Patent Application
20120037848
The present invention relates to a wholly aromatic liquid crystalline polyester resin compound and a method of preparing the same, and more particularly, to a wholly aromatic liquid crystalline polyester resin compound including at least one of a polyethylene-based resin and a polypropylene-based resin as an additive, and a method of preparing the same.
Wholly aromatic liquid crystalline polyester resins have good physical properties of heat resistance, dimensional stability, and fluidity when being melted, and thus are widely used around the world, mainly in the electronic parts industry, as materials for injection molding. Particularly, due to excellent dimensional stability and electricity insulation performance, their usage has been expanding into films for electronic materials and materials for substrates.
If wholly aromatic liquid crystalline polyester resins are used in injection molding, poor mold release by which a molded article is not contracted in the mold or clings to the mold may easily occur.
The present invention provides a wholly aromatic liquid crystalline polyester resin compound including at least one of a polyethylene-based resin and a polypropylene-based resin as an additive.
The present invention also provides a method of preparing a wholly aromatic liquid crystalline polyester resin compound, the method including adding at least one of a polyethylene-based resin and a polypropylene-based resin as an additive.
According to an aspect of the present invention, there is provided a wholly aromatic liquid crystalline polyester resin compound including at least one of a polyethylene-based resin and a polypropylene-based resin as an additive.
Weight average molecular weights of the polyethylene-based resin and the polypropylene-based resin may be in the range of 1,000 to 5,000, respectively.
The total amount of the polyethylene-based resin and the polypropylene-based resin may be in the range of 500 to 10,000 ppm based on the total weight of the wholly aromatic liquid crystalline polyester resin compound.
The polyethylene-based resin may include at least one selected from the group consisting of polyethylene (PE), polyethylene wax (PE Wax), oxidized polyethylene wax (Oxidized PE Wax), high-density polyethylene (HDPE), and ultrahigh-density polyethylene (UHMWPE).
The polypropylene-based resin may include polypropylene.
The wholly aromatic liquid crystalline polyester resin compound may further include an inorganic filler as an additive.
The inorganic filler may include at least one selected from the group consisting of glass fiber, talc, calcium carbonate, mica, and clay.
The wholly aromatic liquid crystalline polyester resin compound may further include a stabilizer as an additive.
The stabilizer may include at least one selected from the group consisting of calcium montanate, calcium behenate, and calcium stearate.
According to another aspect of the present invention, there is provided a method of preparing a wholly aromatic liquid crystalline polyester resin compound, the method including: mixing a wholly aromatic liquid crystalline polyester resin and an inorganic filler, and melt-kneading the mixture; and adding at least one of a polyethylene-based resin and a polypropylene-based resin to the melt-kneaded mixture, mixing and drying the mixture.
According to another aspect of the present invention, there is provided a method of preparing a wholly aromatic liquid crystalline polyester resin compound, the method including mixing a wholly aromatic liquid crystalline polyester resin, at least one of a polyethylene-based resin and a polypropylene-based resin, and an inorganic filler, and melt-kneading the mixture.
The method may include adding at least one of a polyethylene-based resin and a polypropylene-based resin to a wholly aromatic liquid crystalline polyester resin, and mixing and drying the mixture; and mixing the mixture with an inorganic filler and melt-kneading the mixture.
According to an embodiment of the present invention, there may be provided a wholly aromatic liquid crystalline polyester resin compound having enhanced releasing property by including at least one of a polyethylene-based resin and a polypropylene-based resin as an additive, and a method of preparing the same.
Hereinafter, a wholly aromatic liquid crystalline polyester resin compound and a method of preparing the same according to embodiments of the present invention will be described in detail.
A wholly aromatic liquid crystalline polyester resin compound according to an embodiment of the present invention includes at least one of a polyethylene-based resin and a polypropylene-based resin as an additive. The polyethylene resin and the polypropylene resin enhance releasing property of the wholly aromatic liquid crystalline polyester resin compound, resulting in assisting the resin compound to be easily separated from a mold after a molded article is produced.
