CURING SYSTEMS FOR HALOGENATED ELASTOMERS HAVING IMPROVED HIGH TEMPERATURE COMPRESSION SET

Abstract: The invention provides for cured elastomer compositions containing halobutyl rubber and/or halogenated copolymer of isobutylene and para-methylstyrene which exhibit very low compression set values at temperatures as high as about 200 DEG C. The composition contains a specific curing system mixture based on a dialkyl- or diaryl-dithiocarbamate salt, a finely divided hydrotalcite and a polyalkylene glycol, and also preferably contains zinc oxide and stearic acid.

Description: CURING SYSTEMS FOR HALOGENATED ELASTOMERS HAVING IMPROVED HIGH TEMPERATURE COMPRESSION SET FIELD OF THE INVENTION: The present invention relates to the use of a specific curing system for halogenated elastomers, particularly elastomeric copolymers containing isobutylene and parahaloalkyl-substituted styrene, yielding cured products having improved high temperature compression set. - BACKGROUND OF THE INVENTION Halogenated copolymers of isobutylene and up to about 10 mole % of isoprene (butyl rubber) are well known polymer materials whose vulcanizates offer some outstanding properties not possessed by many other diolefin based elastomers. Articles prepared from many cured halogenated elastomers offer improved resistance to oils and greases as well as resistance to oxygen and ozone degradation. Butyl rubber vulcanizates exhibit good abrasion resistance, excellent impermeability to air, water vapor and many organic solvents, as well as resistance to aging and sunlight. These properties render these materials ideal hoses, organic fluid hoses, components in tire construction, gaskets, automotive body and engine mounts, and various molded articles. More recently, a new class of halogenated elastomeric interpolymers have been discovered which offer many ofthe same properties as halogenated butyl rubber, but are even more ozone and solvent resistant and are more readily curable. These materials are the halogenation product of random copolymers of a C 4 to C 7 isoolefin, such as isobutylene, and a para-alkylstyrene comonomer wherein at least some ofthe alkyl substituent groups present in the styrene monomer units contain halogen. Preferred materials may be characterized as isobutylene interpolymers containing the following monomer units randomly spaced along the polymer chain: l * and 2. wherein R and R' are independently hydrogen, lower alkyl, preferably Ci to C 4 alkyl and X is bromine or chlorine, and -wherein the interpolymer is otherwise substantially free of ring halogen or halogen in the polymer backbone chain. Preferably R and R' are each hydrogen. Up to about 60 mole % ofthe para- alkylstyrene present in the interpolymer structure may be the halogenated structure (2) above. These copolymers may be prepared by shiny polymerization ofthe monomer mixtΛ-xe'ύsing a Lewis Acid catalyst, followed by halogenation, e.g. bromination or cUorination, in solution in the presence of halogen and a radical initiator such as heat and/or light and/or a chemical initiator. Preferred copolymers are brominated copolymers generally containing from about 0.1 to about 2 mole % of bromomethyl groups, most of which is monobromomethyl, with less than 0.05 mole % dibromomethyl substituents present in the copolymer. These copolymers and their method of preparation are more particularly disclosed in U.S. Patent 5,162,445, the complete disclosure of which is incorporated herein by reference. The aromatic halomethyl groups present in such copolymers permit facile cross linking to be accomplished in a variety of ways, including by means of zinc oxide or promoted zinc oxide curing systems normally used to cure halogenated butyl rubber. Illustrative of known accelerators which are known for use in conjunction with zinc oxide for curing halogenated butyl rubber are brominated alkyl phenol resin; N,N'-diethylthiourea; di-otho-(tolyl)guanidine salt of dicatechol borate; dipentamethylene thiuram tetrasulfide; ethylene trithiocarbamate; 