Nylon modified rubber composition

Abstract: It is desirable to increase the modulus of rubbers utilized in a wide variety of applications. This invention discloses a technique for modifying rubbers to improve their modulus without sacrificing other properties. The subject invention more specifically relates to a process for preparing a rubber composition having a high modulus which comprises reacting at least one thio acid with at least one polydiene rubber and at least one nylon.

Description: Background of the Invention It is sometimes desirable to increase the modulus of rubber compounds. For instance, it is generally desirable to increase the modulus of rubber compounds which are utilized in tire tread base compositions and in tire wire coat compounds. A higher degree of stiffness in such rubber compositions is conventionally attained by incorporating larger amounts of fillers, such as carbon black, into the rubber compounds and/or by increasing the state of cure of such compounds. Unfortunately, both of these techniques lead to undesirable results. For instance, the incorporation of additional carbon black into rubber compounds typically leads to high levels of hysteresis. Accordingly, the utilization of such compounds in tires results in excessive heat build-up and poor cut growth characteristics. The utilization of high amounts of sulfur to attain a high state of cure typically leads to poor aging resistance. Furthermore, it is highly impractical to reach high levels of stiffness by increased state of cure alone. For these reasons, it is not possible to attain the desired degree of stiffness in tire tread base compounds by simply adding higher levels of fillers or curatives. Summary of the Invention The subject invention discloses a technique for modifying a rubber so as to greatly increase its modulus. This results in the rubber being better suited for applications where a high degree of stiffness is desirable. However, this modification procedure does not generally sacrifice other desirable characteristics of the rubber. For instance, the rubber compositions of this invention have an increased modulus but do not have an increased degree of hysteresis. The rubber compositions of this invention are prepared by grafting nylon onto the rubber. This is done by reacting at least one dithio diacid with the rubber and at least one nylon. This procedure grafts polymer chains which are comprised of nylon onto the polymer chains of the rubber. The subject invention specifically discloses a process for preparing a rubber composition having a high modulus which is characterized by reacting from 0.1 phr to 20 phr at least one dithio diacid having the general structural formula HOOC-A-S-S-A-COOH wherein A represents an alkylene group containing from 1 to 6 carbon atoms with at least one polydiene rubber selected from polybutadiene, styrenebutadiene rubber, synthetic polyisoprene, natural rubber, isoprene-butadiene rubber, isoprene-butadiene-styrene rubber, nitrile rubber, carboxylated nitrile rubber and EPDM rubber (ethylene-propylene-diene monomer rubber) and at least one nylon having a melting point which is within the range of 150°C to 255°C at a temperature which is above the melting point of the nylon. In most cases from 2 phr to 55 phr of nylon will be utilized in the modification procedure. It is generally preferred to react the nylon with the thio acid at a temperature which is within the range of 180°C to 200°C to form a modified nylon containing mercaptan groups and to subsequently react the modified nylon with the rubber at a temperature which is within the range of 180°C to 200°C. However, such reactions will be carried out at a temperature which is at least as high as the melting point of the nylon. Detailed Description of the Invention The process of this invention can be utilized to modify polydiene rubbers selected from polybutadiene, styrene-butadiene rubber (SBR), synthetic polyisoprene, natural rubber, isoprene-butadiene rubber, isoprene-butadiene-styrene rubber, nitrile rubber, carboxylated nitrile rubber, and EPDM rubber (ethylene-propylene-diene monomer rubber). The technique of this invention is particularly well suited for utilization in modifying natural rubber, synthetic polyisoprene, and cis-1,4-polybutadiene. The dithio diacids which are utilized in modifying the polydiene rubber are compounds which have the general structural formula HOOC-A-S-S-A-COOH wherein A represents an alkylene group containing from 1 to 10 carbon atoms. Some representative examples of