powertrain parts that require elastic properties such as gaskets, seals, hoses, dampers, etc. These parts require good heat and oil resistance. A number of synthetic polymeric materials have been provided for these applications. For example, US Patent 3,873,494 describes vulcanization of ethylene/acrylic ester copolymers in the presence of a peroxide curing system and an antioxidant system that is accelerated by the presence of a butadiene/acrylonitrile polymer. US Patent 4,275,180 describes a polymer composition that comprises a crosslinkable or crosslinked blend of an elastomeric ethylene/alkyl acrylate copolymer and a thermoplastic polymer. US Patent 5,498,669 discloses blends of ethylene/alkyl acrylate dipolymers, neutralized ethylene acid copolymers (ionomers) and organic peroxides, useful for continuous pressureless curing processes. US Patents 3,883,472 and 3,904,588 disclose ethylene/acrylic ester/butenedioic acid monoester terpolymers, compounds and vulcanizates thereof.

[0003] Trends in the automotive industry require the elastomeric materials used in making automotive parts to have wider ranges (both high and low) of service temperature capabilities and good fluid resistance to meet new performance demands. It is also desirable that these elastomers have improved dynamic fatigue resistance, especially at higher operating temperatures. Such a combination of properties and moderate cost are highly desired.

SUMMARY OF THE INVENTION

[0004] The invention provides copolymers, compounded compositions involving these copolymers, and vulcanizates. The copolymers are characterized by higher number average molecular weight and/or narrower molecular weight distribution (polydispersity) than similar previous copolymers. The vulcanizates exhibit improved dynamic fatigue resistance and heat resistance over previous vulcanizates. [0005] This invention provides a composition comprising an ethylene copolymer derived from copolymerization of from 45 to 75 weight %, or 50 to 70 weight %, of an alkyl acrylate such as methyl acrylate; and optionally from about 0.5 to about 5 weight %, or about 1 to about 5 weight %, or about 1.5 to about 5 weight %, or about 1.5 to about 4 weight %, or about 1.5 to about 3 weight % of a 1 ,4-butene-dioic acid or its derivative, wherein the derivative is an anhydride of the acid or a monoalkyl ester of the acid wherein the alkyl group in the monoalkyl ester has from 1 to about 6 carbon atoms, or combinations of two or more thereof; and ethylene being the remainder; wherein the copolymer has a number average molecular weight (M _n ) from a lower limit of about 40,000 to an upper limit of about 55,000, about 60,000 or about 65,000; has a melt index from 1 to 14, from 1 to 12, or from 1 to 6 g/10 min; and preferably a polydispersity from about 2 to about 7, more preferably from 2 to 6. [0006] This invention also provides compound compositions (i.e., precursors to vulcanizates and herein referred to as compounded compositions or merely compounds) comprising the above copolymer and further comprising or produced from a curing agent and optionally one or more additives including an antioxidant, an internal release agent, a scorch retarder, a plasticizer, an accelerator, or a filler. [0007] This invention also provides the compounded composition described above further comprising or produced from at least one additional polymer including an ethylene alkyl acrylate copolymer, a polyacrylate copolymer, or combinations thereof.

[0008] This invention also provides vulcanizates comprising the above compounded compositions that are cured (for example at elevated temperatures and elevated pressures or in a heated salt bath) for sufficient

time to crosslink the copolymers, and optionally post-cured (for example at elevated temperature and ambient pressure) to further cure the vulcanizates.

[0009] This invention also provides an article comprising or produced from a composition that is as characterized as above or is the vulcanizate characterized as above wherein the article includes ignition wire jacketing, tubing, hoses, dampers, seals, gaskets, belts, spark plug boots, constant velocity joint boots, or shaft boots.

[00010] This invention also provides a process comprising contacting ethylene with an alkyl acrylate such as methyl acrylate and optionally a 1 ,4-butene-dioic acid or its derivative, wherein the derivative is an anhydride of the acid, monoalkyl ester of the acid, or combinations of two or more thereof under a condition effective to produce an ethylene copolymer; the alkyl acrylate comprises from 45 to 75 weight %, or about 50 to about 70 weight %, the acid or its derivative when present comprises from about 0.5 to about 5 weight %, or about 1 to about 5 weight %, or about 1.5 to about 5 weight %, or about 1.5 to about 4 weight % or about 1.5 to about 3 weight %, and the remainder is ethylene; the weight % is based on total weight of ethylene, alkyl acrylate, and the acid or its derivative; and the condition includes a temperature from 12O ⁰ C to 185 ⁰ C or from 140°C to 165°C, a pressure from about 1900 to 2810 kg/cm ² (186 MPa to 267 MPa), or from 2065 to 2810 kg/cm ² , (196 to 267 MPa), and a feed temperature from 30°C to 90 ⁰ C or from 50°C to 90°C. [00011] Also provided is the process characterized above further comprising combining the ethylene copolymer with a curing agent, optionally one or more additives, and optionally one or more additional polymers to produce a compounded composition; optionally forming the compounded composition into a desired shape and concurrently or sequentially curing and optionally post curing the compounded composition to produce a vulcanizate or article; wherein the additive includes an antioxidant, an internal release agent, a scorch retarder, a plasticizer, an accelerator, or a filler, or combinations of two or more thereof; the additional polymer includes ethylene alkyl acrylate copolymer, a polyacrylate copolymer, or combinations thereof; and the article includes

ignition wire jacketing, tubing, hoses, dampers, seals, gaskets, belts, spark plug boots, constant velocity joint boots, or shaft boots. [00012] This invention also provides compositions comprising the copolymer described above and further comprising or produced from a second polymer including thermosets such as unsaturated polyester resins, vinyl ester resins, epoxy resins or phenolic resins subject to further curing; or thermoplastics such as polyamides; optionally further comprising fillers, reinforcing fibers (continuous or noncontinuous, woven or nonwoven) or fibrous structures including pulps, or combinations of two or more thereof; optionally wherein the composition is further subjected to curing.

[00013] This invention also provides an article comprising or produced from this composition and the article includes electrical parts such as a distributor cap; printed circuit board; brake pad; or clutch facing; wherein the article can be made using processes such as coating, laminating, molding, extruding, filament winding, calendering or combinations thereof, and subsequently curing.

[00014] This invention also provides the process characterized above further comprising combining the ethylene copolymer with a curing agent, one or more additional polymers including thermosets such as epoxy resins, phenolic resins, unsaturated polyester resins or vinyl ester resins subject to further curing or thermoplastics such as polyamides, and optionally one or more additives including filler, reinforcing fiber, fibrous structure of pulps, or combinations of two or more thereof to produce a compounded composition; and fabricating the compounded composition into an article; the article includes electrical parts such as a distributor cap; printed circuit board; brake pad; or clutch facing; and fabricating includes coating, laminating, molding, extruding, filament winding, calendering, or combinations of two or more thereof, and subsequently curing. DETAILED DESCRIPTION OF THE INVENTION [00015] This invention provides copolymers comprising ethylene and an alkyl acrylate such as methyl acrylate and an optional acid cure site, having higher number average molecular weight (M _n ), lower melt index (Ml) and preferably lower polydispersity than other polymers of the same

comonomer proportions. The copolymers can be prepared by carrying out copolymerization at a combination of lower reactor temperature, higher reactor pressure, and higher feed temperature than described in US Patents 3,883,472 and 3,904,588. Preferably, the copolymers are random copolymers.

[00016] Polydispersity is defined as the weight-average molecular weight divided by the number average molecular weight (M _w /M _n or PD). These molecular weight properties can be determined by using size exclusion chromatography.

