RUBBER BLENDS

Abstract: Blends are disclosed of monoolefin rubber with high-diene hydrocarbon rubber in which the monoolefin rubber is in the form of discrete vulcanized particles dispersed in a matrix of unvulcanized high-diene hydrocarbon rubber. The blends can be easily processed, and in a subsequent step, the high-diene hydrocarbon portion cured to give rubber articles having the ozone resistance of the monoolefin rubber and the good physical properties of the high-diene hydrocarbon rubber.

Description: This invention relates to blends of monoolefin rubber and high-diene hydrocarbon rubber and to compositions and products incorporating such blends. Monoolefin rubber, typified by terpolymers of ethylene, propylene and a minor portion of diene monomer (EPDM rubber) has particularly good resistance to the degrading effects of oxygen or ozone, among other good properties. In other respects, however, unvulcanized monoolefin rubber has poor tack properties and is consequently unsuited to the production of built-up molded articles such as tires wherein assembly of uncured components requires good tack. A high-diene hydrocarbon rubber, such as natural and synthetic polyisoprene, polybutadiene and copolymers of butadiene with other monomers such as styrene, has better tack, but is comparatively more susceptible to oxygen and ozone degradation, probably because of the relatively high number of double-bonds in its molecular backbone. Blends of monoolefin rubber (e.g., EPDM) with high-diene rubber (e.g., natural rubber) appeared to be the answer to the search for a rubbery material which would combine the good properties of each component. Unfortunately, simple blends of these two materials have not proved to be successful, except those in which only a small amount of one or the other type of rubber was present. Thus, if enough EPDM rubber is used to give good ozone resistance, because of fundamental dissimilarities in the two types of rubber, blends of significant amounts of one with another result in heterogeneous mixtures with poor properties. The two types of rubber can be said to be "technologically incompatible," differing in such properties as unvulcanized-state viscosity, surface energy, and vulcanization rate. The various methods of attempting to resolve this technological incompatability between monoolefin copolymer rubber and high-diene hydrocarbon rubber have all left something to be desired. Such methods include 1) using special vulcanization systems and special accelerators to try to achieve optimum vulcanization of both phases, 2) making EPDM rubber with significantly higher diene content, 3) modifying EPDM rubber, by using a variety of techniques, in an effort to increase its vulcanization rate and 4) prevulcanizing EPDM rubber before blending high-diene hydrocarbon rubber with it. All of these methods have produced some improvements in the properties of the blends; in most instances the improvements were not sufficient to justify their cost. Accordingly, a blend of monoolefin copolymer rubber and high-diene rubber which would have the good properties of each component is still unrealized by the industry. One application to which such blends are most suited is in tire sidewalls, where the maximum resistance to oxidation, and especially ozone attack, is needed, and yet good processability and low hysteresis are also prerequisites. SUMMARY OF THE INVENTION It has now been discovered that the good properties of both monoolefin rubber and high-diene rubber can be obtained from a mixture comprising from 5-80 weight percent of monoolefin copolymer rubber and from 95-20 weight percent unvulcanized high-diene hydrocarbon rubber wherein the monoolefin copolymer rubber contains pendent acid groups in an amount sufficient, on addition of an equivalent amount of a metal salt, a metal oxide or a diamine, to vulcanize the monoolefin rubber. In one aspect of the invention, the monoolefin copolymer rubber in the mixture is vulcanized and is in the form of particles having an average diameter such that all of the particles are substantially below 50 µm, or their weight average is below 10 µm. With regard to the novel mixture above, monoolefin copolymer rubber means a rubbery polymer from monomers comprising ethylene or propylene and at least one other alpha olefin of the formula CH₂=CHR in which R is alkyl of 1-12 carbon atoms, and from none to a minor portion of one or more copolymerizable dienes. Suitable monoolefin copolymer rubber comprises largely non-crystalline, rubbery copolymer of two or more alpha monoolefins, preferably copolymerized with at least one polyene, usually a diene. However, saturated monoolefin copolymer rubber, commonly called "EPM" rubber, can be used, for example, copolymers of ethylene and propylene. Examples of unsaturated monoolefin copolymer rubber, commonly called "EPDM" rubber, which