POLYALKYLENE ETHERS AS PLASTICIZERS AND FLOW AIDS IN POLY(1,4-CYCLOHEXANEDIMETHYLENE TEREPHTHALATE) RESINS

Abstract: This invention relates to a polyester composition comprising a blend of: (A) 99.5 to 75 weight % of a copolyester having an inherent viscosity of 0.1 to 1.2 dL/g and having a melting point in excess of 250 DEG C, comprising: (a) one or more dicarboxylic acids, and (b) a glycol component comprising at least 80 mole % 1,4-cyclohexanedimethanol; and (B) 0.5 to 25 weight % of one or more polyalkylene ethers, wherein the weight percentages of all components in said blend total 100 weight %.

Description: POLYALKYLENE ETHERS AS PLASTICIZERS AND FLOW AIDS IN POLY(l,4-CYCLOHEXANEDIMETHYLENE TEREPHTHALATE) RESINS Field of the Invention This invention concerns blends of a poly(1,4— cyclohexanedimethylene terephthalate) (PCT) resin with one or more polyalkylene ethers. Background of the Invention Melt viscosity and crystallization rate as a function of temperature are often critical to the process of injection molding semicrystalline engineering thermoplastics. The melt viscosity is critical in that it governs the mold fill of the part (lower melt viscosity leads to faster mold fill and the ability to fill smaller parts) and therefore it is desirable to minimize this important parameter. The crystallization rate as a function of temperature is critical in that it controls the optimum mold temperature and cycle time of the process. It is desirable to operate at mold temperatures of less than 110°C since this allows for the use of traditional water heated, as opposed to oil heated molds. It is also economically desirable to operate at such a temperature as to allow for the optimum crystallization rate as this translates into shorter cycle times. The use of a plasticizer is generally known for some polyesters to enhance both of these critical parameters. Polyalkylene ethers are known plasticizers for low melting polyesters such as poly(butylene terephthalate) (PBT) and poly(ethylene terephthalate) (PET) , but are known to be sensitive to thermal degradation. Polyalkylene ethers are reported to degrade when temperatures exceed 250°C, as stated by W. K. Witsiepe (Adv. Chem. Ser., No. 129, 39-60, 1973). A plasticizer will typically decrease the melt viscosity and depress the glass transition temperature of the thermoplastic which in turn allows for a faster crystallization rate at a lower temperature. Common plasticizers for polyester engineering plastics are low molecular weight organic esters such as neopentylglycoldibenzoate (Benzoflex S312) and dipropyleneglycoldibenzoate (Benzoflex 9—88) . The use of plasticizers in semicrystalline engineering polymers to improve moldability is well known to the art. Furthermore the need for and use of improved plasticizers for semicrystalline polyesters is well known to the art. Polyalkyleneethers have been used as plasticizers for low melting polyesters such as PBT and PET, but are known to be sensitive to thermal degradation. In fact, United States Patents 4,548,978 to Garrison, Jr., 5,028,647 to Haylock et al, 4,914,145 to Tohdon et al, 4,558,085 to Lee, and 5,004,817 to Bastioli et al and JP Patent 1,256,562 to Hara et al teach the use of polyalkylene oxides such as polyethylene glycol as plasticizers in polyethylene terephthalate. However, E. A. Flex an reports in Adv. Chem. Ser. , 233 (Toughened Plastics I), 79-104, 1993 that many additives utilized to improve the properties of low melting polyesters, such as PBT, are not useful in higher melting polyesters because the significantly higher processing temperatures required degrade the additives. Polyalkylene ethers degrade when temperatures exceed 250°C, as reported by W. K. Witsiepe (Adv. Chem. Ser., No. 129, 39-60, 1973) . In fact, the flash point of polyethylene glycol is reported to be 243°C, attesting to its poor thermal stability. Polytetramethylene glycol, when exposed to high temperatures, undergoes a degradation reaction. Therefore, it would be expectsd that polyalkylene ethers would not be useful as plasticizers for semicrystalline polymers with melting points in excess of 250°C. It is reported by Witsiepe (Adv. Chem. Ser., No. 129, 39-60, 1973) that the optimum reaction temperature for polyether esters is 250°C because above this temperature degradation of the polyalkylene ether occurs. In United States Patent 4,438,233 discloses the practice of "end—capping" the polyalkylene ether to increase the thermal stability so that it can be processed at higher temperatures but not exceeding 200°C. United States Patents 3,763,109 to Witsiepe and 3,856,749 to Hoeschele both describe methods of stabilizing polyalkylene ethers to high heat aging. These patents teach the necessity of added stabilizers to provide the polyalkylene ethers enough thermal stability to withstand temperatures of up to 170°C. Furthermore, United States Patent 4,541,884 to Cogswell teaches the necessity for the plasticizer to be melt εtable at least to the processing temperature of the matrix polymer. United States Patent 5,389,710 is of interest which discloses a polyester composition comprising a polyester such aε PCT or PET and an effective amount of a certain type of α, ω-bis(aminoalkyl)—polyoxyalkylene crystallization modifier which is required to chemically react with the PCT or PET composition. These modifiers require an amine group. Summary of the Invention This invention relates to a polyester composition comprising a blend of: (A) 99.5 to 75 weight % of a copolyester having an inherent viscosity of 0.1 to 1.2 dL/g and having a melting point in excess of 250°C, comprising: (a) one or more dicarboxylic acids, and (b) a glycol component comprising at least 80 mole % 1,4—cyclohexanedimethanol; and (B) 0.5 to 25 weight % of one or more polyalkylene ethers, wherein the weight percentages of all components in the blend total 100 weight %. The blend of the one or more polyalkylene ethers with the copolyester useful in the invention results in a decrease in melt viscosity and in glass transition temperature of the copolyester. It is unexpected that polyalkylene ethers would cause these resultε for semicrystalline polymers with melting points in excess of 250°C such as the copolyesters of the invention. Detailed Description of the Preferred Embodiments Poly(1,4—cyclohexanedimethylene terephthalate) (PCT) resins require a significantly higher processing temperature than PET resinε and a much higher proceεεing temperature than PBT reεinε due to itε high melting point (295°C) . This high melting point of PCT therefore requires processing temperatures in excess of 300°C which would be expected to degrade said polyalkylene ethers. However, thiε invention demonstrates the polyalkylene ethers of the invention decrease the melt viscosity of the polymer matrix and depress the glass transition temperature thus improving the processability of PCT without degrading the mechanical properties. The addition of such polyalkylene ethers decreases the melt viscosity of the PCT composition alone or when the PCT resin is reinforced with glass fibers. Since the plasticizers depress the glass tranεition temperature of PCT thuε increaεing cryεtallization rate, it alεo allows for the use of mold temperatureε <lio°C. While not being bound by any theory, theεe observations suggest that, when blended with PCT, the polyalkylene ethers exhibit an unexpected improvement in thermal stability allowing them to survive the high processing temperatures. More particularly, thiε invention relateε to a polyester composition comprising a blend of: (A) 99.5 to 75, preferably 99.5 to 85, more preferably, 99 to 90, and even more preferably, 97 to 93 weight % of a copolyester having an inherent viscosity of 0.1 to 1.2 dL/g, and having a melting point in excesε of 250°C, comprising: (a) one or more dicarboxylic acids, and (b) a glycol component comprising at least 80, preferably at least 90, more preferably at least 95 mole % 1,4— cyclohexanedimethanol; and (B) 0.5 to 25 weight % of one or more polyalkylene ethers, wherein the weight percentages of all components in said polyester composition equal 100 weight % . It is preferable that the dicarboxylic acid component comprise at least 90, preferably 95 mole % terephthalic acid. In this case, it is preferable that the dicarboxylic acid component of the