[00017] "Copolymer" means polymers containing two or more different monomers, "dipolymer" means a copolymer comprising two comonomers and "terpolymer" means a copolymer comprising three comonomers. [00018] The vulcanizates prepared from the copolymers provide improved dynamic flex fatigue resistance of articles made from them, as shown by a DeMattia test at high temperature (e.g. 150 ⁰ C). A DeMattia test ascertains the number of times a test sample can be repeatedly bent to produce cracking, leading to total failure. Higher molecular weight copolymers enhance high temperature dynamic fatigue resistance of the vulcanizates. They also allow the use of pressureless curing processes (e.g. heated salt baths). Higher molecular weight copolymers with a lower weight % of cure sites improve the heat resistance and further enhance high temperature dynamic fatigue resistance of the vulcanizates. [00019] The copolymers comprise ethylene and an alkyl acrylate. The alkyl acrylate may have up to 10 carbon atoms in the alkyl group, which can be branched or unbranched. For example, the alkyl group may be selected from methyl, ethyl, /7-butyl, 2-ethylhexyl, and other alkyl groups and the alkyl acrylate may be selected from methyl acrylate, ethyl acrylate, /7-butyl acrylate, 2-ethylhexyl acrylate, and other alkyl acrylates containing up to 10 carbon atoms in the alkyl groups. Methyl acrylate is a preferred alkyl acrylate.

[00020] Of note is the ethylene copolymer comprising from 62 to 70 weight % of methyl acrylate. Also of note is the ethylene copolymer comprising from 50 to 62 weight % of methyl acrylate.

[000211 The optional acid cure sites when present comprise from about 0.5 to about 5 weight %, or about 1 to about 5 weight %, or about 1.5 to about 5 weight %, or about 1.5 to about 4 weight % or about 1.5 to about 3 weight %, of 1 ,4-butene-dioic acid moieties or anhydrides or monoalkyl esters thereof. Of note are acid cure sites that comprise a monoalkyl ester of 1 ,4-butene-dioic acid, in which the alkyl group of the ester has from 1 to 6 carbon atoms. The 1 ,4-butene-dioic acid and esters thereof exist in either cis or trans form, i.e. maleic acid or fumaric acid, prior to polymerization. Monoalkyl esters of either are satisfactory. Methyl hydrogen maleate, ethyl hydrogen maleate, propyl hydrogen maleate, butyl hydrogen maleate, or combinations of two or more thereof are particularly satisfactory as the acid cure site.

[00022] Ethylene is the second component in the dipolymer and the third component in the terpolymer. As such, ethylene represents essentially the remainder of the copolymer relative to the required alkyl acrylate and the optional 1 ,4-butene-dioic acid moiety or derivative thereof; i.e., polymerized ethylene is present in the copolymers in a complementary amount.

[00023] Examples of copolymers include copolymers of ethylene (E) and methyl acrylate (MA), copolymers of ethylene and ethyl acrylate, and copolymers of ethylene and n-butyl acrylate. For example, the copolymer comprises ethylene and methyl acrylate and has a M _n from about 40,000 to about 60,000, a melt index from 2 to 12 g/10 min, and a polydispersity from about 3 to about 7 or from 4 to 6.

[00024] Examples of copolymers also include copolymers of ethylene, methyl acrylate and methyl hydrogen maleate; copolymers of ethylene, methyl acrylate and ethyl hydrogen maleate; copolymers of ethylene, methyl acrylate and propyl hydrogen maleate; and copolymers of ethylene, methyl acrylate and butyl hydrogen maleate. For example, the copolymer comprises ethylene, methyl acrylate and from about 1 to about 5 weight % or from about 1 to about 3 weight % of an acid cure site monomer or its derivative; the copolymer has a M _n from about 40,000 to about 65,000 or from about 40,000 to about 60,000 and a polydispersity from about 2 to about 6.

[00025} Copolymers without acid cure sites (dipolymers) can be readily prepared by copolymerizing ethylene and an alkyl acrylate in the presence of a free-radical polymerization initiator including for example peroxygen compounds or azo compounds. Copolymers with acid cure sites (terpolymers) can be similarly prepared by copolymerizing ethylene, an alkyl acrylate, and 1 ,4-butene-dioic acid moieties, anhydrides, or monoalkyl esters thereof.

[00026] The copolymerizations may be run by continuously feeding ethylene, an alkyl acrylate such as methyl acrylate, acid cure-site comonomer if desired (for example a monoalkyl ester of the acid), a free radical initiator, and optionally a solvent such as methanol or the like (see e.g., US Patent 5,028,674) to a stirred autoclave of the type disclosed in US 2,897,183. Alternatively, other high-pressure reactor designs with sufficient mixing, residence time, temperature and pressure control, generally known in the art as autoclaves, operated either alone or in series with or without inter-stage cooling or heating, with multiple compartments and feed zones may be employed. Reactor dimensions such as volume, length and diameter may also influence operating conditions. The rate of conversion may depend on variables such as the polymerization temperature and pressure, monomer feed temperature, monomers employed, concentration of the monomers in the reaction mixture, and residence time for the desired yield and copolymer composition. It may be desirable to adjust the residence time and, in some cases, to use a telogen (chain transfer/chain terminating agent) such as propane, to help adjust the molecular weight. The reaction mixture is continuously removed from the autoclave. After the reaction mixture leaves the reaction vessel, the copolymer is separated from the unreacted monomers and solvent (if solvent was used) by, for example, vaporizing the unpolymerized materials and solvent under reduced pressure and at an elevated temperature. The terms "feed temperature" and "monomer feed temperature" refer to the temperature to which the comonomers are controlled prior to their introduction into the reactor.

[00027] The copolymerization can be carried out in a pressurized reactor at elevated temperature, from 120 ⁰ C to 185°C, or from 140 ⁰ C to

165 ^β C, and pressures of from 1900 to 2810 kg/cm ² , or from 2065 to 2810 kg/cm ² , with feed temperatures from 30 ⁰ C to 90 ⁰ C, or from 5O ⁰ C to 9O ⁰ C.

[00028] Appropriate peroxide initiators for the copolymerization process may depend on the reactor operating conditions, such as temperature and pressure, comonomers used, comonomer concentration, and inhibitors that are typically present in commercially available comonomers. The initiator can be employed neat as a liquid, dissolved or diluted in a suitable solvent such as odorless mineral spirits or mixed with another different initiator. Common classes of organic peroxides useful as free radical initiators include dialkyl peroxides, peroxy esters, peroxy dicarbonates, peroxy ketals, and diacyl peroxides. Examples of suitable peroxides include di(3,3,5-trimethyl hexanoyl) peroxide, terf-butyl perpxypivalate, te/t-butyl peroxyneodecanoate, di(sec-butyl) peroxydicarbonate, and tert- amyl peroxyneodecanoate or combinations of two or more thereof. These and other suitable peroxides are available under the Luperox ^® tradename from Arkema or the Trigonox ^® tradename from Akzo Nobel. Similarly, suitable azo initiators may be used.

[00029] After the continuous operation has reached a steady state, the total per-pass conversion of monomers to polymer may vary from 5 to 25 weight %. The melt index (Ml) of a copolymer may be roughly related to its molecular weight; the lower the Ml the higher the molecular weight. The Ml values are determined at 190 ⁰ C as described in ASTM test method D1238-01 (Procedure A, Condition 190/2.16). The copolymers have Ml that vary, depending on polymerization conditions or the use of a telogen additive, typically but not limiting from about 1 to about 14 g/10 minutes. The percent by weight of the acid cure site monomer, for example an alkyl hydrogen maleate, can be determined by end-point titration using a phenolphthalein indicator (or the like) with a standardized methanolic caustic titre and a known weight of polymer dissolved in a heated/refluxed xylene/butanol mixture. The weight percent of alkyl acrylate such as methyl acrylate can be determined by proton nuclear magnetic resonance (NMR) or Fourier-transform infrared (FTIR) analysis, after calibration by NMR.