2- mercapto-benzothiazole; alkyl or aryl benzothiazole disulfides, tetramethylthiuram disulfide, zinc diethyldithiocarbamate, zinc dibutyldithiorcarbamate, and zinc dimethyldithiocarbamate. A known cure system comprises zinc oxide and zinc diethyldithiocarbamate, since this sytems results in a vulcanized rubber with generally low compression set. It is also disclosed in U.S. Patent 4,755,548 that the sodium, zinc, nickel, and piperidium salts of dialkyldithiocarbamic acid may be used as vulcanization - accelerators in the zinc oxide cure of chlorobutyl rubber. Other patents and publications which disclose zinc oxide, stearic acid and various accelerator curing systems for halogenated butyl rubber or halogenated copolymers of isobutylene and a para-alkylstyrene include WO92/16587 and US Patents 4,464,500, 5,246,778 and 5,332,787. Low compression set is a very important property for curable elastomeric compositions which are intended for uses such as gasket material, automotive hoses, and automotive body and engine mounts. Compression set refers to the ability of a cured rubber material to return to its original size or shape dimension after a period of having been compressed and subjected to elevated temperatures, e.g., 70-275°. For example, if one considers a 1 inch high disc of cured rubber, such as might be used as an engine mount, bolted between an engine and body frame and compressed between these mounts such that the compressed height was now 0.75 inch, the degree to which this disc retains the compressed 0.75 inch dimension after the release of compression pressure is referred to as compression set. A high compression set, e.g., 100%, would mean that the disc remained at the compressed 0.75 inch dimension after release of compressive pressure; a low compression set, e.g., 0%, would mean that the disc returned to its original 1 inch height dimension after release of compressive pressure. Accordingly, low compression set is a very desirable property for cured rubber compositions, particularly for gasket and engine mount applications. Certain applications such as pressurized rubber hoses require a combination of high modules to resist expansion under pressure and good compression set resistance to prevent leaks around various clamps and fittings. In addition, performance at elevated temperatures for extended periods of time are important in applications such as steam hoses and automotive air conditioning hoses and engine mounts. While many cured rubber materials have reasonably low compression set when used in applications where temperatures of up to about 125°C are routinely encountered, e.g., cured holobutyl rubber or cured halogenated isobutylene para- - methylstyrene (PMS) rubber, the elastomers of choice for use in applications involving use at temperatures above 125°C generally have been ethylene/propylene diene(EPDM) elastomers, silicone elastomers and fluoroelastomers. The present invention now provides a specific curing system for halobutyl rubber and halogenated isobutylene/PMS copolymer rubber which gives rise to vulcanizates having outstanding low compression set values even where used in applications where temperatures above 125°C, e.g., 150 to 200°C, are routinely or intermittently encountered. Summary of the Invention The present invention provides a curable composition comprising a mixture of a halogenated elastomer selected from the group consisting of chlorinated or brominated butyl rubber and chlorinated or brominated interpolymers of a C 4 to C 7 isoolefin and a para-alkylstyrene comonomer, or mixtures thereof, and a curing system for said halogenated elastomer present in said composition in an amount sufficient to cure said composition, said curing system comprising: a) 0 to about 5 parts by weight phr of zinc oxide; b) At least about 0.25 parts by weight phr of at least one metal or ammonium salt of a dialkyl dithiocarbamic acid wherein the alkyl groups contain 1 to 12 carbon atoms or a diaryl dithiocarbamic acid wherein the aryl