copolyester may comprise repeat units of from 10 mole % or less of one or more other dicarboxylic acids besides terephthalic acid, or suitable synthetic equivalents such as dimethyl terephthalate. Dicarboxylic acids useful in the dicarboxyic acid component of the invention include, but are not limited to aromatic dicarboxylic acids preferably having 8 to 14 carbon atoms, aliphatic dicarboxylic acids preferacly having 4 to 12 carbon atoms, or cycloaliphatic dicarboxylic acids preferably having 8 to 12 carbon atoms. Particularly preferred examples of dicarboxylic acids other than terephthalic acid to be used in forming the copolyester of the invention include: isophthalic acid, naphthalene— 2,6—dicarboxylic acid, 1,4— cyclohexanedicarboxylic acid, 1,4—cyclohexanediacetic acid, diphenyl—4,4'—dicarboxylic acid, succinic acid, glutaric acid, adipic acid, azelaic acid, sebacic acid, and the like. Of these dicarboxylic acids to be included with terephthalic acid, isophthalic acid is preferred. Copolyesters may be prepared from one or more of the above dicarboxylic acids. It εhould be underεtood that the dicarboxylic acid can ariεe from the corresponding acid anhydrides, eεters, and acid chlorides of these acids. The glycol component may comprise up to 20 mole %, preferably up to 10 mole %, of one or more other aliphatic or alicyclic glycols. Such additional diols include cycloaliphatic diols preferably having 6 to 20 carbon atoms or aliphatic diols preferably having 2 to 20 carbon atoms. Examples of such diols are: ethylene glycol, diethylene glycol, triethylene glycol, propane—1, 3—diol, butane—1, 4—diol, pentane-1,5— iol, hexane—1,6—diol, 3—methylpentanediol- (2,4) , 2-methylpentanediol-(1,4), 2,2,4- trimethylpentane—diol—(1,3) , 2-ethylhexanediol-(1,3) , 2 , 2-diethylpropane-diol-(l,3) , hexanediol-(l, 3) , 1,4—di— (hydroxyethoxy)-benzene, 2,2-bis-(4-hydroxycyclohexyl)- propane, 2 , 4-dihydroxy-l, 1, 3 , 3-tetramethyl-cyclobutane, 2 ,2-bis-(3-hydroxyethoxyphenyl)—propane, decalin diol and 2 ,2—bis—(4—hydroxypropoxypheny1)—propane. Copolyesters may be prepared from two or more of the above diols. Ethylene glycol is a preferred glycol. The copolyester resins useful in the blend of this invention are well known and are commercially available. Methods for their preparation are described, for example, in United States Patents 2,465,319 and 3,047,539. The polyesterε of the invention preferably have an inherent viεcosity of 0.1 to 1.2 dL/g, more preferably 0.1 to 0.9 dL/g, and even more preferably, 0.4 to 0.8 dL/g. Copolyesters containing substantially only ethylene glycol, 1,4—cyclohexanedimethanol and terephthalic acid or subεtantially only ethylene glycol, 1,4— cyclohexanedimethanol, iεophthalic and terephthalic acid are preferred. It iε particularly preferred that the copolyeεter uεeful herein have a melting point in excess of 250°C, preferably in excesε of 260°C. Theεe polyalkylene glycols can either be end-capped or not. By end—capped, we mean the polymer is preferably end-capped by reacting the terminal hydroxyl groups with epoxy, isocyanate or carboxylic acid compounds. Preferred polyalkylene ethers contemplated for use in the invention comprise compounds of the formula: wherein, m is an integer from 1 to 3 , inclusive, n is an integer from 4 to 250 inclusive, X is selected from one or more of the group consiεting of CH 3 , C 3 H 7 , C 2 H 5 , and H, A iε hydrogen, alkyl, acyl, aryl or aroyl of 1 to 10 carbon atomε, and B iε hydrogen, alkyl, acyl, aryl or aroyl of 1 to 10 carbon atoms. Preferred polyalkylene ethers for use in the compositions of the present invention are those described above where m is one, or where n is 4 to 14 , or where X iε H. More preferably, iε one, n is 4 to 14, and X is H. Even more preferred plasticizers for use in the compositions of the present invention are those described above where m is one, or where n is 7 to 25, or where A is acyl of 8 carbon atoms or methyl, or where B is acyl of 8 carbon atoms, and especially where m is one, n is 7 to 25, X is H, A is acyl of 8 carbon atoms or methyl, and B is acyl of 8 carbon atoms. Polyethylene glycol 400 bis(2— ethylhexanoate) , methoxy polyethylene