FIELD OF INVENTION

The invention relates to vulcanized natural rubbers or its synthetic analogs (i.e., polyisoprene) having improved thermal degradation properties and their use in vibration damping applications in harsh conditions (e.g., automotive engine mounts and bushings).

BACKGROUND OF INVENTION

Vulcanized natural rubber is widely used in anti-vibration systems, such as automotive engine mounts, because of its excellent strength, fatigue resistance, high resilience and low level of strain sensitivity particularly at low temperatures. It is and has been the elastomer of choice for the majority of applications involving high stress and cyclic flexing. Unfortunately, vulcanized natural rubber tends to degrade when it is used in high temperature environments (>100Â° C.) and the temperatures in today's engine compartments are increasing in order to improve engine efficiency, with an industry target of at least 150Â° C. mentioned. With the industry driving to improve engine efficiencies, vulcanized natural rubber mounts may be more susceptible to early degradation and part failure.

To address the problem of vulcanized natural rubber thermal degradation, heat shields have been described, for example, in US Pat. Appl. No. 2006/0138300. Coatings have also been applied to vulcanized natural rubber to reduce their thermal degradation such as described in U.S. Pat. No. 6,709,758. Crosslinking modification and saturation of the double bonds have also been used to reduce the thermal degradation of vulcanized natural rubber, but these invariably have led to substantial reduction in desirable dynamic properties particularly at lower temperatures. Additives such as reversion modifiers and antioxidants have also been used such as described in Accelerators and Reversion Modifiers for Natural Rubber (Dr. Arie J. de Hoog, Natuurrubber 9, December 1997). Unfortunately, these methods suffer from reduced dynamic properties, complexity, increased weight, and limited improvement at higher application temperatures (i.e., desired underhood temperatures).

From the above, it would be desirable to provide a vulcanized natural rubber having similar dynamic properties to a vulcanized rubber using standard sulfur vulcanization methods that realizes improved thermal degradation properties and avoids one or more problems of the prior art such as those mentioned above.

SUMMARY OF INVENTION

A first aspect of the invention is a method of forming a vulcanized rubber comprising mixing a halogenated unsaturated polymer into a rubber comprised of cis 1-4 polyisoprene to form a vulcanizable polymer blend, adding a vulcanization material to the vulcanizable polymer blend, and vulcanizing the vulcanizable polymer blend to form a homogeneous vulcanized rubber.

A second aspect of this invention is a vulcanized rubber comprised of polyisoprene uniformly crosslinked with a halogenated unsaturated polymer that is a reaction product of (i) an unsaturated polymer miscible with polyisoprene and having conjugated dienes that undergo a Diels Alder reaction and (ii) a polyhalogenated cyclopentadiene represented by:

[Image Omitted]

wherein X is a fluorine, chlorine or bromine and Y is fluorine, chlorine, bromine or alkoxy having 1 to 4 carbons.

A third aspect of the invention is a method of forming a vulcanized rubber solubilizing cis 1-4 polyisoprene with a polyhalogenated cyclopentadiene represented by:

[Image Omitted]

wherein X is a fluorine, chlorine or bromine and Y is fluorine, chlorine, bromine or alkoxy having 1 to 4 carbons to form a blend and vulcanizing the blend to form a homogeneous vulcanized rubber. In this aspect, it is believed, without being limiting, that some portion of the cis 1-4 polyisoprene undergoes a Diels Alder reaction of the second aspect during the vulcanization in situ.

It has been surprisingly found that when forming a vulcanized rubber particularly when using sulfur as the crosslinker or vulcanizer even at conventional levels that allow for excellent dynamic properties of a natural rubber (essentially 100% polyisoprene), a vulcanized rubber having desirable dynamic properties even at low temperatures may be formed while also achieving improved thermal degradation properties even at higher temperatures.