groups contains 6 to 10 carbon atoms; c) At least about 0.25 parts by weight phr of a polyalkylene glycol; and d) At least about 0.1 part by weight phr of at least one finely divided hydrotalcite comprising at least one basic metal carbonate hydroxide wherein said metal is of Group II or III of the Periodic Table. The cured compositions ofthe invention are high modulus materials having good high temperature compression set and are useful in applications where high temperature compression set properties are important. Detailed Description of the Invention The halogenated elastomer present in the curable compositions of this invention may include chlorinated or brominated butyl rubber, chlorinated or brominated interpolymers of a C to C 7 isoolefin and a para-alkyl styrene, mixtures thereof or mixtures of one or both of these elastomers with other elastomers such as polybutadiene, copolymers of butadiene with styrene or acrylonitrile, natural rubber, polychloroprene or elastomeric copolymers of ethylene, propylene and up to 10 mole % of a non-conjugated diene (known as EPDM rubber). The preferred halobutyl rubbers are based or chlorinated or brominated copolymers of isobutylene with up to about 20 mole %, preferably up to 10 mole %, more preferably up to 4 mole % of isoprene. These elastomers generally have a number average molecular weight within the range of about 50,000 up to about 500,000 and may be prepared by polymerization and halogenation methods well known in the art such as disclosed in U.S. Patents 2,940,960 and 3,099,644, the disclosures of which are incoφorated herein by reference. Halogenated interpolymers based on a C 4 to C isoolefin, such as isobutylene, and a para-alkylstyrene, such as para-methylstyrene, are also now known in the art as evidenced by the aforementioned US Patent 5, 162,445. These elastomers are inclusive of those described in the Backgound section of this disclosure. Preferred materials are the halogenation product of a random copolymer of a C to C isoolefin, such as isobutylene, and a para-alkylstyrene comonomer wherein at least some ofthe alkyl substituent groups present in the styrene monomer units contain halogen. Preferred materials may be characterized as isobutylene terpolymers containing mixed monomer materials having the structure - set forth as 1 and 2 above wherein at least about 5 mole % ofthe comonomer units present in the polymer chain are ofthe structure of formula 2, R and R' are independently hydrogen or Ci to C alkyl, and X is bromine or chlorine, and wherein the teφolymer is otherwise substantially free of any halogen in the polymer backbone chain. The most preferred elastomers used in the compositions ofthe present invention are random elastomeric brominated teφolymers comprising isobutylene and para-methylstyrene (PMS) containing from about 0.5 to about 20 mole % PMS, more preferably from about 2 to about 15 mole % PMS, wherein up to about 60 mole % ofthe PMS monomer units contain a mono-bromomethyl group. Preferred elastomeric teφolymers generally exhibit a number average molecular weight in the range of from about 50,000 to about 250,000, more preferably from about 80,000 to about 180,000. From about 5 up to about 60 mole % ofthe total PMS monomer content ofthe teφolymer contains a mono-bromomethyl group with essentially no bromination occurring in the polymer backbone or in the aromatic ring. The bromine content of these teφolymers generally ranges from about 0.1 to about 5 mole %. Suitable dithiocarbamate salts which may be used as the primary vulcanization accelerator include metal salts of dialkyl substituted dithiocarbamic acid wherein the alkyl groups contain 1 to 12 carbon atoms, more preferably 1 to 4 carbon atoms, metal salts of diaryl substituted dithiocarbamic acid wherein the aryl groups contain 6 to 10 carbon atoms and mixtures thereof. Salt forming cations include alkali or alkaline earth metals and other metals such as zinc, bismuth, nickel, copper, selenium , lead, tellurium and cadmium, as