JP2002038002A - Polyphenylene ether resin composition with excellent fluidity - Google Patents

Abstract

(57) [Problem] To provide a resin composition capable of simultaneously achieving a sufficient level of fluidity, heat resistance, flame retardancy, and dimensional stability. SOLUTION: (A) Polyphenylene ether resin 7
0 to 99.9 parts by weight, and (B) 0.1 of liquid crystal polyester
(C) an organic compound containing an isocyanate group in an amount of 0.1 to 30 parts by weight, based on 100 parts by weight of the resin component.
A resin composition obtained by blending from 0.01 to 10 parts by weight.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

TECHNICAL FIELD The present invention relates to fluidity, heat resistance,
The present invention relates to a novel polyphenylene ether-based resin composition having excellent flame retardancy and dimensional stability, and a molded article obtained by using the same as a raw material by injection molding or extrusion molding.

[0002]

2. Description of the Related Art In general, polyphenylene ether is a resin having excellent properties such as heat resistance, hot water resistance, dimensional stability, and mechanical and electrical properties. It has disadvantages such as poor fluidity, poor chemical resistance, and low impact resistance. Alloying of polyphenylene ether with other resins has been conventionally performed in order to improve such disadvantages of polyphenylene ether.

For example, it is widely known that alloying polyphenylene ether with polystyrene or high-impact polystyrene improves fluidity and impact resistance. However, there are problems such as a decrease in heat resistance. there were. On the other hand, for example, JP-A-56-115357 discloses that
It has been proposed to blend a polymer such as polyphenylene ether with liquid crystal polyester to improve the melt processability of polyphenylene ether, but it is not sufficient. JP-A-2-97555 proposes to incorporate various polyarylene oxides into a liquid crystal polyester for the purpose of improving the solder heat resistance. Further, JP-A-6-122762 discloses that amines are added. It has been proposed to mix a polyphenylene ether modified with a liquid crystal polyester with a liquid crystal polyester, but none of these methods is sufficient from the viewpoint of balance of fluidity, heat resistance, flame retardancy and dimensional stability.

Further, when alloying polyphenylene ether and liquid crystal polyester, addition of an organic silane coupling agent is disclosed in JP-A-5-117505,
Although proposed in Japanese Patent Application Laid-Open No. 9-111103, the fluidity is not sufficient. In addition, Japanese Patent Laid-Open No.
Japanese Patent Publication No. 88 proposes a method of increasing the strength and rigidity of a recycled material, but it is not sufficient in terms of fluidity.

[0005]

SUMMARY OF THE INVENTION An object of the present invention is to provide a resin composition capable of simultaneously achieving a sufficient level of fluidity, heat resistance, flame retardancy, and dimensional stability.

[0006]

Means for Solving the Problems The inventors of the present invention have conducted intensive studies to achieve the above object, and have found that an organic compound containing an isocyanate group is added to a resin component composed of a polyphenylene ether resin and a liquid crystal polyester. It has been found that by adding a specific amount, a resin composition that can simultaneously achieve a sufficient level of fluidity, heat resistance, flame retardancy, and dimensional stability can be obtained, thereby completing the present invention. That is, the present invention relates to (A) polyphenylene ether-based resin 7
0 to 99.9 parts by weight, and (B) 0.1 of liquid crystal polyester
(C) an organic compound containing an isocyanate group in an amount of 0.1 to 30 parts by weight, based on 100 parts by weight of the resin component.
An object of the present invention is to provide a resin composition obtained by blending from 0.01 to 10 parts by weight.

[0007]

BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be specifically described below. The polyphenylene ether-based resin (A) of the present invention refers to a repeating unit structure represented by the formula (1).

[0008]

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(R ₁ and R ₄ are each independently hydrogen,
Represents primary or secondary lower alkyl, phenyl, aminoalkyl, hydrocarbonoxy. R ₂ and R ₃ each independently represent hydrogen, primary or secondary lower alkyl, or phenyl. ), Reduced viscosity (0.5 g / dl, chloroform solution, measured at 30 ° C.)
Is a homopolymer and / or a copolymer in the range of 0.15 to 1.0 dl / g. Preferred reduced viscosities are in the range of 0.20 to 0.70 dl / g, most preferably in the range of 0.40 to 0.60.

