PREPARATION OF HIGHLY ELASTOMERIC ETHYLENE-ACRYLIC ESTER COPOLYMERS

Abstract: A process for modifying ethylene-acrylic ester copolym­ ers with sulfonyl chloride and/or chlorine containing modify­ ing agents to produce elastomers by treating granular ethylene copolymer containing 2 to 20 weight % acrylic ester comonomer having a modulus of at least 2000 psi with such modifying agents in a gas phase process.

Description: PREPARATION OF HIGHLY ELASTOMERIC ETHYLENE-ACRYLIC ESTER COPOLYMERS This invention relates to a process for modifying ethylene-acrylic ester copolymers to make elastomeric products therefrom in a gas phase process. More particularly, this invention relates to a gas phase process for producing elastomers from ethylene-acrylic ester copolymers which will contain carbon-chlorine bonds. and. optionally. carbon SO2Cl bonds. High pressure ethylene-acrylic ester copolymers have been treated with chlorination and other modifying agents in aqueous or solvent slurry or solution processes to provide products having improved mechanical and chemical properties. See in this regard for example. U.S. Patents 2.405.971 and 3.960,821. These chlorination type processes. however0 suffer the obvious disadvantages involved in the use of solvents. i.e., the need to completely remove the solvents from the products. and usually under vacuum and/or elevated temperature conditions. These chlorination type processes may also require the use of elevated temperatures and/or the use of relatively large sized reactors, to accommodate the volume of solvent employed. U.S. Patents 3,770,706 and 4.220.739 disclose the surface sulfonation of various ethylene copolymers with relatively low amounts of modifying agents. U.S. Patent 4,029,862 discloses the treatment of certain highly crystalline ethylene hydrocarbon polymers in a gas phase fluidized bed process with gaseous chlorine. The data disclosed in the examples of this patent indicate that the products produced by the process of this patent are also highly crystalline materials. and that. by extrapolation apparently, as noted in Figure 17. in order to obtain a level of crystallinity of below about 20% according to the teachings of this patent it would be necessary to add over about 55t by weight of chlorine to the ethylene polymers disclosed therein. None of such prior art procedures. however. disclose a solventless gas phase process for producing elastomeric ethylene-acrylic ester copolymers, i.e.. those having a crystallinity of less than 10% and a modulus, at 25eC of less than 2000 psi. An object of the present invention is to provide a simple one-step process whereby elastomeric ethylene-acrylic ester copolymers containing relatively low amounts of sulfonyl chloride and/or chlorine can be readily prepared from particulate ethylene-acrylic ester copolymers with a minimum of reactants and under relatively mild reaction conditions. A further object of the present invention is to provide a simple one-step process whereby elastomeric ethylene-acrylic ester copolymers containing a relatively low amount of modifying agents such as chlorine can be prepared from particulate ethylene-acrylic ester copolymers with a variety of treating agents. A still further object of the present invention is to provide a process whereby elastomeric sulfonyl chloride and/or chlorine containing ethylene-acrylic ester copolymers can be readily prepared without the need for post treating such polymers to remove solvent or catalyst residues therefrom. It has now been found that the objects of the present invention can be readily obtained if certain particulate copolymers of ethylene and acrylic esters are treated with certain chlorine containing modifying agents in a low pressure gas phase process as detailed below. Crystalline Ethylene CoPolymers The ethylene-acrylic ester copolymers which are to be used in the process of the present invention are particulate materials formed from about 50 to 99. and preferably about 80 to 98. weight of ethylene and from about 1 to 50. and preferably about 2 to 20. weight t of one or more acrylic esters such as methyl acrylate, ethyl acrylate. butyl acrylate. aethyl methacrylate. ethyl methacrylate. and the like. These polymers have a modulus value of about 2,000 to 20,000. and preferably of about 3.000 to 15.000, psi and a crystallinity of about 30 to 60, and preferably of about 20 to 40%. For use in the process of the present invention they should be in granular form. i.e., having a particle size in the range of about 150 to 1,000 microns. with the average particle size being about 700 + 100 microns. PROCESS The process of the present invention is a simple one-step process which is conducted in the gas phase in the absence of solvents or liquid diluents. The preferred of such gas phase processes are the fluidized or agitated bed type processes. The process is conducted by treating or reacting the granular ethylene copolymers with a modifying agent which is adapted to being in the gaseous state under the operating conditions employed until the desired degree of treatment is achieved. The desired level of treatment is that which will cause sufficient amounts of the modifying agent to react with the ethylene copolymer as to result in the lowering of the crystallinity of such polymer to the level of less than 10%. and preferably. of the order of O to 4%. The modifying agents cause a lowering of the crystallinity. and thus of the modulus. of the starting polymer it is believed. by randomly replacing