Patent Application
20160130393
The present application is based on, and claims priority from, Taiwan Application Serial Number 103138869, filed on Nov. 10, 2014, the disclosure of which is hereby incorporated by reference herein in its entirety.
The technical field relates to a thermoplastic polyester elastomer, and in particular it relates to the composition of the thermoplastic polyester elastomer and a method for manufacturing the same.
Thermoplastic polyester elastomer (TPEE) is a polymer material having an elasticity recovery property at room temperature, which is similar to that of conventional vulcanized rubber. In addition, the TPEE can be plasticized at a high temperature in a formation process utilizing general equipment. While the TPEE can be plasticized by heat, it is also called a thermoplastic elastomer. TPEE is a linear block copolymer of a crystalline hard-segment polyester such as polybutylene terephthalate (PBT)/polyethylene terephthalate (PET) and an amorphous soft-segment such as aliphatic polyester or polyether. The TPEE includes the following properties and process technologies: (1) high thermal resistance, high withstand load, and high elasticity recovery, (2) high alternating fatigue properties and toughness, (3) low-temperature flexibility being higher than that of thermoplastic polyurethane (TPU), and (4) high oil/drug/chemical solvent resistance. The TPEE has the following processing characteristics: it can be processed using standard equipment and skills for thermoplastic plastic, e.g. extrusion, injection, blow molding, or the like. Because the TPEE can be used to produce rubber products without vulcanization, it eliminates the vulcanization step, reduce the investment, lowers the energy consumed, simplifies the technology, shortens the work cycle, enhances production efficiency, and lowers the processing cost. The scraps of TPEE can be recycled to save on resources for environmental protection.
In general, the TPEE should simultaneously have a low melting index and a high crystallization temperature. The low melting index is equal to a high melting strength, and therefore the TPEE can easily be extruded, blow molded, and the like. The high crystallization temperature may shorten the time required for processing of the TPEE. Conventional TEPPs only have either a low melting index or a high crystallization temperature, but not both.
Accordingly, a novel monomer composition and/or a novel process for a TPEE simultaneously having low melting index and high crystallization temperature are called.
One embodiment of the disclosure provides a thermoplastic polyester elastomer, being formed by: reacting 100 parts by weight of an ester and 0.01 to 2 parts by weight of an epoxy resin with two epoxy groups, wherein the ester is formed by reacting a parts by mole of a hard-segment diol, b parts by mole of a soft-segment diol, and 1 part by mole of a diacid, wherein 1≦a≦3 and 0.005≦b≦1.5.
One embodiment of the disclosure provides a method of forming a thermoplastic polyester elastomer, comprising: (a) reacting a parts by mole of a hard-segment diol, b parts by mole of a soft-segment diol, and 1 part by mole of a diacid to form an ester, wherein 1≦a≦3 and 0.005≦b≦1.5; and (b) reacting 100 parts by weight of the ester and 0.01 to 2 parts by weight of an epoxy resin with two epoxy groups to form a thermoplastic polyester elastomer.
A detailed description is given in the following embodiments.
In the following detailed description, for purposes of explanation, numerous specific details are set forth in order to provide a thorough understanding of the disclosed embodiments. It will be apparent, however, that one or more embodiments may be practiced without these specific details.
One embodiment of the disclosure provides a method of forming a thermoplastic polyester elastomer, including: (a) reacting a parts by mole of a hard-segment diol, b parts by mole of a soft-segment diol, and 1 part by mole of a diacid to form an ester, wherein 1≦a≦3 and 0.005≦b≦1.5; and (b) reacting 100 parts by weight of the ester and 0.01 to 2 parts by weight of an epoxy resin with two epoxy groups to form a thermoplastic polyester elastomer.
In one embodiment, the diacid can be terephthalic acid, dialkyl terephthalate such as dimethyl terephthalate, or a combination thereof. In one embodiment, the hard-segment diol can be ethylene glycol, butylene glycol, or a combination thereof. In one embodiment, the soft-segment diol can be polytetramethylene glycol with a number average molecular weight of 250 to 4000. A soft-segment diol with an overly high number average molecular weight will lower the polymerization of the thermoplastic polyester elastomer, such that the thermoplastic elastomer polyester has an insufficient mechanical strength. A soft-segment diol with an overly high number average molecular weight will overly lower the melting point of the thermoplastic polyester elastomer, such that the thermoplastic elastomer polyester has an insufficient mechanical strength. In step (a), an overly high parts by mole of a hard-segment diol will be distilled out, thereby increasing reaction byproducts. An overly high parts by mole of a hard-segment diol will lower the polymerization of the thermoplastic polyester elastomer, such that the thermoplastic elastomer polyester has an insufficient mechanical strength. In one embodiment, step (a) is performed at a temperature of 190° C. to 230° C. An overly low temperature in step (a) will lengthen the reaction period and lower the degree of polymerization of the thermoplastic polyester elastomer. An overly high temperature in step (a) will easily degrade the thermoplastic polyester elastomer and lower its mechanical strength. The molecular weight of the ester formed in step (a) is determined by the molecular weight of the diacid, the diol, and the degree of polymerization of the diol and the diacid. In general, the ester has a molecular weight of 200 to 5000. An ester with an overly high molecular weight will make it so that the thermoplastic polyester elastomer is not easily formed by polymerization, and it will lower the degree of polymerization and mechanical strength of the thermoplastic polyester elastomer. An ester with an overly low molecular weight will make it so that the hard-segment of the thermoplastic polyester elastomer is not easily crystallized, and it will lower the mechanical strength of the thermoplastic polyester elastomer.
