POLYMER COMPOSITION OF A POLYESTER COPOLYMER & POLYVINYL CHLORIDE

Abstract: A thermodynamically miscible polymer composition of polyvinyl chloride and a copolymer of an aromatic dicarboxylic acid and a mixture of 2-methyl-1,3-propanediol and at least one linear alkylene C₂ to C₆ diol.

Description: This invention relates to polymer compositions. In one of its more specific aspects, this invention relates to a thermodynamically miscible polymer composition of thermoplastic polyester copolymer and polyvinyl chloride (PVC). The polymer compositions of this invention have been found to exhibit thermodynamic miscibility; that is, they exhibit a single continuous phase and a single glass transition temperature value. The miscibility of polymers is generally determined using differential scanning calorimetry to measure glass transition temperature. A thermodynamically miscible polymer composition will exhibit a single well-defined glass transition temperature value which typically lies intermedi­ ate between the glass transition temperatures of the indivi­ dual polymeric components. Accordingly, as used herein, the phrase "thermodynamically miscible" is used to define two or more polymers which when combined with one another result in a composition which exhibits a single continuous phase and a single, well-defined glass transition temperature value. According to this invention, there is provided a polymer composition comprising (A) a polyester copolymer comprising the reaction product of at least one C₂ to C₆ linear alkylene diol monomer, at least one aromatic diacid derivative and, 2 methyl-1,3-propanediol and (B) polyvinyl chloride, wherein (A) and (B) are thermodynamically miscible with one another such that the polymer composition exhibits a a single glass transition temperature value. Also according to this invention, there is provided a method of producing a molded polymer composition which comprises forming a polymer composition comprising (A) a polyester copolymer comprising the reaction product of at least one C₂ to C₆ linear alkylene diol monomer, at least one aromatic diacid derivative and 2-methyl-1,3-propanediol and (B) polyvinyl chloride, and molding the resulting composition. According to this invention, there is also provided a molded composition comprising a single continuous phase, the single continuous phase being a polymer composition comprising (A) a polyester copolymer comprising the reaction product of at least one C₂ to C₆ linear alkylene diol monomer, at least one aromatic diacid derivative and, 2-methyl-1,3-propanediol and, (B) polyvinyl chloride. The polymer composition of this invention exhibits thermodynamic miscibility at all blended ratios of polyester copolymer (A) to PVC (B). Typically, the polymer composition will comprise from about 1 to about 99 weight percent of copolymer (A) and 99 to about 1 weight percent of PVC (B). Suitable C₂ to C₆ linear alkylene diols for use in the preparation of copolymer (A) are 1,4-butanediol, 1,3-­ propanediol, ethylene glycol, 1,5-pentanediol and 1,6-hexane­ diol and the like and their mixtures. The preferred linear alkylene diol is 1,4-butanediol. Suitable aromatic diacid derivatives for use in the preparation of copolymer (A) are dimethyl terephthalate, dimethyl isophthalate, dimethyl ester of 1,8-napthalene dicarboxylic acid, dimethyl ester of 2,7-naphthalate di­ carboxlic acid, and the like, and their mixtures. The preferred aromatic diacid derivative is dimethyl terephthalate. The 2-methyl-1,3-propanediol is commercially available. Moreover, methods for its preparation are well known; see, for example, U.S. Pat. 4,096,192. Polyester copolymer (A) can be prepared using any suitable method of polymerization. The preferred method is polycondensation polymerization using about 50 mole % of the aromatic diacid derivative and about a combined total of about 50 mole % of 2-methyl-­ 1,3-propanediol and C₂ to C₆ linear alkylene diol or diols. As is typical in the preparation of polyesters, the diol is employed in a slight excess above 50 mole %. The mole ratio of 2-methyl-1,3-propanediol to C₂ to C₆ linear alkylene diol will be from about 20 to 80 mole % 2-methyl-1,3-propanediol to about 80 to 20 mole % C₂ to C₆ linear alkylene diol in the final polyester copolymer. The preferred mole ratio of 2-methyl-1,3-propanediol to linear alkylene diol in the final copolymer will be within the range of from about 70 to 30 to about 30 to 70. The polymer compositions of this invention can be prepared using any suitable blending method such as, for example, melt mixing as demonstrated in the following ex­ amples. All glass transition temperature values were determined by differential scanning calorimetry (DSC). Example 1 This example demonstrates the preparation of a thermoplastic polyester copolymer (A) suitable for use in the invention. About 2.56 moles of 1,4-butanediol, about 2.56 moles of 2-methyl-1,3-propanediol, and about 1.586 moles of dimethyl terephthalate were changed into a one-liter zipper­ clave reactor equipped with a double helical ribbon-type stirring blade. After the reactor was sealed and purged three times with nitrogen, about 1.01 grams of tetrabutoxy titanium catalyst were added through the vacuum port of the reactor. The reactor contents were heated for about four hours - about one hour at 180°C and then at 230°C for about three hours. The heating was carried out under a nitrogen stream and at atmospheric pressure. Methanol which formed was distilled off. After the methanol was distilled off, the reactor contents were heated to and held at 250°C for about two hours while the system was evacuated to 0.2mm Hg using dual vacuum pumps. The resulting product was recovered and identified as a polyester copolymer of the monomers charged. The copolymer was found to have a glass transition temperature value of 44.8°C and was transparent. The copolymer has no detectable melting point. The mole ratio of 2-methyl-1,3-­ propanediol to 1,4-butanediol in the copolymer was found to be 56:44. Examples 2 and 3 Following substantially the procedure of Example 1, two additional polyester copolymers were prepared using different starting mole ratios of 2-methyl-1,3-propanediol to 1,4-butanediol. The starting and final polymer mole ratios and the properties of the copolymers of Examples 1-3 are set forth in following Table 1. Example 4 The example demonstrates the preparation of a polymer composition of this invention. About 50 parts by weight of the polyester copolymer produced in Example 1 and about 50 parts by weight of polyvinyl chloride (Borden Chemical PVC, 0.80 inherent viscosity, Tg = 85°C) were melt blended in a Brabender mixer for about five minutes at 160°C and 60 rpm. The resultant polymer composition was found to possess a single glass transition temperature valve of 68.7°C. Examples 5, 6 and 7 Following the procedure of Example 4, three more polymer compositions of the invention were separately prepared using the copolymer prepared in Example 1 and the same Borden Chemical PVC. The compositions (Examples 5, 6 and 7) and their glass transition temperatures are shown in Table II. Examples 8, 9 and 10 Using the procedure of Example 4, the copolymer of Example 1, and GEON® 7082 polyvinyl chloride, (B.F. Goodrich Company) three more polymer compositions of this invention were prepared. The compositions (Examples 8, 9 and 10) and their glass transition temperatures are shown in following Table III. The data of Tables II and III show that the polymer compositions of this invention which incorporate a polyester copolymer and PVC are thermodynamically miscible as evidenced by their single glass transition temperature values. It will be evident from the foregoing that various modifications can be made to this invention. Such, however, are considered as being within the scope of the invention.