DETAILED DESCRIPTION OF INVENTIONThe Halogenated Unsaturated Polymer

The halogenated unsaturated polymer is made by reacting an unsaturated polymer that has dienes that undergo Diels Alder reaction with a polyhalogenated cyclopentadiene represented by:

[Image Omitted]

wherein X is a fluorine, chlorine or bromine and Y is fluorine, chlorine, bromine or alkoxy having 1 to 4 carbons. Unsaturated polymers include, for example, polybutadiene having at least about 30% cis 1-4 groups, and cis 1-4 polyisoprene. Preferably, the unsaturated polymer is cis 1-4 polyisoprene, polybutadiene having at least 80%, 90% or 95% 1-4 cis groups to essentially all the groups being cis 1-4 groups by weight. Typically the unsaturated polymer, particularly when such unsaturated polymer is polybutadiene, has a Mw (molecular weight average) from about 300,000 to about 3,500,000 g/mole and a Mn (molecular number average) from about 150,000 to about 175,000 g/mole.

The polyhalogenated cyclopentadiene may be useful to make the halogenated unsaturated polymer. Examples include hexachlorocyclopentadiene, hexabromoocyclopentadiene; 5,5-dibromotrethachlorocyclopentadiene; 5,5-difluorotetrachlorocyclopentadiene; 5,5-dimethoxytetrachlorocyclopentadiene; diethoxytetrachlorocyclopentadiene or mixture thereof. Preferably, the polyhalogenated cyclopentadiene is hexachlorocyclopentadiene.

During the reaction, because a halogen halide may be produced, an acid scavenger is typically used such as an eplihalohydrin (e.g., epichlorohydrin) or other epoxide compounds. Typically, the amount of the acid scavenger is from about 0.01% to 20% by weight of the total amount of the reactants (i.e., unsaturated polymer and polyhalogenated cyclopentadiene).

A control agent also may be used to control the extent of the reaction. The control agent may be a compound such as a nitro-substituted aromatic hydrocarbon, phenol or alkyl-substituted phenol. Examples of the nitro aromatic hydrocarbon include nitrobenzene, ortho-, meta, and para-di nitrobenzene, trinitrobenzene and 2,4-dinitrophenol as well as diphenyl-1-picrylhydrazine. Exemplary phenols include phenol, hydroquinone, catechol, resorcinol, and phloro-glucinol, as well as the quinone forms that exist, such as ortho- and parabenzoquinone. Examples of the alkyl-substituted phenols include meta- and para-isopropylphenol; 3,5-dimethylphenol; 3,5-diethylphenol; 3,5-sec-butylphenol; 3-ethyl-5-isopropylphenol; 2-methyl-4-isopropylphenol; 3,5-dicyclohexylphenol; 2,4,6-trimethylphenol; tertiary butyl catechol; para-cresol; 5-isopropyl resorcinol; 4-n-propyl resorcinol; 4-n-nonyl resorcinol; 4-n-hexylresorcinol and toluhydroquinone. Generally, the alkyl substituents have up to ten carbons. When used, the amount of control agent typically is a small amount such as about 0.001% to about 1% by weight of the total amount of reactants (the unsaturated polymer and polyhalogenated cyclopentadiene).

A solvent may also be used in the reaction, but is not required. Solvents that may be used include, for example, aliphatic, cycloaliphatic and aromatic hydrocarbons such as hexane, iso-octane, normal decane, benzene, toluene, xylene, cyclo-hexane, methylcyclohexane and the like; chlorinated hydrocarbons such as chloroform, trichloroethylene, dichloropropane, tetrachloroethane propylene dibromide, trichlorobenzene, benzotrichloride, the chloro toluenes and the like; ketones such as diethylketone, methylpropylketone, mesityl oxide and the like; esters such as isobutyl acetate, amyl acetate, butyl propionate, ethyl butyrate and the like. Mixtures of the various solvents may also be used. The aromatic hydrocarbons are preferred. It is also preferred that the boiling point of the solvent not exceed about 200Â° C. to facilitate removal from the unreacted halocyclopentadiene. The ratio of solvent used in the reaction mixture generally does not exceed about 100 parts by weight of the unsaturated polymer and polyhalogenated cyclopentadiene.