A catalyst (such as tetra-n-butyl titanate, antimony trioxide, or a combination thereof), an antioxidant (such as hindered phenol, thioester, phosphite, or a combination thereof), or a combination thereof can be further added in step (a).
In step (b), an overly high amount of the epoxy resin with two epoxy groups will overly increase the viscosity of the thermoplastic polyester elastomer, such that the product processing is difficult. An overly low amount of the epoxy resin with two epoxy groups will overly reduce the melting strength of the thermoplastic polyester elastomer. In one embodiment, the epoxy resin with two epoxy groups can be bisphenol A diglycidyl ether epoxy resin, novolac epoxy resin, or a combination thereof. In one embodiment, the epoxy resin with two epoxy groups has a number average molecular weight of 300 to 5000. An epoxy resin with two epoxy groups having an overly low number average molecular weight will make it so that the thermoplastic polyester elastomer have a low crystallization temperature. An epoxy resin with two epoxy groups having an overly high number average molecular weight will make it so that the thermoplastic polyester elastomer has an insufficient melting strength. In one embodiment, step (b) is performed at a temperature of 230° C. to 260° C. An overly low temperature in step (b) will make it so that the thermoplastic polyester elastomer has a low degree of polymerization. An overly low temperature in step (b) will easily degrade the thermoplastic polyester elastomer and lower its mechanical strength. In step (b), the ester can be further polymerized to form a polyester, and the carboxyl group or hydroxyl group of the ester can be reacted with the epoxy groups of the epoxy resin with two epoxy groups during the polymerization. As such, the thermoplastic polyester elastomer is obtained by step (b). Note that if the diacid and the diol are directly heated to 230° C. to 260° C. to form the polyester, and the epoxy resin with two epoxy groups is then added to react with the polyester, the product thereof will not simultaneously own the low melting index and the high crystallization temperature as the thermoplastic polyester elastomer in the disclosure.
Below, exemplary embodiments will be described in detail so as to be easily realized by a person having ordinary knowledge in the art. The inventive concept may be embodied in various forms without being limited to the exemplary embodiments set forth herein. Descriptions of well-known parts are omitted for clarity, and like reference numerals refer to like elements throughout.
291 g of dimethyl terephthalate and 186 g of ethylene glycol were mixed, and then heated to 190° C. to 230° C. for 3 hours to be esterified to form an ester.
217 g of polytetramethylene glycol (commercially available from Aldrich, Mn˜1000), 0.025 phr of catalyst tetra-n-butyl titanate, 0.02 phr of catalyst antimony trioxide, 0.22 phr of antioxidant CHEMNOX-1010 (commercially available from CHEMBRIDGE) were then added to the above ester, and heated to 230° C. to 260° C. and vacuumed for 3 hours to be polymerized to form a polyester. The properties of the polyester were then measured by several standards, such as tensile strength (ASTM D-638), tensile ratio (ASTM D-638), hardness (ASTM D2204-05), melting index (ASTM D 1238), crystallization temperature (ASTM D3418), and melting point (ASTM D3418), as tabulated in Table 1.
Comparative Example 2 was similar to Comparative Example 1, and the difference in Comparative Example 2 was 0.2 phr of glycerol being added to the ester before vacuuming and heating the ester to form the polyester. The other factors such as the amount and type of the dimethyl terephthalate, the ethylene glycol, the polytetramethylene glycol, the catalyst, and the antioxidant, the esterification temperature and period, the vacuumed polymerization temperature and period, and the measurement standards of the polyester were similar to those of Comparative Example 1.
Comparative Example 3 was similar to Comparative Example 1, and the difference in Comparative Example 3 was 0.3 phr of nucleating agent Na-32 (commercially available from Shanghai KeSu Macromolecule Functional Materials Co., Ltd) being added to the ester before vacuuming and heating the ester to form the polyester. The other factors such as the amount and type of the dimethyl terephthalate, the ethylene glycol, the polytetramethylene glycol, the catalyst, and the antioxidant, the esterification temperature and period, the vacuumed polymerization temperature and period, and the measurement standards of the polyester were similar to those of Comparative Example 1.
291 g of dimethyl terephthalate, 186 g of ethylene glycol, 217 g of polytetramethylene glycol (commercially available from Aldrich, Mn˜1000), 0.025 phr of catalyst tetra-n-butyl titanate, 0.02 phr of catalyst antimony trioxide, and 0.22 phr of antioxidant CHEMNOX-1010 (commercially available from CHEMBRIDGE) were mixed, and then heated to 190° C. to 230° C. for 3 hours to be esterified to form an ester.