are satisfactory comprise the products from the polymerization of monomers comprising two monoolefins, generally ethylene and propylene, and a lesser quantity of non-conjugated diene. Suitable alpha monoolefins are illustrated by the formula CH₂=CHR in which R is hydrogen or alkyl of 1-12 carbon atoms, examples of which include ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 2-methyl-1-propene, 3-methyl-1-pentene, 4-methyl-1 pentene, 3,3-dimethyl-1-butene, 2,4,4-trimethyl-1-pentene, 5-methyl-1-hexene, 4-ethyl-1-hexene and others. Satisfactory non-conjugated dienes include straight chain dienes such as 1,4-hexadiene, cyclic dienes such as cyclooctadiene and bridged cyclic dienes such as ethylidenenorbornene and dicyclopentadiene. The high diene hydrocarbon rubbers in the mixtures of the invention are essentially random, noncrystalline, rubbery homopolymers from diolefin monomers or copolymers the major components of which are derived from diolefins. The high diene rubber can be a natural polymer, such as Hevea or guayule, or a synthetic polymer. Examples of suitable high diene rubbers include natural rubber, synthetic polyisoprene, polybutadiene, and copolymers of isoprene or butadiene with one or more other copolymerizable monomers such as styrene, alpha methyl styrene, and isobutylene. Of these materials, natural (e.g. Hevea) rubber, synthetic polyisoprene rubber, polybutadiene and SBR (styrene/butadiene rubber) rubber are preferred. Mixtures of two or more high diene hydrocarbon rubbers can be used. The mixtures of the invention are, by definition, processable, so the amount of particulate, vulcanized monoolefin copolymer rubber cannot be so great as to result in an unprocessable mixture. By "processable" is meant capable of being processed in ordinary rubber processing equipment, such as extruders, calenders or the like. Examples of unprocessable rubber compounds are those which are insufficiently cohesive, forming particulate or "crumbly" masses which cannot be handled. The mixtures must be capable of extrusion to produce extrudate preforms, or be capable of forming a continuous sheet on a calender or roll mill. Preferred mixtures will contain from 5 to 80% by weight, based on the total weight of both rubbers in the blend, of monoolefin copolymer rubber. More preferred mixtures contain from 20 to 60% by weight of monoolefin copolymer rubber. Fillers which can be present include carbon black, clay, talc, calcium carbonate, feldspar, aluminum trihydrate and any other filler materials normally added to rubber. Oils, either parafinic or naphthenic can be present in the blends, if desired. Colorants, such as pigments or dyes can be present as well. Minor portions of unvulcanized monoolefin rubber can also be present. The monoolefin rubber, which is acid modified, is combined with unvulcanized high-diene hydrocarbon rubber. The monoolefin rubber is also unvulcanized, but vulcanizable. The acid-modified monoolefin rubber contains sufficient pendent acid groups so as to be vulcanizable upon the addition of a vulcanizing agent, which is a metal salt or oxide or a diamine. In the mixture of the invention the vulcanizing agent may be present, or it can be subsequently added. If the vulcanizing agent is present, care must be taken so that, at this step, vulcanization does not take place. Typically, the mixture containing such a vulcanizing agent can be maintained at a temperature which is below that at which significant vulcanization will take place. This mixture can be considered an intermediate form, and can be treated as a "master-batch," and will be stable at room temperatures. If desired, the mixture can be formed into pellets for convenience of handling and further processing. The mixture should contain from 5-80 weight percent of acid-modified monoolefin rubber and from 95-20 weight percent of high-diene hydrocarbon rubber, based on the total weight of both rubbers. Other compounding ingredients can also be included, such as the vulcanizing agents for the acid-modified monoolefin rubber, as previously indicated, including fillers, oils, antidegradants and vulcanizing agents for the high-diene hydrocarbon rubber. Typically, the amount of pendent acid groups present will be from about 0.1 to 10.0 weight percent, based on the monoolefin rubber, and they can be introduced on the monoolefin rubber in known ways. Some slight degree of cross-linking of the monoolefin rubber can occur in this introduction of the pendent groups without significant adverse effect on the mixture or on its final properties. A preferred acid-modified monoolefin rubber is produced by the reaction therewith of maleic acid or anhydride, preferably in the presence of a free-radical initiator, to introduce pendent succinic acid or anhydride groups on the rubber. Sulfonic acid groups may also be introduced, as shown in the art. PREFERRED