hydrogen atoms on the polymeric backbones with more bulky groups. C1 and 6O2Cl. The time required for this to occur will vary from about 3 to 10 hours depending. in part. on the particular modifying agent and/or ethylene copolymer employed and the copolymer's particle size. Thus, the lower the crystallinity, and the smaller the particle size of the copolymer. the faster will the modification process proceed. The temperature to be used is in the range of about 50 to 1000C and the pressure to be used is in the range of from atmospheric pressure up to about 1000 psi. The pressure should also be one at which none of the reactants or by-products will condense under the overall reaction condition scheme. The higher the pressure and temperature, the shorter will be the reaction time. if all the other conditions are the same. The modifying agents that may be used would include: for chlorination: C12 for chlorosulfonation: SO2Cl2 or S02 plus C12 The process can be conducted without an initiator. If the use of an initiator is desired the preferred initiator is a azobisisobutyronitrile. As a result of the chlorination treatment, the chlorinated polymers vill contain carbon-chlorine bonds randomly distributed throughout the backbone of the polymer. In such products the chlorine concentration will range between 5 to 55 weight , and preferably between 15 to 30 weight 8. As a result of the chlorosulfonation treatment, the backbone of the chlorosulfonated polymers will contain randomly distributed carbon-chlorine bonds and carbon-So2Cl bonds. In the chlorosulfonated polymers. the total chlorine concentration will range from about 5 to 55 weight 8, and preferably from about 15 to 30 weight 8, and the sulfur content will range from about 0.1 to 10 weight 8. and preferably from about0.5 to 5 weight 8. D-14007 The amount of the gaseous modifying agent to be used in the reactor relative to the amounts of the granular copolymers to be treated therewith is about 10 to 200, and preferably of about 20 to 100, weight %. When S02 and C12 are used as the modifying agent the molar ratio of C12 to S02 to be used is about 5:1 to 10:1 and preferably about 5:1. About 10 to 50 volume % of an inert gas such as nitrogen may be used in conjunction with the gaseous modifying agent. It has been found that after the modified. elastomeric copolymers are made in the process of the present invention it is much easier to remove any residual unreacted materials such as monomer or modifying agent. or HC1 by-product. from the copolymer by merely flushing them out with an inert gas such as nitrogen. Since there are no components of the reaction system. other than monomer. modifying agent(s). HC1 by-product. and. optionally, inert gas, used in the process of the present invention. such as solvents. diluents, swelling agents. fluidizing agents. or catalysts. there is no need to expend any efforts to remove any materials of these latter types from the elastomeric product. The properties of the copolymers discussed herein were determined by the following test methods: Crystallinity Heasured by Differential Scanning Calorimeter (DSC) using a DuPont-990 analyzer with pressure DSC cell Tensile Modulus (psi) 1t secant modulus a film 4n x4 x 0.020 is compression molded at 130-150eC. and its modulus is measured according to ASTM-63S. Tensile Strength (psi) A similar film, prepared as described above for tensile modulus. is tested according to ASTM-638. s Elongation at Break A similar film, prepared as described above for tensile modulus and tensile strength, is elevated according to ASTh-638. The following Examples are provided to illustrate the process of the present intention and are not intended as a limitation upon the scope thereof. The ethylene-acrylic ester copolymer used in the examples was a copolymer of 82 weight % ethylene and 18 weight % ethyl acrylate made with a free radical initiator under high pressure conditions. This copolymer was 32% crystalline, had a tensile modulus of 5,560 psi, a tensile strength of 2,300 psi, an elongation of 919S and was in the form of particles having an average particle size of 500 microns. APParatus/Process The ethylene ethyl acrylate copolymers were chlorinated or chlorosulfonated in a two liter glass-lined stainless steel or Hastelloy (55Ni, 17Mo. 16Cr, 6Fe. 4W) reactor equipped with a thermocouple thermometer and a motor activated U shaped Hastelloy stirrer. ,. A Hastelloy dip tube (-2 cm in diameter) was used to feed the gaseous modifying agent(s) into the reactor. Unreacted modifying agent and HC1 were vented to a collection trap containing 25\ aqueous NaOh. The gaseous modifying agents were fed at the rate of 10 to 12 grams C12 per hour and 2-3g SO2/hour under a pressure of about 15 to 450 psi. The polymer to be treated. about 100 to 200 grams. was charged to the reactor and heated therein by an external heater. No catalysts were used in any of these experiments. After the polymer was added to the reactor and heated to the desired reaction temperature the resin was agitated by the stirrer and the gaseous modifying agent(s) were fed in. During the course of the modifying process samples of the modified resin were taken from the reactor to test for S and and/or C1 content. and % crystallinity. When the modification process had proceeded to the point where the crystallinity of the resin had reached less than about 10t the flow of gaseous modifying agent(s) was terminated and the product was alloved to cool in the reactor while being purged with nitrogen to remove S02 and/or C1 and HC1. 