Specific examples of the polyphenylene ether resin include poly (2,6-dimethyl-1,4-phenylene ether) and poly (2-methyl-6-ethyl-).
1,4-phenylene ether), poly (2-methyl-6)
-Phenyl-1,4-phenylene ether), poly (2,6-dichloro-1,4-phenylene ether),
And polyphenylene ether copolymers such as copolymers of 2,6-dimethylphenol with other phenols (eg, 2,3,6-trimethylphenol and 2-methyl-6-butylphenol). Coalescence is also included. Among them, poly (2,6-dimethyl-1,4-phenylene ether), 2,6-dimethylphenol and 2,2
A copolymer with 3,6-trimethylphenol is preferred, and poly (2,6-dimethyl-1,4-phenylene ether) is more preferred.

US Pat. No. 3,306,687 is an example of a method for producing (A) the polyphenylene ether used in the present invention.
There is a method in which 2,6-xylenol is oxidatively polymerized using a complex of a cuprous salt and an amine described in the specification of Patent No. 4 as a catalyst. U.S. Pat. Nos. 3,306,875 and 325
Nos. 7357 and 3257358, JP-B-52-17880, JP-A-50-51197 and JP-A-63-152628 also describe (A) a method for producing polyphenylene ether. preferable.

The polyphenylene ether-based resin (A) of the present invention may be used as it is after the polymerization step,
By using an extruder, under N ₂ gas atmosphere or non-N ₂ gas atmosphere may be used in pelletized by melt kneading with desalted揮下or non de揮下.

The polyphenylene ether resin (A) of the present invention also includes a polyphenylene ether functionalized with various dienophile compounds. Various dienophile compounds include, for example, compounds such as maleic anhydride, maleic acid, fumaric acid, phenylmaleimide, itaconic acid, acrylic acid, methacrylic acid, methyl acrylate, methyl methacrylate, glycidyl acrylate, glycidyl methacrylate, stearyl acrylate, and styrene. No. As a method for functionalization with these dienophile compounds, an extruder or the like may be used in the presence or absence of a radical generator, and may be functionalized in a molten state under devolatilization or non-devolatilization. Alternatively, the functionalization may be performed in a non-molten state in the presence or absence of a radical generator, that is, in a temperature range from room temperature to the melting point. At this time, the melting point of the polyphenylene ether is defined as a peak top temperature of a peak observed in a temperature-heat flow graph obtained when the temperature is increased at 20 ° C./min in a measurement by a differential scanning calorimeter (DSC). If there are a plurality of peak top temperatures, the highest temperature is defined.

The polyphenylene ether-based resin (A) of the present invention may contain an aromatic vinyl-based polymer, if necessary, within a range that does not impair the features and effects of the present invention. Examples of the aromatic vinyl polymer include polystyrene, high impact polystyrene, and acrylonitrile-styrene copolymer. The liquid crystal polyester (B) of the present invention is a polyester called a thermotropic liquid crystal polymer, and a known polyester can be used. For example, a thermotropic liquid crystal polyester having p-hydroxybenzoic acid and polyethylene terephthalate as main constitutional units, p-hydroxybenzoic acid and 2-
Thermotropic liquid crystal polyester having hydroxy-6-naphthoic acid as a main structural unit, p-hydroxybenzoic acid, and thermotropic liquid crystal polyester having 4,4'-dihydroxybiphenyl and terephthalic acid as main structural units, and the like. No restrictions. As the liquid crystal polyester (B) used in the present invention, those composed of the following structural units (a) and (b), and if necessary, (c) and / or (d) are preferably used.