The reaction proceeds best at elevated temperatures such as 70Â° C. or 100Â° C. to 200Â° C. or 180Â° C. The reaction may be carried out at a useful pressure, but desirably is performed at or near ambient pressures (Ëœ1 atm).

The unsaturated polymer and polyhalogenated cyclopentadiene are provided in an amount and reacted for a time sufficient to form the halogenated unsaturated polymer. This typically means that the time is from several minutes to several days, but tends to be from 30 minutes or 1 hour to 48 or 36 hours. The molar ratio of the amount of polyhalogenated cyclopentadiene/unsaturated polymer may be in excess of the amount of double bonds in the unsaturated polymer that react with the polyhalogenated cyclopentadiene. Typically, the polyhalogenated cyclopentadiene/unsaturated polymer molar ratio is at least 1 to 20, 10 or 5. Generally, the molar ratio and reaction conditions are such that the amount of halogen and desirably Cl in the halogenated unsaturated polymer reaction product is from about 5%, 10%, 15%, 20% to 60%, 50%, 40% or 30%.

Forming the Vulcanized Rubber

In making the vulcanized rubber of the present invention, the halogenated unsaturated polymer is mixed into a rubber comprised of cis 1-4 polyisoprene to form a vulcanizable polymer blend. The cis 1-4 polyisoprene containing rubber may be any suitable rubber having a sufficient amount of cis 1-4 units to realize the desired mechanical properties. Typically, the amount of cis 1-4 units is at least about 30%, but desirably is at least 90%, 95% or essentially all cis 1-4 units by weight of said rubber. The rubber comprised of cis 1-4 polyisoprene may be any known natural rubber or synthetic polyisoprene rubber such as those known in the art and further described by Morton, M. 2009, Elastomers, Synthetic, Survey, Kirk-Othmer Encyclopedia of Chemical Technology. 1-20 and Baker, C.S.L, Fulton, W.S. and Updated by Staff 2012, Rubber Natural. Kirk-Othmer Encyclopedia of Chemical Technology, 1-28.

The blending may be performed in any suitable mixing apparatus known in the art such as rubber mills and Banbury mixers. The blending may be performed at any temperature typical in the rubber arts such as from room temperature (Ëœ20Â° C.) to about 150Â° C. The amount of time may be any amount necessary to sufficiently blend the halogenated unsaturated polymer into the cis 1-4 polyisoprene containing rubber to the vulcanizable polymer blend. Typically, the time is as short as practicable and, for example, is from several minutes to 1, 2, 5, 10 or 24 hours. The halogenated unsaturated polymer is suitably mixed when the vulcanizable polymer blend has a uniform consistency with no obvious phase separation by eye.

The halogenated unsaturated polymer and rubber comprised of cis 1-4 polyisoprene are provided in a ratio sufficient to provide improved thermal degradation while retaining in essence the same or to a large extent the desired mechanical (dynamic) properties of the vulcanized rubber. The particular ratio depends, for example, on the amount of halogen in the halogenated unsaturated polymer and the particular properties desired. Generally, the halogenated unsaturated polymer/rubber ratio by weight varies from about 0.01 to 1. Typically, the ratio is from about 0.05 or 0.1 to about 0.5 or 0.25. The ratio generally realizes an amount of halogen in the vulcanized rubber of about 1% to 25% by weight of the total weight of the vulcanized rubber (total weight includes all materials retained and used to make the rubber and includes, for example, vulcanization materials as well as other additives such as fillers).