well as ammonium salts such as alkyl ammonium or piperidium salts. Examples of such accelerators include zinc dimethyldithiocarbamate, zinc diethyldithiocarbamate, zinc dibutyldithiocarbamate, nickel dibutyldithiocarbamate, calcium diethyldithiocarbamate, zinc diphenyldithiocarbamate, diethylammonium diethyldithiocarbamate, sodium dimethyldithiocarbamate, sodium - diethyldithiocarbamate, sodium dibutyldithiocarbamate, sodium diphenyldithiocarbamate, calcium diethyldithiocarbamate, magnesium diethyldithiocarbamate and like metal salts and their hydrates, as well as mixturesthereof. The preferred material is zinc diethyldithiocarbamate. The quantity ofthe dithiocarbamate used to accelerate the cure ofthe halogenated elastomer composition will vary as a function ofthe halogen content ofthe elastomer. Generally, it is employed in the range of from about 0.25 to about 2.5 parts by weight, more preferably in the range of about 0.25 to about 2.0 parts by weight per 100 parts by weight of halogenated elastomer. Suitable polyalkylene glycols which may be used as a co-curative include C 2 to C alkylene glycols having a molecular weight in the range of from about 60 up to about 6000, more preferably from about 100 to about 4000. Suitable polyalkylene glycols include polyethylene glycol, polypropylene glycol, polybutylene glycol as well as relatively non-volatile lower molecular weight polyalkylene glycols, such as trimethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, dipropylene glycol and tripopylene glycol. Triethylene glycol is a preferred polyalkylene glycol. The amount of glycol added to the composition may be in the range of from about 0.25 up to about 5.0 parts by weight phr, more preferably from about 0.5 to 4 parts by weight per 100 parts by weight rubber (phr). The hydrotalcite component ofthe curing system may be described as a basic metal carbonate hydroxide material wherein the metal is of Group II or Group III ofthe Periodic Table, e.g., magnesium, zinc, or aluminum carbonates. Preferred metal carbonate hydroxides are magnesium/aluminum compounds having the structure Mg 4 Al 2 (OH)ι 2 CO 3 XH 2 0 (X is 0-3) and zinc carbonate hydroxides having the structure; ZnMg3Al 2 (OH), 2 CO 3 XH 2 0 (X is 0-3); 5ZnO 2CO 3 4H 2 O; ZnCO 3 2Zn(OH)2 H 2 O and 2ZnCO 3 3Zn(OH) 2 as well as dehydrated versions thereof. These materials are finely divided powders having an average particle size of less than 1 micron and are present in the composition at a level of from about 0.1 to 5 parts by weight, more particularly from about 0.25 to 4 parts by weight phr. The curing system is preferably used in conjunction with zinc oxide as the primary curative agent. Zinc oxide is normally used in such systems at a level of from about 0.2 to about 7 parts by weight per 100 parts by weight of halogenated elastomer. The present invention provides for particularly good low cure reversion and low precure scorch where zinc oxide is present at relatively low levels in the range of from about 0.3 to about 1.5 parts by weight per 100 parts by weight of halogenated elastomer. Zinc oxide may be excluded from the curing system where other sources of zinc are present, e.g., zinc stearate, a zinc dithiocarbamate or a zinc-containing hydrotalcite. The compositions of this invention may also contain a blend ofthe halogenated elastomers with other elastomers such as natural rubber, polybutadiene, copolymers of butadiene with styrene or acrylonitrile, EPDM elastomers and like materials. The most preferred blends are those containing the halogenated elastomer in major proportion, e.g., greater than 50% by weight ofthe elastomer content ofthe composition is the halogenated elastomer. When making such blends, sulfur or other well known sulfur-containing curatives may be included in the composition, provided they do not detract from the good low compression set properties ofthe other curatives present in the composition. Examples of such compounds are sulfur, benzothiazyl disulfide, N- oxydiethylene