such dithio diacids include dithio diacetic acid, dithio dipropanoic acid, dithio dibutanoic acid, dithio dipentanoic acid, and dithio dihexanoic acid. Dithio dipropanoic acid is the most highly preferred of the dithio diacids. The utilization of mercaptans in chemical processes is generally associated with undesirable odors. However, dithio diacids can be utilized in the process of this invention with virtually no undesirable odors being generated. Additionally, dithio diacids react readily with both the polydiene rubber and the nylon being utilized in the modification procedure. Virtually any type of nylon can be utilized in preparing the rubber compositions of this invention. These nylons are polyamides which can be prepared by reacting diamines with dicarboxylic acids. The diamines and dicarboxylic acids which are utilized in preparing such nylons will generally contain from 2 to 12 carbon atoms. Nylons can also be prepared by addition polymerization. Nylon which is prepared by reacting hexamethylene diamine with adipic acid (hexanedioic acid) can be utilized in the process of this invention. It is generally referred to as nylon-6,6 because it is derived from a diamine which contains 6 carbon atoms and a dicarboxylic acid which contains 6 carbon atoms. Nylon-6,6 typically has a number average molecular weight of 12,000 to 20,000, is exceptionally strong, abrasion resistant, and available from a wide variety of sources. The nylons which are preferred for utilization in the process of this invention have melting points which are within the range of 150°C to 255°C. Some representative examples of such preferred nylons include nylon-6,6, nylon-6, nylon-7, nylon-8, nylon-9, nylon-10, nylon-11, nylon-12 and nylon-6,12. The most preferred nylons have melting points which are within the range of 175°C to 210°C. Some representative examples of such highly preferred nylons include nylon-8, nylon-9, nylon-10, nylon-11 and nylon-12. Polycapryllactam, which is generally referred to as nylon-8, is generally prepared by polymerizing capryllactam. This polymerization takes place readily in the melt with a small amount of amino acid initiator. Capryllactam is prepared by dimerization of butadiene to cyclooctadiene, which is hydrogenated to cycloctane, oxidized to cycloctanone, converted to the oxime with hydroxylamine, and subjected to the Beckmann rearrangement. Nylon-8 has a melting point of 200°C. Poly(ω-aminoundecanoic acid), known as nylon-11, can be prepared by the melt polymerization of ω-aminoundecanoic acid under an inert gas atmosphere at a temperature of 215°C. Nylon-11 has a melting point of 190°C. Nylon-12 or poly(ω-dodecanolactam) is normally prepared by the polymerization of ω-dodecanolactam at a high temperature of at least 300°C utilizing an acid catalyst. ω-dodecanolactam is prepared by trimerization of butadiene to cyclododecatriene, the subsequent hydrogenation to cyclododecane, followed by oxidation to cyclododecanone, which is converted to the oxime with hydroxylamine, with the oxime being rearranged by Beckmann rearrangement to yield the ω-dodecanolactam. Nylon-12 has a melting point of 179°C and is very highly preferred for use as the nylon in the process of this invention. The nylons used in the process of this invention will typically have number average molecular weight which is within the range of 8,000 to 40,000. Such nylons will more typically have number average molecular weights which are within the range of 10,000 to 25,000. The nylon utilized can be capped or can have free primary amine end groups. However, nylons having free amine end groups are believed to react more quickly with thio acids and are accordingly preferred. The modified rubber compositions of this invention are prepared by simply reacting the dithio diacid with the polydiene rubber and the nylon. This can be accomplished by simply mixing the dithio diacid homogeneously throughout a blend of the polydiene rubber and the nylon and heating the thio acid/nylon/polydiene rubber blend. The modification procedure of this invention can be carried out utilizing several satisfactory techniques. For instance, the dithio diacid, nylon, and polydiene rubber can be simultaneously mixed together and heated to graft the nylon onto the rubber. In another scenario, the dithio diacid can be reacted with the rubber to produce a rubber having carboxyl groups bound thereto and the rubber can then be subsequently reacted with the nylon to produce the modified rubber of this invention. In the preferred technique of this