EMBODIMENTS OF THE INVENTION A particularly preferred embodiment of the invention involves a blend of cured EPDM rubber dispersed in natural rubber. EPDM rubber has outstanding resistance to degradation from oxygen or ozone attack, and natural rubber has excellent stress-strain, and hysteresis properties when vulcanized, and excellent tack and green strength in its unvulcanized state. In order to make such a blend by the dynamic vulcanization method it is necessary to modify the EPDM rubber so that it can be vulcanized in the presence of natural rubber without the natural rubber itself being vulcanized. A preferred method of modifying the EPDM rubber is to treat it with maleic anhydride (or a derivative thereof) so as to engraft a pendant succinic anhydride functionality on molecules of the EPDM rubber. To facilitate this reaction, a free-radical generating material is effective, for example, benzothiazolyl disulfide (MBTS). Of course, other treatments can be used to modify the EPDM rubber so as to attach functional groups to it which are available for cross-linking, to permit vulcanization of the EPDM rubber. Other functional groups useful for selective-vulcanization sites on the monoolefin rubber molecules include carboxyl groups, sulfonic acid groups, halogen atoms (especially allylic), amino groups, hydroxyl groups, ester groups, mercapto groups, aldehyde groups, keto groups, epoxide groups, maleimide-derived groups, acrylic-derived groups, maleamic acid- and substituted maleamic acid-derived groups, phenolic groups, etc. Each of these groups can be used in conjunction with an appropriate vulcanization system which normally does not readily vulcanize high-diene rubbers at the temperature of the process of the invention. Attempts to vulcanize EPDM rubber in a mixture with natural rubber by using conventional sulfur vulcanization techniques, would result in the faster-reacting natural rubber quickly consuming all or most of the vulcanizing agents, leaving the slower-reacting EPDM rubber either partially or almost totally unvulcanized. If extra vulcanizing agents (i.e., sulfur and accelerators) were employed, the natural rubber portion of the mixture would merely overcure, with a resultant loss in most of its properties. Where the EPDM is first "functionalized," by grafting maleic anhydride-derived groups thereon, it can then be vulcanized in a blend with natural rubber by adding a material which reacts with the pendant succinic anhydride or acid groups and cross-links the EPDM rubber without significantly affecting the natural rubber. Cross-linking materials effective for this purpose include metal oxides, such as zinc oxide, calcium oxide, magnesium oxide, and diamines. EXAMPLE I In order to investigate the properties of blends according to the invention, a series of experimental rubber mixtures was prepared and tested according to the following description, in which all parts are by weight unless otherwise noted. For convenience, a number of materials are expressed in abbreviated form, as follows: Abbreviated Designation Material EPDM Terpolymer of ethylene, propylene and ethylidenenorbornene sold by Copolymer Corp. under the trademark "Epsyn 70A" SMR 5 Natural rubber Black N 326 Carbon Black Oil Extender oil sold by Sun Oil Co. under the trademark "Circosol 4240" Accelerator N-(t-butyl)-2-benzothiazolyl sulfenamide Antidegradant N-(1,3-dimethylbutyl)-N'-phenyl-p-phenylenediamine Modified EPDM rubber (MEPDM) was first prepared by mixing the following ingredients in a BR Banbury mixer: 950g EPDM, 19g maleic anhydride and 1.9g benzothiazyl disulfide (MBTS). The ingredients were mixed at high speed until the indicated stock temperature was 232-260°C. Mixing was then continued at the appropriate speed so as to maintain the desired temperature range, for a period of 5 minutes. The stock temperature was 232°C at dump. Three masterbatches were then prepared in the OO Banbury mixer according to the following recipes: Ingredient MEPDM UEPDM UNR Modified EPDM 2000 - - EPDM - 2000 - SMR-5 - - 2000 Black 1000 1000 1000 Oil 200 200 200 Thus, MEPDM was based on the modified EPDM produced above, UEPDM on unmodified EPDM, and UNR on natural rubber (also unmodified). Vulcanizable stocks were prepared to give the compositions described in Table I. In each stock, EPDM and natural rubber black masterbatches were mixed for about 2.5 minutes at a speed so as to bring the temperature to about 135°C, then the zinc oxide and stearic acid were added and mixing was continued for about 1/2 minute. Each batch was then blended on a roll mill, where the sulfur and accelerator were added. The stocks in Table I are identified on the basis of 100 weight parts of rubber. The stocks are blends of various proportions of either modified EPDM rubber or unmodified EPDM rubber with natural rubber, as shown. After mixing, tack and green