A wholly aromatic liquid crystalline polyester resin used in the preparation of the wholly aromatic liquid crystalline polyester resin compound may be prepared according to the following steps:
(a) synthesizing a wholly aromatic liquid crystalline polyester pre-polymer by condensation polymerizing at least two monomers; and
(b) synthesizing a wholly aromatic liquid crystalline polyester resin by solid phase condensation polymerizing the pre-polymer.
The monomers used in step (a) may include at least one compound selected from the group consisting of aromatic diol, aromatic diamine, and aromatic hydroxylamine; and aromatic dicarboxylic acid. In addition, the monomer may further include aromatic hydroxy carboxylic acid and/or aromatic amino carboxylic acid.
The synthesis of step (a) may be performed using solution condensation polymerization or bulk condensation polymerization. In addition, a monomer having reactivity enhanced (i.e., acylated monomer) by pre-treatment with chemicals such as an acylating agent (particularly, acetylating agent) may be used in step (a) in order to expedite the condensation polymerization.
To perform the solid phase condensation polymerization in step (b), the pre-polymer is required to be heated using, for example, a heating plate, hot air, hot fluid, or the like. By-products produced during the solid phase condensation polymerization may be removed by purging with inert gas or by applying vacuum thereto.
In addition, the wholly aromatic liquid crystalline polyester resin may include a variety of repeating units in the chain thereof. For example, the repeating units are as follows.
(1) Repeating unit derived from aromatic diol:
—O—Ar—O—
(2) Repeating unit derived from aromatic diamine:
—HN—Ar—NH—
(3) Repeating unit derived from aromatic hydroxy amine:
—HN—Ar—O—
Repeating unit derived from aromatic dicarboxylic acid:
—OC—Ar—CO—
Repeating unit derived from aromatic hydroxy carboxylic acid:
—O—Ar—CO—
Repeating unit derived from aromatic amino carboxylic acid:
—HN—Ar—CO—
In the formulae defined above, Ar may be phenylene, biphenylene, naphthalene, an aromatic compound in which two phenylene are bonded to each other via a carbon or non-carbon element, or an aromatic compound selected from the group consisting of phenylene, biphenylene, naphthalene, or two phenylene bonded to each other by carbon or a non-carbon element in which at least one hydrogen atom is substituted with other elements.
Weight average molecular weights of the polyethylene-based resin and the polypropylene-based resin may respectively be in the range of 1,000 to 5,000. If the weight average molecular weight of each of the polyethylene-based resin and the polypropylene-based resin is less than 1,000, effects of adding them are negligible. On the other hand, if the weight average molecular weight of each of the polyethylene-based resin and the polypropylene-based resin is greater than 5,000, a flow mark may be formed on the surface of a product produced by using the wholly aromatic liquid crystalline polyester resin compound including them (i.e. the resins).
The total amount of the polyethylene-based resin and the polypropylene-based resin may be in the range of 500 to 10,000 ppm based on the total weight of the wholly aromatic liquid crystalline polyester resin compound. If the total amount of the polyethylene-based resin and the polypropylene-based resin is less than 500 ppm based on the total weight of the wholly aromatic liquid crystalline polyester resin compound, effects of adding them are negligible. On the other hand, if the total amount of the polyethylene-based resin and the polypropylene-based resin is greater than 10,000 ppm, a large amount of gas is generated.
The polyethylene-based resin may include at least one selected from the group consisting of polyethylene (PE), polyethylene wax (PE Wax), oxidized polyethylene wax (Oxidized PE Wax), high-density polyethylene (HDPE), and ultrahigh-density polyethylene (UHMWPE), and the polypropylene-based resin may include polypropylene.
The wholly aromatic liquid crystalline polyester resin compound may further include an inorganic filler as an additive. The inorganic filler may include at least one selected from the group consisting of glass fiber, talc, calcium carbonate, mica, and clay. The inorganic filler improves mechanical strength of a product obtained by injection molding.
The wholly aromatic liquid crystalline polyester resin compound may further include a stabilizer as an additive. The stabilizer may include at least one selected from the group consisting of calcium montanate, calcium behenate, and calcium stearate.