[0015]

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[0016]

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[0017]

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[0018]

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Here, the structural units (a) and (b) are a structural unit of a polyester formed from p-hydroxybenzoic acid and a structural unit formed from 2-hydroxy-6-naphthoic acid, respectively. By using the structural units (a) and (b), it is possible to obtain the thermoplastic resin composition of the present invention having excellent balance of mechanical properties such as excellent heat resistance, fluidity and rigidity. X in the above structural units (C) and (D) can be arbitrarily selected from one or two or more types according to the following (Formula 2).

[0020]

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Preferred in the structural formula (C) are structural units formed from each of ethylene glycol, hydroquinone, 4,4'-dihydroxybiphenyl, 2,6-dihydroxynaphthalene and bisphenol A, and more preferred are: Ethylene glycol, 4,
Structural units formed from each of 4'-dihydroxybiphenyl and hydroquinone, and particularly preferred are
It is a structural unit formed from each of ethylene glycol and 4,4'-dihydroxybiphenyl. In the structural formula (d), preferred are structural units formed from terephthalic acid, isophthalic acid, and 2,6-dicarboxynaphthalene, and more preferred are structural units formed from terephthalic acid and isophthalic acid. It is.

In the structural formulas (c) and (d), at least one or more of the above-mentioned structural units can be used in combination. Specifically, when two or more kinds are used in combination, in the structural formula (C), 1) a structural unit generated from ethylene glycol / a structural unit generated from hydroquinone, 2) a structural unit generated from ethylene glycol / 4, Structural units generated from 4'-dihydroxybiphenyl; 3) structural units generated from hydroquinone / 4 structural units generated from 4,4'-dihydroxybiphenyl;

In the structural formula (d), 1) a structural unit formed from terephthalic acid / a structural unit formed from isophthalic acid, 2) a structural unit formed from terephthalic acid / 2, formed from 2,6-dicarboxynaphthalene And other structural units. Here, the amount of terephthalic acid is preferably at least 40% by weight, more preferably at least 60% by weight, particularly preferably at least 80% by weight in the two components. By setting the amount of terephthalic acid to 40% by weight or more of the two components, a resin composition having relatively good fluidity and heat resistance can be obtained. The ratio of the amounts of the structural units (a), (b), (c), and (d) in the liquid crystal polyester (B) component is not particularly limited. However, the structural units (c) and (d) are basically in equimolar amounts.

Further, the structural unit (e) composed of the structural units (c) and (d) can be used as the structural unit in the component (B). Specifically, 1) a structural unit generated from ethylene glycol and terephthalic acid, 2) a structural unit generated from hydroquinone and terephthalic acid, 3) 4,
Structural units formed from 4'-dihydroxybiphenyl and terephthalic acid, 4) structural units formed from 4,4'-dihydroxybiphenyl and isophthalic acid, 5) structural units formed from bisphenol A and terephthalic acid, and the like. it can.

[0025]

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In the liquid crystal polyester component (B) of the present invention, other aromatic dicarboxylic acids, aromatic diols and aromatic hydroxycarboxylic acids may be added in a small amount as long as the characteristics and effects of the present invention are not impaired. Structural units generated from acids can be introduced. The temperature at which the component (B) of the present invention starts to exhibit a liquid crystal state upon melting (hereinafter referred to as "liquid crystal onset temperature") is preferably 150 to 350C, more preferably 180 to 320C. By setting the liquid crystal onset temperature within this range, the obtained resin composition can have a favorable balance of color tone, heat resistance and moldability.

The (B) liquid crystal polyester component 2 of the present invention
The dielectric loss tangent (tan δ) at 5 ° C. and 1 MHz is preferably 0.03 or less, more preferably 0.02 or less.
It is as follows. The smaller the value of the dielectric loss tangent is, the smaller the dielectric loss becomes, and when this resin composition is used as a raw material for electric / electronic parts, electric noise generated is preferably suppressed. In particular, at 25 ° C. in a high frequency range, that is, in a 1 to 10 GHz range, a dielectric loss tangent (tan)
δ) is preferably 0.03 or less, more preferably 0.02 or less.