[00030] The composition often contains some monomer residuals, mainly of alkyl acrylate. Removal of monomer residuals is generally known in the art as a devolatilization or finishing step. For small laboratory scale preparations, devolatilization can be accomplished by heating in a vacuum oven for a period of time (for example, heating to 100 ⁰ C with a 635 mm Hg vacuum for four hours). For larger-scale preparations, the residuals can be removed by processing through a single or twin-screw extruder with vacuum ports at elevated temperature. Optionally, in finishing the copolymer a release agent (such as R2 listed in Table A) may be added at about 0.1 to 1 weight % in order to improve handling. [00031] In the finishing operation, screw size and design and use of vacuum may impact the amount of copolymer that can be processed and may in turn impact the selection of the appropriate processing variables, including for example screw speed, residence time and temperature. One skilled in the art can design the appropriate processing variables to achieve a balance among these variables for preparation of suitable finished compositions. Adjusting finishing variables can impact the levels of residual monomers (i.e., free comonomers, measured by gas chromatography headspace analysis) present in the finished composition. [00032] The finished ethylene copolymers described above are mixed with additional materials (a process known in the art as compounding) to provide a compounded composition that can be cured (a process known in the art as vulcanization) to provide a vulcanizate. The compositions can be compounded and cured according to the following procedures. [00033] Compounding involves combining the finished copolymer with added ingredients such as cure agents, antioxidants, internal release agents, scorch retarders, plasticizers, accelerators, fillers and the like. Preferred and notable compounded compositions comprise the preferred and notable copolymers described above.

[00034] Optionally, the copolymers can be combined or blended with ethylene alkyl acrylate copolymers, including ethylene di- and terpolymers as generally known in the art (so-called AEM type materials); for example, an ethylene/methyl acrylate dipolymer or an ethylene/methyl acrylate/acid cure site terpolymer with number average molecular weight of less than

40,000, and the like; as well as in combination with polyacrylate copolymers, as generally known in the art (so-called ACM type materials); for example, ethyl acrylate/butyl acrylate/methoxyethyl acrylate/cure site and the like. Blends with AEM materials (e.g. ethylene/methyl acrylate/acid cure site with lower molecular weight) may provide improved processibility such as green strength, collapse resistance or extrusion speed as well as improved dynamic fatigue resistance. Blends with polyacrylate ACM materials (e.g. ethyl acrylate/butyl acrylate/methoxyethyl acrylate, ethyl acrylate/butyl acrylate/cure site and the like) may provide improved processibility.

[00035] The ingredients of the compound (including the copolymer, cure agents, additives, and/or additional polymers) can be mixed in known equipment such as an internal mixer (e.g., a Banbury mixer), a two-roll mill and other similar mixing devices known in the art to achieve a well- dispersed mixture.

[00036] After compounding, the compositions can be vulcanized. Preferred and notable vulcanized compositions comprise the preferred and notable copolymers and compounded compositions described above. A compound comprising the uncrosslinked (unvulcanized) copolymer and a curing agent optionally along with various fillers, other additives and/or polymers is subjected to a curing step at sufficient time, temperature and pressure to achieve covalent chemical bonding (i.e., crosslinking). Vulcanization involves curing the compounded composition at elevated temperature and optionally at elevated pressure for sufficient time to crosslink the copolymer (often referred to as press-curing in laboratory preparations), followed by an optional post-cure heating at ambient pressure to further cure the elastomer. For example, the vulcanizate may be formed and cured using known procedures at about 16O ⁰ C to about 200 ⁰ C for about 2 to 60 minutes. Post-cure heating is conducted at about 160 ⁰ C to about 200°C for one to several hours. [00037] The compounded compositions, such as those comprising a copolymer without an acid cure site, can be vulcanized, for example, in the presence of a peroxide curing system comprising a peroxide and

optionaflf arcoagefϊt. Suitable peroxides and coagents include essentially any such curative system as generally known in the art, including those described herein, operative at the temperature being employed during vulcanization. A preferred peroxide is α,α-bis(f-butylperoxy)- diisopropylbenzene (available from GEO Specialty Chemicals under the tradename Vul-cup ^® ). About 0.5 to 5 parts by weight of peroxide per 100 parts of polymer (phr) may be employed to vulcanize a composition. For safer handling and mixing, the peroxide may be provided on an inert carrier. Peroxide curing systems can be used with either dipolymers or terpolymers.

[00038] The coagent or accelerator used in peroxide cure can be, for example, N,N'-(m-phenylene) dimaleamide, trimethylolpropane trimethylacrylate, tetraallyloxyethane, triallyl cyanurate, tetramethylene diacrylate, or polyethylene oxide glycol dimethacrylate. A preferred coagent/accelerator is N,N'-(/77-phenylene) dimaleamide, available from DuPont Performance Elastomers as HVA-2. The amount of the coagent may be about 0 to 5 parts by weight of coagent per 100 parts of polymer, preferably about 1 to 5 parts by weight per 100 parts of polymer. [00039] Optionally the compound can be cured with heat, with or without extra pressure, to form a vulcanizate with either a solid structure or a foam structure. These higher molecular weight copolymers may be useful for curing processes with minimal or no post-cure heating. [00040] Vulcanizing or curing agents that can be used with copolymers containing acid cure sites include di- and multi-functional amine curing systems, such as hexamethylenediamine carbamate (HMDAC), hexamethylenediamine (HMDA), triethylenetetramine, tetramethylene- pentamine, hexamethylenediamine-cinnamaldehyde adduct, and hexamethylenediamine dibenzoate salt. Aromatic amines can also be used as curing agents. Combinations of two or more curing agents may also be used. The curing agent(s) may be added neat or in an inert carrier. Methods for curing using aqueous HMDA are described in US Patent 7,001 ,957.

[00041] The vulcanization of acid cure site containing polymers can also include various vulcanization accelerators as generally known in the art.

Representative accelerators include guanidine, arylguanidines, alkylguanidines or mixtures thereof. Example accelerators are tetramethylguanidine, tetraethylguanidine, diphenylguanidine and di-ortho- tolyl guanidine. The level of application of guanidine type accelerators is 1 to 6 parts per hundred (phr) of copolymer, preferably 3 to 5 phr. The preferred accelerators are diphenylguanidine (DPG) and di-o/fλo-tolyl guanidine (DOTG), or a combination thereof.

[00042] A curing process may use, for example, 1.25 parts of HMDAC and 4 parts DOTG (alternatively 2 parts DPG and 2 parts DOTG) per 100 parts by weight of the copolymer along with other ingredients being mixed in a Banbury-type internal mixer or on a roll mill followed by a curing step for 30 minutes at 180 ⁰ C at a pressure of about 84 kg/cm ² (8.24 MPa) (see US 3,904,588).

[00043] The vulcanizates may contain an antioxidant system typically based on, but not limited to a phosphorus ester antioxidant, a hindered phenolic antioxidant, an amine antioxidant, or a mixture of two or more of these compounds. The proportion of the antioxidant compound in the vulcanizing composition is 0.1 to 5 parts by weight per 100 parts of polymer, preferably about 0.5 to 2.5 parts by weight per 100 parts of polymer. The antioxidant improves the air heat aging of the vulcanizate. Below the lower limit of this range, the antioxidant effect may be low. The weight ratio of the phenolic or amine antioxidant to the phosphorus compound in mixtures can be about 0.5 to 3; preferably about 1. [00044] The phosphorus ester can be for example, tri(mixed mono-and dinonylphenyl) phosphite, tris(3,5-di-t-butyl-4-hydroxyphenyl phosphate, high molecular weight poly(phenolic phosphonates), and 6-(3,5-di-t-butyl- 4-hydroxy)benzyl-6H-dibenz-[c,c][1 ,2]oxaphosphorin-6-oxide, or combinations of two or more thereof.