The wholly aromatic liquid crystalline polyester resin compound may be prepared by mixing the wholly aromatic liquid crystalline polyester resin and the inorganic filler in a predetermined ratio, melt-kneading the mixture, adding at least one of a polyethylene-based resin and a polypropylene-based resin to the melt-kneaded mixture by a predetermined amount, and mixing and drying the resultant. In the melt-kneading, a batch type kneader, a twin-screw extruder, or a mixing roll may be used. In addition, a lubricant may be used during the melt-kneading for smooth melt-kneading.
Meanwhile, the wholly aromatic liquid crystalline polyester resin compound may be prepared using any other method. That is, the wholly aromatic liquid crystalline polyester resin compound may also be prepared by mixing the wholly aromatic liquid crystalline polyester resin, at least one of the polyethylene-based resin and the polypropylene-based resin, and the inorganic filler in a predetermined ratio, and melt-kneading the mixture. In particular, the wholly aromatic liquid crystalline polyester resin compound may be prepared by adding at least one of the polyethylene-based resin and the polypropylene-based resin to the wholly aromatic liquid crystalline polyester resin by a predetermined amount, and mixing and drying the mixture, and then mixing the mixture with the inorganic filler in a predetermined ratio, and melt-kneading the resultant.
Hereinafter, one or more embodiments will be described in detail with reference to the following examples. However, these examples are not intended to limit the purpose and scope of the invention.
A KF grade wholly aromatic polyester resin manufactured by Samsung Fine Chemicals Co., Ltd. was used. A melting point of the resin measured using a differential scanning calorimetry (DSC) was 305° C.
The wholly aromatic liquid crystalline polyester resin prepared in Preparation Example 1 and a glass fiber, e.g., a ground glass fiber having a diameter of 10 μm and an average length of 150 μm, were mixed at a weight ratio of 6:4 (i.e., resin:glass fiber), and the mixture was melt-kneaded using a twin-screw extruder (L/D: 40, diameter: 25 mm). While the mixture was melt-kneaded, by-products were removed therefrom by applying vacuum to the twin-screw extruder.
Then, 5,000 ppm of polyethylene wax (PE Wax, Mitsui, Hi-wax), based on the total weight of the final wholly aromatic liquid crystalline polyester resin compound, was added to the melt-kneaded mixture and the mixture was mixed using an automatic mixing unit (manufactured by Jeil Industry Device Co., Ltd.) for 10 minutes, and then the resultant was dried using a hot-air dryer (A-Sung Plant Co., Ltd.) at 130° C. for 2 hours. Then, 300 ppm of calcium stearate (Ca-ST), based on the total weight of the wholly aromatic liquid crystalline polyester resin compound was added thereto, as a stabilizer, to prepare the wholly aromatic liquid crystalline polyester resin compound.
A wholly aromatic liquid crystalline polyester resin compound was prepared in the same manner as in Example 1, except that 3,000 ppm of the polyethylene wax (Mitsui, Hi-wax) was used based on the total weight of the final wholly aromatic liquid crystalline polyester resin compound.
A wholly aromatic liquid crystalline polyester resin compound was prepared in the same manner as in Example 1, except that 1,000 ppm of the polyethylene wax (Mitsui, Hi-wax) was used based on the total weight of the final wholly aromatic liquid crystalline polyester resin compound.
A wholly aromatic liquid crystalline polyester resin compound was prepared in the same manner as in Example 1, except that polypropylene (PP, GS Caltex, H150) was used instead of polyethylene wax (Mitsui, Hi-wax).
5,000 ppm of polyethylene wax (Mitsui, Hi-wax), based on the total weight of the final wholly aromatic liquid crystalline polyester resin compound, was added to the wholly aromatic liquid crystalline polyester resin prepared in Preparation Example 1, and the mixture was mixed using an automatic mixing/drying unit (A-Sung Plant Co., Ltd.) for 2 hours. Then, the mixture was mixed with a glass fiber, e.g., a ground glass fiber having a diameter of 10 μm and an average length of 150 μm, at a weight ratio of 6:4 (i.e., the mixture:glass fiber), and the mixture was melt-kneaded using a twin-screw extruder (L/D: 40, diameter: 25 mm), resulting in preparing a wholly aromatic liquid crystalline polyester resin compound. By-products were removed in the preparation of the wholly aromatic liquid crystalline polyester resin compound by applying vacuum to the twin-screw extruder.