glycol 550 2- ethylhexanoate and tetraethylene glycol bis(2— ethylhexanoate) are especially preferred. Polyethylene glycol 400 biε(2—ethylhexanoate) is even more preferred. The polyalkylene ethers even more useful in the invention are preferably selected from the group consisting of polyethylene glycol, polytetramethylene glycol, and polypropylene glycol or mixtures thereof. The actual molecular weight of the poly(alkylene glycol) iε not critical, however it iε preferred that it be of sufficient molecular weight as to prevent volatilization during compounding. It is preferred that the polyalkylene etherε have a number average molecular weight of from 200 to 10,000, preferably 400 to 1,500. Theεe polyalkylene glycolε can either be end—capped or not. By end—capped, we mean the polymer is preferably end—capped by reacting the terminal hydroxyl groups with epoxy, isocyanate or carboxylic acid compounds. It is understood that other additives such as stabilizerε, flame retardantε, tougheners, epoxy compounds, mold release agents, nucleating agents, and colorants might also be deεirable in εuch formulations. Such additives are generally present at 0.1 to about 20 weight % based on the total weight of said polyester compoεition. Useful flame retardants, include, but are not limited to, brominated polystyrene combined with sodium anti onate. Examples of reinforcing agents are glass fibers, carbon fiberε, mica, clay, talc, wollaεtonite, and calcium carbonate. A particularly preferred reinforcing agent iε glaεε fiber. It is preferable that the glass fibers be present in the polyester composition at from 0.1 to 40 %, preferably 0.1 to 30 %, by weight based on the total weight of said polyester composition. Glass fibers εuitable for uεe in the polyeεter compoεitionε of the invention may be in the form of glaεε filaments, threads, fibers, or whiskers, etc., and may vary in length from about 1/8 inch to about 2 inches. Chopped glaεε εtrands having a length of about 1/8 inch to about 1/4 inch are preferred. Such glass fibers are well known in the art. Of course, the size of these glass fibers may be greatly diminished depending on the blending means employed, even to lengths of 300 to 700 microns or lower. The polyester compositions of the invention may be reinforced with a mixture of glass and other reinforcing agents as described above, such as mica or talc, and/or with other additives. The polyester compositions of the invention containing reinforcing agents may be molded at mold temperatures below 120°C and are therefore easily molded without the need for expensive mold heating equipment. The preferred molding temperature of the glass filled polyester compositionε of the invention iε in the range of 20 - 110°C. The components of the blend of the invention may blended and/or mixed by any suitable technology known in the art. The inherent viscoεitieε (I.V.) of the copolyeεterε are determined in 60/40 (wt./wt.) phenol/tetrachloroethane at a concentration of 0.5 g/100 ml aε determined at 25°C. Molded objectε and films may be prepared from the polyester compositionε of the invention including any preferred embodiment. Also, a method for decreasing the glass transition temperature and the melt viscoεity of the copolyesters of the polyester composition of the invention is desirable using the polyalkylene ethers of the invention. In this method, all preferred embodiments of the polyeεter compoεition of the invention are alεo deεirable. The following abbreviations are used herein: T refers to the glass transition temperature; DSC refers to Differential Scanning Calorimetry. This invention can be further illustrated by the following examples of preferred embodiments thereof, although it will be understood that these examples are included merely for purposes of illustration and are not intended to limit the scope of the invention unless otherwise specifically indicated. The starting materials are commercially available unless otherwise indicated. Percentages aε referred to herein are percentageε by weight unless otherwise specified. Examples All of the following exampleε were prepared using poly(1,4—cyclohexanedimethylene terephthalate) (PCT) having