To crosslink or vulcanize the vulcanizable polymer blend, vulcanization material is added. The addition of the vulcanization material may occur at any convenient point such as when mixing the halogenated unsaturated polymer and polyisoprene containing rubber or after this have become blended together. It has surprisingly been found that conventional vulcanization may be used allowing for desired mechanical properties that such vulcanizing offers, while also realizing much improved thermal degradation properties. â€œConventional vulcanizingâ€ means that the cross-linking agent is elemental sulfur, insoluble sulfur, an accelerator and a cross-linking activator such as zinc oxide combined with a fatty acid such as stearic acid, zinc laurate, zinc stearate or zinc 2-ethoxylhexoate. In such a conventional vulcanization, the ratio of the accelerator to sulfur (accelerator/sulfur) by weight is typically from 0.05 to 0.5 and the amount of sulfur is sufficient to realize mostly crosslinks that are polysulfidic (e.g., sulfur is present in an amount from 0.1 parts to 5 parts by weight of the vulcanizable polymer blend). â€œPolysulfidicâ€ means the cross-link has at least 3 sulfur atoms to typically at most about 8 sulfur atoms.

The ratio may however be other ratios such as those typically characterized as efficient or semi-efficient vulcanization wherein there is a corresponding decrease in polysulfidic cross-links and decrease in the dynamic properties of the rubber, but with further improved thermal degradation properties. For example, the ratio of accelerator to sulfur may be greater than 0.5 to 10 or 5.

The accelerator, when employing vulcanization using sulfur to cross-link, may be any suitable accelerator such as those known in the art including sulfenamides, thiazoles, thiuram sulfides, dithocarbamates and guanidines. Examples of accelerators include 2-mercaatptbenzothiazole; bis(2,2â€²-benzothiazolyl)disulfide; zinc 2-mercaptobenzothiazole; N-tert-butyl-2-benzothiazolesulfenamide; N-cyclohexyl-2-benzothiazolesulfenamide; N-oxydiethylene-2-benzothiazolesulfenamide; 4-morpholinyl-2-benzothiazole disulfide; N-dicyclohexyl-2-benzothiazolesulfenamide; N-tert-butyl-2-benzothiazolesulfenimide; N-oxydiethylenethiocarbamyl-N-oxydiethylenesulfenamide; N-oxydiethylenethiocarbamyl-N-oxydiethylenesulfenamide; cadmium diethyldithiocarbamate; copper dimethyldithiocarbamate; lead diamyldithiocarbamate; lead dimethyldithiocarbamate; piperidinium; pentamethylenedithiocarbamate; selenium dimethyldithiocarbamate; sodium di-n-butyldithiocarbamate; tellurium diethyldithiocarbamate; zinc diamyldithiocarbamate; zinc dibenzyldithiocarbamate; zinc di-n-butyldithiocarbamate: zinc di-iso-butyldithiocarbamate: zinc diethyldithiocarbamate; zinc dimethyldithiocarbamate; zinc di-iso-nonyldithiocarbamate; zinc pentamethyldithiocarbamate; and dipentamethylenethiuram disulfide.

Other cross-linkers other than sulfur may be used depending on the properties desired, but for applications requiring good dynamic properties (mechanical properties related repeating stress/strain typically sinusoidal at varying frequencies and in particular the ability to dampen vibrations in engine mount applications) sulfur is generally preferred. Other cross-linking compounds that may be used include, for example, 4,4-dithiodimorpholine, N,N-caprolactam disulfide, dicumyl peroxide, 2,5-dimethyl-2,5-di(tbutylperoxy)hexane, 2,5-dimethyl-2,5-di(tbutylperoxy)hexyne, 2,5-dimethyl-2,5-di(benzoylperoxy)hexane, 2,2-bis(t-butylperoxy)-di-isopropylbenzene, 1,1-bis(t-butylperoxy)-3,3,5-trimethylcyclo-hexane, n-butyl 4,4-bis(t-butyl-peroxy)valerate, t-butyl-perbenzoate, benzoyl peroxide, para-quinone dioxime, alkylphenol disulfide, methylolphenol-formaldehyde resin, brominated alkylphenol formaldehyde resin, 2-mercapto-1,3,4-thia-diazole-5-thiobenzoate, 5,5-thiobis-1,3,4-thia-diazole-2(3H)thione, trithiocyanuric acid, hexamethylenediamine carbamate, N,N-dicinnamylidene-1,6-hexanediamine, 4,4-methylenebis-(cyclohexylamine)carbamate, 4,4-methylenedianiline, hexamethylene-1,6-bis-thiosulfate, disodium salt, 3-bis(ditraconimido-methyl)benzene, and N,N-meta-phenylenebis-maleimide.