[00045] Suitable hindered phenolic antioxidants can be, for example, 4,4'-butylidenebis(6-t-butyl-m-cresol), 1,3,5-trimethyl-2,4,6-tris-(3,5-di~t- butyl-4-hydroxybenzyl)benzene, 2,6-di-t-butyl-α-dimethylamino-p-cresol and 4,4'-thiobis-(3-methyl-6-t-butylphenol) , or combinations of two or more thereof.

[00046] Amine antioxidants include, for example, polymerized 2,2,4- trimethyl-1 ,2-dehydroquinoline; N-phenyl-N'-(p-toluenesulfonyl)-p- phenylenediamine, N,N'-di(β-naphthyl)-p-phenylenediamine, and 4,4'- bis(α,α-dimethylbenzyl)diphenylamine, or combinations of two or more thereof.

[00047] Antioxidant compositions can contain tri(mixed mono-and dinonylphenyl) phosphite mixed with either 4,4'-butylidenebis(6-t-butyl-m- cresol) or 4,4'-bis(α,α-dimethylbenzyl)diphenylamine. Particularly preferred antioxidant compositions contain 4,4 ^I -bis(α,α-dimethylbenzyl)~ diphenylamine (available commercially as Naugard ^® 445 from Chemtura). [00048] Fillers can be used to reduce cost and to improve mechanical properties. A vulcanized composition may contain from 25 to 60 or 70 volume percent of fillers, alternatively from 30 to 120 or 150 parts of filler per hundred parts of polymer. Suitable fillers include, for example but not by way of limitation, carbon black, calcium carbonate, magnesium silicate or silica, notably carbon black. The preferred proportion can depend on the reinforcing effect of the filler used, which can be influenced by factors such as particle size of the filler.

[00049] Once cross-linked, the compositions described herein are not thermoplastic, perse, so articles may be prepared by forming the compound into the desired shape by molding or extrusion procedures and concurrently or subsequently curing the compound. [00050] The vulcanizates can be used in a wide variety of automotive and nonautomotive articles, including ignition wire jacketing, spark plug boots, tubing, hoses, belts, miscellaneous molded boots, dampers, seals and gaskets. Tubing includes but is not limited to crank case vent tubing, diesel particle filter tubing and engine management tubing. Hoses include but are not limited to turbocharger hoses, turbo diesel air cooler hoses, transmission oil cooler hoses, power steering hoses (low pressure), air conditioning hoses, air ducts, fuel line covers, and vent hoses. The vulcanizates are also useful for crankshaft torsional dampers and for noise management parts such as grommets.

[00051] A higher molecular weight dipolymer or terpolymer can be used alone or in blends with other copolymers of ethylene and one or more alkyl

acrylates optionally having an acid cure site (e.g. ethylene/methyl acrylate/acid cure site) as well as with polyacrylates (e.g. ethyl acrylate/butyl acrylate/methoxyethyl acrylate, ethyl acrylate/butyl acrylate/cure site and the like) for applications such as hoses, dampers, and seals for improved dynamic fatigue resistance and processability. [00052] The articles can be prepared by compounding the copolymer with added ingredients such as cure agents, antioxidants, internal release agents, scorch retarders, plasticizers, accelerators, fillers and the like and forming the composition into the desired shape by, for example, injection molding, compression molding or transfer molding. The compositions are held in the molds at elevated temperature and pressure for a period of time to initiate crosslinking (curing) and the shaped compositions are then removed from the molds and optionally heated further at ambient pressure (post-curing) to continue the curing.

[00053] In some cases such as tubing or hoses, the compounded composition as described above can be formed into a shaped article by extrusion through an appropriately designed die. The initially-shaped article can be further shaped by forming with a mandrel while still pliable prior to curing. Hoses and tubing can be cured by treatment with super heated steam, hot air or hot inert gases such as nitrogen to provide the necessary heat and pressure. Straight tubing made from peroxide-curable compounds can be cured in a heated salt bath at ambient pressure. [00054] Some articles may comprise elements in addition to the compositions as described herein. For example, articles (e.g. seals) may be prepared in which the composition of this invention is molded around a metal or plastic element. Other articles (e.g. hoses) can be extruded with reinforcing fibers, fiber structures or cording incorporated therein. [00055] Although the copolymers are discussed herein primarily in terms of their use in compositions capable of forming elastomeric vulcanizates, they may also be used in other applications. Accordingly, this invention also provides compositions comprising the copolymers described above and further comprising or produced from a second polymer including thermosets such as unsaturated polyester resins, vinyl

ester resins, epoxy resins or phenolic resins subject to further curing; or thermoplastics such as polyamides; optionally further comprising fillers, reinforcing fibers or fibrous structures such as pulps. Reinforcing fibers can be continuous or noncontinuous, woven or nonwoven. The fibers may be made of glass, carbon (graphite), para-aramids, meta-aramids, metal or mineral. Curing processes include, for example but not limited to, use of di- and multi-functional amine systems, with application of heat and optionally pressure.

[00056] The copolymers provide, for example but not limited to, toughening for polyamide compositions (for example, at less than 30 weight % of copolymer in the polyamide composition). Polyamides include those known in the art. Polyamides generally can be prepared from lactams or amino acids (e.g. nylon-6 or nylon-11), or prepared from condensation of diamines such as hexamethylenediamine with dibasic acids such as succinic, adipic, or sebacic acid. Copolymers and terpolymers of these polyamides are also included. Polyamides include polyepsiloncaprolactam (nylon-6), polyhexamethylene adipamide (nylon-66), nylon-11, nylon-12, nylon-12, 12 and copolymers and terpolymers such as nylon-6/66, nylon-6/10, nylon-6/12, nylon-66/12, nylon-6/66/610 and nylon-6/6T, or combinations of two or more thereof. Notable polyamides are polyepsiloncaprolactam (nylon-6), polyhexamethylene adipamide (nylon-66), particularly nylon-6, or combinations thereof. In addition to the polyamides described above, other polyamides such as amorphous polyamides may also be used. [00057] An article comprising or produced from compositions comprising the copolymer and further comprising at least one additional polymer (e.g. thermosets such as unsaturated polyester resins, vinyl ester resins, epoxy resins or phenolic resins) can be made from processes such as coating, laminating, molding, extruding, filament winding, calendering or combinations thereof. Examples of such articles include electrical parts including distributor caps; printed circuit boards; brake pads; clutch facings and other articles fabricated from toughened thermosets. [00058] While the invention has been particularly shown and described with reference to certain embodiments thereof, it may be understood by

those skilled ^' Fn the art that various changes in form and details may be made without departing from the spirit and scope of the invention. The following Examples are merely illustrative, and are not to be construed as limiting the scope of the invention described and/or claimed herein.

EXAMPLES

[00059] Copolymers of this invention were produced in a high pressure pilot-scale autoclave reactor with reaction parameters summarized in the following Tables. Amounts of comonomers in the final copolymer are indicated in weight percent, unless indicated otherwise. [00060] The molecular weights of the copolymers were determined by using the size exclusion chromatography (also known as GPC, Gel Permeation Chromatography) technique common to the field. An integrated multi-detector size exclusion chromatography system, such as GPCV 2000™ from Waters Corporation (Milford, MA) was used. It is capable of keeping a constant temperature across the entire path of a polymer solution from the injector through detectors. Two differential online detectors were used in series: a refractive index detector and a capillary viscometer detector. There were four 8mm x 300 mm styrene- divinyl benzene columns in the system, for separation: two linear GPC KF806M, one GPC KF802 and one GPC KF-801 , all from Shodex (Japan). The mobile phase was tetrahydrofuran stabilized with 0.05% butylated hydroxytoluene, (JT. Baker, Phillipsburg, NJ). The columns were calibrated with a set of 10 narrow polydispersity (<1.1) polystyrene (PS) standards with peak molecular weights from 580 through 7,500,000 (Polymer Laboratories). Test samples were prepared by dissolving the polymer in mobile phase solvent at 40 °C with continuous moderate agitation without filtration (automatic sample preparation system PL 260™ from Polymer Laboratories, Church Stretton, UK). The sample was injected into the column and data collected. The operating conditions were: temperature, 4O ⁰ C; flow rate, 1.0 ml/min; injection volume, 0.219 ml; run time, 90 minutes. The data were analyzed with the software Empower™ 1.0 Chromatography Data Manager from Waters.