an inherent viscosity in the range of 0.65 to 0.75 dL/g as determined at 25°C using 0.5 gram of polymer per 100 L of a solvent compoεed of 60 wt% phenol and 40 wt% tetrachloroethane. The abbreviations "PCT", in these Examples refers only to poly(1,4— cyclohexanedimethylene terephthalate) . The polyalkylene ethers used were hydroxyl functional polyethylene glycol endcapped with ethyl hexanoate or reacted so that the ends of the polyethylene glycol are ethyl hexanoate esterε (Plaεticizer A) and polytetramethylene glycol (PTMG) (Plaεticizer B) . Benzoflex 312 (neopentylglycoldibenzoate) , a common plaεticizer for polyesters, was included as a control. The compositions were prepared by mixing the desired components on a twin screw extruder with set temperatures of 300°C, extruded into a cold water bath and pelletized. All compoεitionε are reported on a weight percent baεiε with the exception of the plasticizer concentration which is reported on a weight percent basiε relative only to the matrix reεin. The thermal analysiε (DSC) and melt viscosity measurements were performed on the compounded pellets. The effectiveneεε of the plasticizer on increasing the crystallization rate aε well aε lowering the optimum temperature for cryεtallization waε determined by the evaluation of the temperature of cryεtallization on heating (Teh) by DSC with a scan rate of 20°C per minute after quenching from the melt. An effective plasticizer will lower the Teh. Therefore, the lower the Teh value, the better the plasticizing effect. Melt viscosity was measured on a capillary rheometer (Gottferd rheometer) at the specified frequency and temperature. Mechanical propertieε were evaluated on injection molded εpecimens following ASTM methods as follows: Tensile Strength and Tensile Elongation to Break were determined by ASTM Method D638; Notched Izod was determined by ASTM Method D256; Flexural Strength, Modulus and Strain to Break were determined by ASTM Method D790; and Heat Deflection Temperature was meaεured at 264 pεi uεing ASTM Method D648. Comparative Example 1 showε poly(1,4— cyclohexanedimethylene terephthalate) (PCT) compounded with glass, but no plasticizer was added. The glasε transition temperature iε 89°C and the Teh iε 133°C as reported in Table 1. This Teh is >110°C indicating that it εhould not be molded with a water—heated mold. In Table 2 the melt viεcoεity of example 1 is reported as 299 Pa*s. Comparative Example 2 shows PCT and glass compounded with 7.5 wt% of the commercial plasticizer Benzoflex 312. The glass transition temperature is depresεed to 72°C, Teh decreaεeε to 114°C and the melt viscoεity is lowered to 212 Pa*s. All three measurements indicate that Benzoflex 312 is indeed an effective plasticizer for PCT. Examples of the Invention, Examples 3—6 show PCT and glass compounded with polyalkylene etherε. Example 3 shows Plasticizer A at 7.5% which lowers Tg and Teh to 56 C C and 95°C, respectively. The melt viscoεity of Example 3 is also lowered to 237 Pa*s compared to 299 Pa*s for the unplasticized PCT. Thiε indicateε that at the εame level, Plaεticizer A (polyethylene glycol end—capped with ethyl hexoate) is a more effective plasticizer than Benzoflex 312 when considering crystallization kineticε and iε εtill effective at reducing melt viεcoεity. Example 5 εhowε PCT and glass compounded with 7.5 wt% polytetramethylene glycol (PTMG) . PTMG depresses the Tg to 64°C the Teh to 100°C and the melt viscoεity to 196 Pa*ε. PTMG, when used at equivalent levels as Benzoflex 312, iε a εuperior plaεticizer in terms of both crystallization kinetics and melt viscosity. The polyalkylene ethers are effective plaεticizers and did not degrade the mechanical properties of the molded compositeε aε reported in Table 3. This showε that the polyalkylene etherε are better plasticizers for PCT than some of the conventional plasticizers in spite of the high processing temperature required to melt PCT. In Table 3 , Examples 2 and 3 are comparable formulations and Examples 2b and 5 are comparable. Example 2b is identical to example 1, except no flame retardant was added. The addition of flame retardant alters the mechanical properties, thus 