benzothiazole-2-sulfenamide, 2-mercaptobenzothiazole, tetramethylthiuram disulfide, M-phenylene bis maleimide, 2-mercapto-4, 5-methyl- benzimidazole and like materials. The vulcanizable composition may also contain other conventional additives know in the art, including fillers such as carbon black or silica, stabilizers, antioxidants, plasticizers, processing oils, pigments, flame retardants, blowing agents and like additives as are known in the art. Preferred additives for the applications of this invention include reinforcing grade carbon black, present at a level of from about 10 to 70 parts by weight phr, - aromatic or aliphatic processing oils present at a level of from about 1 to 15 parts phr, fatty acids or fatty acid salts, e.g., stearic acid or zinc stearate, present at a level of from about 0.25 to 5 parts by weight phr and low molecular weight extrusion/molding aids such as paraffin waxes or low molecular weight polyethylene, present at a level of from about 1 to 10 parts by weight phr. The vulcanizable composition may be prepared and blended using any suitable mixing device such as a two-roll mill, an internal mixer (Brabender Plasticorder), a Banbury Mixer, a kneader or a similar mixing device. Blending temperatures and times may range about 15° to 180°C and from about 4 to 10 minutes respectively. After forming a homogeneous masterbatch mixture ofthe halogenated elastomer and the optional fillers, processing aids and the like, the mixture is then prepared for vulcanization by the further incoφoration ofthe curing system of this invention in the mixing device or on a separate mixing device such as a two roll mill at temperatures generally below 100°C, after which the mixture is sheeted out and molded into shaped articles, as is well known in the art. Alternatively, the composition may be blended in a mixer/extruder, extruded into shapes which shapes may then be vulcanized into cured shaped articles. The shaped articles may be cured by heating to a temperature of about 140°C to 190°C for a period of time sufficient to vulcanize the composition, e.g., from about 5 to 60 minutes. The following examples are illustrative ofthe invention. In the Examples, the halogenated elastomer employed (designated BIPMS) was a brominated teφolymer of isobutylene and para-methyl styrene (PMS) having the following characteristics: PMS CONTENT 2.35 mole % (7.5 wt %) BROMINE CONTENT 1.2 mole % (2.0 wt %) MOONEY VISCOSITY ML [ (1 + 8) 125°C] = 45±5 PHENOLIC ANTIOXIDANT 0.03 wt % CALCIUM STEARATE 1.0 wt% EXAMPLES 1-3 The brominated polymer described above was compounded, vulcanized, and evaluated for curing activity and vulcanizate properties. A series of three formulations as described in Table 1 were prepared by first compounding 100 parts by weight ofthe brominated polymer (BIPMS), 55 parts by weight of a reinforcing carbon black (N-330), 5 parts by weight of an aliphatic process oil and 4 parts by weight of a polyethylene process aid on a laboratory Banbury mixer at a temperature between 150°F and 320°F for about 10 minutes. Portions of this masterbatch were then formulated with a curative mixture of stearic acid, zinc oxide and various curing system additives as shown in Table 1 by adding the curative mixture to the rubber stock and milling the mixture on a two roll mill at a temperature of less than about 100°C for about 5 minutes. Other materials identified in Table 1 are as follows: SULF ADS - dipentamethylene thiuram tetrasulfide ETHYL ZIMATE - zinc diethyldithiocarbamate DHT-4A2 - a hydrotalcite from Kyowa Chemical Industries of Japan having the structure Mg 4 Al 2 (OH)ι 2 CO 3 . The curable mixtures were evaluated for vulcanization activity using a Monsanto Oscillating Disc Rheometer and then physical properties ofthe vulcanizates were evaluated by vulcanizing test pads under the various cure conditions set forth in Table 1 using standard ASTM laboratory test practice as follows: ASTM Test D-3182-89 Mixing and curing procedure D-412-92 Tensile D-573-88 Oven aging