Other useful additives may be employed when vulcanizing including adhesion promoters, antidegradants, processing agents, activators and retarders, fillers and reversion inhibitors and the like that are known in the industry. Activators and retarders such as magnesium oxide, lead monoxide, lead tetroxide, calcium oxide, zinc carbonate, phthalic anhydride benzoic acid, salicylic acid, N-(cyclohexyl-thio)phthalimide, and tetra-iso-butyl thiurammonosulfide may be employed. Processing agents may be employed to assist in making the viscosity of vulcanizable polymer blend more workable. Examples include arenemercaptans, arenesulfonic acids, pentachlorothiophenol or its zinc salt and dithiobenzanilide or its zinc salt, clay, oils and waxes. Antidegradants may include N-isopropyl-Nâ€²-phenylene diamine, N-(1,3-dimethylbutyl)-Nâ€²-phenyl-p-phenylene diamine, octylated diphenylamine, 2,2,4-trimethyl-1,2-dihydroquinoline, polymerized, and 2,2â€²-methylene-bis-(4-methyl-6-tert.-butylphenol). Anti-reversion agents may also be used. These agents inhibit or repair breaks of the polysulfidic cross links in conventional vulcanization and may include PERKALINK 900 (1,3-bis(citraconimidomethyl)benzene) available from Lanxess GmbH, Germany and DURALINK HTS (Hexamethylene-1,6-bis(thiosulfate) available from Eastman Chemical Comp., Kingsport, Tenn.

Fillers may be used in any amount to achieve the desired mechanical properties. Typically, the filler is a carbon black, which includes any carbon having a submicron particulate size formed from any number of hydrocarbon sources (e.g., oil, natural gas or acetylene). Likewise, other inorganic fillers may be used such as silica and in particular fumed silica and other inorganic particulates such as calcium carbonate. The amount of fillers typically is present in an amount in the vulcanized rubber from about 5 to 75% by weight of the total weight of the vulcanized rubber.

The vulcanization temperature may be any suitable temperature, but generally is from 100Â° C. to 200Â° C. and typically from 120 or 140Â° C. to 190 or 180Â° C. The vulcanization may be performed at any pressure, but typically is performed under ambient pressures or slightly elevated pressures, such as up to 100 pounds per square inch. The time may be suitable or practicable such as several minutes to a day or two and may depend on many factors such as size of the component being vulcanized and the ultimate properties desired.

The Vulcanized Rubber

The method of the invention forms a vulcanized rubber comprised of polyisoprene uniformly cross-linked with the halogenated unsaturated polymer described above. â€œUniformlyâ€ means that the halogenated unsaturated polymer and polyisoprene were compatible as described above, which is believed to lead to a crosslinking of the two polymers on a molecular scale. The uniformity may be assessed, for example, by pulverizing or rending the vulcanized rubber into a powder having an average particle size on the order of 1 to 10 micrometers and analyzing a random sampling of the powder particles for halogen content. Typically, the standard deviation will be within 20% of the mean of the average of the halogen detected.

The vulcanized rubber desirably has an amount of halogen that is at least about 5 phr (parts per hundred by weight), 10 phr, or 20 phr, to at most about 35 phr of the total weight of the vulcanized rubber including fillers and other additives.