100061] ^' The copolymers were compounded with additional components including cure agents, accelerators, fillers, release aids, and antioxidants (see Table A below) according to the following general procedure. [00062] The respective starting ingredients were mixed on a B or OOC size Banbury-type internal mixer using an upside-down mixing procedure and a dump temperature of 100 to 105 ⁰ C followed by further mixing on a two-roll mill at about 25°C to achieve a homogeneous mixture. Amounts of components in the Tables hereafter are provided in parts per hundred (phr) of polymer. In the Tables "- -" stands for no data.

Table A

Material Trade Name Supplier

Release Aids/

Scorch Retarders

R1 Octadecyl Amine Armeen ^® 18D Akzo Nobel

R2 Complex Organic Vanfre ^® VAM R. T. Vanderbilt

Phosphate Ester

R3 Stearic Acid

Anti-oxidants

A1 4,4'-bis(α,α-dimethylbenzyl)- Naugard ^® 445 Chemtura diphenylamine

Plasticizers

P1 Mixed Ether/Ester Plasticizer TP ^® -759 Rohm & Haas

Filler

F1 Carbon Black (FEF N-550)

Curative System

CA1 α,α-bis(f-butylperoxy)- Vul-cup® GEO Specialty diisopropylbenzene 40KE Chemicals

CA2 N,N'-(rø-phenylene) HVA-2 DuPont dimaleamide Performance

Elastomers

CA3 Hexamethylene Diamine Diak ^tm #1 DuPont

Carbamate (HMDAC) Performance

Elastomers

CA4 Di-ortho-tolyl Guanidine

(DOTG)

CA5 Diphenyl Guanidine (DPG) Swan

[00063] Vulcanized slabs of 1.9 mm nominal thickness were prepared by curing the compounded composition for 5 to 10 minutes at 18O ⁰ C at a pressure of about 43.2 kg/cm ² (4240 kPa) and then post-cured at 175°C for one hour at ambient pressure. Slabs at 3 mm nominal thickness were prepared similarly. Samples for the DeMattia testing were prepared by molding the compounded composition into test coupons for 5 to 10 minutes at 180 ⁰ C at a pressure of about 43.2 kg/cm ² (4240 kPa), followed by post-cure heating at 175 ⁰ C for one to four hours.

JOO064] Compression set testing was conducted according to ASTM D395-02. Mooney viscosity and Mooney scorch testing were conducted according to ASTM D1646-03. MDR testing was conducted according to ASTM D5289-95 (reapproved 2001). DeMattia testing was conducted according to ASTM D430-95 Type 2 (reapproved 2000). [00065] For example, a dipolymer of this invention was produced in a high pressure pilot-scale autoclave reactor at a reactor temperature of 145 ⁰ C and a pressure of 2110 kg/cm ² (207 MPa) with an ethylene feed rate of 11.34 kg/h, a methyl acrylate feed rate of 1.82 kg/h, a methanol solvent feed rate of 450 g/h, and a propane telogen feed rate of 1.29 kg/h at a feed temperature of 70°C. Di(sec-butyl) peroxydicarbonate (Luperox ^® 225 from Arkema) initiator was used, diluted to 4 volume % in odorless mineral spirits. This process provided a copolymer at a rate of 1.36 kg/h. The resulting copolymer had 69.2 weight % of methyl acrylate with a melt index of 11.8 g/10 minutes and a polydispersity of 3.84, having a M _n of 49,800. Additional dipolymer examples were prepared similarly. [00066] The following Examples in Table 1 illustrate materials comprising dipolymers derived from ethylene and methyl acrylate, having from 60 to 70 weight % methyl acrylate. The Examples illustrate that lower reactor temperature, higher pressure and higher feed temperature were factors in raising molecular weight and lowering polydispersity compared to Comparative Example C1.

Table 1

Copolymer

Reaction Conditions Cl 2 3

Pressure (kg/cm ² ) 2110 2180 2110

Reactor Temperature ( ⁰ C) 165 145 145

Feed Temperature ( ⁰ C) 40 50 70

MA level 62.8 62.8 69.2

Melt Index 15.2 7.3 11.8

M _n divided by 1000 32.8 43.8 49.8

Mw divided by 1000 185.8 173.8 191.1

Polydispersity 5.66 3.97 3.84

Compounded Composition

Compound C101 102 103

Copolymer C1 2 3

Amount of Copolymer, phr 100 100 100

A1 1 1 1

R2 1 1 1

R3 0.5 0.5 0.5

R1 0.5 0.5 0.5

F1 50 50 50

CA1 5 5 5

CA2 2 2 2

Total phr 160.0 160.0 160.0

Stock Properties

Compound C101 102 103

MOONEY VISCOSITY, MU1+4) at 100 ⁰ C 37.7 39.6 31.8

MOONEY SCORCH. MS at 121 °C

Minimum, mu 11.7 11.5 8.5 t(3), min >20 >20 >20

MDR at 180 °C. 0.5 ARC. 20 MIN.

ML, dNm 0.44 0.55 0.49

MH, dNm 11.71 13.64 10.01 ts2, min 0.77 0.69 0.77 t(50), min 1.36 1.22 1.22 t(90), min 4.22 3.82 3.89

Vulcanizate Properties

Vulcanizate C201 202 203

Compound C101 102 103

^• I) COMPRESSION SET. METHOD B. PLIED PELLETS

After 70 hrs. at 150 °C 22.1 20.4 21.1

2) STRESS-STRAIN AND HARDNESS. ORIGINAL AT 23 ⁰ C

Hardness, Shore A, points 69.0 68.2 70.6

M, 50%, MPa 2.2 2.2 2.3

M, 100%, MPa 5.1 5.0 4.9

Tb, MPa 14.6 16.4 15.9

Eb, % 257 280 304

Tear, Die C, kN/m 28.2 30.5 30.3

[00067] Table 2 illustrates DeMattia testing of vulcanizates from Table 1. The results indicate that greater than 7-fold increase in dynamic fatigue resistance under this testing condition can be achieved.

TaBIe ¹ Z ^'" - ^" DeMattia Fatigue Resistance at 150 °C

Vulcanizate C201 202 203

Cycles to total failure (median of 6 samples) 10 75 155

[00068] For example, a terpolymer of this invention was produced in a high pressure pilot-scale autoclave reactor at a reactor temperature of 145°C and a pressure of 2180 kg/cm ² (214 MPa) with an ethylene feed rate of 11.34 kg/h, a methyl acrylate feed rate of 1.63 kg/h, an ethyl hydrogen maleate feed rate of 27.2 g/h, a methanol solvent feed rate of 435.5 g/h, and a propane telogen feed rate of 726 g/h at a feed temperature of 70 ⁰ C. Di(sec-butyl) peroxydicarbonate (Luperox ^® 225 from Arkema) initiator was used, diluted to 10 volume % in odorless mineral spirits. This process provided a copolymer at a rate of 1.1 kg/h. The resulting terpolymer had 1.6 weight % ethyl hydrogen maleate and 60.9 weight % methyl acrylate with a melt index of 2.8 g/10 minutes and a polydispersity of 4.1, having 67 % higher M _n than the comparative examples in the Tables. Additional Examples were prepared similarly. [00069] The Examples in Tables 3 to 11 illustrate materials comprising ethylene copolymers derived from ethylene, methyl acrylate and an additional acid cure site comonomer, having 54 to 62 weight % methyl acrylate. Unless noted otherwise, the compounds were vulcanized by being press cured for five minutes at 177 ⁰ C and post cured for 4 hours at 175 ⁰ C. Vulcanizates prepared from the example terpolymers exhibited over 200 times better cycles to failure in a DeMattia test (at 15O ⁰ C on samples that were pre-heat aged 94 hours at 200 ⁰ C before testing) than lower molecular weight materials.