A wholly aromatic liquid crystalline polyester resin compound was prepared in the same manner as in Example 5, except that 3,000 ppm of the polyethylene wax (Mitsui, Hi-wax) was used based on the total weight of the final wholly aromatic liquid crystalline polyester resin compound.
A wholly aromatic liquid crystalline polyester resin compound was prepared in the same manner as in Example 5, except that polypropylene (PP, GS Caltex, H150) was used instead of polyethylene wax (Mitsui, Hi-wax).
A wholly aromatic liquid crystalline polyester resin was prepared in the same manner as in Example 1, except that the polyethylene wax was not used.
Releasing property, melt viscosity, tensile strength, flexural strength, and heat resistance of the wholly aromatic liquid crystalline polyester resin compounds prepared in Examples 1 to 7 and Comparative Example 1 were measured using the following methods.
Releasing Property
A molded article was prepared using an injection molding apparatus (FANUC ROBOSHOT 2000i-50B) at a cylinder temperature of 380° C., at a mold temperature of 120° C., at an injection speed of 150 mm/s, for 4.5 seconds of cooling time, and at a holding pressure of 500 Kgf/cm2. Then, the molded article was tried to be separated from a mold by protruding an ejector pin at a forward speed of the ejector of 50 mm/s, and the separation aspect was observed.
Then, the injection molding experiment was repeated while increasing the holding pressure by 100 Kgf/cm2 at a time. In this regard, as the holding pressure decreases, it is easier to separate the molded article from the mold by the protrusion of the ejector pin. On the other hand, as the holding pressure increases, it is more difficult to separate the molded article from the mold. Accordingly, a maximum holding pressure at which the molded article is easily separated from the mold was measured. (Hereinafter, the maximum holding pressure is regarded as ‘the degree of releasing property’. As the degree of releasing property increases, releasing property is enhanced).
Melting Viscosity
Melt viscosity of each of the wholly aromatic liquid crystalline polyester resin compounds was measured according to ASTM D3835.
Tensile Strength
Tensile strength of each of the wholly aromatic liquid crystalline polyester resin compounds were measured according to ASTM D638.
Flexural Strength
Flexural strength of each of the wholly aromatic liquid crystalline polyester resin compounds was measured according to ASTM D790.
Heat Resistance
Heat resistance of each of the wholly aromatic liquid crystalline polyester resin compounds were measured according to ASTM D648.
Referring to Table 1, the wholly aromatic liquid crystalline polyester resin compounds prepared in Examples 1 to 7 had better releasing property, and similar melt viscosity, tensile strength, flexural strength, and heat resistance compared to the wholly aromatic liquid crystalline polyester resin compound prepared in Comparative Example 1. In addition, physical properties of the wholly aromatic liquid crystalline polyester resin compound according to an embodiment of the present invention do not significantly change after being recycled a number of times. In particular, tensile strength and flexural strength were maintained up to 90% or more based on the initial tensile strength and flexural strength, respectively, and heat resistance was maintained up to 80% or more based on the initial heat resistance, until the wholly aromatic liquid crystalline polyester resin compound was recycled three times. If the recycled and non-recycled wholly aromatic liquid crystalline polyester resin compounds were mixed in a weight ratio of 50:50, tensile strength and flexural strength were maintained up to 95% or more based on the initial values, respectively, and heat resistance was maintained up to 90% or more based on the initial value even after being recycled three times.
While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it will be understood by those of ordinary skill in the art that various changes in form and details may be made therein without departing from the spirit and scope of the present invention as defined by the following claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2009-0037686 | Apr 2009 | KR | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/KR2010/002033 | 4/2/2010 | WO | 00 | 9/23/2011 |