The apparent melt viscosity (liquid crystal onset temperature + 30 ° C., shear rate 100 / sec) of the liquid crystal polyester component (B) of the present invention is preferably 100 to 30,000 poise, more preferably 100 to 20,000. Poise, particularly preferably 100 to 10,000 poise. Controlling the apparent melt viscosity in this range may make the resulting composition flowable. The thermal conductivity of the component (B) of the present invention in a molten state (liquid crystal state) is preferably 0.1 to 2.0 W / mK, more preferably 0.2 to 2.0 W / mK.
1.5 W / mK, particularly preferably 0.3 to 1.0 W / m
K. By setting the thermal conductivity in the molten state (liquid crystal state) within this range, the injection molding cycle of the obtained composition can be relatively shortened.

The (C) organic compound having an isocyanate group of the present invention is an organic compound having one isocyanate group in a molecule or an organic compound having two isocyanate groups in a molecule. These preferred organic compounds include aliphatic isocyanate compounds, alicyclic isocyanate compounds, aryl aliphatic isocyanate compounds, aromatic isocyanate compounds, and the like. Examples of the organic compound having one isocyanate group in the molecule include phenyl isocyanate, cyclohexyl isocyanate, and alkylene monoisocyanate having 4 to 12 carbon atoms in the alkylene group, such as 1-dodecane isocyanate and 1-pentamethylene. Isocyanate, 1-hexamethylene isocyanate and the like. On the other hand, the organic compound having two isocyanate groups in the molecule is an alkylene diisocyanate having 4 to 12 carbon atoms in the alkylene group, for example, dodecane 1,12-diisocyanate, 2-ethyltetramethylene 1,4 -Diisocyanate, pentamethylene 1,5-diisocyanate, tetramethylene 1,4
Diisocyanates and, preferably, hexamethylene 1,6-diisocyanate, alicyclic diisocyanates such as cyclohexane 1,3- and 1,4-diisocyanates, and any mixtures of isomers thereof;
-Isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclohexane (isophorone diisocyanate), hexahydrotolylene 2,4- and 2,6-diisocyanate, and the corresponding mixture of isomers, dicyclohexamethane 4, 4'-, 2,2'- and 2,4'-diisocyanates and the corresponding mixture of isomers, aromatic diisocyanates and polyisocyanates such as tolylene 2,4- and 2,6-diisocyanate (TD
I) and the corresponding mixture of isomers, diphenylmethane 4,
4'-, 2,4'- and 2,2'-diisocyanates (MDI) and corresponding isomer mixtures, naphthalene 1,5-diisocyanate (NDI), diphenylmethane 4,4'- and 2,4'-diisocyanate A mixture of NDI and diphenylmethane 4,4'- and / or 2,4'-diisocyanate, 3,3'-dimethyl-4,4'-diisocyanatobiphenyl (TOD
I), mixtures of TODI with diphenylmethane 4,4'- and / or 2,4'-diisocyanate, polyphenylpolymethylene polyisocyanate, diphenylmethane 4,4'-, 2,4'- and 2,2'-diisocyanate And polyphenylpolymethylene polyisocyanate (crude MDI) and a mixture of crude MDI and tolylene diisocyanate.

The (D) inorganic filler of the present invention includes glass fibers, carbon fibers, whiskers, mica, talc, carbon black, titanium oxide, calcium carbonate, potassium titanate, wollastonite, conductive metal fibers, and conductive metal fibers. Carbon black, and the like. Among them, glass fibers are preferred. The fibrous filler such as glass fiber may be covered or bundled with a thermoplastic resin such as an ethylene / vinyl acetate copolymer or a thermosetting resin such as an epoxy resin.