invention, the dithio diacid is first reacted with the nylon to produce a modified nylon containing mercaptan groups and the modified nylon is subsequently reacted with the rubber. It is preferred to prereact the thio acid with the nylon in a first reaction step and to subsequently react the reaction product with the rubber because the rubber is subjected to elevated temperatures for a shorter duration of time and accordingly less degradation occurs. The reaction between the dithio diacid and the nylon will typically be carried out at a temperature which is within the range of 150°C to 300°C. It will preferably be carried out at a temperature which is within the range of 165°C to 250°C and will more preferably be conducted at a temperature which is within the range of 180°C to 200°C. The reaction between the rubber and the nylon will typically be carried out at a temperature which is within the range of 120°C to 250°C. In most cases it will be preferred to carry out the reaction between the dithio diacid and the rubber at a temperature within the range of 125°C to 200°C with the most preferred temperature range for the reaction being from 130°C to 150°C. In cases where the dithio diacid is reacted with the nylon and the rubber simultaneously, a temperature which is within the range of 150°C to 250°C will be utilized. In such cases the simultaneous reaction between the dithio diacid, the nylon, and the rubber will more preferably be carried out at a temperature which is within the range of 165°C to 200°C. However, reactions between the dithio diacid and the nylon and reactions between the rubber and modified nylon containing mercaptan groups will be carried out at a temperature which is at least as high as the melting point of the nylon. In other words, reactions which are carried out in the presence of nylon will be conducted at a temperature which is at least as high as the melting point of the nylon. In most cases, preferred reaction temperatures will be slightly above the melting point of the nylon. The dithio diacid is mixed throughout the rubber and/or the nylon utilizing conventional mixing procedures. For example, the mixing can be carried out in a Banbury mixer or a mill mixer. Normally, such blends will be prepared by mixing from 2 phr to 55 phr (parts per hundred parts of rubber) of the nylon throughout the polydiene rubber. The nylon can, of course, be prereacted with the dithio diacid prior to mixing it with the rubber. In most cases it will be preferred to utilize from 10 phr to 50 phr of nylon in the blend. It will be typically more preferred to utilize from 20 phr to 45 phr of nylon in the blend. The amount of thio acid utilized will typically be within the range of 0.1 phr to 20 phr. In most cases it will be preferred to utilize from 0.5 phr to 3 phr. It is generally most preferred to utilize from 0.8 phr to 2 phr of the thio acid. This invention is illustrated by the following working examples which are presented merely for the purpose of illustration and are not to be regarded as limiting the scope of the invention or the manner in which it can be practiced. Unless specifically indicated otherwise, parts and percentages are given by weight. Examples 1-4 In this series of experiments, high cis-1,4-polyisoprene was modified in accordance with the process of this invention. In the procedure utilized, 1,150 grams of high cis-1,4-polyisoprene was mixed with 11.5 grams of dithiodipropionic acid, and 5.75 grams of thiodiphenyl amine (a high temperature antidegradant) in a laboratory size Banbury mixer which was operated at a temperature of 130 to 150°C at an initial speed of 70 rpm which was reduced to 40 rpm after about 5 minutes to reduce temperature build up. The Banbury was run at 40 rpm for two additional minutes. During this procedure dithiodipropionic acid reacted with some of the double bonds in the high cis-1,4-polyisoprene to produce a rubber having carboxyl groups bound thereto. In Example 1 200 grams of the carboxylated polyisoprene produced was mixed with 50 grams of nylon-12 and 1 gram of diaryl-p-phenylene diamine in a 280 gram preparative Brabender mixer which was operated at 196°C for a mixing period of about 7 minutes. In Example 2, 185 grams of the carboxylated polyisoprene was mixed with 64.8 grams of nylon-12 and 0.8 grams of diaryl-p-phenylene diamine in the Brabender mixer for a period of about 7 minutes at a temperature which was within the range of 190 to 195°C. In Example 3, the procedure utilized in Example 2 was repeated except that 200 grams