strength values were determined on each. Green strength measurements are performed by using a standard tensile testing machine. Samples of the stock to be tested are pressed into slabs approximately three millimeters in thickness, from which slab specimens, measuring about 20.3 X 2.4 cm, are die-cut. The specimens are bench marked (to a test length of 2.54 cm.) in the center, and the exact width and thickness are measured. Specimens are pulled at a crosshead speed of 50.8 cm. per minute, with the stress recorded at desired levels of elongation up to 1200% or break. Stress values are calculated based on the original cross-section area of each specimen, and the maximum stress value is also recorded. Tack measurements are made by using the Monsanto Tel-Tak instrument, as described in an article by J. R. Beatty in Rubber Chemistry and Technology, 42, 1040 (1969). Fabric-backed rubber specimens are cut to a width of 6.35 mm and placed at right angles to give a contact area of 0.403 cm². A contact pressure of 227 grams is used for all tests, with a 30-second dwell time. Sample "stickiness" is measured by substituting a polished stainless steel surface for one specimen, and the result is subtracted from the tack value to give a "true tack" measurement. The units of these measurements are in grams per square centimeter, representing the maximum force per unit area required to separate the specimens, at a separation rate of 2.54 cm. per minute. Based on the rheometer results the stocks were cured at 153°C to optimum levels, and the stress-strain and hardness properties of the vulcanizates were measured, both unaged and after aging for 24 hours at 100°C according to the procedures of ASTM D-412. The hardness and stress-strain properties are set forth in Table II. Further testing on cured samples was performed, with the test results set forth in Table III. Compression set testing was done according to ASTM D-395. The rebound test was done according to the description of the Lupke rebound test in the Vanderbilt Rubber Handbook (1958), pages 315, 316. Torsional hysteresis was determined by the method of Mooney and Gerke, Rubber Chem. Tech 14 (1941). Tensile set was performed according to ASTM D-412, with 100% elongation of the T-50 sample for ten minutes, then measurement after ten minutes recovery. The fatigue-to-failure test was run according to ASTM D-4482-85. Tear testing was done according to ASTM D-624, and the Goodrich flexometer results were obtained by the method of ASTM D-623. The stocks were also tested, after curing, for ozone resistance. First, samples were tested in air containing 25 parts per hundred million (pphm) of ozone. T-50 specimens were measured for modulus at 100% elongation, and then exposed to the ozone atomosphere in static, dynamic and intermittent modes. Test results were reported as the number of hours until a 20% loss in apparent modulus was reached. Ozone resistance was also measured according to ASTM D-3395 on a belt flexer at a concentration of 50 pphm ozone, with the time to first crack recorded, in hours. Values in parentheses were extrapolated, when samples broke. Samples were also rated by the Shell rating system on a scale of 1 to 10 (with 10 being the highest rating) after 174 hours and 485 hours of exposure. The ozone test results are summarized in Table IV. The samples tested represent a comparison of blends of natural rubber with EPDM rubber, and with the modified EPDM rubber in amounts as specified, together with control samples. The uncured properties (Table I) show a slight loss of tack with increased levels of EPDM rubber, both modified and unmodified. The green strength increases slightly with increased concentrations of unmodified EPDM, and sharply with increased concentration of modified EPDM. Rheometer data show that the cure time is slowed with increasing levels of EPDM rubber, and that the viscosity of the stocks increases slightly with increased levels of EPDM. Mooney Scorch data indicate little change in scorch times. The hardness of cured samples appears to increase with increasing levels of EPDM rubber, modified or unmodified. Aging reduced this difference, so that all samples showed equivalent hardness values after 24 hours at 100°C. Modulus values drop off with higher levels of unmodified EPDM, but increase slightly as levels of modified EPDM are increased. Stress-strain measurements of aged samples show that the antidegradant provides a marked superiority in retention of ultimate tensile strength. Turning to Table III, compression set values appear essentially equivalent for all samples, while rebound seems to improve at higher levels of modified EPDM. Torsional hysteresis values appear to increase with increasing levels of unmodified EPDM, and to decrease with increasing levels of modified EPDM. Tensile set increases with increasing levels of both modified