In the present invention, the compounding amount of the polyphenylene ether resin (A) is 70 to 99.9 parts by weight, preferably 75 to 98 parts by weight, and more preferably 80 to 97 parts by weight.
Parts by weight. If the amount is more than 99.9 parts by weight, the moldability will be greatly reduced. If the amount is less than 70 parts by weight, the proportion of the component (B) will increase and the cost will increase. The compounding amount of the liquid crystal polyester of the component (B) in the present invention is 0.1 to 30 parts by weight, preferably 1 to 30 parts by weight.
２５25 parts by weight, more preferably 3-20 parts by weight. If the amount is more than 30 parts by weight, the cost increases and the weld strength further decreases. If the amount is less than 0.1 part by weight, sufficient fluidity and dimensional stability cannot be obtained.

In the present invention, the amount of the organic compound having an isocyanate group of the component (C) is 0.01 to 1 based on 100 parts by weight of the total of the components (A) and (B).
0 parts by weight, preferably 0.05 to 5 parts by weight, more preferably 0.08 to 3 parts by weight. If the blending amount is 10
If it is more than 10 parts by weight, it causes a problem of bleeding out to the surface of the molded article or a decrease in appearance, and if it is less than 0.01 part by weight,
A sufficient effect of the fluidity cannot be obtained.

In the present invention, the amount of the inorganic filler (D) is 0.1 to 300 parts by weight, preferably 1 to 100 parts by weight of the total of the components (A) and (B). 200 parts by weight, more preferably 5-150
Parts by weight. High rigidity can be obtained by the addition. When the addition amount is more than 300 parts by weight, the appearance of the molded article and the fluidity are reduced. If the amount is less than 0.1 part by weight, it is difficult to obtain sufficient rigidity.

In the present invention, in addition to the above-mentioned components, other additional components such as an antioxidant and a flame retardant (organic phosphoric acid ester-based compound) may be used, if necessary, as long as the characteristics and effects of the present invention are not impaired. , Inorganic phosphorus compounds, aromatic halogen-based flame retardants, etc.), elastomers (ethylene / propylene copolymer, ethylene / 1-butene copolymer, ethylene / propylene / non-conjugated diene copolymer, ethylene / ethyl acrylate copolymer) Polymers, ethylene / glycidyl methacrylate copolymer, ethylene / vinyl acetate / glycidyl methacrylate copolymer, ethylene / propylene-g-maleic anhydride copolymer, olefin copolymers such as ABS, polyester polyether Elastomer, polyester polyester elastomer, vinyl aromatic compound-conjugated diene compound Lock copolymer, hydrogenated product of vinyl aromatic compound-conjugated diene compound block copolymer), plasticizer (oil, low molecular weight polyethylene, epoxidized soybean oil, polyethylene glycol, fatty acid esters, etc.), flame retardant aid Agents, weathering (light) resistance improvers, nucleating agents for polyolefins, slip agents, various colorants, release agents and the like may be added.

The resin composition of the present invention can be produced by various methods. For example, a heat-melt kneading method using a single-screw extruder, a twin-screw extruder, a roll, a kneader, a Brabender plastograph, a Banbury mixer, or the like can be mentioned, and the melt-kneading method using a twin-screw extruder is most preferable. The melt-kneading temperature at this time is not particularly limited, but can be arbitrarily selected usually from 150 to 350 ° C. The resin composition of the present invention thus obtained can be obtained by various methods known in the art, for example, injection molding,
By extrusion molding and hollow molding, it can be molded as molded bodies of various parts. These various parts are suitable for, for example, automobile parts and electronic / electric parts.

Although the reason why the resin composition of the present invention exhibits excellent physical properties is not necessarily clear, surprisingly, the addition of the isocyanate compound (C) in the present invention makes the resin composition even higher than that without the addition. It was found that fluidity was obtained. The reactivity of the isocyanate group is very high, and the viscosity of the polyphenylene ether is reduced by some reaction or interaction with the terminal group of the liquid crystal polyester or the terminal group of the polyphenylene ether. It is considered that the orientation was increased, and as a result, the viscosity was greatly reduced.