The vulcanized rubber typically will have dynamic properties that are within 20%, 10% or even 5% of a rubber made in the same manner using only the rubber comprised of cis 1-4 polyisoprene (in the absence of any other rubber polymer including the halogenated unsaturated polymer). The vulcanized rubber generally will have substantially improved thermal degradation characteristics. â€œImproved degradation propertiesâ€ means that desired mechanical properties will be maintained longer without the same degree of degradation or that the temperature where similar degradation occurs is at a higher temperature. Typically, the degradation characteristics are improved by 10%, 20%, or even 50% or even more. That is the time realizing the same dynamic property decrease is 10%, 20, or even 50% or even longer.

Test MethodsTensile Strength:

Tensile strength was determined as per ASTM D573.

Elongation:

Elongation was determined as per ASTM D573.

Shore Hardness:

Shore hardness was determined by ASTM 240

TABLE 1NameDescriptionCompanySIR 3CV60Natural RubberAltonHCCPHexachlorocyclopentadieneVelsicolCorporationN-550Carbon BlackCabotSantoflexâ€‰â„¢N-(1,3-Dimethylbutyl)-Nâ€²-phenyl-Flexsys America6PPD1,4-benzenediamine (AO)LiquidTMQTMQ Powder (2,2,4-trimethyl-1,ChemSpec Ltd2-dihydroquinoline) (AO)HM 97-WaxPolyethylene waxStruktolCTPN-(cyclhexyl thio) phthalimideAkrochemAntiscorching agentZinc OxideRhein-ChemieSteric AcidSigma-AldrichSulfurSigma-AldrichCBSN-Cyclohexyl-2-Harwick StandardbenzothiazolesulfenamideDoverphos 10Triphenylphosphate (TPP)Dover ChemicalPolybutadiene1-4 cis polybutadieneRhein-Chemie(LanxessCorporation)TBBSN-Tertiarybutyl-2-benzothiazaoleHarwick StandardsulfennamideTMTDTetramethylthiuram disulfideHarwick Standard

Example 1Preparation of the Halogenated Polymer

The halogenated polymer was synthesized by reacting 1,4 polybutadiene (PBD) and hexachlorocyclopentadiene (HCCP) via inverse electron demand [4+2] cycloaddition (Diels-Alder) reaction at a ratio of PBD:HCCP=1:1.35 by wt. at âˆ’12.5% HCCP grafting of 32-34% solids.

In a one liter flask under a nitrogen purge, 97 grams of 1,4 polybutadiene (PBD) and 641 grams of Hi Sol 10 (mixture of aromatic solvents available from Rodda Paint Co., Portland, Oreg.) were added to a vessel. The mixture was heated to 120Â° C. and agitated until all of the PBD was dissolved. Then 264 grams of HCCP was added to the blend and heated to 150Â° C. and reacted under nitrogen. During the reaction, Hi Sol is added to maintain the volume of the blend as needed. The reaction was carried out until the % solids of reaction product reached 31.5% by weight. % solids is determined using viscometry. Once the % solids is realized, the halogenated polymer was separated from the Hi Sol 10 by filtering and dried at ambient temperature until essentially no further unreacted HCCP or Hi Sol is present.

Vulcanization

The Example 1 formulation shown in Table 2 was vulcanized by charging the natural rubber and halogenated polymer into a mixer at 40Â° C. and then adding the zinc oxide, steric acid and wax and mixing for 2 minutes. The carbon black was then added and the mixture mixed for 4 minutes. Following this mixing, the sides of the container were scraped and the antioxidants TMQ and 6PPD were added and the mixture was mixed for 1 more minute. This mixture was pressed into strips and cooled for at least 8 hours.

The cooled mixture was then mixed with the sulfur, TBBS and TMTD in the amounts shown in Table 2. This mixture was then compression molded into test specimens at 160Â° C. for a time of 10 to 30 minutes depending on the particular formulation.