and unmodified EPDM, but more sharply with the latter. The Fatigue to Failure tests demonstrate that the modified EPDM gives a significant improvement with increasing levels, but the unmodified EPDM gives poorer fatigue life with increasing levels. These trends were evident in both the constant-strain testing and the constant-energy testing. Tear resistance decreased, both at room temperature and at 100°C, with increasing levels of EPDM, although the modified EPDM greatly outperformed the unmodified EPDM. In Flexometer tests, the temperature rise is increased with increasing levels of EPDM, though the unmodified EPDM gives a greater rate of increase with increases in its concentration. Higher levels of EPDM give increased set values. Interpreting the ozone data in Table IV, it is immediately apparant that, at levels of 30% or more, EPDM greatly improves ozone resistance of the stocks. This effect is apparent in both modified and unmodified EPDM stocks. EXAMPLE II In order to investigate higher levels of EPDM rubber in blends with natural rubber, a series of compounds was prepared following the procedures of Example I. In these compounds, a small amount of hexamethylenediamine (HMD) was added after the modified EPDM was mixed with the natural rubber, as an additional curative for the modified EPDM. Proportions and results are set forth in Table V. Stock No. 8 9 10 11 Modified EPDM 40 60 75 80 SMR 5 60 40 25 20 Black 50 50 50 50 Oil 10 10 10 10 HMD 0.26 0.23 0.26 0.29 Zinc Oxide 5.5 5.5 5.5 5.5 Sulfur 2 2 2 2 Accelerator 2 2 2 2 Cure Time, @ 153°C, Min. 25 30 50 50 Hardness, Shore A 45 46 50 52 Modulus @ 200%, MPa 1.36 1.61 1.85 2.17 Modulus @ 300%, MPa 2.16 2.87 3.47 4.29 Ult. Tensile, MPa 18.8 5.41 4.90 4.72 Ult. Elong., % 647 404 354 314 Tensile set, % 2.5 2.0 2.5 2.0 Torsional Hysteresis, % 3.9 3.9 3.8 3.8 The physical test results in Table V show that ultimate tensile strength drops significantly as the amount of EPDM rubber reaches 60%. However, the physical properties generally indicate the blends are useful. Ozone tests were not run, as it was assumed that ozone resistance is excellent in blends with higher levels of EPDM rubber. To summarize the data, in most tests, the blends containing modified EPDM outperformed those containing unmodified EPDM at equal levels. Most significant improvements were noted in respect to fatigue life, tearing resistance and tensile strength. Thus, vulcanizates from the blends of the invention achieved excellent ozone resistance with little or no sacrifice of physical properties.

Claims: A mixture comprising from 5-80 weight percent of monoolefin copolymer rubber and from 95-20 weight percent unvulcanized high-diene hydrocarbon rubber wherein the monoolefin copolymer rubber contains pendent acid groups in an amount sufficient, on addition of an equivalent amount of a metal salt, a metal oxide or a diamine, to vulcanize the monoolefin rubber. The mixture of Claim 1, wherein the monoolefin copolymer rubber is a polymer from ethylene, propylene and a non-conjugated diene monomer. The mixture of Claim 1, wherein the high-diene hydrocarbon rubber is natural or synthetic polyisoprene rubber. The mixture of Claim 2 wherein the monoolefin copolymer rubber is a terpolymer from ethylene, propylene and a third monomer selected from 1,4-hexadiene, cyclooctadiene, dicyclopentadiene and ethylidenenorbornene, and is present in an amount of from 20 to 60 weight percent based on the total weight of the monoolefin copolymer rubber and the high-diene hydrocarbon rubber together. The mixture of Claim 1, wherein the pendent acid groups are carboxylic acid groups. The mixture of Claim 1, wherein the pendent acid groups are present in an amount of from 0.1 to 10 weight percent, based on the weight of the monoolefin copolymer rubber. The mixture of Claim 1, wherein the pendent acid groups are succinic acid groups, the high-diene rubber is natural rubber, and the mixture also contains carbon black and oil. The mixture of Claim 1 wherein the monoolefin copolymer rubber has been treated with maleic anhydride and a free-radical initiator at an elevated temperature. The mixture of Claim 1, wherein the monoolefin copolymer rubber is vulcanized and is in the form of particles having an average diameter such that all of the particles are substantially below 50 µm, or their weight average is below 10 µm. The mixture of Claim 9 wherein the monoolefin copolymer rubber is vulcanized with a metal oxide or a diamine. The mixture of Claim 10 wherein the metal oxide is zinc oxide, calcium oxide, magnesium oxide or a mixture of two or more metal oxides. The mixture of Claim 9 wherein vulcanizing agent for the high-diene hydrocarbon rubber is present.

Inventors: CORAN, AUBERT YAUCHER
Applicants: MONSANTO COMPANY
Application year: 1986
Main classification: C08L21
IPC codes: C08L23, C08L101, C08L9, C08L7, C08L21