D3183-84/92 Curing non-tensile pad parts D-395-89 Compression set D-2240-91 Hardness D-2084-93 Oscillating Disc Rheometer D-l 349-87/92 Std. test temperatures TABLE 1 EXAMPLE * 1 2 3 Master Batch BI-PMS 100 100 100 BLACK N-330 55 55 55 SUNPAR 2280 5 5 5 POLYETHYLENE AC617 4 4 4 Accelerators STEARIC ACID 2 2 2 ZINC OXIDE 1 1 1 SULFADS 1 ETHYL ZIMATE 1 1 TRIETHYLENE GLYCOL 2 2 2 DHT-4A2 2 2 Mixing Conditions Dump Time, min. 3.9 3.9 4 Batch Dump Temp., °F 310 310 320 Batch Weight, grams 1348 1348 1338 Curing Conditions Time, min. 30 30 30 Temperature, °C 171 171 171 PHYSICAL PROPERTIES Mooney Scorch T3 @ 132c, min. 6.78 8.61 7.95 Mooney Viscosity 1+4 @ 100C 74.3 75.9 76.1 1+8 @ 100C 72.2 74 74.5 Rheometer Cure, ODR @ 171°C MH, dNm 80.19 73.47 78.33 ML, dNm 16.6 16.17 13.64 T90, min 14.99 21.48 22.34 ts2,min 1.39 2.07 2.33 EXAMPLE * 1 2 3 Rate 7.8 4.5 6.1 Hardness, Shore A Room Temperature 59.5 59.5 59.9 After Aging 22 hr @ 150°C 59.5 59.9 61.1 70 hr @ 150°C 64.1 64.3 63.3 96 hr @ 175°C 67.9 68.9 69.7 170 hr @ 150°C 74.3 73.1 74.7 Stress Strain 100% Modulus, MPa 3.8 4.3 3.8 300% Modulus, MPa 0 0 0 Elongation @ Break, % 211 209 252 Tensile @ Break, MPa 11.9 12.9 14.1 Stress Strain, Aged 22 hr @ 150°C 100% Modulus, MPa 4 4.1 3.8 300% Modulus, MPpa 0 0 0 Elongation @ Break, % 216 216 234 Tensile @ Break, MPa 13.4 13.4 13.9 Stress Strain, Aged 70 hr @ 150°C 100% Modulus, MPa 4.4 4.5 4.5 300% Modulus, MPa 0 0 0 Elongation @ Break, % 193 198 226 Tensile @ Break, MPa 12.2 12.9 13.3 Stress Strain, Aged 170 hr @ 150°C 100% Modulus, MPa 6.3 6 5.5 300% Modulus, MPa 0 0 0 Elongation @ Break, % 152 161 184 Tensile @ Break, MPa 12.8 13.1 13.8 Stress Strain, Aged 96 hr @ 175° C 100% Modulus, MPa 7.1 6 5.9 EXAMPLE * 1 2 3 300% Modulus, MPa 0 0 0 Elongation @ Break, % 122 162 154 Tensile @ Break, MPa 10.8 12.5 12.3 % Compression Set 22hr @ 150°C 11.9 15.8 31.2 70hr @ 150°C 24.4 22.1 42.4 170hr @ 150°C 36.1 31.9 47.9 96hr @ 175°C 51.3 37.2 56.7 22hr @ 200°C RT. 29.7 N.T. 70hr @ 200° C N.T. 48.6 N.T. *N.T. - not tested The physical property data shown in Table 1 demonstrates that the specific curing system ofthe present invention (Example 2) gives rise to cured elastomers having not only high modulus values, but, also much improved compression set when compared with analogous curing systems outside the scope ofthe invention (Examples 1 and 3). For example, Example 1 differs from Example 2 only in the exclusion ofthe DHT-4A2 component in Example 1, and demonstrates a significantly higher compression set after 96 hours at 175°C than does Example 2. Similarly, Example 3 differs from Example 2 only in the replacement of Ethyl Zimate with Sulfads, and the compression set is significantly lower for Example 2 at all tested conditions. Example 4 The brominated copolymer described above was compounded as described in Examples 1-3 using a different masterbatch formulation as shown in Table 2. Flexon™ 815 is an aliphatic processing oil from Exxon Chemical Co. and PEG 3350 is a polyethylene glycol having a molecular weight of about 3350. TABLE 2 BI-PMS 100 FEF N-550 Carbon Black 60 Flexon™ 815 Process oil 10 Zinc Oxide 1 Ethyl Zimate 1 DHT-4A2 2 PEG 3350 2 MDR 1° Arc, 60 min. @ 165°C ML lb. in. 3.3 MH lb. in. 19.8 Ts2, min. 3.3 T90, min 34.1 MDR 1° Arc, 60 min. @ 175°C ML lb. in. 3.2 MH lb. in. 19.8 Ts2, min 2.2 T90, min 23.3 Physical Properties, Cure @ 165°C Tensile @ Break, MPa 12.8 100% Modulus, MPa 3.9 Elongation @ Break 239 Cure Time, min 40 Shore A Hardness 65 Compression Set, 70 Hours @ 200°C No Post-Cure 59.1 Post-Cure, 2 h. @ 165°C 44.3 Once again, the cured composition exhibits a low compression set value of 59.1 after 70 hours at 200°C and an even lower value of 44.3 where the sample was post cured for 2 hours in an oven at 165°C. Thus, the invention provides for cured elastomer compositions having both high modulus properties and compression set values of less than 50% even at high temperatures in the order of 200°C, and compression set values of less than 40% after 96 hours at 175°C.