[00070] In Table 3, the Examples illustrate that lower reactor temperature, higher pressure and higher feed temperature were factors in raising molecular weight and lowering polydispersity compared to Comparative Example C4.

Table 3

Copolymer

Reaction Conditions C4 5 6 7

Pressure (kg/cm ² ) 1900 2320 2320 2320

Reactor Temperature ( ⁰ C) 165 145 145 165

Feed Temperature ( ⁰ C) 10 10 75 10

Mn divided by 1000 27.6 44.7 53.6 44.1

Mw divided by 1000 235.1 336.3 234.8 267.0

Polydispersity 8.52 7.53 4.38 6.05

Ml 31.8 1.5 1.8 4.6

MA level 53.9 57.0 55.8 55.8

Cure site level 4 4 4 4

Compounded Composition

Compound C104 105 106 107

Copolymer C4 5 6 7

Amount of Copolymer, phr 100 100 100 100

A1 2 2 2 2

R3 1.5 1.5 1.5 1.5

R2 1.5 1.5 1.5 1.5

R1 0.5 0.5 0.5 0.5

F1 60 60 60 60

P1 10 10 10 10

CA3 1.5 1.5 1.5 1.5

CA4 4 4 4 4

Total phr 181.0 181.0 181.0 181.0

Stock Properties

Compound C104 105 106 107

MOONEY VISCOSITY.

MU1+4) at 100 °C 28.7 121.7 221.7 99.2

Vulcanizate Properties

Vulcanizate C204 205 206 207

ComDound C104 105 106 107

1) COMPRESSION SET. METHOD B. PLIED PELLETS After 70 hours at 150 °C 23.9 16.3 14.4 16.3

2) STRESS-STRAIN AND HARDNESS. ORIGINAL AT 23 °C Hardness, Shore A, points 67.7 66.4 66.7 66.6

M 100%, MPa 4.4 4.9 4.6 4.6

Tb, MPa 12.8 16.1 16.5 15.6

Eb, % 303 281 283 288

Tear, Die C, kN/m 35.9 35.5 34.0 36.1

[00071] The Examples in Tables 4 and 5 illustrate the effects of varying lower cure site levels with higher molecular weight for improved heat resistance. The heat resistance reported in the Tables is assessed by 1) accelerated heat aging (94 hours at 200 ⁰ C) followed by testing of tensile properties at room temperature; and 2) air heat aging according to ASTM D573-99. Comparative Example C8 was a commercially available AEM copolymer having lower molecular weight.

Table 4

Copolymer

Reaction Conditions C8 9 10 11

Pressure (kg/cm ² ) _. 2320 2110 2110

Reactor Temperature ( ⁰ C) — 145 165 145

Feed Temperature (°C) — 70 70 70

Mn divided by 1000 37.2 59.2 46.3 51.7

Mw divided by 1000 163 205 206 211

Polydispersity 4.38 3.47 4.44 4.09

Ml 8 1 2.5 1.7

MA level 55.0 55.3 56.9 55.3

Cure site level 2.5 2.5 1.5 2.55

Compounded Copolymer

Compound C108 109 110 111

Copolymer C8 9 10 11

Amount of Copolymer, phr 100.5 100 100 100

A1 2 2 2 2

R3 1.5 1.5 1.5 1.5

R2 1 1.5 1.5 1.5

R1 0.5 0.5 0.5 0.5

F1 50 50 50 50

CA3 1.5 1.25 0.75 1.3

CA4 4 4 4 4

Total phr 161.00 160.75 160.25 160.80

Stock Properties

Compound C108 109 110 111

MOONEY VISCOSITY.

ML(1+4) at 100 °C 45.0 >228 78.2 >228

Vulcanizate Properties

Vulcanizate C208 209 210 211

Compound C108 109 110 111

1) COMPRESSION SET. METHOD B. PLIED PELLETS

After 70 hours at 150 ⁰ C 23.5 16.3 30.6 17.2

2) STRESS-STRAIN AND HARDNESS. ORIGINAL AT 23 ⁰ C Hardness, Shore A, points 74.3 71.8 64.9 70.3 M 100%, MPa 4.7 4.7 2.8 5.0 Tb, MPa 17.3 18.0 15.2 18.7 Eb ₁ % 376 321 576 334

Tear, Die C, kN/m 41.8 36.9 46.9 36.2

3) 23 ⁰ C STRESS AND STRAIN AFTER HEAT AGING 94 HOURS at 200 ⁰ C

Hardness, Shore A, Points 81.6 76.5 71.9 75.8

M 100%, MPa 7.0 6.1 3.6 6.6

Tb, MPa 11.9 11.8 9.8 14.8

Eb, % 168 182 294 200

4) STRESS-STRAIN AND HARDNESS AFTER AGING 1 WEEK at 175 ⁰ C IN AIR

Hardness, Shore A, Points 73.8 72.8 68.8 73.3

M 100%, MPa 5.2 4.8 3.1 5.2

Tb, MPa 15.8 16.5 11.9 16.0

Eb, % 366 358 556 301

5) STRESS-STRAIN AND HARDNESS AFTER AGING 1 WEEK at 180 ⁰ C IN AIR

Hardness, Shore A, Points 77.5 72.8 66.8 73.2

M 100%, MPa 5.7 5.2 3.2 5.3

Tb, MPa 16.0 17.0 11.8 17.5

Eb, % 339 348 546 336

6) STRESS-STRAIN AND HARDNESS AFTER AGING 1 WEEK at 185 ⁰ C IN AIR

Hardness, Shore A, Points 90 75.2 67.1 77.5

M 100%, MPa 6.1 5.5 3.1 6.1

Tb, MPa 13.5 15.6 10.4 15.5

Eb ₁ % 219 282 389 263

Table 5

Copolymer

Reaction Conditions C8 12 13 14 15 16

Pressure (kg/cm^) — 2320 2110 2110 2110 2110

Reactor Temperature ( ⁰ C) — 145 165 145 145 145

Feed Temperature ( ⁰ C) - 70 70 70 70 70

Mn divided by 1000 37.2 59.2 46.3 51.7 46.4 46.1

Mw divided by 1000 163 205 206 211 203 200

Polydispersity 4.38 3.47 4.44 4.09 4.38 4.33

Ml 8 1 2.5 1.7 2.1 2.1

MA level 55.0 55.3 56.9 55.3 55.7 55.1

Cure site level 2.5 2.5 1.6 2.6 1.5 2.0

Compounded Copolymer

Compound C117 112 113 114 115 116

Copolymer C8 12 13 14 15 16

Amount of Copolymer, phr 100.5 100 100 100 100 100

A1 2 2 2 2 2 2

R3 1.5 1.5 1.5 1.5 1.5 1.5

R2 1 1.5 1.5 1.5 1.5 1.5

R1 0 0.5 0.5 0.5 0.5 0.5

F1 50 50 50 50 50 50

CA3 1.25 1.25 0.8 1.25 0.8 1.0

CA4 2 2 2 2 2 2

CA5 2 2 2 2 2 2

Total phr 160.25 160. 75 160.30 160. 75 160. 30 160.51

Stock Properties

Compound C117 112 113 114 115 116

MOONEY VISCOSITY.

ML(1+4) at 100 °C 49.9 >221.4 80.8 210.0 >211.7 >221..