The vulcanized rubber was tested as made and after aging for differing times and temperatures as shown in Table 3. Likewise, the results of the testing are also shown in Table 3.

Examples 2-6 and Comparative Examples 1-6

Examples 2-6 and Comparative Examples 1-6 were made in the same way using the same polyhalogenated polymer as Example 1 except that the formulations were changed as shown in Table 2. The testing results for these are shown in Table 3. From the results shown in Table 3, the use of the polyhalogenated polymer in the vulcanized rubber exhibits improved retention of elongation properties when made with the same amount of vulcanizing sulfur. Likewise, improved retention of properties are shown when using greater amounts of sulfur (conventional vulcanization), which is expected to retain improved damping properties too.

TABLE 2Example #123456Comp. 1Comp. 2Comp. 3Comp. 4Comp. 5Comp. 6Cure SystemCVSemi-EVEVEVEVEVCVSemi-EVEVEVEVEVMaterialgmsgmsgmsgmsgmsgmsgmsgmsgmsgmsgmsgmsSIR 3CV60725725725453716693906900900903903725Y-1736181181181453179173N-550390390390390385373390390390388388390Zinc Oxide454545454587454545454545Steric Acid181818181817181818181818HM 97 -Wax.1818181818171818181818186-PPD14141414131314141413.513.514TMQ999999999999Doverphos 101817Polybutadiene181Valcuren4.5Perkalink-9004.5TBBS6.314.518.118.117.917.36.314.518.118.118.118.1TMTD4.518.118.117.917.34.518.118.118.118.1Sulfur15.410.91.81.81.81.715.410.91.81.81.81.8CV = conventional vulcanization;EV = Efficient vulcanization;Semi EV = Semi-Efficient vulcanization