2 and 5 are not comparable. Table 4 reflects data which compares the stability of Plasticizer A (PEG) to a blend of PCT and Plaεticizer A. The value of "1% weight loεε in air" iε measured by dynamic thermogravimetric analysis (TGA) at 20°C increase in temperature per minute. The value of "% weight loss at 300°C for 30 minutes" is measured by isothermal TGA. One would expect that the Plasticizer A by itself would be as stable or more stable than the Plasticizer A blended with the PCT. However, this data εhows that the blend of PCT and Plasticizer A is more stable than Plasticizer A alone. TABLE 1 Thermal Analysis of 30% Glass Reinforced PCT Example Plasticizer Weight Tg (°C) Teh (°C) TM (°C) % Plasticizer 1 None 89 133 291 2 Benzoflex 312 7.5 72 114 289 3 Plasticizer A 7.5 56 95 282 4 Plasticizer A 3.75 77.5 121 290 5 PTMG 7.5 64 100 290 6 PTMG 5.0 75.5 116 289 TABLE 2 Melt Viscoεity of 30% Glass Reinforced PCT .mple Plasticizer Weight % Melt Viscosity Plasticizer (Pa*s) * 1 None 299 2 Benzoflex 312 7.5 212 3 Plasticizer A 7.5 237 4 PTMG 7.5 196 •Measured at 305°C, with a shear rate of 400 sec' and reported in Pa*s TABLE 3 Mechanical Properties of 30% Glass Reinforced PCT EXAMPLE 2 EXAMPLE 3 EXAMPLE 2b Example 5 Tensile Strength 130.0+5 125.5+5 118.5+5 108.0+5 (MPa) Tensile 1.8+0.2 1.9+0.2 1.6+0.2 1.7+0.2 Elongation to Break (%) Notched Izod @ 64.0+5 69.0+5 96.0+5 96.0+5 23°C (Joules/meter) Flex Strength 189.0+5 179.0+5 155.0+5 146.0+5 (MPa) Flex Modulus 9,310+600 8,760+600 8,070+600 7,170+600 (MPa) Flex Strain to 2.3+0.2 2.3+0.2 2.1+0.2 2.3+0.2 Break (%) HDT @ 1.8 MPa 249+5 251+5 262+5 270+5 (°C) Table 4 COMPARISONS OF THERMAL STABILITY % Wt loss at 1 % 10 % 300°C Wt loss Wt loss air (air)°C (air)°C 30 min Plasticizer A 123.0 205.3 100.0 Plasticizer A + 0.25% Irganox 1010* 130.0 220.1 100.0 Plasticizer A + 0.5% Irganox 1010* 129.0 227.5 97.0 Plasticizer A + 1.0% Irganox 1010* 132.0 234.9 95.0 PCT + 375% Plasticizer A 318.0 392.9 2.7 PCT Control 362.0 398.2 1.2 I Irganox 1010 is an additive which is a hindered phenol. The invention has been described in detail with particular reference to preferred embodiments thereof, but it will be understood that variations and modifications can be effected within the spirit and scope of the invention. Moreover, all patents, patent applications (published and unpublished, foreign or domestic) , literature references or other publications noted above are incorporated herein by reference for any disclosure pertinent to the practice of this invention.

Claims: CLAIMS We claim: 1. A polyester composition comprising a blend of: (A) 99.5 to 75 weight % of a copolyester having an inherent viscosity of 0.1 to 1.2 dL/g and having a melting point in excess of 250°C, comprising: (a) one or more dicarboxylic acidε, and (b) a glycol component comprising at least 80 mole % 1,4—cyclohexanedimethanol; and (B) 0.5 to 25 weight % of one or more polyalkylene ethers, wherein the weight percentages of all components in said blend total 100 weight %. 2. The polyester compoεition of Claim 1 wherein said one or more dicarboxylic acids comprise at least 90 mole % terephthalic acid. 3. The polyester composition of Claim 1 wherein said copolyester is present in an amount of 99.5 to 85 weight %. 4. The polyester composition of Claim 3 wherein said copolyester is present in an amount of 99.5 to 90 weight %. 5. The polyester composition of Claim 4 wherein said copolyester is present in an amount of 97 to 93 weight %. 6. The polyester composition of Claim 2 wherein said acid component comprises repeat units of from 10 mole % or less of one or more other dicarboxylic acids. 