2 Example 1 In this example the ethylene-ethyl acrylate (EEA) copolymer was chlorinated at -700C for up to -10 hours. until it acquired a chlorine content of 21 weight %. The properties of the starting material. and of an intermediate product. and of the final product vere as follovs: Table 1 Properties of Chlorinated EEA Resin: Starting Intermediate Final Material Product Cl. H O 10 21 Crystallinity. 8 32 15 6 Tensile modulus. psi 5.560 3.020 1.800 HPa 38.4 20.8 12.4 Tensile strength psi 2,300 1.410 900 Mpa 15.8 9.7 6.2 Elongation. t 919 483 287 MPa = Mega Pascal The data of this Example 1 indicates that ethylene ethyl acrylate copolymer can be easily chlorinated, in accordance with the present invention. to give elastomeric products having a crystallinity below 10%. and a modulus of less than 2000 psi. ExamPle 2 In this example a series of five different chlorosulfonated products were made from five different batches of the same starting copolymer. In each case the copolymer was chlorosulfonated at 60-700C for about 6-10 hours. The properties of the starting material and of each of the final products were as follows: Properties of Chlorosulfonated EEA Resin: Starting Final Product Material 1 2 3 4 5 Properties: Cl. % 0 16 24 28 29 30 S, % 0 0.85 0.45 0.15 0.9 2.2 Crystallinity, % 32 6 < 10 5.4 3 5 Tensile Modulus at - 25 , psi 5,560 1,810 1,350 1,100 885 900 MPs 38.4 12.5 9.3 7.6 6.1 6.2 Tensile Strength, psi 2,300 1,360 1,300 830 850 1,210 15.9 9.4 9.0 5.7 5.9 8.3 Elongation, % 919 742 660 340 527 694 The data of this Example 2 shows that ethylene ethyl acrylate copolymers can be easily chlorosulfonated, according to the present invention. to produce elastomeric products with module less than 2000 psi and crystallinity less than 10%. Example 3 The elastomeric products produced by the process of the present invention have a wide variety of uses because of their flexibility, chemical resistance and flame retardancy. They may be used. for example. as wire and cable insulation and as plasticizers for polyvinyl chloride resins. A chlorinated ethylene-ethyl acrylate copolymer. made by the process of the present invention was used as the base resin in a cured wire and cable jacket formulation. The chlorinated ethylene-ethyl acrylate copolymer was formed from a starting resin which contained 82 weight t ethylene and 18 weight % ethyl acrylate and was 32 s crystalline and had a modulus of 5560 psi. The chlorinated material contained 21 weight t chlorine. had a 38 crystallinity and had a modulus value of - 900 psi. The wire and cable jacket formulation was as follows: PPW 79.4 chlorinated ethylene-ethyl acrylate copolymers zp,o CaC03 (filler) 0.6 Azerite MA (Stabilizer) 100.0 The formulation was then cured according to the procedure described in the Example of U.S. 4.328.323 using silane to produce a cured product having the following properties: : Tensile strength, psi 1350 Elongation, t 400 Tensile modulus. psi at 230C 700 at 900C 180 at 2500C 230 Flammability (ASTM-D 2863-70) Limiting oxygen index (LOI) 31 Smoke 10 Ash 12 The data of this Example 3 shovs that formulated products made from chlorinated copolymers prepared according to the process of the present invention have utility in the vire and cable area. Such formulated products have excellent room temperature flexibility. which is retained at elevated temperatures. Furthermore, such formulated products also have good flame retardent properties.

Claims: CLAIMS 1. A process for modifying ethylene-acrylic ester copolymer to produce elastomers therefrom which comprises treating granular ethylene-acrylic ester copolymer containing about 50 to 99 weight % ethylene and about 1 to 50 weight % of at least one acrylic ester and having modulus of at least 2000 psi in a gas phase process with at least one chlorine containing modifying agent selected from chlorinating and chlorosulfonating agents said agent being adaptable to being in the gas phase during said process, until sufficient amounts of said agents are reacted with said copolymer as to lower its crystallinity to no more than about 10%. 2. A process as in claim 1 wherein said polymer is treated with a chlorinating agent. 3. A process as in claim 2 wherein said polymer is treated with sufficient amounts of chlorinating agent as to produce a polymer containing about 5 to 55 weight % of chlorine. 4. A process as in claim 1 wherein said polymer is treated with a chlorosulfonating agent. 5. A process as in claim 4 wherein said polymer is reacted with sufficient amounts of chlorosulfonating agent as to produce a polymer containing about 5 to 55 weight % of chlorine, and about 0.1 to 10 weight % of sulfur. 6. A process as in any of claims 1 to 5 wherein said copolymer is a copolymer of ethylene and at least one acrylic ester selected from methyl acrylate, ethyl acrylate, butyl acrylate, methyl methacrylate and ethyl methacrylate. 7. A process as in claim 6 wherein said acrylic ester is ethyl acrylate. 8. Chlorosulfonated ethylene-acrylic ester copolymer containing about 5 to 55 weight % of chlorine and about 0.1 to 10 weight % of sulfur, and having a modulus of less than about 2000 psi, at 25 C, and being less than 10% crystalline. 9. Chlorosulfonated ethylene-ethyl acrylate copolymer as in claim 8. 10. A product obtainable by the process of any of claims 1 to 7.

Inventors: RIFI, MAHMOUD RASHAD
Applicants: UNION CARBIDE CORPORATION
Application year: 1984
Main classification: C08F8
IPC codes: C08F8