Vulcanizate Properties

Vulcanizate C217 212 213 214 215 216

Compound C117 112 113 114 115 116

1) COMPRESSION SET. METHOD B. PLIED PELLETS

After 70 hours at 150 ⁰ C 26.8 20.7 45.3 22.9 44.4 30.0

2) STRESS-STRAIN AND HARDNESS. ORIGINAL AT 23 °C

Hardness, Shore A, points 72.6 67.5 61.2 69.0 66.3 66.7

M 100%, MPa 4.0 3.9 2.5 4.5 2.6 3.2

Tb, MPa 17.3 19.4 13.4 18.8 14.4 15.5

Eb, % 452 386 577 354 579 417

Tear, Die C, kN/m 38.9 35.0 51.7 37.5 49.6 40.3

3) STRESS-STRAIN AND HARDNESS AFTER AGING 94 HOURS at 200 ⁰ C IN AIR,

TESTED AT ^" 23 ⁰ C

Hardness, Shore A, Points 76.7 74.4 73.0 75.7 72.8 74.1

M 100%, MPa 5.2 4.8 3.0 5.4 3.1 3.9

Tb, MPa 10.1 10.8 7.2 10.6 7.2 9.9

Eb, % 184 201 278 178 265 252

4) STRESS-STRAIN AND HARDNESS AFTER AGING 1 WEEK at 175 ⁰ C IN AIR

Hardness, Shore A, Points 74.8 69.6 67.2 71.2 69.0 70.9

M 100%, MPa 4.1 4.1 2.5 4.6 2.6 3.2

Tb, MPa 14.3 15.9 9.1 15.6 ₍ 9.6 12.0

Eb, % 428 403 494 370 537 481

5) STRESS-STRAIN AND HARDNESS AFTER AGING 1 WEEK at 180 ⁰ C IN AIR

Hardness, Shore A, Points 74.5 73.1 69.0 71.8 69.9 71.4

M 100%, MPa 4.6 4.4 2.7 5.0 2.7 3.6

Tb, MPa 14.8 16.5 9.4 16.1 10.0 12.4

Eb, % 376 369 478 337 497 411

6) STRESS-STRAIN AND HARDNESS AFTER AGING 1 WEEK at 185 ⁰ C IN AIR

Hardness, Shore A, Points 75.4 72.3 70.0 73.7 69.6 71.6

M 100%, MPa 4.8 4.3 2.8 5.1 2.8 3.8

Tb, MPa 10.9 13.0 8.0 12.3 8.3 10.7

Eb, % 218 264 382 219 388 312

[00072] The Examples in Table 6 illustrate the evaluation of vulcanizates of this invention for high temperature dynamic fatigue resistance. The compound properties are shown in Table 6 and the dynamic fatigue resistance, as indicated by DeMattia testing, is summarized in Table 9.

Table 6

Copolymer

Reaction Conditions C8 18 19

Pressure (kg/cnn^) — 2110 2110

Reactor Temperature ( ⁰ C) — 145 145

Feed Temperature ( ⁰ C) - 70 70

Mn divided by 1000 37.2 46.4 46.1

Mw divided by 1000 163 203 200

Polydispersity 4.38 4.38 4.33

Ml 8 2.5 2.2

MA level 55.0 55.7 55.1

Cure site level 2.5 1.4 1.98

Compounded Copolymer

Compound C120 118 119

Copolymer C8 18 19

Amount of copolymer, phr 100.5 100 100

A1 2 2 2

R3 1.5 1.5 1.5

R2 1 1.5 1.5

R1 0 0.5 0.5

F1 50 50 50

CA3 1.25 1.05 0.83

CA4 2 2 2

CA5 2 2 2

Total phr 160.25 160.55 160.33

Stock Properties

Compound C120 118 119

MOONEY VISCOSITY.

ML(1+4) at 100°C 43.8 83.5 100.1

MOONEY SCORCH. MS at 12' 1 °C

Minimum, mu 14.0 34.7 44.2 t(3), min 9.74 8.37 5.05 t(10), min 18.03 — 8.15 t(18), min >20 >20 13.87

MDR at 177 °C/0.5 deαrees/20 minutes

ML, dNm 0.52 1.18 1.37

MH, dNm 9.00 6.46 6.92 ts2, min 1.53 2.43 1.64 t(50), min 2.79 2.91 2.05 t(90), min 12.05 10.61 10.59

Vulcanizate Properties

Vulcanizate C220 218 219

Compound C120 118 119

1) COMPRESSION SET. METHOD B. I ³ LIED PELLETS

After 70 hrs. at 150 ⁰ C 43.5 49.3 46.1

2) STRESS-STRAIN AND HARDNESS . ORIGINAL AT 23 ⁰ C

Hardness, Shore A, points 69.4 66.0 65.0

M 100%, MPa 3.9 3.0 2.9

Tb, MPa 16.3 16.2 15.8

Eb, % 440 543 537

Tear, Die C, kN/m 38.9 42.2 45.9

3) STRESS-STRAIN AND HARDNESS AFTER AGING 94 HOURS at 200 ⁰ C IN AIR.

TESTED AT 23 ⁰ C

Hardness, Shore A, Points 73.9 70.4 68.6

M 100%, MPa 5.1 3.4 3.5

Tb, MPa 11.9 11.0 11.0

Eb, % 233 328 313

4} STRESS-STRAIN AND HARDNESS AFTER AGING 1 WEEK at 175 ⁰ C IN AIR

Hardness, Shore A, Points 74.8 69.2 69.6

M 100%, MPa 4.5 3.5 3.5

Tb, MPa 15.1 13.0 12.6

Eb, % 440 539 524

5) STRESS-STRAIN AND HARDNESS AFTER AGING 1 WEEK at 180 ⁰ C IN AIR

Hardness, Shore A, Points 75.8 68.4 69.7

M 100%, MPa 4.7 3.3 3.1

Tb, MPa 12.8 10.6 10.1

Eb, % 308 443 419

[00073] The Examples in Table 7 are high molecular weight copolymers with cure site levels lower than 2 weight %. The tensile properties of vulcanizates after accelerated heat aging at 200 °C, and long-term heat aging properties at 165, 170 and 175 ⁰ C are reported in Table 7 and dynamic fatigue resistance testing (DeMattia) are shown in Table 10.

Table 7

Copolymer

Reaction Conditions C8 21 22 23 24

Pressure (kg/cm^) — 2180 2180 2180 2110

Reactor Temperature ( ⁰ C) - 155 155 145 145

Feed Temperature ( ⁰ C) — 50 70 70 70

Mn divided by 1000 37.2 40.0 46.3 47.1 46.1

Mw divided by 1000 163 198 159 193 200

Polydispersity 4.38 4.94 3.45 4.09 4.33

Ml 8 4.7 5.8 2.8 1.9

MA level 55.0 59.5 58.9 60.9 55.1

Cure site level 2.5 1.70 1.80 1.63 1.86

Compoundec I Copolymer

Compound C125 121 122 123 124

Copolymer C8 21 22 23 24

Amount of Copolymer, phr 100.5 100 100 100 100

A1 2 2 2 2 2

R3 1 1.5 1.5 1.5 1.5

R2 1.5 1.5 1.5 1.5 1.5

R1 0 0.5 0.5 0.5 0.5

F1 50 50 50 50 50

CA3 1.25 0.85 0.90 0.82 0.93

CA4 2 2 2 2 2

CA5 2 2 2 2 2

Total phr 160.25 160.35 160.40 160.32 160.43

Stock Properties

Compound C125 121 122 123 124

MOONEY VISCOSITY.