7. The polyester composition of Claim 1 wherein said dicarboxylic acids are selected from the group consisting of terephthalic acid, cyclohexanedicarboxylic acid, isophthalic acid, 1,4—cyclohexanediacetic acid, diphenyl—4,4'— dicarboxylic acid, succinic acid, glutaric acid, adipic acid, azelaic acid, naphthalenedicarboxylic acid, and sebacic acid. 8. The polyester composition of Claim 7 wherein said acid component comprises isophthalic acid. 9. The polyester composition of Claim 7 wherein said acid component comprises 1,4— cyclohexanedicarboxylic acid. 10. The polyester composition of Claim 7 wherein said acid component comprises naphthalenedicarboxylic acid. 11. The polyester composition of Claim 2 wherein said other dicarboxylic acids are selected from the group consisting of isophthalic acid, cyclohexanedicarboxylic acid, 1,4— cyclohexanediacetic acid, diphenyl—4,4 '— dicarboxylic acid, succinic acid, glutaric acid, adipic acid, azelaic acid, naphthalenedicarboxylic acid, and sebacic acid. 12. The polyester composition of Claim 1 wherein said glycol component comprises 95 to 100 mole % 1,4- cyclohexanedimethanol. 13. The polyester composition of Claim 1 wherein said glycol component comprises up to 20 mole % of one or more other aliphatic or alicyclic glycols. 14. The polyester composition of Claim 13 wherein said glycol component comprises up to 10 mole % of one or more other aliphatic or alicyclic glycols. 15. The polyester composition of Claim 14 wherein said one or more other glycols is selected from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, propanediol, butanediol, pentanediol, hexanediol, and tetramethylcyclobutanediol. 16. The polyester composition of Claim 15 wherein said one or more other glycols comprises ethylene glycol. 17. The polyester compoεition of Claim 1 wherein said polyalkylene ethers comprise compounds of the formula: wherein, m is an integer from 1 to 3, inclusive, n is an integer from 4 to 250 inclusive, X is selected from one or more of the group consisting of CH 3 , C 3 H 7 , C 2 H 5 , and H, A is hydrogen, alkyl, acyl, aryl or aroyl of 1 to 10 carbon atoms, and B is hydrogen, alkyl, acyl, aryl or aroyl of 1 to 10 carbon atoms. 18. The polyester composition of Claim 17 wherein said polyalkylene ethers comprise polyethylene glycol, polytetramethylene glycol, and polypropylene glycol. 19. The polyester composition of Claim 18 wherein said polyalkylene ether is poly(ethylene glycol) . 20. The polyester composition of Claim 18 wherein εaid polyalkylene ether is polytetramethylene glycol. 21. The polyester composition of Claim 18 wherein said polyalkylene ethers have a number average molecular weight of from 200 to 10,000. 22. The polyester composition of Claim 21 wherein said polyalkylene etherε have a number average molecular weight of 400 to 1,500. 23. The polyester composition of Claim 1 further comprising one or more additives. 24. The polyester composition of Claim 23 wherein said additives are present at 0.1 to about 20 weight % based on the total weight of said polyester composition. 25. The polyester composition of Claim 23 wherein said additives are selected from the group consisting of stabilizers, flame retardants, tougheners, epoxy compounds, mold release agents, nucleating agents, and colorants. 26. The polyester composition of Claim 1 comprising one or more reinforcing agents. 27. The polyester composition of Claim 26 wherein said one or more reinforcing agents comprise glass fibers. 28. The polyester composition of Claim 27 wherein said glass fiberε are present in said polyester composition at from 0.1 to 40 % by weight based on the total weight of said polyester composition. 29. The polyester composition of Claim 5 wherein said additives comprise flame retardants. 30. A molded object prepared from the composition of Claim 1. 31. A method for decreasing the glass transition temperature and the melt viscosity of a polyester composition comprising a copolyester having an inherent viscosity of 0.1 to 1.2 dL/g and having a melting point in excesε of 250°C, said copolyester comprising: (a) one or more dicarboxylic acids, and (b) a glycol component comprising at least 80 mole % 1,4—cyclohexanedimethanol; wherein said method comprises the step of adding to said polyester composition 0.5 to 25 weight % of one or more polyalkylene ethers, wherein the weight percentages of said copolyester and said one or more polyalkylene ethers total 100 weight %.

Inventors: BRINK ANDREW EDWIN, KEEP GERALD TIMOTHY, TURNER SAM RICHARD, BRINK, ANDREW, EDWIN, KEEP, GERALD, TIMOTHY, TURNER, SAM, RICHARD
Applicants: EASTMAN CHEM CO, EASTMAN CHEMICAL COMPANY
Application year: 1996
Main classification: C08L67
IPC codes: C08L67