Claims: 1. A polymer composition comprising: (A) a polyester copolymer comprising the reaction product of at least one C₂ to C₆ linear alkylene diol, at least one aromatic diacid derivative and 2-methyl-1,3-propanediol and, (B) polyvinyl chloride, wherein (A) and (B) are thermodynamically miscible with one another and the polymer composition exhibits a single glass transition temperature value. 2. A polymer composition as claimed in claim 1 in which (A) is produced by polycondensation polymerisation. 3. A polymer composition as claimed in claim 1 or claim 2 in which (A) is produced from about 50 mole % of said at least one aromatic diacid derivative and a combined total of about 50 mole % of said 2-methyl-1,3-­ propanediol and said at least one C₂ to C₆ linear alkylene diol. 4. A polymer composition as claimed in any one of claims 1 to 3 in which the ratio of 2-methyl-1,3-propanediol to said at least one C₂ to C₆ linear alkylene diol is within the range of from about 80 to 20 to about 20 to 80 in the final copolymer. 5. A polymer composition as claimed in claim 4 in which the ratio of 2-methyl-1,3-propanediol to said at least one C₂ to C₆ linear alkylene diol is within the range of from about 70 to 30 to about 30 to 70 in the final copolymer. 6. A polymer composition as claimed in any one of claims 1 to 5 in which said C₂ to C₆ linear alkylene diol is selected from 1,4-butanediol, 1,3-propanediol, ethylene glycol, 1,5-pentanediol, 1,6-hexanediol and mixtures of two or more thereof. 7. A polymer composition as claimed in any one of claims 1 to 6 in which said aromatic diacid derivative is selected from dimethyl terephthalate, dimethyl isophthalate, the dimethyl ester of 1,8-naphthalene dicarboxylic acid, the dimethyl ester of 2,7-naphthalene dicarboxylic acid, and mixtures or two or more thereof. 8. A polymer composition as claimed in any one of claims 1 to 7 comprising in weight percent from about 1 to about 99 of (A) and from about 99 to about 1 of (B). 9. A polymer composition as claimed in any one of claims 1 to 8 which has been prepared by melt mixing (A) and (B). 10. A method of producing a molded polymer composition which comprises forming a polymer composition as claimed in any one of claims 1 to 9, and molding the resulting composition. 11. A molded composition comprising a single continuous phase, the single continuous phase being a polymer composition as claimed in any one of claims 1 to 9.

Inventors: LE-KHAC, BI
Applicants: ARCO CHEMICAL TECHNOLOGY INC.
Application year: 1986
Main classification: C08L67
IPC codes: C08L67, C08L1, C08L27