Hereinafter, the present invention will be described with reference to examples. However, the present invention is not limited to the following examples as long as the gist is not exceeded. a-1: Polyphenylene ether (poly (2,6-dimethyl-1,4 having a reduced viscosity of 0.43 obtained by oxidative polymerization of 2,6-dimethylphenol)
-Phenylene ether) in powder form. b-1: Maleic anhydride (Production Example 1) Production example of polyphenylene ether (PPE-1) Using a powder (a-1) itself obtained after the polymerization step, a scanning calorimeter (DSC) was used to measure 20. The melting point was a single peak when the peak top temperature in the temperature-heat flow graph obtained when the temperature was raised at a rate of ° C./min was 250 ° C.

(Production Example 2) Production Example of Functionalized Polyphenylene Ether (PPE-2) 10 kg of polyphenylene ether (a-1) and 0.05 k of maleic anhydride (b-1) as a dienophile compound
g was placed in an autoclave equipped with a thermometer for measuring the internal temperature, an oil jacket, and a gas inlet equipped with a stirrer. At room temperature, through the gas inlet, 10
After reducing the pressure to mmHg, nitrogen at atmospheric pressure was introduced,
The inside was replaced with nitrogen.

This operation was repeated three times, and the autoclave was sealed. Out of the system at the time of decompression and nitrogen replacement (a-
When 1) and (b-1) were collected, (a-
1) and (b-1) are each 0.1 kg and
It was 0.008 kg. 200 ℃ in oil jacket
Was circulated, the stirrer was operated, and stirring was continued for 1 hour. After stopping the oil circulation and allowing the internal temperature to reach room temperature, the autoclave was opened, and the powdery content (c-1) was collected. The content (c-1) does not contain a melt, and the mass of the content (c-1) is 1
It was 0.0 kg.

The content (c-1) was washed with 50 liters of acetone and filtered off using a filter. This operation 5
This was repeated twice to obtain a washed product 1 (d-1) and a filtrate 1 (e-1). As a result of gas chromatogram analysis, maleic anhydride (b) contained in filtrate 1 (e-1) was analyzed.
-1) was 0.005 kg. Wash 1 (d-
20 g of the dried product 1 (f-1) obtained by drying 1) was subjected to ring distillation extraction with 40 ml of acetone using a Soxhlet extractor. Washed article 2 washed with hot acetone
(G-1) and an extract (h-1) were obtained. As a result of gas chromatogram analysis, maleic anhydride (b-1) was not contained in the extract (h-1).

1 g of the dried product 1 (f-1) is sandwiched between layers of a polytetrafluoroethylene sheet, an aluminum sheet, and an iron plate in this order from the inside, and compression molded at 10 MPa using a press molding machine set at 280 ° C. Film (i
-1) was obtained. By the same operation, a film (a-1) was obtained from the polyphenylene ether (a-1). About the obtained film (i-1), FT / IR manufactured by JASCO Corporation
When infrared spectroscopy was performed using a -420 type Fourier transform infrared spectrophotometer, a peak derived from maleic acid added to polyphenylene ether was observed at 1790 cm ^-1 in the measurement for (i-1). It was confirmed that the added amount of maleic anhydride (b-1) was 0.3 parts by weight.

This dried product 1 (f-1) was used in Examples as a functionalized polyphenylene ether (PPE-2). (Production Example 3) Production Example of Liquid Crystal Polyester (LCP-1) Under a nitrogen atmosphere, p-hydroxybenzoic acid, 2-
Hydroxy-6-naphthoic acid and acetic anhydride were charged, heated and melted, and polycondensed to obtain a liquid crystal polyester (LCP-1) having the following theoretical structural formula. In addition, the component ratio of a composition represents a molar ratio.

[0043]

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(Production Example 4) Liquid crystal polyester (LCP-
Production Example 2) Under a nitrogen atmosphere, p-hydroxybenzoic acid, polyethylene terephthalate, and acetic anhydride are charged, heated and melted, and polycondensed to obtain a liquid crystal polyester (LCP-2) having the following theoretical structural formula. Was. In addition, the component ratio of a composition represents a molar ratio.