ML(1+4) at 100 °C 47.2 62.0 64.0 78.3 91.1

MOONEY SCORCH. MS at 121 ⁰ C

Minimum, mu 16.4 23.6 25.1 32.3 40.4 t(3), min. 9.58 10.05 8.46 7.54 5.65 t(10), min. 18.02 >20 17.84 14.64 8.89 t(18), min. >20 >20 >20 >20 14.21

MDR at 177 °C/0.5 deqrees/20 minutes

ML, dNm 0.54 0.78 0.80 1.07 1.30

MH, dNm 9.28 4.82 5.56 5,36 8.06 ts2, min. 1.51 3.07 2.47 2.75 1.38 t(50), min. 2.77 2.66 2.62 2.58 2.04 t(90), min. 11.33 11.04 11.02 10.51 9.77

Vulcanizate Properties

Vulcanizate C225 221 222 223 224

CorriDound C125 121 122 123 124

1) COMPRESSION : SET. METHOD B. PLIED PELLETS

After 70 hrs. at 15C ) ⁰ C 33.0 49.1 44.5 46.7 34.6

2} STRESS-STRAIN AND HARDNESS. ORIGINAL AT 23 ⁰ C

Hardness, Shore i \ points 67.8 65.3 65.6 65.2 64.1

M 100%, MPa 4.33 3.0 3.1 2.9 3.5

Tb, MPa 17.5 13.8 14.7 14.5 17.5

Eb, % 459 620 592 604 532

Tear, Die C, kN/m 45.5 46.6 46.0 54.6 45.2

3) STRESS-STRAIN AND HARDNESS AFTER AGING 94 HOURS at 200 ⁰ C IN AIR

TESTED AT 23 ⁰ C

Hardness, Shore A, Points 77.0 70.4 73.6 69.0 68.7

M 100%, MPa 5.6 3.3 3.8 2.9 3.8

Tb, MPa 12.4 9.2 10.0 9.8 12.1

Eb, % 218 311 298 396 295

4A) STRESS-STRAIN AND HARDNESS AFTER AGING 1 WEEK at 165 ⁰ C IN AIR

Hardness, Shore A, Points 72.0 68.9 70.5 67.4 67.8

M 100%, MPa 4.3 2.9 3.1 2.7 3.2

Tb, MPa 15.5 10.4 11.8 11.0 14.4

Eb, % 431 607 564 625 547

4B) STRESS-STRAIN AND HARDNESS AFTER AGING 6 WEEKS at 165 ⁰ C IN AIR

Hardness, Shore A, Points 83.8 76.0 76.7 79.1 74.9

M 100%, MPa — 5.8 6.0 5.8 6.7

Tb, MPa 8.1 8.0 7.4 6.9 7.1

Eb, % 84 126 130 131 113

5A) STRESS-STRAIN AND HARDNESS AFTER AGING 1 WEEK at 170 ⁰ C IN AIR

Hardness, Shore A, Points 74.2 67.1 70.5 69.5 67.4

M 100%, MPa 4.4 2.9 3.4 3.0 3.4

Tb, MPa 15.8 10.7 11.9 11.2 14.7

Eb, % 446 598 588 648 558

5B)STRESS-STRAIN AND HARDNESS AFTEF * AGING 6 ' WEEKS ai t 170 ⁰ C Ih J AIR

Hardness, Shore A, Points 81.2 77.6 77.8 76.4 75.5

M 100%, MPa — 5619 5336 4812 5922

Tb, MPa 8.7 7.2 7.2 7.2 8.1

Eb, % 99 138 149 164 142

6) STRESS-STRAIN AND HARDNESS AFTER AGING 3 WEEKS at 175 ⁰ C IN AIR

Hardness, Shore A, Points 75.4 70.4 71.2 70.2 70.7

M 100%, MPa 5.4 3.2 2.9 3.0 3.7

Tb ₁ MPa 10.7 7.2 7.8 7.3 9.4

Eb, % 207 291 295 314 266

[00074] The Examples in Table 8 are selected copolymers that confirm the improved high temperature dynamic fatigue resistance. Vulcanization conditions for the ASTM testing slabs were: press cure at 180 ⁰ C for 5 minutes, then post cure at 175 °C for 4 hours. Static heat aging properties of the vulcanizates are shown in Table 8 and high temperature dynamic fatigue resistance testing (DeMattia) is shown in Table 11.

Table 8

Copolymer

Reaction Conditions C8 26 21 28

Pressure (kg/cm ² ) — 2180 2180 2110

Reactor Temperature ( ⁰ C) — 155 145 145

Feed Temperature ( ⁰ C) - 70 70 70

Mn divided by 1000 37.2 46.3 47.1 46.1

Mw divided by 1000 163 159 193 200

Polydispersity 4.38 3.45 4.09 4.33

Ml 8 5.8 2.8 1.8-2.0

MA level 55.0 58.9 60.9 55.1

Cure site level 2.5 1.80 1.63 1.86

Compounded Copolymer

Compound C129 126 127 128

Copolymer C8 26 27 28

Amount of Copolymer, phr 100 100 100 100

F1 50 50 50 50

A1 2 2 2 2

R1 — 0.5 0.5 0.5

R3 1.5 1.5 1.5 1.5

R2 1 1 1 1

CA5, 80% in inert carrier 2.5 2.5 2.5 2.5

CA4 2 2 2 2

CA3 1.25 0.90 0.82 0.93

Total phr 160.25 160.40 160.32 160.43

Stock Properties

Compound C129 126 127 128

MOONEY VISCOSITY.

ML(1+4) at 100 °C 46.4 58.6 70.1 87.7

MOONEY SCORCH ,TS2 at 121 I ⁰ C 7.15 7 7.28 5

MDR at 180 °C/0.5 deα/12 min

ML, dNm 0.45 0.69 0.89 1.27

MH, dNm 8.62 5.3 5.09 8.05 ts1, min 0.78 0.95 1.01 0.67

Ts2, min 1.14 1.63 1.8 0.99 tc10, min 0.72 0.64 0.63 0.58 tc50, min 1.98 1.88 1.9 1.54 tc90, min 5.83 5.55 5.59 4.46

Vulcanizate Properties

Vulcanizate C229 226 227 228

Compound C129 126 127 128

1) COMPRESSION SET. METHOD B. PLIED PELLETS

37 44 53 36

2) STRESS-STRAIN AND HARDNESS. ORIGINAL AT 23 ⁰ C

Hardness, Shore A, Points) 68 65 66 65

M 100%, MPa 3.8 2.8 2.6 3.5

Tb, MPa 17.6 14.9 14.6 17.6

Eb, % 485 617 668 534

Tear Crescent Die C, kN/m 29.4 32.0 30.6 30.9

[00075] Tat>les ^™ 9 through 11 summarize DeMattia dynamic fatigue resistance testing at 150 ⁰ C. Samples for the DeMattia testing were prepared by molding the compounded composition into test coupons for 10 to 20 minutes at 177 ⁰ C to 180 ⁰ C at a pressure of about 43.2 kg/cm ² (4240 kPa) and then post-curing at 175°C for four hours at ambient pressure.

[00076] Table 9 illustrates vulcanizates from Table 6, after aging in air for 94 hours at 200 ⁰ C, showing improved dynamic fatigue resistance.

Table 9

Number of Cycles to reach a total failure

Vulcanizate C220 218 219 median of 6 samples 92 297 469

[00077] Table 10 illustrates a DeMattia test on non-heat aged vulcanizates from Table 7.

Table 10

Number of Cycles to reach a total failure

Vulcanizate C225 221 222 223 224 median of 6 samples 320 51235 51200 20480 1280

[00078] Table 11 illustrates DeMattia testing of vulcanizates from Table 8, after aging 94 hours at 200 ⁰ C. The results of Table 10 and Table 11 indicate a greater than 100-fold increase in dynamic fatigue resistance under this testing condition can be achieved.

Table 11

Number of Cycles to reach a total failure

Vulcanizate C229 226 227 228 median of 6 samples 5 640 1920 40

[00079] Having thus described and exemplified the invention with a certain degree of particularity, the following claims are not to be so limited but are to be afforded a scope commensurate with the wording of each element of the claim and equivalents thereof.