Claims: CLAIMS What is claimed is: 1. A curable composition comprising a mixture of a halogenated elastomer selected from the group consisting of chlorinated or brominated butyl rubber and chlorinated or brominated inteφolymers of a C to C isoolefin and a para- alkylstyrene comonomer, and mixtures thereof, and a curing system for said halogenated elastomer, said curing system comprising: a) O to about 5 parts by weight phr of zinc oxide; b) At least about 0.25 parts by weight phr of at least one metal or ammonium salt of a dialkyl dithiocarbamic acid wherein the alkyl groups contain 1 to 12 carbon atoms or a diaryl dithiocarbamic acid wherein the aryl groups contains 6 to 10 carbon atoms; - c) At least about 0.25 parts by weight phr of a polyalkylene glycol; and d) At least about 0.1 part by weight phr of at least one finely divided hydrotalcite comprising at least one basic metal carbonate hydroxide wherein said metal is of Group II or III ofthe Periodic Table. 2. The composition of claim 1 wherein zinc oxide is present at a level of at least about 0.2 parts by weight phr. 3. The composition of claim 2 wherein said hydrotalcite has the formula Mg4Al 2 (OH)ι 2 CO 3 • X H 2 O, where X is 0 to 3. 4. The composition of claim 3 where X is O. 5. The composition of claim 1 further containing at least about 0.25 parts by weight phr of stearic acid or zinc stearate. 6. The composition of claim 2 further containing at least about 0.25 parts by weight phr of stearic acid. 7. The composition of claim 3 wherein said salt of dithiocarbamic acid is zinc diethydithiocarbamate. 8. The composition of claim 7 wherein said glycol is triethylene glycol. 9. The composition of claim 1 wherein said halogenated elastomer comprises a brominated inteφolymer of isobutylene and para-methylstyrene. 10. The composition of claim 9 further containing from about 10 to 70 parts by weight phr of a filler. - 11. The composition of claim 10 wherein said filler is a reinforcing grade carbon black. 12. The composition of claim 9 further containing from about 0.25 to 5 parts by weight phr of a low molecular weight polyethylene processing aid. 13. The composition of claim 9 comprising: a) from about 0.3 up to about 1.5 parts by weight phr of zinc oxide b) from about 0.25 up to about 2.0 parts by weight phr ofthe zinc salt of said dialkyldithiocarbamic acid; c) from about 0.25 up to about 4.0 parts by weight phr of said polyalkylene glycol; and d) from about 0.1 up to about 5 parts by weight phr of said hydrotalcite. 14. The composition of claim 13 further containing from about 0.25 up to about 5 parts by weight phr of stearic acid. 15. The composition of claim 13 wherein said hydrotalcite has the formula Mg 4 Al 2 (OH), 2 CO 3 . 16. The composition of claim 15 wherein said zinc salt is zinc diethyldithiocarbamate. 17. The composition of claim 16 wherein said polyalkylene glycol is triethylene glycol. 18. The composition of claim 16 wherein said polyalkylene glycol is polyethylene glycol. 19. A method for preparing a vulcanized composition comprising heating the composition of claim 1 at a temperature and for a period of time sufficient to cure said composition. 20. A method for preparing a vulcanized composition comprising heating the composition of claim 13 at a temperature and for a period of time sufficient to cure said composition. 21. A vulcanized shaped article prepared by the process of claim 19, said article having a compression set after 96 hours at 175°C of less than 50%. 22. A vulcanized shaped article prepared by the process of claim 20, said article having a compression set after 96 hours at 175°C of less than 50%. 23. The article of claim 22 having a compression set after 96 hours at 175°Coflessthan40%

Inventors: MCELRATH KENNETH O, MCELRATH, KENNETH, O.
Applicants: EXXON CHEMICAL PATENTS INC, EXXON CHEMICAL PATENTS INC.
Application year: 1996
Main classification: C08K13
IPC codes: C08K3, C08K5, C08K13, C08L23