[0045]

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The physical properties of each resin composition were evaluated according to the following methods. (1) Fluidity The obtained pellets were heated at a cylinder temperature of 330/330 /
When forming a 1.6 mm thick tankaku test piece using an injection molding machine [IS-80EPN: manufactured by Toshiba Machine Co., Ltd.] set at 320/310 ° C. and a mold temperature of 140 ° C. The gauge pressure at the time of measurement was measured.
This pressure is referred to as SSP [Short Shot Pressure] (Kg / c
m ² ), and the smaller the value, the better the fluidity.

(2) Heat resistance ASTM D648 under the same molding conditions as in (1) above.
It was molded into a molded piece conforming to. Using the obtained molded piece, the heat deformation temperature under a load of 1.82 MPa was measured.

(3) Flame Retardancy Under the same molding conditions as in (1) above, a 1.6 mm thick tankaku test piece was molded, and a combustion test was carried out in accordance with UL-94. After 10 seconds of flame contact, the burning time from release of the flame to the disappearance of the flame is defined as t ₁ (second), and after 10 seconds of flame contact, the combustion time from the release of the flame to the disappearance of the flame is t.
₂ (seconds), and the average combustion time between t ₁ and t ₂ was T (seconds). ：: Average burning time (T) is less than 10 seconds. X: Average burning time (T) is 10 seconds or more.

(4) Dimensional stability Under the same molding conditions as in the above (1), a 1.6 mm-thick tankaku test piece was molded, and its length was measured. The shrinkage (%) was determined based on the dimension value.

[0050]

Examples 1 to 5 Polyphenylene ether (PPE-1)
Or PPE-2), liquid crystal polyester (LCP-1 or LCP-2), phenyl isocyanate (Ph
I), glass fiber (average length 3 mm, chopped fiber; abbreviated as “filler”) at the ratio shown in Table 1
Twin screw extruder with vent port set to 50-310 ° C (ZSK-25; WERNER & PFLEIDERER)
And melt-kneaded using the same to obtain pellets. Using the pellets, molding was performed by the method described above, and physical properties were evaluated. The results are shown in Table 1.

[0051]

Comparative Examples 1 and 3 Polyphenylene ether (PPE-1) and liquid crystal polyester (LC) were used without using PhI.
P-1) was performed in the same manner as in Example 1 except that the proportions shown in Table 1 were used, to obtain pellets. Using this pellet,
Molding was performed by the method shown above, and physical properties were evaluated. The results are shown in Table 1.

[0052]

Comparative Example 2 Except that polyphenylene ether (PPE-1) and polystyrene [manufactured by A & M Co., polystyrene 685 (abbreviated as “GPS”) were used in the proportions shown in Table 1 without using LCP-1 and PhI. Was carried out in the same manner as in Example 1 to obtain pellets. Using the pellets, molding was performed by the method described above, and physical properties were evaluated.
The results are shown in Table 1.

[0053]

[Table 1]

As can be seen from Table 1, by adding an organic compound containing an isocyanate group, the flowability was greatly improved, and the flowability, heat resistance, flame retardancy and dimensional stability were simultaneously achieved at a sufficient level. We can see that we can do it.

[0055]

According to the present invention, it has become possible to provide a resin composition which can simultaneously achieve a sufficient level of fluidity, heat resistance, flame retardancy and dimensional stability.

Claims (5)

[Claims] 1. A polyphenylene ether-based resin (A)
0 to 99.9 parts by weight, and (B) 0.1 of liquid crystal polyester
(C) an organic compound containing an isocyanate group in an amount of 0.1 to 30 parts by weight, and
A resin composition obtained by blending from 0.01 to 10 parts by weight. 2. The resin composition according to claim 1, wherein the component (C) contains one or two isocyanate groups in the molecule. 3. The resin composition according to claim 1, wherein the component (C) contains one isocyanate group in the molecule. 4. The method according to claim 1, wherein 0.1 to 300 parts by weight of the inorganic filler (D) is added to 100 parts by weight of the total of the components (A) and (B). The resin composition according to any one of the above. 5. The resin composition according to claim 1, wherein the component (C) is phenyl isocyanate.