0.3 phr of epoxy resin with two epoxy groups Epikote 1009 (commercially available from Momentive) was then added to the ester, and heated to 230° C. to 260° C. and vacuumed for 3 hours to be polymerized to form a thermoplastic polyester elastomer. As such, the carboxyl group or hydroxyl group of the ester can be reacted with the epoxy groups of the epoxy resin with two epoxy groups during the polymerization. The measurement standards of the thermoplastic polyester elastomer were similar to those of Comparative Example 1.
An ester was prepared as Example 1. 0.3 phr of epoxy resin with two epoxy groups 828 (commercially available from Momentive) was then added to the ester, and heated to 230° C. to 260° C. and vacuumed for 3 hours to be polymerized to form a thermoplastic polyester elastomer. As such, the carboxyl group or hydroxyl group of the ester can be reacted with the epoxy groups of the epoxy resin with two epoxy groups during the polymerization. The measurement standards of the thermoplastic polyester elastomer were similar to those of Comparative Example 1.
An ester was prepared as Example 1. 0.3 phr of epoxy resin with two epoxy groups Epikote 1001 (commercially available from Momentive) was then added to the ester, and heated to 230° C. to 260° C. and vacuumed for 3 hours to be polymerized to form a thermoplastic polyester elastomer. As such, the carboxyl group or hydroxyl group of the ester can be reacted with the epoxy groups of the epoxy resin with two epoxy groups during the polymerization. The measurement standards of the thermoplastic polyester elastomer were similar to those of Comparative Example 1.
An ester was prepared as Example 1. 0.3 phr of epoxy resin with two epoxy groups Epikote 1004 (commercially available from Momentive) was then added to the ester, and heated to 230° C. to 260° C. and vacuumed for 3 hours to be polymerized to form a thermoplastic polyester elastomer. As such, the carboxyl group or hydroxyl group of the ester can be reacted with the epoxy groups of the epoxy resin with two epoxy groups during the polymerization. The measurement standards of the thermoplastic polyester elastomer were similar to those of Comparative Example 1.
An ester was prepared as Example 1. 0.3 phr of epoxy resin with two epoxy groups Epikote 1007 (commercially available from Momentive) was then added to the ester, and heated to 230° C. to 260° C. and vacuumed for 3 hours to be polymerized to form a thermoplastic polyester elastomer. As such, the carboxyl group or hydroxyl group of the ester can be reacted with the epoxy groups of the epoxy resin with two epoxy groups during the polymerization. The measurement standards of the thermoplastic polyester elastomer were similar to those of Comparative Example 1.
194 g of dimethyl terephthalate, 180 g of 1,4-butylene glycol, 166 g of polytetramethylene glycol (commercially available from Aldrich, Mn˜1000), 0.025 phr of catalyst tetra-n-butyl titanate, 0.02 phr of catalyst antimony trioxide, and 0.22 phr of antioxidant CHEMNOX-1010 (commercially available from CHEMBR1DGE) were mixed, and then heated to 190° C. to 230° C. for 3 hours to be esterified to form an ester.
The ester was then heated to 230° C. to 260° C. and vacuumed for 3 hours to be polymerized to form a polyester. The measurement standards of the polyester were similar to those of Comparative Example 1.
Comparative Example 5 was similar to Comparative Example 4, and the difference in Comparative Example 5 was 0.2 phr of glycerol being added to the ester before vacuuming and heating the ester to form the polyester. The other factors such as the amount and type of the dimethyl terephthalate, the 1,4-butylene glycol, the polytetramethylene glycol, the catalyst, and the antioxidant, the esterification temperature and period, the vacuumed polymerization temperature and period, and the measurement standards of the polyester were similar to those of Comparative Example 4.
An ester was prepared as Comparative Example 4. 0.3 phr of epoxy resin with two epoxy groups Epikote 1009 (commercially available from Momentive) was then added to the ester, and heated to 230° C. to 260° C. and vacuumed for 3 hours to be polymerized to form a thermoplastic polyester elastomer. As such, the carboxyl group or hydroxyl group of the ester can be reacted with the epoxy groups of the epoxy resin with two epoxy groups during the polymerization. The measurement standards of the thermoplastic polyester elastomer were similar to those of Comparative Example 1.
As shown in Tables 1 and 2, if the epoxy resin with two epoxy groups was added before the ester polymerization, the thermoplastic polyester elastomer would have a lower melting index and a higher crystallization temperature.
It will be apparent to those skilled in the art that various modifications and variations can be made to the disclosed methods and materials. It is intended that the specification and examples be considered as exemplary only, with a true scope of the disclosure being indicated by the following claims and their equivalents.
| Number | Date | Country | Kind |
|---|---|---|---|
| 103138869 | Nov 2014 | TW | national |