of the polyisoprene was mixed with 50 grams of nylon-12. In Example 4, the procedure utilized in Example 2 was also repeated except that 173 grams of the high cis-1,4-polyisoprene was mixed with 77.9 grams of the nylon-12. In Examples 1 and 3, 25 phr of nylon-12 was utilized. In Examples 2 and 4, 35 phr and 45 phr of nylon-12 was utilized, respectively. The rubber compositions made were compounded with 45 phr or carbon black, 9 phr of an oil, 2 phr of N-phenyl-N′-(1,3-dimethylbutyl)-p-phenylenediamine, 1 phr of diaryl-p-phenylene diamine, 1 phr of a wax, 3 phr of stearic acid, 3 phr of zinc oxide, 0.8 phr of N-oxydiethylene benzothiazole-2-sulfenamide, 0.4 phr of guanidine, and 1.6 phr of insoluble sulfur. The rubber compositions were then cured at 300°F (149°C) for 25 minutes. The 50% modulus, 100% modulus, tensile strength and elongation of the cured rubber samples made are reported in Table I. Example 50% Modulus 100% Modulus Tensile Strength Elongation 1 5.2 9.0 16.5 250% 2 4.4 7.2 12.5 220% 3 5.0 9.1 16.8 220% 4 4.8 8.3 12.1 160% As can be determined by reviewing Table I, very significant improvements in the modulus and tensile strength of the polyisoprene were realized by utilizing the modification procedure of this invention. For instance, in Example 3 a 50% modulus of 5.0 MPa and a 100% modulus of 9.1 MPa was realized. The rubber compositions made also had very high tensile strength. For instance, the tensile strength of the rubber composition prepared in Example 3 was 16.8 MPa. The rubber compositions made possessed a greater bending modulus and increased stretching modulus at low elongation. While certain representative embodiments and details have been shown for the purpose of illustrating the subject invention, it will be apparent to those skilled in this art that various changes and modifications can be made therein without departing from the scope of the subject invention.

Claims: A process for preparing a rubber composition having a high modulus which is characterized by reacting from 0.1 phr to 20 phr at least one dithio diacid having the general structural formula: HOOC-A-S-S-A-COOH wherein A represents an alkylene group containing from 1 to 6 carbon atoms with at least one polydiene rubber selected from the group consisting of polybutadiene, styrene-butadiene rubber, synthetic polyisoprene, natural rubber, isoprene-butadiene rubber, isoprene-butadiene-styrene rubber, nitrile rubber, carboxylated nitrile rubber and EPDM rubber (ethylene-propylene-diene monomer rubber) and at least one nylon having a melting point which is within the range of 150°C to 255°C, at a temperature which is above the melting point of the nylon. A process as specified in claim 1 which is characterized by being conducted at a temperature which is within the range of 150°C to 300°C. A process as specified in claim 2 characterized in that said process is carried out at a temperature which is within the range of 165°C to 255°C. A process as specified in claim 1 characterized in that said process is carried out at a temperature which is within the range of 180°C to 200°C. A process as specified in claim 1 which is characterized by being carried out by reacting the dithio diacid with the nylon to form a modified nylon containing mercaptan groups; and subsequently reacting the modified nylon containing mercaptan groups with the polydiene rubber. A process as specified in claim 5 characterized in that the dithio diacid is reacted with the nylon at a temperature which is within the range of about 150°C to about 300°C, wherein the modified nylon containing mercaptan groups are reacted with the polydiene rubber at a temperature which is within the range of 120°C to 250°C. A process as specified in claim 1, 5 or 6 characterized in that the dithio diacid is dithio dipropionic acid, wherein 0.5 phr to 3 phr of the dithio dipropionic acid is utilized. A process as specified in any of the preceding claims characterized in that the nylon is selected from the group consisting of nylon-6,6, nylon-6, nylon-7, nylon-8, nylon-9, nylon-10, nylon-11, nylon-12, and nylon-6,12. A process as specified in any of the preceding claims characterized in that the nylon is nylon-12. A rubber composition which is characterized by being made by the process specified in any of the preceding claims.

Inventors: BAUER RICHARD GEORGE, PYKE JAMES BOLTON, BAUER, RICHARD GEORGE, PYKE, JAMES BOLTON
Applicants: GOODYEAR TIRE & RUBBER, THE GOODYEAR TIRE & RUBBER COMPANY
Application year: 1989
Main classification: C08G81
IPC codes: C08G81