TABLE 3stdevTensileTensile% RetentionElongation% RetentionShore AReference #Aging(MPa)(MPa)Tensile(%)ElongationHardnessExample 1Not heat aged210.7210035410072Example 11 day heat aged at 120Â° C.111.43511494278Example 13 days heat aged at 120Â° C.60.2630932676Example 17 days heat aged at 100Â° C.122581624678Example 110 days heat aged at 90Â° C.131.29641785079Example 120 days heat aged at 85Â° C.151.89741785081Example 130 days heat aged at 70Â° C.171.758021360Example 2Not heat aged22110041810067Example 21 day heat aged at 120Â° C.150.86682225374Example 23 days heat aged at 120Â° C.111.31501453573Example 27 days heat aged at 100Â° C.160.65722285473Example 210 days heat aged at 90Â° C.191852716574Example 220 days heat aged at 85Â° C.180.73782626374Example 230 days heat aged at 70Â° C.Example 3Not heat aged211.810037810072Example 31 day heat aged at 120Â° C.161.04772426475Example 33 days heat aged at 120Â° C.130.59611965275Example 37 days heat aged at 100Â° C.173822426477Example 310 days heat aged at 90Â° C.181.62862536777Example 320 days heat aged at 85Â° C.171.96832446577Example 330 days heat aged at 70Â° C.172.478430280Example 4Not heat aged220.9610036010074Example 41 day heat aged at 120Â° C.151.26702005582Example 43 days heat aged at 120Â° C.142.37651784982Example 47 days heat aged at 120Â° C.121.16541273585Example 47 days heat aged at 100Â° C.161.56711815082Example 410 days heat aged at 90Â° C.151.88671764983Example 420 days heat aged at 85Â° C.171.61772085885Example 430 days heat aged at 70Â° C.170.827722562Example 5Not heat aged211.510042810066Example 51 day heat aged at 120Â° C.151.53712666273Comp. Ex. 330 days heat aged at 70Â° C.180.688535983Example 53 days heat aged at 120Â° C.121.07592245274Example 57 days heat aged at 100Â° C.143682465775Example 510 days heat aged at 90Â° C.172.1822756474Example 520 days heat aged at 85Â° C.161.86762475875Example 530 days heat aged at 70Â° C.201.729638189Example 6Not heat aged180.410043310064Example 61 day heat aged at 120Â° C.161.39913016972Example 63 days heat aged at 120Â° C.102.35582104872Example 67 days heat aged at 120Â° C.50.52301383270Example 67 days heat aged at 100Â° C.160.93892886674Example 610 days heat aged at 90Â° C.170.88942956874Example 620 days heat aged at 85Â° C.161.27912936874Example 630 days heat aged at 70Â° C.181.4510237486Comp. Ex. 1Not heat aged230.1810046410065Comp. Ex. 11 day heat aged at 120Â° C.91.43401793968Comp. Ex. 13 days heat aged at 120Â° C.40.6217831862Comp. Ex. 17 days heat aged at 100Â° C.111.88491894169Comp. Ex. 110 days heat aged at 90Â° C.141.78622385171Comp. Ex. 120 days heat aged at 85Â° C.140.78582234871Comp. Ex. 130 days heat aged at 70Â° C.182.17730766Comp. Ex. 2Not heat aged230.410048210062Comp. Ex. 21 day heat aged at 120Â° C.161.18722865969Comp. Ex. 23 days heat aged at 120Â° C.91.33401633467.5Comp. Ex. 27 days heat aged at 100Â° C.180.82803076470Comp. Ex. 210 days heat aged at 90Â° C.191.05823326969Comp. Ex. 220 days heat aged at 85Â° C.181.2181342.87170Comp. Ex. 230 days heat aged at 70Â° C.211.739238680Comp. Ex. 3Not heat aged210.6610043410063Comp. Ex. 31 day heat aged at 120Â° C.180.37853227469Comp. Ex. 33 days heat aged at 120Â° C.151.13712626067Comp. Ex. 37 days heat aged at 120Â° C.60.75301543564Comp. Ex. 37 days heat aged at 100Â° C.180.97843047070Comp. Ex. 310 days heat aged at 90Â° C.181.65853357770Comp. Ex. 320 days heat aged at 85Â° C.171.85803147270Comp. Ex. 4Not heat aged240.1110044710062Comp. Ex. 41 day heat aged at 120Â° C.170.675733046868Comp. Ex. 43 days heat aged at 120Â° C.151.21632575765Comp. Ex. 47 days heat aged at 120Â° C.70.23311804063Comp. Ex. 47 days heat aged at 100Â° C.180.54763066868Comp. Ex. 410 days heat aged at 90Â° C.181783167168Comp. Ex. 420 days heat aged at 85Â° C.181.06753297470Comp. Ex. 430 days heat aged at 70Â° C.190.688238987Comp. Ex. 5Not heat aged211.6310041510063Comp. Ex. 51 day heat aged at 120Â° C.151.14702716566Comp. Ex. 53 days heat aged at 120Â° C.111.92532245466Comp. Ex. 57 days heat aged at 120Â° C.80.47351984864Comp. Ex. 57 days heat aged at 100Â° C.173772796766Comp. Ex. 510 days heat aged at 90Â° C.161.603772957170Comp. Ex. 520 day heat aged at 85Â° C.171.389782836870Comp. Ex. 530 days heat aged at 70Â° C.190.588935886Comp. Ex. 6Not heat aged220.3610044310064Comp. Ex. 61 day heat aged at 120Â° C.160.79753046969Comp. Ex. 63 days heat aged at 120Â° C.150.77692666068Comp. Ex. 67 days heat aged at 120Â° C.70.16331733965Comp. Ex. 67 days heat aged at 100Â° C.181.33832886570Comp. Ex. 610 days heat aged at 90Â° C.151.65672646070Comp. Ex. 620 days heat aged at 85Â° C.170.84762976770Comp. Ex. 630 days heat aged at 70Â° C.181.52823437782